ILLINOIS POLLUTION CONTROL BOARD
December 20,
1990
IN THE MATTER OF:
)
R90—1l
RCRA UPDATE, USEPA REGULATIONS
)
(Identical
in Substance Rules)
(4—1—90 THROUGH 6—30—90)
)
PROPOSAL FOR PUBLIC COMMENT
PROPOSED ORDER OF THE BOARD
(By J. Anderson):
Pursuant to Sections 22.4(a) of the Environmental Protection Act (Act),
the Board proposes amendments to the Resource Conservation and Recovery Act
(RCRA)
regulations.
Section 22.4(a)
provides for quick adoption of regulations which are
“identical
in substance” to federal regulations and that Title VII of the Act
and Section
5 of the Administrative Procedure Act (APA)
shall not apply.
Because this rulemaking is not subject to Section 5 of the APA, it
is not
subject to first notice or to second notice review by the Joint Committee on
Administrative Rules
(JCAR).
The federal RCRA regulations are found at 40 CFR
260 through 268.
This rulemaking updates RCRA rules to correspond with
federal amendments more fully outlined in the accompanying Opinion.
This Order
is supported by an Opinion adopted on the
same
day.
The
Board will receive public comment on the proposal for a period of 45 days
following
its publication in the Illinois Register.
The complete text of the
proposed rules follows.
IT IS SO ORDERED.
I,
Dorothy M.
Gunn,
Clerk of the Illinois Pollution Control Board,
hereby
certify that the above Order was adopted on the
______________
day of
______________
1990,
by a vote of
7
O
~~74
#/~
Dorothy M. ~
Clerk
Illinois Pol~htionControl Board
117—321

2
TITLE
35:
ENVIRONMENTAL PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER
I:
POLLUTION CONTROL BOARD
SUBCHAPTER b:
PERMITS
PART 703
RCRA PERMIT
PROGRAM
SUBPART A:
GENERAL PROVISIONS
SUBPART B:
PROHIBITIONS
Prohibitions in General
RCRA Permits
Specific Inclusions in Permit Program
Specific Exclusions from Permit Program
Discharges of Hazardous Waste
Reappiicatioris
Initial Applications
Federal Permits (Repealed)
SUBPART
C:
AUTHORIZATION BY RULE
AND
INTERIM STATUS
Purpose and Scope
Permits by Rule
Application by Existing HWM Facilities
QualificationB
Application by New
HWM
Facilities
Amended Part A Application
Qualifying for Interim Status
Prohibitions During Interim Status
Changes During Interim Status
Interim Status Standards
Grounds for Termination of Interim Status
Permits for Less Than an Entire Facility
Closure by Removal
Procedures for Closure Determination
SUBPART D:
APPLICATIONS
Scope and Relation to Other Parts
Purpose
References
Section
703. 100
703.101
703.110
Section
703. 120
703. 121
703.122
703. 123
703.124
703. 125
703. 126
703. 127
Section
703. 140
703. 141
703. 150
703. 151
703. 152
703. 153
703.154
703. 155
703. 156
703. 157
703. 158
703.159
703. 160
Section
703. 180
703. 181
703. 182
703. 183
703. 184
703.
185
703.186
703.187
and Interim Status
Applications in General
Contents of Part A
Contents of Part B
General Information
Facility Location Information
Groundwater Protection Information
Exposure Information
Solid Waste Management Units
117—32 2

3
703.188
Other Information
703.200
Specific Information
703.201
Containers
703.202
Tank Systems
703.203
Surface Impoundments
703.204
Waste Piles
703.205
Incinerators
703.206
Land Treatment
703.207
Landfills
703.209
Miscellaneous Units
SUBPART E:
SHORT TERM AND PHASED PERMITS
Section
703.221
Emergency Permits
703.222
Incinerator Conditions Prior to Trial Burn
703.223
Incinerator Conditions During Trial Burn
703.224
Incinerator Conditions After Trial Burn
703.225
Trial Burns for Existing Incinerators
703.230
Land Treatment Demonstration
703.231
Research,
Development and Demonstration Permits
SUBPART F:
PERMIT CONDITIONS OR DENIAL
Section
703.240
Permit Denial
703.241
Establishing Permit Conditions
703.242
Noncompliance Pursuant to Emergency Permit
703.243
Monitoring
703.244
Notice of Planned Changes
703.245
Twenty-four Hour Reporting
703.246
Reporting Requirements
703.247
Anticipated Noncompliance
SUBPART G:
CHANGES TO PERMITS
Section
703.260
Transfer
703.270
Modification
703.271
Causes for Modification
703.272
Causes
for Modification or Reissuance
703.273
Facility Siting
703.280
Permit Modification at the Request of the Permittee
703.281
Class
1 Modifications
703.282
Class
2 Modifications
703.283
Class
3 Modifications
Appendix A
Classification of Permit Modifications
AUTHORITY:
Implementing Section 22.4 and authorized by Section
27 of the
Environmental Protection Act (Ill. Rev.
Stat.
1989, ch.
111
1/2,
pars.
1022.4
and 1027).
SOURCE:
Adopted in R82-19,
53 PCB
131,
at
7
Ill. Reg.
14289, effective
October
12,
1983;
amended in R83—24 at 8
Ill. Reg.
206, effective December 27,
117—323

4
1983; amended
in R84—9 at
9
Ill.
Reg.
11899, effective July 24,
1985;
amended
in R85-22 at 10
Ill.
Reg.
1110, effective January
2,
1987;
amended in R85-23
at
10
Ill. Reg.
13284, effective July 28,
1986;
amended in R86-1 at 10
Ill.
Reg.
14093, effective August
12,
1986; amended in R86—19 at
10
Ill.
Reg.
20702, effective December
2,
1986;
amended in R86—28 at
11 Ill. Reg.
6121,
effective March 24,
1987;
amended in R86—46 at 11 Ill. Reg.
13543, effective
August
4,
1987;
amended in R87—5 at
11
Ill. Reg.
19383, effective November 12,
1987;
amended in R87—26 at
12
Ill. Reg.
2584,
effective January 15,
1988;
amended in R87—39
at
12
Ill. Reg.
13069, effective July 29,
1988;
amended in
R88-16 at
13
Ill.
Reg. 447, effective December 27,
1988; amended in R89—1
at
13
Ill.
Reg.
18477, effective November 13,
1989; amended in R89—9 at
14
Ill.
Reg.
6278,
effective April
16,
1990; amended in R90—2 at
14
Ill.
Reg.
14492,
effective August
22,
1990;
amended
in R90—11 at 15
Ill.
Reg.
,
effective
SUBPART D:
APPLICATIONS
Section 703.183
General Information
The following information is required in the Part
B application for all HWM
facilities,
except as
35
Ill. Adm. Code 724.101 provides otherwise:
a)
A general description of the facility;
b)
Chemical and physical analyses of the hazardous wastes to be
handled at the facility.
At a minimum,
these analyses must
contain all the information which must be known to treat,
store or
dispose of the wastes properly in accordance with 35 Ill.
Adrn.
Code 724;
c)
A copy of the waste analysis plan required by 35
Ill.
Adxn.
Code
724.113(b)
and,
if applicable,
35
Ill.
Adm. Code 724.113(c);
d)
A description of the security procedures and equipment required by
35
Ill. Adm.
Code 724.114,
or a justification demonstrating the
reasons for requesting a waiver of this requirement;
e)
A copy of the general inspection schedule required by 35
Ill.
Adm.
Code 724.115(b).
Include where applicable,
as part of the
inspection schedule,
specific requirements in 35
Ill.
Adxn. Code
724.274,
724.293(i),
724.295,
724.326,
724.354,
724.373, 724.403~
et~4724.702, 724.933,
724.952, 924.953 and 724.958
f)
A justification of any request for
a waiver of the preparedness
and prevention requirements of 35
Ill. Adm. Code 724.Subpart
C;
g)
A copy of the contingency plan required by 35
Ill. Adm. Code
724.Subpart D;
BOARD NOTE:
Include, where applicable,
as part of the contingency
plan,
specific requirements in 35
Ill. Adm. Code 724.327 and
724.355.
35
Ill. Adm. Code 724.355 has not yet been adopted.
117—324

5
h)
A description of procedures,
structures or equipment used at the
facility to:
1)
Prevent hazards in unloading operations
(for example,
ramps,
special forklifts);
2)
Prevent runoff from hazardous waste handling areas to other
areas of the facility or environment,
or to prevent flooding
(for example, berms, dikes,
trenches);
3)
Prevent contamination of water supplies;
4)
Mitigate effects of equipment failure and power outages; et~4
5)
Prevent undue exposure of personnel to hazardous waste
(for
example, protective clothing); ~
~j
Prevent releases to the atmosphere.
i)
A description of precautions to prevent accidental ignition or
reaction of ignitable, reactive or incompatible wastes as required
to demonstrate compliance with 35
Ill. Adm. Code 724.117 including
documentation demonstrating compliance with
35
Ill.
Adm. Code
724.117(c);
j)
Traffic pattern, estimated volume
(number, types of vehicles)
and
control
(for example,
show turns across traffic lanes and stacking
lanes
(if appropriate); describe access road surfacing and load
bearing capacity;
show traffic control signals);
k)
Facility location information as required by Section 703.184;
1)
An outline of both the introductory and continuing training
programs by owners or operators to prepare persons to operate or
maintain the HWM facility in a safe manner as required to
demonstrate compliance with 35
Ill.
Adin.
Code 724.116.
A brief
description of how training will be designed to meet actual job
tasks in accordance with requirements in 35 Ill.
Adxn.
Code
724. 116(a) (3);
m)
A copy of the closure plan and, where applicable, the post—
closure plan required by 35
Ill. Adm.
Code 724.212, 724.218 and
724.297.
Include where applicable, as part of the plans,
specific
requirements in 35
Ill. Adm. Code 724.278,
724.297,
724.328,
724.358,
724.380,
724.410, 724.451,
724.701 and 724.703;
n)
For
hazardous
waste
disposal
units
that
have
been
closed,
documentation that notices required under 35 Ill.
Adm
Code
724.219
have been filed;
117—325

6
0)
The most recent closure cost estimate for the facility prepared in
accordance with 35
Ill. Mm.
Code
724.242 and a copy of the
documentation required to demonstrate financial assurance under 35
Ill. Adm. Code 724.243.
For a new facility,
a copy of the
required documentation may be submitted 60 days prior to the
intitial receipt of hazardous wastes,
if
it
is later than the
submission of the Part B;
p)
Where applicable,
the most recent post—closure cost estimate for
the facility prepared in accordance with 35
Ill. Adm. Code 724.244
plus a copy of the documentation required to demonstrate financial
assurance under 35
Ill. Adm. Code 724.245; For a new facility, a
copy of the required documentation may be submitted 60 days prior
to the intitial receipt of hazardous wastes,
if
it is later than
the submission of the Part
B;
q)
Where applicable,
a copy of the insurance policy or other
documentation which comprises compliance with the requirements of
35
Ill. Adm. Code 724.247.
For a new facility, documentation
showing the amount of insurance meeting the specification
of 35
Ill.
Adm.
Code 724.247(a) and,
if applicable,
35 Ill.
Adm.
Code
724.247(b), that the owner or operator plans to have
in effect
before initial receipt of hazardous waste for treatment,
storage
or disposal.
A request for an alternative level of required
coverage,
for
a new or existing facility, may be submitted as
specified in 35
Ill. Adm.
Code 724.247(c);
s)
A topographic map showing a distance of 1000 feet around the
facility at
a scale of 2.5 centimeters
(1
inch)
equal to not more
than 61.0 meters
(200 feet).
Contours must be shown on the map.
The contour interval must be sufficient to clearly show the
pattern of surface water flow in the vicinity of and from each
operational unit of the facility.
For example,
contours with an
interval
of 1.5 meters
(5 feet),
if relief is greater than 6.1
meters (20 feet),
or an interval of 0.6 meters
(2 feet),
if relief
is less than 6.1 meters
(20 feet).
Owners and operators of HWM
facilities located
in mountainous areas shall use larger contour
intervals to adequately show topographic profiles of facilities.
The map must clearly show the following:
1)
Map scale and date;
2)
100—year floodplain area;
3)
Surface waters including intermittent streams;
4)
Surrounding land uses
(residential,
commercial,
agricultural,
recreational);
5)
A wind rose
(i.e., prevailing windspeed and direction);
6)
Orientation of the map (north arrow);
117—326

7
7)
Legal boundaries of the HWM facility site;
8)
Access control
(fences,
gates);
9)
Injection and withdrawal wells both on-site and off—site;
10)
Buildings; treatment,
storage or disposal operations;
or
other structures (recreation areas,
runoff control systems,
access and internal roadB,
8torm, sanitary and process
sewage systems,
loading and unloading areas,
fire control
facilities,
etc.);
11)
Barriers for drainage or flood control;
12)
Location of operational units within the HWM facility site,
where hazardous waste is
(or will be) treated,
stored or
disposed (include equipment cleanup areas);
BOARD NOTE:
For large HWM facilities, the Agency shall
allow the use of other scales on a case by case basis.
t)
Applicants shall submit such information as the Agency determines
is necessary for
it to determine whether to issue
a permit and
what conditions to impose
in any permit issued.
u)
For land disposal facilities,
if a case—by-case extension has been
approved under 35
Ill.
Adm.
Code 728.105,
or if a petition has
been approved under 35
Ill.
Adm. Code 728.106,
a copy of the
notice of approval of the extension or of approval of the petition
is required.
BOARD NOTE:
Derived from
40
CFR
270.14(b)
(1988),
as amended at
54
Fed.
Reg.
617, January 9,
1989.
(Source:
Amended at
15
Ill.
Reg.
,
effective
Section 703.210
Process Vents
Except
as otherwise provided in 35 111.
Adm. Code 724.101,
owners and
operators of facilities which have process vents to which 35
Ill.
Adm. Code
724.Subpart AA applies shall provide the following additional information:
~j
For facilities which cannot
install a closed—vent system and
control device to comply with 35
Ill.
Adm. Code 724.Subpart AA,
on
the effective date on which the facility becomes
sub-lect to that
Subpart or
35 Ill. Adm. Code 725.Subpart AA,
an implementation
schedule
as specified in
35
Ill. Adm. Code 724.933(aY(2).
~j
Documentation of compliance with the process vent standards
in
35
Ill.
Adm. Code 724.932,
includinQ:
117—32 7

8
fl
Information and data identifying all affected process vents,
annual throughput and operating hours of each affected unit,
estimated emission rates for the affected vent and for the
overall facility (i.e.,
the total emissions for all affected
vents at the facility)
and the a~~roximatelocation within
the facility of each affected unit (e.g..
identify the
hazardous waste management units on
a facility plot plan~.
~
Information and data su~~ortinaestimates of vent emissions
and emission reduction achieved by add—on control devices
based on engineering calculations or source tests.
For the
purpose of determining compliance, estimates of vent
emissions and emission reductions must be made using
operating parameter values
(e.g., temperatures,
flow rates
or concentrations) which represent the conditions which
exist when the waste management unit is operating at the
highest load or capacity level reasonably expected to occur.
~j
Information and data used to determine whether or not a
process vent
is subject to 35 Ill.
Adrn. Code 724.932.
çj
Where an owner or operator applies for permission to use a control
device
other
than a thermal vapor incinerator, catalytic vapor
incinerator,
flare, boiler,
process heater,
condenser or carbon
adsorption system to comply with 35
Ill.
Adm. Code 724.932,
and
chooses to use test data to determine the organic removal
efficiency or the total organic compound concentration achieved by
the control device,
a performance test plan as specified
in
35
Ill.
Adm.
Code 724.935(b) (3).
~j
Documentation of compliance with 35
Ill.
Adm.
Code
724.933,
including:
fl
A list of all information references and sources used in
preparing the documentation.
~J
Records
including the dates of each compliance test required
by 35
Ill. Adm. Code 724.933(k).
~j.
A design analysis, specifications,
drawings,
schematics,
and
piping and instrumentation diagrams based on the appropriate
sections of APTI Course 415,
incorporated by reference in 35
Ill. Adm. Code 720.111,
or other engineering texts approved
by the Agency which present basic control device design
information.
The design analysis must address the vent
stream
characteristics
and
control
device
parameters
as
sepcified in 35
Ill.
Adm.
Code
724.935(b)
(4) (CI.
~).
A statement signed and dated by the owner or operator
certifying that the o~eratina~arametere used in the design
analysis reasonably represent the conditions which exist
when the hazardous wapte management unit
is or would be
117—328

9
when
the
hazardous
waste
management
unit
is
or
would
be
operating at the highest load or capacity level reasonably
expected
to
occur.
~J.
A
statement
signed
and
dated
by
the
owner
or
operator
certifying that the control device
is designed to operate at
an
efficiency
of
95
weight
percent
or
greater
unless
the
total
organic
emission
limits
of
35
Ill.
Adm.
Code
724.932(a)
for
affected
process
vents
at
the
facility
can
be
attained
by
a
control
device
involving
vapor
recovery
at
an
efficiency
less
than
95
weight
percent.
(Source:
Added
at
15
Ill.
Reg.
,
effective
Section
703.211
Equipment
Except
as
otherwise
provided
in
35
Ill.
Adm.
Code
724.101,
owners
and
operators
of
facilities
which
have
equipment
to
which
35
Ill.
Ad.m.
Code
724.Subpart
BB
applies
shall
provide
the
following
additional
information:
~J
For
each
piece
of
equipment to which
35
Ill.
Adm.
Code
724.Subpart
BB
applies:
fl
Equipment
identification
number
and
hazardous
waste
management
unit
identification.
2.1
Approximate
locations
within
the
facility
(e.g.,
identify
the
hazardous
waste
management
unit
on
a
facility
plot
plan).
~j
Type
of
equipment
(e.g.,
a
pump
or
pipeline
valve).
j)
Percent
by
weight
total
organica
in
the
hazardous
wastestream
at
the
equipment.
.~j
Hazardous
waste
state
at
the
equipment
(e.g.,
gas/vapor
or
liquid).
QJ
Method
of
compliance
with
the
standard
(e.g.,
“monthly
leak
detection
and
repair”
or
“eguipped
with
dual
mechanical
seals”).
~j.
For
facilities
which
cannot
install
a
closed-vent
system
and
control
device
to
comply
with
35
Ill.
Adm.
Code
724.Subpart
BB
on
the
effective
date
that
facility
becomes
subiect
to
this
Subpart
or
35
Ill.
Adm.
Code
724.Subpart
BB.
an
implementation schedule
as
specified
in
35
Ill.
Mm.
Code
724.933(a)
(2).
~j
Where
an
owner
or
operator
applies
for
permission
to
use
a
control
device
other
than
a
thermal
vapor
incinerator,
catalytic
vapor
incinerator,
flare,
boiler,
process
heater,
condenser
or
carbon
adsorption
system
and
chooses
to
use
test
data
to
determine
the
117—32 9

10
concentration
achieved
by
the
control
device,
a
performance
test
plan
as
specified
in
35
Ill.
Adni.
Code
724.935(b)
(3).
~j
Documentation which demonstrates compliance with the equipment
standards in 35
Ill.
Adrn.
Code 724.952 or 724.959.
this
documentationmust
contain
the
records
re~uirad
under
35
Ill.
Adm.
Code 724.964.
The Agency shall request further documentation
if
necessary to demonstrate compliance.
Documentation to demonstrate
compliance with 35
Ill.
Adm.
Code 724.960m must include the
following information:
fl
A
list
of
all
information
references
and
sources
used
in
preparing
the
documentation.
21
Records including the dates of each compliance test required
by 35
Ill.
Adm. Code 724.933(1).
fl
A
design
analysis,
specifications,
drawings,
schematics,
and
piping
and instrumentation diagrams based on the appropriate
sections of APTI Course 415,
incorporated by reference
in
35
Ill.
Mm.
Code
720.111,
or
other
engineering
texts
appproved
by
the
Agency
which
present
basic
control
device
design
information.
The
design
analysis must address the vent
stream
characteristics
and
control
device
parameters
as
specified
in
35
Ill.
Adm.
Code
724.935(b)
(4) (C).
j).
A statement signed and dated by the owner or operator
certifying
that
the
operating
parameters
used
in
the
design
analvsis reasonably represent the conditions which exist
when
the
hazardous waste management unit
is or would be
operating
at
the
highest
load
or
capacity
level
reasonably
expected
to
occur.
~j
A
statement
signed
and
dated
by
the
owner
or
operator
certifying
that
the
control
device
is
designed
to
operate
at
an
efficiency
of
95
weight
percent
or
greater.
(Source:
Added
at
15
Ill.
Reg.
,
effective
)
117—330

11
Section 703.Appendix A
Classification of Permit Modifications
Class Modifications
A.
General Permit Provisions
1
1.
Administrative and informational changes.
1
2.
Correction of typographical errors.
1
3.
Equipment replacement or upgrading with functionally
equivalent
components
(e.g., pipes,
valves,
pumps,
conveyors,
controls).
4.
Changes in the frequency of or procedures for monitoring,
reporting, sampling or maintenance activities by the
permittee:
1
a.
To provide for more frequent monitoring, reporting or
maintenance.
2
b.
Other changes.
5.
Schedule of compliance:
1*
a.
Changes in interim compliance dates,
with prior
approval of the Agency.
BOARD NOTE:
“*“
indicates that prior Agency approval
is required.
3
b.
Extension of final compliance date.
1*
6.
Changes in expiration date of permit to allow earlier permit
termination, with prior approval of the Agency.
1*
7.
Changes in ownership or operational control of a facility,
provided the procedures of Section 703.260(b) are followed.
B.
General Facility Standards
1.
Changes to waste sampling or analysis methods:
1
a.
To conform with Agency guidance or Board regulations.
.1
b.
To incorporate chances associated with F039
(multi—
source leachate) sampling or analysis methods.
2
~.
Other changes.
2.
Changes to analytical quality assurance/control plan:
117—33 1

12
1
a.
To
conform
with
agency
guidance
or
regulations.
2
b.
Other changes.
1
3.
Changes in procedures for maintaining the operating record.
2
4.
Changes in frequency or content of inspection schedules.
5.
Changes
in the training plan:
2
a.
That affect the
type
or decrease the amount of
training given to employees.
1
b.
Other changes.
6.
Contingency plan:
2
a.
Changes in emergency procedures
(i.e.,
spill or
release response procedures).
1
b.
Replacement with functionally equivalent equipment,
upgrade or relocate emergency equipment listed.
2
c.
Removal of equipment from emergency equipment list.
1
d.
Changes
in name,
address or phone number of
coordinators or other persons or agencies identified
in the plan.
Note:
When a permit modification (such as
introduction of a new unit) requires a change in
facility plans or other general facility standards,
that change must be reviewed under the same procedures
as the permit modification.
C.
Groundwater Protection
1.
Changes to wells:
2
a.
Changes in the number,
location,
depth or design of
upgradient or downgradient wells of permitted
groundwater monitoring system.
1
b.
Replacement of an existing well that has been damaged
or
rendered
inoperable,
without
change
to
location,
design or depth of the well.
1*
2.
Changes in groundwater sampling or analysis procedures or
monitoring schedule, with prior approval of the Agency.
1*
3.
Changes in statistical procedure for determining whether a
statistically significant change in groundwater quality
117—332

13
between upgradient and downgradient wells has occurred,
with
prior approval of the Agency.
2*
4.
Changes in point of compliance.
5.
Changes in indicator parameters, hazardous constituents or
concentration limits
(including ACLa
(Alternate
Concentration Limits)):
3
a.
As specified in the groundwater protection standard.
2
b.
As specified in the detection monitoring program.
2
6.
Changes to
a detection monitoring program as required by 35
Ill.
Adm. Code 724.198(j), unless otherwise specified in
this Appendix.
7.
Compliance monitoring program:
3
a.
Addition of compliance monitoring program as
required
by 35
Ill. Adm.
Code 724.198(h)(4)
and 724.199.
b.
Changes to a compliance monitoring program as required
by 35
Ill.
Adni.
Code 724.199(k), unless otherwise
specified in this Appendix.
B.
Corrective action program:
3
a.
Addition of
a corrective action program as required by
35
Ill.
Adm.
Code
724.199(i)
(2)
and
724.200.
2
b.
Changes
to
a
corrective
action
program
as
required
by
35
Ill.
Adm.
Code
724.200(h),
unless
otherwise
specified
in
this
Appendix.
D.
Closure
1.
Changes
to
the
closure
plan:
1*
a.
Changes
in
estimate
of
maximum
extent
of
operations
or
maximum
inventory
of
waste
on—site
at
any
time
during
the
active
life
of
the
facility,
with
prior
approval
of
the
Agency.
1*
b.
Changes
in
the
closure
schedule
for
any
unit,
changes
in
the
final closure schedule for the facility or
extension
of
the
closure
period,
with
prior
approval
of
the
Agency.
1*
c.
Changes
in
the
expected
year
of
final
closure,
where
other
permit
conditions
are
not
changed,
with
prior
approval
of
the
Agency.
117—33 3

14
1*
d.
Changes
in
procedures
for
decontamination
of
facility
equipment
or
structures,
with
prior
approval
of
the
Agency.
2
e.
Changes
in
approved
closure
plan
resulting
from
unexpected
events
occurring
during
partial
or
final
closure,
unless
otherwise
specified
in
this
Appendix.
2
f.
Extension
of
the
closure
period
to
allow
a
landfill,
surface
impoundment
or
land
treatment
unit
to
receive
non—hazardous
wastes
after
final
receipt
of
hazardous
wastes
under
35
Ill.
Mm.
Code
724.213(d)
or
(e)..
3
2.
Creation
of
a
new
landfill
unit
as
part
of
closure.
3.
Addition
of
the
following
new
units
to
be
used
temporarily
for
closure
activities:
3
a.
Surface
impoundments.
3
b.
Incinerators.
3
c.
Waste
piles
that
do
not
comply
with
35
Ill.
Adin.
Code
724.350(c).
2
d.
Waste
piles
that
comply
with
35
Ill.
Adni.
Code
724.350(c).
2
e.
Tanks
or
containers
(other
than
specified
below).
1*
f.
Tanks
used
for
neutralization,
dewatering,
phase
separation
or
component
separation,
with
prior
approval
of
the
Agency.
E.
Post—Closure
1
1.
Changes
in
name,
address
or
phone
number
of
contact
in
post—
closure
plan.
2
2.
Extension
of
post—closure care period.
3
3.
Reduction
in
the
post—closure
care
period.
1
4.
Changes
to
the
expected
year
of
final
closure,
where
other
permit
conditions
are
not
changed.
2
5.
Changes
in
post—closure plan necessitated by eventB
occurring during the active life of the facility,
including
partial and final closure.
F.
Containers
117—334

15
1.
Modification
or
addition
of
container
units:
3
a.
Resulting in greater than 25
increase in the
facility’s container storage capacity, except as
provided in F(l)(c)
and F(4)(a).
2
b.
Resulting in up to 25
increase
in the facility’s
container storage capacity,
except as provided in
F(1)(c) and F(4)(a).
c.
Or treatment processes necessary to treat wastes that
are
restricted
from
land
disposal
to
meet
some
or
all
of
the
applicable
treatment
standards
or
to
treat
wastes
to
satisfy
(in
whole
or
in
part)
the
standard
of
“use
of
practically
available
technology
that
yields
the
greatest
environmental
benefit”
contained
in
40
CFR
268.8(a)(2)(ii),
incorporated by reference
in
35
Ill.
Adm.
Code
728.108,
with
prior
approval
of
the
Agency.
This
modification
may
also
involve
the
addition
of
new
waste
codes
or
narrative
description
of
wastes.
It
is
not
applicable
to
dioxin—containing
wastes
(FO2O,
F021,
F022,
F023,
F026,
F027
and
F028).
2.
2
a.
Modification
of
a
container
unit
without
increasing
the
capacity
of
the
unit.
b.
Addition
of
a
roof
to
a
container
unit
without
alteration
of
the
containment
system.
3.
Storage
of
different
wastes
in
containers,
except
as
provided
in
F(4):
3
a.
That
require
additional
or
different
management
practices
from
those
authorized
in
the
permit.
2
b.
That
do
not
require
additional
or
different
management
practices
from
those
authorized
in
the
permit.
Note:
See
Section
703.280(g)
for
modification
procedures
to
be
used
for
the
management
of
newly
listed
or
identified
wastes.
4.
Storage
or
treatment
of
different
wastes
in
containers:
2
a.
That require addition of units or change in treatment
process or management standards, provided that the
wastes are restricted from land disposal and are to be
treated to meet some or all of the applicable
treatment
standards,
or
are
to
be
treated
to
satisfy
117—335

16
(in whole or
in part)
the standard of “use of
practically available technology that yields the
greatest environmental benefit” contained in 40 CFR
268.8(a)(2)(ii),
incorporated by reference in 35 Ill.
Adm.
Code
728.108.
It
is
not
applicable
to
dioxin—
containing wastes
(F020,
F021,
F022, F023,
F026, F027
and F028).
b.
That do not require the addition of units or a change
in the treatment process or management Btandards, and
provided
that
the
units
have
previously
received
wastes of the same type (e.g., incinerator scrubber
water).
This modification is not applicable to
dioxin—containing
wastes
(F020,
F021,
F022,
F023,
F026, F027 and F028).
S.
Tanks
1.
3
a.
Modification or addition of tank units resulting in
greater than 25
increase in the facility’s tank
capacity,
except as provided in paragraphs G(1)(c),
G(1)(d)
and G(1)(e).
2
b.
Modification or addition of tank units resulting in up
to 25
increase in the facility’s tank capacity,
except as provided in paragraphs G(1)(d)
and G(1)(e).
2
c.
Addition of a new tank that will operate for more than
90 days using any of the following physical or
chemical treatment technologies:
neutralization,
dewatering,
phase separation or component separation.
1*
d.
After prior approval of the Agency,
addition of a new
tank that will operate for up to 90 days using any of
the following physical or chemical treatment
technologies:
neutralization, dewatering, phase
separation or component separation.
e.
Modification or addition of tank units or treatment
processes that are necessary to treat wastes that are
restricted from land disposal to meet some or all of
the applicable treatment standards or to treat wastes
to satisfy (in whole or in part)
the standard of “use
of practically available technology that yields the
greatest environmental benefit” contained in 40 CFR
268.8(a)(2)(ii),
incorporated by reference in 35
111.
Adm. Code 728.108, with prior approval of the Agency.
This modification may also involve the addition of new
waste codes.
It is not applicable to dioxin-
117—3 36

17
containing wastes (F020,
F021,
F022,
F023,
F026, F027
and F028).
2
2.
Modification of a tank unit or secondary containment system
without increasing the capacity of the unit.
3.
Replacement of a tank with
a tank that meets the same design
standards and has a capacity within
+1-
10
of the replaced
tank provided:
a.
The capacity difference is no more than 1500 gallons,
b.
The facility’s permitted tank capacity is not
increased and
c.
The replacement tank meets the same conditions in the
permit.
2
4.
Modification of
a tank management practice.
5.
Management of different wastes in tanks:
3
a.
That require additional or different management
practices, tank design,
different fire protection
specifications or significantly different tank
treatment process from that authorized in the permit,
except as provided in paragraph G(5)(c).
2
b.
That do not require additional or different management
practices,
tank design, different fire protection
specification or significantly different tank
treatment process than authorized in the permit,
except as provided in paragraph G(5)(d).
Note:
See Section 703.280(g)
for modification
procedures to be used for the management of newly
listed or identified wastes.
c.
That require addition of units or change in treatment
processes or management standards, provided that the
wastes are restricted from land disposal and are to be
treated to meet some or all of the applicable
treatment standards,
or that are to be treated to
satisfy (in whole or in part) the standard of “use of
practically available technology that yields the
greatest environmental benefit” contained in 40 CFR
268.8(a)(2)(ii), incorporated by reference in
35
Ill.
Adm. Code 728.108.
The modification
is not applicable
to dioxin—containing wastes
(F020,
F021, F022,
F023,
F026,
F027 and F028).
117— 33 7

18
d.
That do not require the addition of units or a change
in the treatment process or management standards,
and
provided that the units have previously received
wastes of the same type (e.g.,
incinerator scrubber
water).
This modification is not applicable to
dioxin—containing wastes (F020,
F021, P022,
P023,
F026,
F027 and P028).
H.
Surface Impoundments
3
1.
Modification or addition of surface impoundment units that
result in increasing the facility’s surface impoundment
storage or treatment capacity.
3
2.
Replacement of a surface impoundment unit.
2
3.
Modification of a surface impoundment unit without
increasing the facility’s surface impoundment storage or
treatment capacity and without modifying the unit’s liner,
leak detection system or leachate collection system.
2
4.
Modification of a surface impoundment management practice.
5.
Treatment,
storage or disposal of different wastes in
surface impoundments:
3
a.
That require additional or different management
practices or different design of the liner or leak
detection system than authorized in the permit.
2
b.
That do not require additional or different management
practices or different design of the liner or leak
detection system than authorized in the permit.
Note:
See Section 703.280(g)
for modification
procedures to be used for the management of newly
listed or identified wastes.
c.
That are wastes restricted from land disposal that
meet the applicable treatment standards or that are
treated to satisfy the standard of “use of practically
available technology that yields the greatest
environmental benefit” contained in 40 CFR
268.8(a)(2)(ii), incorporated by reference
in
35
Ill.
Adm.
Code 728.108,
and provided that the unit meets
the minimum technological reguirements stated in 40
CFR 268.5(h)(2),
incorporated by reference in
35
Ill.
Adm.
Code 728.105.
This modification is not
applicable to dioxin—containing wastes
(F020, F021,
F022, F023, P026,
F027 and F028).
117—338

19
d.
That
are
residues from wastewater treatment or
incineration,
provided the disposal occurs in a unit
that meets the minimum technological reguirements
stated in 40 CFR 268.5(h)(2),
incorporated by
reference in 35
Ill.
Adni. Code 728.105,
and provided
further that the surface
impoundment has previously
received wastes of the same type (for example,
incinerator scrubber water).
This modification is not
applicable to dioxin-containing wastes (F020, F02l,
F022,
F023,
F026,
F027 and P028).
I.
Enclosed Waste Piles.
For all waste piles, except those complying
with 35
Ill.
Adm.
Code 724.350(c), modifications are treated the
same as for a landfill.
The following modifications are
applicable only to waste piles complying with 35 Ill. Adm. Code
724.350(c).
1.
Modification or addition of waste pile units:
3
a.
Resulting in greater than 25
increase in the
facility’s waste pile storage or treatment capacity.
2
b.
Resulting in up to 25
increase in the facility’s
waste pile storage or treatment capacity.
2
2.
Modification of waste pile unit without increasing the
capacity of the unit.
3.
Replacement of
a waste pile unit with another waste pile
unit of the same design and capacity and meeting all waste
pile conditions in the permit.
2
4.
Modification of a waste pile management practice.
5.
Storage or treatment of different wastes in waste piles:
3
a.
That require additional or different management
practices or different design of the unit.
2
b.
That do not require additional or different management
practices or different design of the unit.
Note:
See Section 703.280(g)
for modification
procedures to be used for the management of newly
listed or identified wastes.
J.
Landfills and Unenclosed Waste Piles
3
1.
Modification or addition of landfill units that result in
increasing the facility’s disposal capacity.
3
2.
Replacement of a landfill.
117—339

20
3
3.
Addition or modification of a liner,
leachate collection
system,
leachate detection system,
run—off control or final
cover system.
2
4.
Modification of
a landfill unit without changing
a liner,
leachate collection system,
leachate detection system, run—
off control or final cover system.
2
5.
Modification of
a landfill management practice.
6.
Landfill
different
wastes:
3
a.
That
require additional or different management
practices,
different
design of the liner,
leachate
collection
system
or
leachate
detection system.
2
b.
That
do
not
require
additional
or
different
management
practices, different design of the liner,
leachate
collection
system
or
leachate
detection
system.
Note:
See
Section 703.280(g)
for modification
procedures
to
be
used
for
the management of newly
listed
or
identified
wastes.
c.
That
are wastes restricted from land disposal that
meet
the
applicable
treatment
standards
or
that
are
treated
to
satisfy
the
standard
of
“use
of
practically
available technology that yields the greatest
environmental benefit” contained in 40 CFR
268.8(a)(2)(ii),
incorporated by reference in 35 Ill.
Adm. Code 728.108,
and provided that the
landfill unit
meets the minimum technological reguirements stated in
40 CFR 268.5(h)(2),
incorporated by reference in 35
Ill. Adm.
Code 728.105.
This modification is not
applicable to dioxin—containing wastes
(F020, P021,
F022, F023, F026,
F027 and F028).
d.
That are residues from wastewater treatment or
incineration,
provided the disposal occurs in a
landfill unit that meets the minimum technological
reguirements stated in 40 CFR 268.5(h) (2),
incorporated by reference in
35
Ill.
Adm. Code
728.105,
and provided further that the landfill has
previously received wastes
of the same type
(for
example,
incinerator ash).
This modification
is not
applicable to dioxin—containing wastes (F020, P021,
F022,
P023,
P026, F027
and F028).
K.
Land Treatment
117—340

21
3
1.
Lateral expansion of or other modification of
a land
treatment unit to increase area extent.
2
2.
Modification of run—on control system.
3
3.
Modify run-off control system.
2
4.
Other modification
of land treatment unit component
specifications or standards required in permit.
5.
Management of different wastes in land treatment units:
3
a.
That
require
a
change
in
permit
operating
conditions
or
unit
design
specifications.
2
b.
That
do
not
require
a
change
in
permit
operating
conditions
or
unit
design
specifications.
Note:
See
Section
703.280(g)
for
modification
procedures
to
be
used for the management of newly
listed
or
identified
wastes.
6.
Modification
of
a
land
treatment
unit
management
practice
to:
3
a.
Increase
rate
or
change
method
of
waste
application.
1
b.
Decrease
rate
of
waste
application.
2
7.
Modification
of
a
land
treatment
unit
management
practice
to
change
measures
of
pH
or
moisture
content
or
to
enhance
microbial
or
chemical
reactions.
3
8.
Modification
of
a
land
treatment
unit
management
practice
to
grow
food
chain
crops,
to
add
to
or
replace
existing
permitted
crops
with
different
food
chain
crops
or
to
modify
operating
plans
for
distribution
of
animal
feeds
resulting
from such crops.
3
9.
Modification of operating practice due to detection of
releases from the land treatment unit pursuant to 35 Ill.
Adm. Code 724.378(g) (2).
3
10.
Changes in the unsaturated zone monitoring system resulting
in a change to the location,
depth, number of sampling
points
or replace unsaturated zone monitoring devices or
components of devices with devices or components that have
specifications different from permit requirements.
2
11.
Changes in the unsaturated zone monitoring system that do
not result
in a change to the location, depth,
number of
sampling points, or that replace unsaturated zone monitoring
117— 34
1

22
devices or components of devices with devices or components
having specifications different from permit requirements.
2
12.
Changes in background values for hazardous constituents in
soil
and
Boil-pore
liquid.
2
13.
Changes in sampling,
analysis or statistical procedure.
2
14.
Changes
in
land
treatment
demonstration
program
prior
to
or
during the demonstration.
1*
15.
Changes in any condition specified in the permit for
a land
treatment unit to reflect results of the land treatment
demonstration, provided performance standards are met,
and
the Agency’s prior approval has been received.
1*
16.
Changes to allow
a second land treatment demonstration to be
conducted when the results of the first demonstration have
not shown the conditions under which the wastes can be
treated completely, provided the conditions
for the second
demonstration are substantially the same as the conditions
for the first demonstration and have received the prior
approval of the Agency.
3
17.
Changes to allow a second land treatment demonstration to be
conducted when the results of the first demonstration have
not shown the conditions under which the wastes can be
treated completely, where the conditions for the second
demonstration are not substantially the same as the
conditions for the first demonstration.
2
18.
Changes
in vegetative cover requirements for closure.
L.
Incinerators
3
1.
Changes to increase by more than 25
any of the following
limits authorized in the permit: A thermal feed rate limit,
a waste feed rate limit or an organic chlorine feed rate
limit.
The Agency shall require a new trial burn to
substantiate compliance with the regulatory performance
standards unless this demonstration can be made through
other means.
2
2.
Changes to increase by up to 25
any of the following limits
authorized in the permit:
A thermal feed rate limit,
a waste
feed limit or an organic chlorine feed rate limit.
The
Agency shall require a new trial burn to substantiate
compliance with the regulatory performance standards unless
this demonstration can be made through other means.
3
3.
Modification of an incinerator unit by changing the internal
size or geometry of the primary or secondary combustion
117—342

23
units,
by adding
a primary or secondary combustion unit,
by
substantially changing the design of any component used to
remove HC1 or particulates from the combustion gases or by
changing other features of the incinerator that could affect
its capability to meet the regulatory performance standards.
The Agency shall require a new trial burn to substantiate
compliance with the regulatory performance standards,
unless
this demonstration can be made through other means.
2
4.
Modification of an incinerator unit in a manner that will
not
likely
affect
the
capability
of
the
unit
to
meet
the
regulatory performance standards but which will change the
operating conditions or monitoring requirements specified in
the permit.
The Agency may require a new trial burn to
demonstrate compliance with the regulatory performance
standards.
5.
Operating requirements:
3
a.
Modification of the limits specified in the permit for
minimum combustion gas temperature, minimum combustion
gas residence time or oxygen concentration in the
secondary combustion chamber.
The Agency shall
require a new trial burn to substantiate compliance
with the regulatory performance standards unless this
demonstration can be made through other means.
3
b.
Modification of any stack gas emission limitB
specified
in
the
permit,
or
modification
of
any
conditions in the permit concerning emergency shutdown
or automatic waste feed cutoff procedures or controls.
2
c.
Modification of any other operating condition or any
inspection or recordkeeping requirement specified in
the permit.
6.
Incineration of different wastes:
3
a.
If the waste contains
a POHC that is more difficult to
incinerate than authorized by the permit or
if
incineration of the waste requires compliance with
different regulatory performance standards than
specified
in the permit.,
the Agency shall require a
new trial burn to substantiate compliance with the
regulatory performance standards,
unless this
demonstration can be made through other means.
b.
If the waste does
not
contain
a
POHC that
is more
difficult to incinerate than authorized by the permit
and
if
incineration
of
the
waste
does
not
require
compliance
with
different
regulatory
performance
standards than specified in the permit.
117—34 3

24
BOARD NOTE:
See Section 703.280(g)
for modification
procedures to be used for the management of newly
listed
or
identified
wastes.
7.
Shakedown and trial burn:
2
a.
Modification of the trial burn plan or any of the
permit conditions applicable during the shakedown
period for determining operational readiness after
construction,
the trial burn period or the period
immediately following the trial burn.
1*
b.
Authorization of up to an additional 720 hours of
waste incineration during the shakedown period for
determining operational readiness after construction,
with the prior approval of the Agency.
1*
c.
Changes
in the operating requirements set in the
permit for conducting a trial burn,
provided the
change
is minor and has received the prior approval of
the Agency.
1*
d.
Changes
in
the
ranges
of
the
operating
requirements
set
in
the
permit
to
reflect
the results of the trial
burn,
provided the change
is minor and has received
the prior approval of the Agency.
8.
Substitution of an alternate type of fuel that
is not
specified in the permit.
BOARD NOTE:
Derived from 40 CFR 270.42, Appendix
I,
se
adopted
at
Z3 Fed.
Itcg.
37934, Ccptember
28,
1088
(1990).
(Source:
Amended
at
15
Ill.
Reg.
,
effective
)
117— 344

25
TITLE
35:
ENVIRONMENTAL
PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER
I:
POLLUTION CONTROL BOARD
SUBCHAPTER
c:
HAZARDOUS WASTE OPERATING REQUIREMENTS
PART 720
HAZARDOUS
WASTE
MANAGEMENT
SYSTEM:
GENERAL
SUBPART A:
GENERAL PROVISIONS
Section
720.101
Purpose,
Scope and Applicability
720.102
Availability of Information; Confidentiality of Information
720.103
Use of Number and Gender
SUBPART B:
DEFINITIONS
Section
720.110
Definitions
720.111
References
SUBPART C:
RULEMAKING PETITIONS AND OTHER PROCEDURES
Section
720.120
Rulemaking
720.121
Alternative Equivalent Testing Methods
720.122
Waste Delisting
720.130
Procedures for Solid Waste Determinations
720.131
Solid Waste Determinations
720.132
Boiler
Determinations
720.133
Procedures for Determinations
720.140
Additional
regulation
of
certain
hazardous
waste
Recycling
Activities on
a case—by—case Basis
720.141
Procedures for case—by—case regulation of hazardous waste
Recycling
Activities
Appendix A
Overview of
40
CFR,
Subtitle
C
Regulations
AUTHORITY:
Implementing Section 22.4 and authorized by Section 27 of
the
Environmental Protection Act
(Ill.
Rev.
Stat. 1989,
ch. 111
1/2,
pars.
1022.4
and 1027).
SOURCE:
Adopted
in R81—22,
43 PCB 427,
at 5 Ill. Reg.
9781,
effective as
noted
in 35 Ill.
Adm. Code 700.106;
amended and codified in R81—22, 45 PCB
317,
at
6 Ill. Reg.
4828, effective as noted in 35 Ill.
Adin.
Code 700.106;
amended
in R82—l9 at 7
Ill. Reg.
14015, effective Oct.
12, 1983;
amended in
R84-9,
53 PCB
131 at 9 Ill. Reg. 11819, effective July 24,
1985;
amended in
R85-22 at 10
Ill. Reg.
968, effective January
2,
1986;
amended in R86-1 at 10
Ill.
Reg.
13998, effective August
12,
1986;
amended in R86—19 at 10 Ill. Reg.
20630, effective December
2,
1986; amended in R86—28 at 11
Ill. Reg. 6017,
effective March 24, 1987;
amended in R86—46 at 11
Ill. Reg.
13435, effective
August
4,
1987;
amended in R87—5 at
11
Ill.
Reg. 19280,
effective November 12,
1987;
amended in R87—26 at
12 Ill.
Reg.
2450, effective January 15,
1988;
amended in R87—39 at
12
Ill.
Reg.
12999, effective July 29,
1988; amended in
R88-l6 at
13
Ill.
Reg.
362, effective December 27,
1988;
amended in R89—1 at
117—345

26
13
Ill.
Reg. 18278, effective November 13,
1989;
amended in R89—2 at
14 Ill.
Reg.
3075,
effective February 20,
1990;
amended in R89—9
at
14
Ill.
Reg.
6225,
effective April
16,
1990;
amended
in R90—10 at
14 Ill. Reg.
,
effective
September 25,
1990;
amended in R90—17 at
14
Ill. Reg.
,
effective
; amended in R90—ll at
15 Ill.
Reg.
,
effective
SUBPART B:
DEFINITIONS
Section 720.111
References
a)
The following publications are incorporated by reference:
ANSI.
Available from the American National Standards
Institute,
1430 Broadway,
New York, New York
10018,
(212)
354—3300:
ANSI
B31.3 and B31.4.
See
ASME/ANSI
B3l.3 and B31.4
API.
Available from the American Petroleum Institute,
1220
L Street, N.W., Washington,
D.C.
20005,
(202)
682—8000:
“Guide
for
Inspection
of
Refinery
Equipment, Chapter
XIII,
Atmospheric
and
Low
Pressure
Storage Tanks,” 4th
Edition,
1981,
reaffirmed December,
1987.
“Cathodic Protection of
Underground
Petroleum
Storage
Tanks and Piping Systems,” API Recommended Practice
1632, Second Edition, December,
1987.
“Installation of Underground Petroleum Storage
Systems,” API Recommended Practice 1615,
Fourth
Edition, November,
1987.
APTI.
Available from the Air and Waste Management
Association, Box 2861,
Pittsburg, PA
15230,
(412)
232—
3444:
APTI Course 415:
Control of Gaseous Emissions, EPA
Publication EPA—450/2—81—005, December,
1981.
ASME.
Available
from
the American Society of Mechanical
Engineers,
345 East 47th Street, New York, NY
10017,
(212)
705—7722:
“Chemical Plant and Petroleum Refinery Piping”,
ASME/ANSI
B3l.3—1987,
as supplemented by B31.3a—1988
and B31.3b—1988.
Also available from ANSI.
“Liquid Transportation Systems for Hydrocarbons,
Liquid Petroleum Gas, Anhydrous Ammonia,
and
117—346

27
Alcohols”, ASME/ANSI B31.4—1986,
as supplemented by
B31.4a—1987.
Also available from ANSI.
ASTM.
Available from American Society for Testing and
Materials,
1916 Race Street,
Philadelphia, PA 19103,
(215)
299—5400:
ACTII Standard Test Methods
for
Flash roint of
Liqui
Cetafla3h Closed Tester,”
ACTM
Standard
D
3828
87
ASTM D93-85.”ACTM Standard Test Methods for Flash
Point ~yPensky—Martens
Closed Tester,” ACTM Standard
D 03
70 or
D 03 80approved October 25,
1985.
ASTM D1946—90,
Standard Practice for Analysis of
Reformed Gas by Gas Chromatography, Approved March 30,
1990.
ASTM D2267—88,
Standard Test Method for Aromatics in
Light Naphthas and Aviation Gasolines by Gas
Chromatography,
approved November 17.
1988.
ASTM D2382-88,
Standard Test Method for Heat of
Combustion of Hydrocarbon Fuels by Bomb Calorimeter
(High Precision Method), approved October 31,
1988.
ASTM D2879-86,
Standard
Test
Method for Vapor
Pressure-Temperature Relationship and Initial
Decomposition Temperature
of Liquids by Isoteniscope,
approved October 31,
1986.
ASTM D3828-87,
Standard Test Methods for Flash Point
of Liquids by Setaflash Closed Tester,
approved
December
14,
1988.
ASTM El68-88,
Standard Practices
for General
Techniques of Infrared Quantitative Analysis,
approved
May 27,
1988.
ASTM E169—87,
Standard Practices for General
Techniques of Ultraviolet—Visible Ouantitative
Analysis,
approved February
1,
1987.
ASTM E260—85,
Standard Practice for Packed Column Gas
Chromatography, approved June 28,
1985.
GPO.
Available from the Superintendent of Documents, U.S.
Government Printing Office,
Washington,
D.C.
20401,
(202)
783—3238:
Standard Industrial Classification Manual
(1972),
and
1977 Supplement, republished in 1983
117—34 7

28
NACE.
Available from the National Association of Corrosion
Engineers,
1400 South Creek Dr., Houston,
TX
77084,
(713)
492—0535:
“Control of External Corrosion on Metallic Buried,
Partially Buried,
or Submerged Liquid Storage
Systems”, NACE Recommended Practice RP0285-85,
approved March,
1985.
NFPA.
Available from the National Fire Protection
Association, Batterymarch Park, Boston, MA
02269,
(617)
770—3000 or
(800)
344—3555:
“Flammable and Combustible Liquids Code” NFPA 30,
issued July 17,
1987.
Also available from ANSI.
NTIS.
Available from the National Technical Information
Service,
5285 Port Royal Road,
Springfield, VA
22161,
(703)
487—4600:
“Generic Quality Assurance Project Plan for Land
Disposal Restrictjons Program”, EPA/530—SW—87—011,
March
15,
1987.
(Document
number
PB
88—170766.j
“Methods for Chemical Analysis of Water and Wastes”,
Third Edition, March,
1983.
(Document number PB 84—
128677)
“Petitions to Delist Hazardous Wastes
——
A Guidance
Manual”,
EPA/530—SW—85—003,
April,
1985.
(Document
Number PB 85—194488
“Procedures Manual for Ground Water Monitoring at
Solid Waste Disposal Facilities”, EPA—530/SW—6ll,
1977.
(Document number PB 84—174820)
“Test Methods for Evaluating Solid Waste,
Physical/Chemical Methods,” EPA Publication number SW-
846 (Second Edition, 1982 as amended by Update
I
(April,
1984)
and Update
II
(April,
1985))
(Document
number PB 87-120291)
STI.
Available from the Steel Tank Institute, 728 Anthony
Trail, Northbrook,
IL
60062,
(312)
498—1980:
“Standard for Dual Wall Underground Steel Storage
Tanks”
(1986).
USEPA.
Available from United States Environmental
Protection Agency,
Office of Drinking Water,
State Programs
Division,
WH 550
E, Washington,
D.C.
20460:
117—348

29
“Technical Assistance Document:
Corrosion,
Its
Detection and Control
in Injection Wells”,
EPA 570/9-
87—002, August,
1987.
b)
Code of
Federal Regulations.
Available from the Superintendent of
Documents,
U.S. Government Printing Office, Washington,
D.C.
20401,
(202)
783—3238:
10 CFR 20, Appendix B ~1089)(19901
40 CFR 60
(1990)
40 CFR 61, Subpart V
(19901
40 CFR 136 (1080)(1990)
40 CFR 142
(1989)(l990)
40 CFR 220
(1080)119901
40 CFR 260.20 (1989)11990)
40 CFR 264
.(l989) (1990)
40 CFR 302.4,
302.5 and 302.6 (1989)(1990)
40 CFR 761
(1089)(19901
C)
Federal Statutes
Section 3004 of the Resource Conservation and Recovery Act
(42
U.S.C.
6901 et seq.),
as amended through December 31,
1987.
d)
This Section incorporates no later editions or amendments.
(Source:
Amended at
15
Ill. Reg.
,
effective
117—349

30
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER
I:
POLLUTION CONTROL
BOARD
SUBCHAPTER
C:
HAZARDOUS
WASTE
OPERATING
REQUIREMENTS
PART
721
IDENTIFICATION AND LISTING OF
HAZARDOUS
WASTE
SUBPART A:
GENERAL
PROVISIONS
Purpose of Scope
Definition of Solid Waste
Definition of Hazardous Waste
Exclusions
Special Requirements for Hazardous Waste Generated by Small
Quantity Generators
Requirements for Recyclable Materials
Residues of Hazardous Waste in Empty Containers
PCB Wastes Regulated under TSCA
SUPBART
B:
CRITERIA FOR IDENTIFYING
THE CHARACTERISTICS
OF
HAZARDOUS
WASTE AND FOR LISTING HAZARDOUS WASTES
Criteria for Identifying the Characteristics of Hazardous Waste
Criteria for Listing Hazardous Waste
SUBPART C:
CHARACTERISTICS OF HAZARDOUS WASTE
SUBPART
D:
LISTS OF
HAZARDOUS
WASTE
General
Hazardous Wastes From Nonspecific Sources
Hazardous Waste from Specific Sources
Discarded Commercial Chemical Products, Off—Specification Species,
Container Residues and Spill Residues Thereof
Appendix A
Appendix B
Appendix C
Table A
Table B
Table
C
Appendix G
Appendix
H
Appendix
I
Table
A
Representative Sampling Methods
Method 1311 Toxicity Characteristic Leaching Procedure (TCLP)
Chemical Analysis Test Methods
Analytical Characteristics of Organic Chemicals
(Repealed)
Analytical Characteristics of Inorganic Species
(Repealed)
Sample Preparation/Sample Introduction Techniques
(Repealed)
Basis for Listing Hazardous Wastes
Hazardous Constituents
Wastes Excluded under Section 720.120 and 720.122
Wastes Excluded from Non—Specific Sources
Sect ion
721. 101
721.102
721.103
721.104
721. 105
721. 106
721. 107
721.108
Section
721.110
721.111
Section
721. 120
721.121
721. 122
721.123
721.
124
Section
721.130
721.131
721.132
721.133
General
Characteristic of Ignitability
Characteristic of Corrosivity
Characteristic of Reactivity
Toxicity Characteristic
117—350

31
Table
B
Wastes Excluded from Specific Sources
Table C
Wastes Excluded From Commercial Chemical Products,
Off—
Specification Species,
Container Residues,
and Soil Residues
Thereof
Appendix
J
Method of Analysis for Chlorinated Dibenzo—p—Dioxins and
Dibenzofurans
Appendix
Z
Table to Section 721.102
AUTHORITY:
Implementing Section 22.4 and authorized by Section 27 of the
Environmental Protection Act
(Ill.
Rev. Stat.
1989,
ch.
111 1/2, pars.
1022.4
and 1027).
SOURCE:
Adopted in R81—22, 43 PCB 427, at
5 Ill. Reg. 9781,
effective as
noted
in
35
Ill.
Mm.
Code
700.106; amended and codified in R81—22,
45 PCB
317,
at
6
Ill.
Reg.
4828,
effective
as
noted
in
35
Ill.
Mrs.
Code
700.106;
amended
in R82—18,
51 PCB 31, at
7
Ill. Reg. 2518,
effective February 22,
1983;
amended
in
R82—19,
53
PCB
131,
at
7
Ill.
Reg.
13999,
effective
October
12,
1983; amended in R84—34,
61 PCB 247, at
8 Ill.
Reg.
24562, effective
December
11,
1984;
amended
in
R84—9,
at
9
Ill.
Reg.
11834,
effective
July
24,
1985;
amended
in
R85—22
at
10
Ill.
Reg.
998,
effective
January
2,
1986;
amended
in R85—2 at 10 Ill. Reg. 8112,
effective May 2, 1986;
amended in R86—
1 at
10 Ill.
Reg.
14002, effective August
12,
1986;
amended in R86—19 at 10
Ill.
Reg. 20647, effective December
2,
1986;
amended in R86—28 at
11
Ill.
Reg.
6035,
effective March 24,
1987;
amended in R86—46 at 11 111. Reg.
13466,
effective
August
4,
1987;
amended
in
R87—32
at
11
Ill.
Reg.
16698,
effective
September 30,
1987; amended in R87—5 at
11 Ill. Reg. 19303,
effective November
12,
1987; amended in R87—26 at 12
Ill.
Reg.
2456, effective January
15, 1988;
amended
in R87—30
at
12
Ill.
Reg. 12070,
effective July 12,
1988;
amended in
R87—39 at
12
Ill.
Reg.
13006, effective July 29,
1988; amended in R88—l6 at
13
Ill. Reg.
382, effective December 27,
1988;
amended in R89—.
at 13
Ill. Reg.
18300, effective November 13,
1989;
amended in R90—2 at 14 Ill. Reg.
14401,
effective August 22,
1990;
amended in R90—10 at 14 Ill. Reg.
16472, effective
September 25,
1990;
amended in R90—17 at 14
Ill. Reg.
,
effective
amended in R90—11 at
15
Ill. Reg.
,
effective
SUBPART
A:
GENERAL PROVISIONS
Section 721.104
Exclusions
a)
Materials which are not solid wastes.
The following materials are
not solid wastes for the purpose of this Part:
1)
Sewage:
A)
Domestic sewage; and
B)
Any mixture of domestic sewage and other waste that
passes through
a sewer system to publicly—owned
treatment works for treatment.
“Domestic sewage”
means untreated sanitary wastes that pass through a
sewer
system.
117—35 1

32
2)
Industrial wastewater discharges that are point source
discharges with NPDES permits issued by the Agency pursuant
to Section 12(f)
of the Environmental Protection Act and 35
Ill.
Adm.
Code 309.
BOARD
NOTE:
This exclusion applies only to the actual
point
source discharge.
It does not exclude industrial
wastewaters while they are
being
collected,
stored or
treated before discharge, nor does it exclude sludges that
are generated by industrial wastewater treatment.
3)
Irrigation return flows.
4)
Source,
special nuclear or by—product material as defined by
the Atomic Energy Act of
1954, as amended
(42 U.S.C. 2011 et
seq.)
5)
Materials subjected to in—situ mining techniques which are
not removed from the ground as part of the extraction
process.
6)
Pulping liquors
(i.e., black liquor) that are reclaimed in a
pulping liquor recovery furnace and then reused
in the
pulping process,
unless accumulated speculatively as defined
in Section 721.101(c);
7)
Spent sulfuric acid used to produce virgin sulfuric acid,
unless
it
is accumulated speculatively as defined in Section
721.101(c).
8)
Secondary materials that are reclaimed and returned to the
original process or processes in which they were generated
where they are reused in the production process,
provided:
A)
Only tank storage is involved,
and the entire process
through completion of reclamation is closed by being
entirely connected with pipes or other comparable
enclosed means of conveyance;
B)
Reclamation does not involve controlled flame
combustion (such as occurs in boilers,
industrial
furnaces or incinerators);
C)
The Becondary materials are never accumulated in auch
tanks for over twelve months without being reclaimed;
and
D)
The reclaimed material
is not used to produce a fuel,
or used to produce products that are used in a manner
constituting disposal.
117—352

33
b)
Solid wastes which are not hazardous wastes.
The following solid
wastes are not hazardous wastes:
1)
Household waste,
including household waste that has been
collected,
transported,
stored,
treated,
disposed,
recovered
(e.g., refuse—derived fuel)
or reused.
“Household waste”
means any waste material (including garbage, trash and
sanitary wastes in septic tanks) derived from households
(including single and multiple residences, hotels and
motels,
bunkhouses, ranger stations,
crew quarters,
campgrounds,
picnic
grounds
and
day-use
recreation
areas).
A resource recovery facility managing municipal solid waste
shall not be deemed to be treating, storing, disposing of or
otherwise managing hazardous wastes for the purposes of
regulation under this Part,
if such facility:
A)
Receives and burns only:
i)
Household waste (from single and multiple
dwellings, hotels, motels and other residential
sources) and
ii)
Solid
waste
from
commercial
or
industrial
sources that does not contain hazardous waste;
and
B)
Such facility does not accept hazardous waste and the
owner or operator of such facility has established
contractural requirements or other appropriate
notification or inspection procedures to assure that
hazardous wastes are not received at or burned in such
facility.
2)
Solid wastes generated by any of the following and which are
returned
to
the
soil
as
fertilizers:
A)
The growing and harvesting of agricultural crops.
B)
The raising of animals, including animal manures.
3)
Mining overburden returned to the mine site.
4)
Fly ash waste,
bottom ash waste,
slag waste, and flue gas
emission control waste generated primarily from the
combustion of coal or other fossil fuels.
5)
Drilling fluids, produced waters, and other wastes
associated with the exploration, development,
or production
of crude oil, natural gas or geothermal
energy.
6)
Chromium wastes:
117—353

34
A)
Wastes which fail the test for the toxicity
characteristic (Section 721.124 and Appendix B)
because chromium is present or are listed in Subpart
D
due to the presence of chromium, which do not fail the
test for the toxicity characteristic for any other
constituent
or
are
not
listed
due to the presence of
any other constituent, and which do not fail the test
for any other characteristic,
if
it is shown by a
waste generator or by waste generators that:
i)
The chromium in the waste
is exclusively
(or
nearly exclusively) trivalent chromium; and
ii)
The waste is generated from an industrial
process which uses trivalent chromium
exclusively (or nearly exclusively) and the
process
does
not
generate
hexavalent
chromium;
and
iii)
The waste
is typically and frequently managed in
non—oxidizing environments.
B)
Specific
wastes
w1~ichmeet
the
standard
in
subsections
(b)(6)(A)(i),
(ii)
and
(iii)
(so long as they do not
fail the test for the characteristic of EP toxicity,
and do not fail the test for any other characteristic)
are
i)
Chrome
(blue) trimmings generated by the
following subcategories of the leather tanning
and finishing industry; hair pulp/chrome
tan/retan/wet finish;
hair save/chrome
tan/retan/wet finish;
retan/wet finish;
no
beaxnhouse; through—the-blue; and shearling.
ii)
Chrome
(blue)
shavings generated by the
following subcategories of the leather tanning
and finishing industry; hair pulp/chrome
tan/retan/wet finish;
hair gave/chrome
tan/retan/wet finish; retan/wet finish;
no
beamhouse; through-the-blue;
and ahearling.
iii)
Buffing dust generated by the following
subcategories of the leather tanning and
finishing industry:
hair pulp/chrome
tan/retan/wet finish; hair save/chrome
tan/retan/wet
finish; retan/wet finish; no
beamhouse; through-the-blue.
iv)
Sewer screenings generated
by
the
following
subcategories of the leather tanning and
finishing industry:
hair pulp/chrome
117—354

35
tan/retan/wet finish; hair save/chrome
tan/retan/wet finish; retan/wet finish;
no
beamhouge;
through-the-blue;
and
shearling.
v)
Wastewater treatment sludges generated by the
following subcategories of the leather tanning
and finishing industry:
hair pulp/chrome
tan/retan/wet finish; hair save/chrome
tan/retan/wet finish; retan/wet finish;
no
beamhouse; through—the—blue;
and shearling.
vi)
Wastewater treatment sludges generated by the
following subcategories of the leather tanning
and finishing industry:
hair pulp/chrome
tan/retan/wet finish; hair save/chrome
tan/retan/wet finish; and through—the-blue.
vii)
Waste
scrap
leather
from the leather tanning
industry, the shoe manufacturing industry, and
other leather product manufacturing industries.
viii) Wastewater treatment sludges
from
the
production
of titanium dioxide pigment using chromium-
bearing ores by the chloride process.
7)
Solid waste from the extraction, beneficiation and
processing of ores and minerals
(including coal),
including
phosphate rock and overburden from the mining of uranium
ore.
For purposes of
this
subsection, beneficiation of ores
and minerals
is restricted to the following activities:
crushing,
grinding,
washing,
dissolution,
crystallization,
filtration,
sorting, sizing,
drying,
aintering,
pelletizing,
briquetting, calcining to remove water or carbon dioxide,
roasting,
autoclaving or chlorination in preparation for
leaching
(except where the roasting or autoclaving or
chlorination)/leaching sequence produces a final or
intermediate product that does not undergo further
beneficiation
or
processing),
gravity
concentration,
magnetic separation, electrostatic separation, floatation,
ion exchange,
solvent extraction, electrowinning,
precipitation,
amalgamation,
and heap,
dump, vat Stank and in
situ leaching.
•For the purposes of this subsection,
solid
waste from the processing of ores and minerals will include
only
the
following wastes:
A)
Slag
from
primary
copper
processing;
B)
Slag from primary lead processing;
C)
Red and brown muds from bauxite refining;
D)
Phosphogypsum from phosphoric acid production;
117—355

36
E)
Slag from elemental phosphorus production;
F)
Gasifier ash from coal gasification;
G)
Process wastewater from coal gasification;
H)
Calcium sulfate wastewater treatment plant sludge from
primary copper processing;
I)
Slag tailings from primary copper processing;
J)
Fluorogypsum from hydrofluoric acid production;
K)
Process wastewater from hydrofluoric acid production;
L)
Air pollution control dust/sludge from iron blast
furnaces;
M)
Iron blast furnace slag;
N)
Treated residue from roasting/leaching of chrome ore;
0)
Process wastewater from primary magnesium processing
by the anhydrous process;
P)
Process wastewater from phosphoric acid production;
Q)
Basic oxygen furnace and open hearth furnace air
pollution control dust/sludge from carbon steel
production;
R)
Basic oxygen furnace and open hearth furnace slag from
carbon steel production;
5)
Chloride processing waste solids from titanium
tetrachloride production;
T)
Slag from primary zinc smelting;
and,
U)
Until June 30,
1991,
process wastewater, acid plant
blowdown
and
wastewater
treatment
plant
solids
from
primary zinc smelting and refining, except for
wastewater treatment plant solids which are hazardous
by characteristic and which are not processed.
8)
Cement kiln dust waste.
9)
Solid
waste
which
consists
of
discarded
wood
or
wood
products
which
fails
the
test
for
the
toxicity
characteristic solely
for arsenic and which is not
a
hazardous
waste
for
any
other
reason
or
reasons
if
the
waste
117—356

37
is
generated
by
persons
who
utilize
the
arsenical—treated
wood and wood products for these materials’
intended and
use.
10)
Petroleum-contaminated media and debris that fail the test
for
the
toxicity
characteristic
of
Section
721.124
(hazardous waste codes D018 throuah D043 only) and are
subject to corrective action regulations under 35
Ill.
Adm.
Code 731.
c)
Hazardous wastes which are exempted from certain regulations.
A
hazardous waste which is generated in a product or raw material
storage tank,
a product or raw material
transport
vehicle or
vessel,
a product or raw material pipeline,
or in a manufacturing
process unit or an associated non—waste—treatment manufacturing
unit,
is
not
subject
to
regulation
under
35
Ill.
Adxn.
Code 702,
703,
705
and
722 through 725 and 728 or to the notification
requirements of Section 3010 of RCRA until
it exits the unit in
which
it was generated, unless the unit is
a surface impoundment,
or
unless
the
hazardous waste remains in the unit more than 90
days after the unit ceases to be operated for manufacturing, or
for
storage
or
transportation
of
product
or
raw
materials.
d)
Samples
1)
Except
as provided in subsection
(d)(2),
a sample of solid
waste or a sample of water,
soil or air, which is collected
for the sole purpose of testing to determine its
characteristics or composition,
is not subject to any
requirements of this Part or
35
Ill.
Adm.
Code 702,
703, 705
and
722 through 728.
The sample qualifies when:
A)
The sample is being transported to a laboratory for
the
purpose
of
testing;
or
B)
The
sample
is
being transported back to the sample
collector
after testing;
or
C)
The
sample
is
being
stored
by
the
sample
collector
before transport to
a laboratory for testing; or
D)
The sample
is being stored in a laboratory before
testing;
or
E)
The sample is being stored in a laboratory for testing
but before
it
is returned to the sample collector;
or
F)
The sample is being stored temporarily in the
laboratory
after
testing
for
a specific purpose (for
example,
until conclusion of a court case or
enforcement
action
where
further testing of the sample
may
be
necessary).
117—357

38
2)
In order to qualify for the exemption in subsection
(d)(l)(A) and
(B),
a sample collector shipping samples to a
laboratory and
a laboratory returning samples to a sample
collector must:
A)
Comply with U.S. Department of Transportation (DOT),
U.S.
Postal Service (USPS) or any other applicable
shipping requirements;
or
B)
Comply with the following requirements if the sample
collector determines that DOT, USPS or other shipping
requirements do not apply to the shipment of the
sample:
i)
Assure that the following information
accompanies the sample:
The sample collector’s
name,
mailing address and telephone number;
the
laboratory’s name, mailing address and telephone
number;
the
quantity
of
the
sample;
the
date
of
the shipment; and a description of the sample.
ii)
Package the sample so that it does not leak,
spill or vaporize from its packaging.
3)
This exemption does not apply
if the laboratory determines
that the waste is hazardous but the laboratory is no longer
meeting any
of the conditions stated in subsection (d)(1).
e)
Treatability study samples.
1)
Except as is provided in subsection
(e)(2), persons who
generate or collect samples for the purpose of conducting
treatability studies,
as defined in 35
Ill.
Adm.
Code
720.110,
are
not
subject
to
any requirement of 35
Ill.
Adm.
Code 721 through 723 or to the notification requirements of
Section 3010 of the Resource Conservation and Recovery Act.
Nor are such samples included in the quantity determinations
of Section 721.105 and
35
Ill.
Mm.
Code
722.134(d)
when:
A)
The sample is being collected and prepared for
transportation by the generator or sample collector;
or,
B)
The sample
is being accumulated or stored by the
generator or sample collector prior to transportation
to a laboratory or testing facility;
or
C)
The sample
is being transported to the laboratory or
testing facility for the purpose of conducting a
treatability study.
117—358

39
2)
The exemption in subsection
(e)(1)
is applicable to samples
of hazardous waste being collected and shipped for the
purpose of conducing treatability studies provided that:
A)
The generator or sample collector uses
(in
“treatability studies”)
no more than 1000 kg of any
non—acute hazardous waste,
1 kg of acute hazardous
waste or 250 kg of soils, water or debris contaminated
with acute hazardous waste for each process being
evaluated for each generated wastestream; and
B)
The mass of each shipment does not exceed 1000 kg of
non—acute hazardous waste,
1 kg of acute hazardous
waste or 250 kg of soils, water or debris contaminated
with acute hazardous waste; and
C)
The sample must be packaged so that
it
does
not
leak,
spill or vaporize from its packaging during shipment
and the requirements of subsections
(i)
or
(ii)
are
met.
i)
The transportation of each sample shipment
complies
with
U.S.
Department
of
Transportation
(DOT),
U.S.
Postal Service (USPS) or any other
applicable shipping requirements;
or
ii)
If the DOT,
USPS or other shipping requirements
do not apply to the shipment of the sample,
the
following information must accompany the sample:
The name,
mailing address and telephone number
of the originator of the sample; the name,
address and telephone number of the facility
that will perform the treatability study; the
quantity of the sample; the date of the
shipment;
and,
a
description
of
the
sample,
including
its
USEPA hazardous waste number.
D)
The sample
is shipped to a laboratory or testing
facility which is exempt under
subsection
(f)
or has
an appropriate
RCRA
permit or interim status.
E)
The generator or sample collector maintains the
following records
for a period ending
3 years after
completion of the treatability study:
i)
Copies of the shipping documents;
ii)
A copy of the contract with the facility
conducting the treatability study;
iii)
Documentation showing:
The amount of waste
shipped under this exemption; the name,
address
117—359

40
and USEPA identification number of the
laboratory or testing facility that received the
waste; the date the shipment was made;
and,
whether or not unused samples and residues were
returned to the generator.
F)
The generator reports the information required in
subsection
(e)(2)(E)(iii)
in
itB
report under 35 Ill.
Adm. Code 722.141.
3)
The Agency may grant requests, on a case—by—case basis,
for
quantity limits
in excess of those specified in subsection
(e)(2)(A),
for up to an additional
500 kg of any non-acute
hazardous waste,
1 kg of acute hazardous waste and 250 kg of
soils, water or debris contaminated with acute hazardous
waste,
to conduct further treatability study evaluation
when:
-
There has been an equipment or mechanical failure
during the conduct of the treatability study;
there is need
to verify the results of a previously conducted treatability
study; there
is
a need to study and analyze alternative
techniques within a previously evaluated treatment process;
or, there is
a need to do further evaluation of an ongoing
treatability study to determine final specifications for
treatment.
The additional quantities allowed are subject to
all the provisions in subsections
(e)(1) and (e)(2)(B)
through
(F).
The generator or sample collector must apply
to the Agency and provide in writing the following
information:
A)
The reason why the generator or sample collector
requires additional quantity of sample for the
treatability study evaluation and the additional
quantity needed;
B)
Documentation accounting for all samples of hazardous
waste from the wastestrearn which have been sent for or
undergone treatability studies, including the date
each previous sample was shipped, the quantity of each
previous shipment,
the laboratory or testing facility
to which it was shipped, what treatability study
processes were conducted on each sample shipped,
and
the available results of each treatability study;
C)
A description of the technical modifications or change
in specifications which will be evaluated and the
expected results;
D)
If such further study is being required due to
equipment or mechanical failure, the applicant must
include information regarding the reason for the
failure or breakdown and also include what procedures
117—360

41
or equipment have been made to protect against further
breakdowns; and,
E)
Such other information as the Agency determines is
necessary.
4)
Final Agency determinations pursuant to this subsection may
be appealed to the Board.
f)
Samples undergoing treatability studies at laboratories or testing
facilities.
Samples undergoing treatability studies and the
laboratory or testing facility conducting such treatability
studies
(to the extent such facilities are not otherwise subject
to
RCRA
requirements)
are not subject to any requirement of this
Part,
or of 35
Ill. Adm. Code 702,
703,
705,
722 through 726,
and
728,
or to the notification requirements of Section 3010 of the
Resource Conservation and Recovery Act, provided that the
requirements of subsections
(f)(1) through (f)(11)
are met.
A
mobile treatment unit may qualify as a testing facility subject to
subsections
(f)(l) through (f)(11).
Where a group of mobile
treatment units are located at the same site,
the limitations
specified in subsections
(f)(1) through
(f)(11)
apply to the
entire group of mobile treatment units collectively as
if the
group were one mobile treatment unit.
1)
No less than 45 days before conducting treatability studies,
the facility notifies the Agency in writing that it intends
to conduct treatability studies under this subsection.
2)
The laboratory or testing facility conducting the
treatability study has
a USEPA identification number.
3)
No more than a total of 250 kg of “as received” hazardous
waste is subjected to initiation of treatability studies
in
any single day.
“As received” waste refers to the waste as
received
in the shipment from the generator or sample
collector.
4)
The quantity of “as received” hazardous waste stored at the
facility for the purpose of evaluation in treatability
studies does not exceed 1000 kg, the total of which can
include 500 kg of soils, water or debris contaminated with
acute hazardous waste or
1 kg of acute hazardous waste.
This quantity limitation does not include:
A)
Treatability study residues; and,
B)
Treatment materials
(including nonhazardous solid
waste)
added to
“as received” hazardous waste.
5)
No more than 90 days have elapsed since the treatability
study
for the sample was completed,
or no more than one year
117—361

42
has elapsed since the generator or sample collector shipped
the sample to the laboratory or testing facility, whichever
date first occurs.
6)
The treatability study does not involve the placement of
hazardous waste on the land or open burning of hazardous
waste.
7)
The facility maintains records for 3 years following
completion of each study that show compliance with the
treatment rate limits and the storage time and quantity
limits.
The following specific information mua be included
for each treatability study conducted:
A)
The name,
address and USEPA identification umber of
the generator or sample collector of each waste
sample;
B)
The date the shipment was received;
C)
The quantity of waste accepted;
D)
The quantity of “as received” waste in storage each
day;
E)
The date the treatment study was initiated and the
amount of “as received” waste introduced to treatment
each day;
F)
The date the treatability study was concluded;
G)
The date any unused sample or residues generated from
the treatability study were returned to the generator
or sample collector or,
if sent to a designated
facility, the name of the facility and the USEPA
identification number.
8)
The facility keeps,
on-site,
a copy of the treatability
study contract and all shipping papers associated with the
transport of treatability study samples to and from the
facility for a period ending
3 years from the completion
date of each treatability study.
9)
The facility prepares and submits
a report to the Agency by
March 15 of each year that estimates the number of studies
and the amount of waste expected to be used in treatability
studies during the current year,
and includes the following
information for the previous calendar year:
A)
The name,
address and USEPA identification number of
the facility conducting the treatability studies;
117—36 2

43
B)
The types
(by process)
of treatability studies
conducted;
C)
The names and addresses of persons for whom studies
have been conducted (including their USEPA
identification numbers);
D)
The total quantity of waste in storage each day;
E)
The quantity and types of waste subjected to
treatability studies;
F)
When each treatability study was conducted;
G)
The final disposition of residues and unused sample
from each treatability study;
10)
The facility determines whether any unused sample or
residues generated by the treatability study are hazardous
waste under Section 721.103 and,
if
so,
are subject to 35
Ill. Mm.
Code 702,
703 and 721 through 728, unless the
residues and unused samples are returned to the sample
originator under the subsection
(e)
exemption.
11)
The facility notifies the Agency by letter when the facility
is no longer planning to conduct any treatability studies at
the site.
(Source:
Amended at
15 Ill. Reg.
,
effective
)
Section 721.106
Requirements for Recyclable Materials
a)
Recyclable materials:
1)
Hazardous wastes that are recycled are subject to the
requirements for generators, transporters and storage
facilities of subsections
(b) and
(c), except for the
materials listed in subsections
(a)(2) and (a)(3).
Hazardous wastes that are recycled will be known as
“recyclable materials”.
2)
The following recyclable materials are not subject to the
requirements of this Section but are regulated under 35
Ill.
Adm. Code 726.Subparts C through G and all applicable
provisions in 35 Ill. Adm. Code 702,
703 and 705.
A)
Recyclable materials used in a manner constituting
disposal
(35 Ill. Adm.
Code 726.Subpart C);
B)
Hazardous wastes burned
for energy recovery in boilers
and industrial furnaces that are not regulated under
117—363

44
35
Ill. Adm. Code 724 or 725.Subpart 0
(35 Ill. Adm.
Code 726.Subpart D.)
C)
Used oil that exhibits one or more of the
characteristics of hazardous waste and is burned for
energy recovery in boilers or industrial furnaces that
are not regulated under 35
Ill.
Adrn.
Code 724 or
725.Subpart 0.
(35 Ill. Adm. Code 726.Subpart
E);
D)
Recyclable materials from which precious metals are
reclaimed
(35 Ill. Mm. Code 726.Subpart F);
E)
Spent lead-acid batteries that are being reclaimed
(35
Ill. Adm.
Code 726.Subpart G).
3)
The following recyclable materials are not subject to
regulation under 35 Ill. Adm. Code 722 through 726, 728, or
702,
703 or 705 and are not subject to the notification
requirements of Section
3010 of the Resource Conservation
and Recovery Act:
A)
Industrial ethyl alcohol that
is reclaimed except
that,
unless provided otherwise in an international
agreement as specified
in
35
Ill.
Adxn.
Code 722.158:
i)
A person initiating
a shipment for reclamation
in a foreign country, and any intermediary
arranging for the shipment, shall comply with
the requirements applicable to a primary
exporter in
35
Ill.
Adm. Code 722.153,
722.156(a)(1)
through (a)(4),
(a)(6) and
(b),
and 722.157,
shall export such materials only
upon consent of the receiving country and in
conformance with the USEPA Acknowledgement of
Consent as defined in
35 Ill. Adm. Code
722.Subpart
E,
and shall provide a copy of the
USEPA Acknowledgement of Consent to the shipment
to the transporter transporting the shipment for
export;
ii)
Transporters transporting a shipment
for export
shall not accept a shipment if the transporter
knows the shipment does not conform to the USEPA
Acknowledgement of Consent, shall ensure that
a
copy of the USEPA Acknowledgement of Consent
accompanies the shipment and shall ensure that
it is delivered to the facility designated by
the person initiating the shipment.
B)
Used batteries
(or used battery cells) returned to
a
battery manufacturer for regeneration;
117—364

45
C)
Used oil that exhibits one or more of the
characteristics of hazardous waste but is recycled in
some other manner than being burned for energy
recovery;
D)
Scrap metal;
E)
Fuels produced from the refining of oil—bearing
hazardous wastes along with normal process streams at
a petroleum refining facility if such wastes result
from normal petroleum refining,
production and
transportation practices;
F)
Oil reclaimed from hazardous waste resulting from
normal petroluem refining, production and
transportation practices, which oil
is to be refined
along with normal process streams at a petroleum
refining facility;
G)
Coke and coal tar from the iron and steel industry
that contains USEPA hazardous waste number K087
(decanter tank tar sludge from coking operations)
(Section 721.132) from the ironand steel production
process;
H)
Petroleum refining wastes.
i)
Hazardous waste fuel produced from oil—bearing
hazardous wastes from petroleum refining,
production or transportation practices,
or
produced from oil reclaimed from such hazardous
wastes, where such hazardous wastes are
reintroduced into
a process that does not use
distillation or does not produce products from
crude oil so long as the resulting fuel meets
the used oil specification under 35 Ill. Ada.
Code 726.140(e) and so long as no other
hazardous wastes are used to produce the
hazardous waste fuel;
ii)
Hazardous waste fuel produced from oil—bearing
hazardous waste from petroleum refining
production and transportation practices, where
such hazardous wastes are reintroduced into a
refining process after a point at which
contaminants are removed, so long as the fuel
meets the used oil fuel specification under 35
Ill. Ada. Code 726.140(e); and
iii)
Oil reclaimed from oil-bearing hazardous wastes
from petroleum refining, production and
transportation practices, which reclaimed oil
is
117—365

46
burned as a fuel without reintroduction to a
refining process,
so long as the reclaimed oil
meets the used oil fuel specification under 35
Ill.
Ada. Code 726.140(e); and
I)
Petroleum coke produced from petroleum refinery
hazardous wastes containing oil at the same facility
at which such wastes were generated, unless the
resulting coke product exceeds one or more of the
characteristics of hazardous waste in Subpart C.
b)
Generators and transporters of recyclable materials are subject to
the applicable requirements of
35 Ill. Ada. Code 722 and 723 and
the notification requirements under Section 3010 of the Resource
Conservation and Recovery Act, except as provided in subsection
(a).
c)
Storage and recycling:
1)
Owners or operators of facilities that store recyclable
materials before they are recycled are regulated under all
applicable provisions of 35
Ill. Ada.
Code 724.Subparta A
through L, AA and BB and 725.Subparts A through L,
AA and
~,
726, 728,
702,
703 and 705 and the notification
requirement under Section 3010 of the Resource Conservation
and Recovery Act, except as provided in subsection
(a).
(The recycling process itself is exempt from regu.ation~.
except
as provided
in subsection
(d).)
2)
Owners or operators of facilities that recycle recyclable
materials without storing them before they are recycled are
subject to the following requirements, except as provided in
subsection
(a).
A)
Notification requirements under Section 3010 of the
Resource Conservation and Recovery Act.
B)
35
Ill. Ada.
Code 725.171 and 725.172
(dealing with
the use of the manifest and manifest discrepancies)
Q~.
Subsection
(dl.
~j
Owners or operators of
facilities reguired to have a RCRA permit
pursuant to
35
Ill. Ada.
Code 703 with hazardous waste management
units which recycle hazardous wastes are subject to 35
Ill. Ada.
Code 724.Subpart AA and BE and 725.Subpart AA and BB.
(Source:
Amended at
15 Ill. Reg.
,
effective
117—366

47
SUBPART B:
CRITERIA FOR IDENTIFYING THE CHARACTERISTICS OF
HAZARDOUS WASTE AND FOR LISTING HAZARDOUS WASTES
Section 721.111
Criteria for Listing Hazardous Waste
a)
UOErA’e criteria for listing hazardous waste are given at 40 CFR
Cectjon 261.11.
USEPA lists
a solid waste as
p
hazardous
waste
only upon determining that the solid waste meets one of the
following criteria:
jj.
It exhibits any of the characteristics of hazardous waste
identified
in Subpart
C;
or
b~
2.).
“P” list;
Acutc hazardous wastes are listtd in Ccction
721.133(c).
Acute hazardous wastes are those which have
been found to be fatal.
Acute toxic wastes are those which
haveAcute hazardous waste.
It
has been found to be fatal to
humans in low doses or,
in the absence of data on human
toxicity,
it has been shown in studies to have an oral LD
50
toxicity (rat) of less than 50 mg/kg,
an inhalation LC 50
toxicity
(rat)
of less than 2 mg/*~,or
a dermal LD
50
toxicity
(rabbit) of less than 200 mg/kg or is otherwise
capable of causing or significantly contributing to an
increase
in serious irreversible or incapacitating
reversible,
illness.
BOARD NOTE:
+Waste listed
in accordance with these criteria
will bt~ designated Acute Hazardous Waste-)-.
~j
Toxic waste.
It contains any of the toxic constituents
listed
in A~~endix
H unless,
after considering any of the
following factors, USEPA concludes that the waste
is capable
of posing a substantial present or potential hazard to human
he&ltl-i or the environment when improperly treated,
stored,
transported or disposed of,
or otherwise managed:
~j
The nature of the toxicity presented by the
constituent.
~j
The concentration of the constituent in the waste.
~j.
The potential of the constituent or any toxic
degradation product of the constituent to migrate from
the waste into the environment under the tvtea of
improper management considered
in subsection
(al (3) (G).
~J
The persistence of the constituent or any toxic
degradation product
of the constituent.
117—36 7

48
~j
The potential for the constituent
or any toxic
degradation product of the constituent to dearade into
nonharaful constituents and the rate of degradation.
fi
The degree to which the constituent or any degradation
product of the constituent bioaccumulates in
ecosystems.
~).
The plausible tv~esof improper management to which
the waste could be subjected.
!U
The guantities of the waste generated at individual
generation sites or on
p
regional or national basis.
fl
The nature and severity of the human health and
environmental
damage
that
has
occurred
as
a result of
the
improper management of the
wastes
containing
the
constituent.
Qj
Action taken by other governmental agencies or
regulatory programs based on the health or
environmental hazard posed by the waste or waste
constituent.
~j
Such
other
factors
as
may
be
appropriate.
BOARD
NOTE:
Wastes
listed
in
accordance
with
these
criteria
are
designated
toxic
wastes.
ii
Substances
are
listed
in
Appendix
H
only
if
they
have
been
shown in scientific studies to have toxic,
carcinogenic,
mutagenic or teratogenic effects on humans or other life
forms.
~j
USEPA may list classes or
types
of solid waste as hazardous waste
if USEPA has reason
to
believe
that
individual
wastes,
within
the
class or
type
of waste, typically or freguently are hazardous
under
the
definition
of
hazardous
waste
found
in
Section
1004(5)
of the Resource Conservation and Recovery Act
(42 USC 6901 et
seg.)
c)
UCEt’A’s criteria for
~i~tn,i
haziardous waste are t1(ven at 40
cm
Cection 261.ll.USEPA will use the criteria for listing specified
in
this
Section
to
establish
the
exclusion
limits
referred
to
in
Section 721.105(c~.
(Source:
Amended at 15 Ill. Reg.
,
effective
)
117—368

49
SUBPART C:
CHARACTERISTICS OF
HAZARDOUS
WASTE
Section 721.120
General
a)
A solid waste,
as defined
in Section 721.102, which is not
excluded from regulation as a hazardous waste under Section
721.104(b),
is
a hazardous waste if it exhibits any of the
characteristics identified in this Subpart.
(Board NoteiBOARD NOTE:
35
Ill.
Ada. Code 722.111 sets forth the
generator’s responsibility to determine whether the generator’s
waste exhibits one or more characteristics identified in this
Subpart.-)-
b)
A hazardous waste which
is identified by ~ characteristic in this
Subpart,
but
is not listed as a hatardous wacte in Cubpart D,
is
assigned t~eeveryUSEPA Hazardous Waste Number which
is applicable
as
set forth in the respective charactcrietic in this Subpart.
This number must be used in complying with the notification
requirements of Section 3010 of the Resource Conservation and
Recovery Act and certainall applicable recordkeeping and reporting
requirements under
35
Ill.
Ada. Code 702,
703, 722 through 725
and
728.
c)
For purposes of this Subpart,
a sample obtained using any of the
applicable sampling methods specified in Appendix A is
a
representative sample within the meaning of
35
Ill.
Ada. Code 720.
(Board Note;BOARD NOTE:
Since the Appendix A sampling methods are
not being formally adopted,
a person who desires to employ an
alternative sampling method is not required to demonstrate the
equivalency of the person’s method under the procedures set forth
in 35
Ill.
Ada. Code 720.121.1-
(Source:
Amended at
15 Ill. Reg.
,
effective
)
Section 721.121
Characteristic of Ignitability
a)
A solid waste exhibits the characteristic of ignitability if a
representative sample of the waste has any of the following
properties:
1)
It is a liquid, other than an aqueous solution containing
less than 24 percent alcohol by volume, and has
a flash
point less than 60°C(140°F),as determined by
a Pensky-
Martens Closed Cup Tester,
using the test method specified
in the American Doeiety of Testing Materials
(AOTM) Ctandar~
D
03
70 or
D 03 80
(incorporated by refercnce,
see
5720. l11)ASTM D—93,
incorporated by reference in 35
Ill.
Adm. Code 720.111,
or a Setaflash Closed Cup Tester, using
the test method specified in ASTM Standard D-32283278 78
(incorporated by reference,
see 5720.111),
incorporated by
117—369

50
reference in 35
Ill.
Ada.
Code 720.111,
or as determined by
an equivalent test method approved by the Board
(S~35 Ill.
Adm. Code 720.120).
2)
It
is not a liquid and is capable, under standard
temperature and pressure,
of causing fire through friction,
absorption of moisture or spontaneous chemical changes and,
when ignited, burns
so vigorously and persistently that it
creates a hazard.
3)
It
is an ignitable compre8sed gas as defined in 49 CFR
173.300, incorporated by reference in 35
Ill. Ada. Code
720.111,
and as determined by the test methods described in
that regulation or equivalent test methods approved by the
Board (~35Ill. Ada. Code 720.120).
4)
It
is an oxidizer as defined in 49 CFR 173.151, incorporated
by reference
in
35
Ill.
Ada. Code 720.111.
b)
A solid waste that exhibits the characteristic of ignitability-r
but
is not listed as a hazardous waste
in Subpart
D, has the EPA
Hazardous Waste Number of D001.
(Source:
Amended at
15
Ill.
Reg.
,
effective
Section 721.122
Characteristic of Corrosivity
a)
A solid waste exhibits the characteristic of corrosivity if a
representative sample of the waste has either of the following
properties:
1)
It
is aqueous and has a pH less than or equal to
2
or
greater than or equal to 12.5,
as determined by a pH meter
using either an EPA test method or an equivalent test method
(S~35 Ill. Ada.
Code 720.121).
The EPA test method for pH is
specified as Method 5.2
in “Teat Methods for the Evaluation
of Solid Waste, Physical/Chemical Methods” -(-it~eorpcratedby
reference,
eec 5720.111), incorporated by reference in 35
Ill. Ada. Code 720.111.
2)
It
is a liquid and corrodes steel
(SAE
1020) at a rate
greater than 6.35 mm (0.250 inch) per year at a test
temperature of 55°C(130°F)as determined by the test method
specified in NACE (National Association of Corrosion
Engineers) Standard TM—01—69 as standardized in “Test
Methods for the Evaluation of Solid Waste,
Physical/Chemical
Methods”
(incorporated by reference,
ccc 572O.lll)L.
incorporated by reference in 35
Ill. Ada. Code
720.13.1, or
an equivalent test method (~35Ill. Adm. Code 720.121).
117—370

51
b)
A solid waste that exhibits the characteristic of corrosivity
,-
but
is not listed as a hazardous waste in
Cubpart
B,
has the EPA
Hazardous Waste Number of D002.
(Source:
Amended at
15
Ill.
Reg.
,
effective
Section 721.123
Characteristic of Reactivity
a)
A solid waste exhibits the characteristic of reactivity
if
a
representative sample of the waste has any of the following
properties:
1)
It
is normally unstable and readily undergoes violent change
without detonating.
2)
It reacts violently with water.
3)
It forms potentially explosive mixtures with water.
4)
When mixed with water,
it generates toxic gases,
vapors or
fumes
in a quantity sufficient to present a danger to human
health or the environment.
5)
It
is
a cyanide or sulfide bearing waste which,
when exposed
to pH conditions between 2 and 12.5 can generate toxic
gases,
vapors or fumes in a quantity sufficient to present
a
danger to human health or the environment.
6)
It
is capable of detonation or explosive reaction
if
it
is
subjected to
a strong initiating source or
if heated under
confinement.
7)
It
is readily capable of detonation or explosive
decomposition or reaction at standard temperature and
pressure.
8)
It is a forbidden explosiveas defined in 49 CFR 173.51,
or
a Class A explosive as defined
in 49 CFR 173.53 or
a Class B
explosive as defined in 49 CFR 173.88,
incorporated by
reference in 35
Ill. Ada. Code 720.111.
b)
A solid waste that exhibits the characteristic of reactivity
,
but
io not listcd as a hazardous waste in Subpart
D, has the EPA
Hazardous Waste Number of D003.
(Source:
Amended at
15
Ill.
Reg.
,
effective
Section 721.124
Toxicity Characteristic
a)
A solid waste exhibits the characteristic of toxicity
if, using
the test methods described in Appendix B or equivalent methods
approved by the Agency under the procedures
set forth in Sections
117—37 1

52
720.120 and 720.121, the extract from a representative sample of
the waste contains any of the contaminants listed in the table in
subsection
(b)
at a concentration equal to or greater than the
respective value given in that table.
Where the waste contains
less than 0.5 percent filterable solids, the waste itaelf, after
filtering using the methodology outlined in Appendix B,
is
considered to be the extract for the purpose of this Section.
BOARD NOTE:
Generators are required to use the TCLP test
for the
hazardous waste determination under
35
Ill.
Ada. Code 722.120 as
of September 25, 1990.
Provided, however,
that, as specified at
55 Fed. Reg.
11850, March 29, 1990,
small quantity generators of
100 to 1000 kg! month,
as defined in 35
Ill. Ada. Code 721.105,
may continue to use the EP toxicity test until March 29,
1991.
The EP toxicity test is Method 1310 in SW 846,
“Test Methods for
Evaluating Solid Wastes, Physical/Chemical Methods”,
incorporated
by reference in
35
Ill. Ada. Code 720.111.
The reference to the
“EP toxicity test” in 35
Ill. Ada.
Code 808.410(b)(4)
is to be
understood as referencing the test required by this Section.
b)
A solid waste that exhibits the characteristic of toxicity,
but
is
not
listed as a hazardous waste in Cubpart D,
has the USEPA
Hazardous Waste Number specified in the following table which
corresponds to the toxic cont~.minantcausing it to be hazardous.
MAXIMUM CONCENTRATION OF CONTAMINANTS
FOR THE TOXICITY CHARACTERISTIC
USEPA
Hazardous
CAS
Regulatory
Waste No.
Contaminant
Number
Note
Level(mg/L)
D004
Arsenic
7440—38—2
5.0
DOOS
Barium
7440—39—3
100.0
D018
Benzene
71—43—2
0.5
D006
Cadmium
7440—43—9
1.0
D019
Carbon tetra-
56—23-5
0.5
chloride
D020
Chlordane
57—74—9
0.03
D021
Chlorobenzene
108—90-7
100.0
D022
Chloroform
67—66—3
6.0
D007
Chromium
7440—47—3
5.0
D023
o—Cresol
95—48—7
4
200.0
D024
m—Cresol
108—39—4
4
200.0
D025
p—Cresol
106-44—5
4
200.0
D026
Cresol
4
200.0
D0l6
2,4—D
94—75—7
10.0
D027
1,4—Dichioro—
106—46—7
7.5
benzene
D028
1,2—Dichloroethane
107—06—2
0.5
D029
1,l—Dichloro—
75—35—4
0.7
ethylene
117—372

53
D030
2,4-Dinitrotoluene
121—14—2
3
0.13
D012
Endrin
72—20—8
0.02
D031
Heptachior (and its
76—44—8
0.008
epoxide)
D032
Hexachlorobenzene
118—74—1
3
0.13
D033
Hexachlorobuta—
87—68—3
0.5
diene
0034
Hexachloroethane
67-72—1
3.0
0008
Lead
7439—92—1
5.0
0013
Lindane
58—89—9
0.4
D009
Mercury
7439—97—6
0.2
D0l4
Methoxychior
72—43—5
10.0
D035
Methyl ethyl ketone
78—93—3
200.0
D036
Nitrobenzene
98—95—3
2.0
D037
Pentachlorophenol
87—86—5
100.0
D038
Pyridine
110—86—1
3
5.0
DOlO
Selenium
7782—49—2
1.0
DOll
Silver
7440—22—4
5.0
D039
Tetrachloro—
127—18—4
0.7
ethylene
D015
Toxaphene
8001—35—2
0.5
D040
Trichioroethylene
79—01-6
0.5
D041
2,4,5—Trichloro—
95—95—4
400.0
phenol
D042
2,4,6—Trichloro—
88—06—2
2.0
phenol
D017
2,4,5—TP
(Silvex)
93—72—1
1.0
D043
Vinyl chloride
75—01—4
0.2
Notes to Table:
3
Quantitation limit is greater than the calculated regulatory
level.
The quantitation limit therefore becomes the
regulatory level.
4
If
o—, a—, p—cresol concentrations cannot be differentiated,
the total
creso.
(D026) concentration is used.
The
regulatory level of total
creso.
is 200.0 mg/L.
(Source:
Amended at
15
Ill.
Reg.
,
effective
SUBPART D:
LISTS OF HAZARDOUS WASTE
Section 721.131
Hazardous Wastes From Nonspecific Sources
The following solid wastes are listed hazardous wastes from non—specific
sources unless they are excluded under
35
Ill.
Ada. Code 720.120 and 720.122
and listed
in Appendix
I.
117—37 3

54
EPA
Hazardous
Hazard
Waste No.
Industry and Hazardous Waste
Code
FOOl
The following spent halogenated solvents used in
(T)
degreasing:
tetrachloroethylene, trichloroethylene,
methylene chloride,
1,1,1—trichloroethane, carbon
tetrachloride and chlorinated fluorocarbons;
all
spent solvent mixtures and blends used in degreasing
containing, before use,
a total of ten percent or
more
(by volume)
of one or more of the above
halogenated solvents or those solvents listed in
F002,
F004 or F005;
and still bottoms from the
recovery of these spent solvents and spent solvent
mixtures.
F002
The following spent halogenated solvents:
tetra—
(T)
chloroethylene, methylene chloride, trichloro—
ethylene,
1,1,1—trichloroethane,
chlorobenzene,
1, 1, 2-trichloro-1,2 ,2—trifluoroethane,
orthodichlorobenzene, trichlorofluoromethane and
l,1,2-trichloroethane; all spent solvent mixtures
and blends containing, before use,
a total of ten
percent or more (by volume) of one or more of the
above halogenated solvents or those solvents listed
in FOOl,
F004 or F005; and still bottoms from the
recovery of these spent solvents and spent solvent
mixtures.
F003
The following spent non—halogenated solvents:
(I)
xylene, acetone, ethyl acetate, ethyl benzene, ethyl
ether,
methyl isobutyl ketone,
n—butyl alcohol,
cyclohexanone and methanol;
all spent solvent
mixtures and blends containing, before use, only the
above spent non—halogenated solvents; and all spent
solvent mixtures and blends containing, before use,
one or more of the above non—halogenated solvents
and a total of ten percent or more
(by volume) of
one or more of those solvents listed in FOOl,
F002,
F004 or F005; and still bottoms from the recovery of
these spent solvents and spent solvent mixtures.
F004
The following spent non—halogenated solvents:
(T)
cresols and cresylic acid and nitrobenzene; all
spent solvent mixtures and blends containing, before
use,
a total of ten percent or more
(by volume)
of
one or more of the above non—halogenated solvents or
those solvents listed in FOOl,
F002 or F005; and
still bottoms from the recovery of these spent
solvents and spent solvent mixtures.
117—374

55
F005
The following spent non—halogenated solvents:
(I,
T)
toluene, methyl ethyl ketone,
carbon disulfide,
isobutanol,
pyridine, benzene, 2—ethoxyethanol and
2—nitropropane; all spent solvent mixtures and
blends,
containing, before use,
a total of ten
percent or more
(by volume)
of one or more of the
above non—halogenated solvents or those solvents
listed in FOOl,
F002 or P004;
and still bottoms from
the recovery of these spent solvents and spent
solvent mixtures.
F006
Wastewater treatment sludges from electroplating
(T)
operations except from the following processes:
(1)
sulfuric acid anodizing of aluminum;
(2) tin plating
on carbon steel;
(3)
zinc plating
(segregated basis)
on carbon steel;
(4) aluminum or zinc—aluminum
plating on carbon steel;
(5) cleaning/stripping
associated with tin,
zinc and aluminum plating on
carbon steel; and
(6)
chemical etching and milling
of aluminum.
F019
See Below
F007
Spent cyanide plating bath solutions from
(R,
T)
electroplating operations.
FOO8
Plating bath residues from the bottom of plating
(R,
T)
baths
from electroplating operations where cyanides
are used in the process.
F009
Spent stripping and cleaning bath solutions from
(R,
T)
electroplating operations where cyanides are used in
the process.
FOb
Quenching bath residues from oil baths from metal
(R,
T)
heat treating operations where cyanides are used in
the process.
FOll
Spent cyanide solutions from salt bath pot cleaning
(R,
T)
from metal heat treating operations.
F012
Quenching wastewater treatment sludges from metal
(T)
heat treating operations where cyanides are used in
the process.
F0l9
Wastewater treatment sludges from the chemical
(T)
conversion coating of aluminum except from zirconium
phosphating in aluminum can washing when such
phosphating
is
an exclusive conversion coating
process.
117—375

56
FO2O
Wastes (except wastewater and spent carbon from
(H)
hydrogen chloride purification)
from the production
or manufacturing use (as a reactant,
chemical
intermediate or component in a formulating process)
of tn— or tetrachlorophenol, or of intermediates
used to produce their pesticide derivatives.
(This
listing does not include wastes from the production
of hexachlorophene from highly purified 2,4,5-tn—
chlorophenol.)
F021
Wastes
(except wastewater and spent carbon from
(H)
hydrogen chloride purification)
from the production
or manufacturing use
(as a reactant,
chemical
intermediate or component in a formulating process)
of pentachlorophenol,
or of intermediates used to
produce
its derivatives.
F022
Wastes
(except wastewater and spent carbon from
(H)
hydrogen chloride purification)
from the
manufacturing use
(as a reactant, chemical
intermediate or component
in
a formulating process)
of tetra—,
penta— or hexachlorobenzenes under
alkaline conditions.
P023
Wastes
(except wastewater and spent carbon from
(H)
hydrogen chloride purification)
from the production
of materials on equipment previously used for the
production or manufacturing use (as a reactant,
chemical intermediate or component in a formulating
process)
of tn— and tetrachlorophenols.
(This
listing does not include wastes from equipment used
only for the production or use of hexachlorophene
from highly purified 2,4,5— tnichlorophenol.
F024
Process wastes including but not limited to,
(T)
distillation residues,
heavy ends,
tars,
and reactor
cleanout wastes,
from the production of certain
chlorinated aliphatic hydrocarbons by free radical
catalyzed processes.
These chlorinated aliphatic
hydrocarbons are those having carbon chain lengths
ranging from one to and including five, with varying
amounts and positions of chlorine substitution.
(This listing does not include wastewaters,
wastewater treatment sludges,
spent
catalysts and
wastes listed in this Section or Section 721.132.)
117—37 6

57
P025
Condensed light ends,
spent filters and filter aids,
(T)
and spent dessicant wastes from the production of
certain chlorinated aliphatic hydrocarbons by free
radical catalyzed processes.
These chlorinated
aliphatic hydrocarbons are those having carbon chain
lengths ranging from one to and including five, with
varying amounts and positions of chlorine
substitution.
F026
Wastes
(except wastewater and spent carbon from
(H)
hydrogen chloride purification)
from the production
of materials on equipment previously used for the
manufacturing use (as a reactant, chemical
intermediate or component in aformulating process)
of tetra—,
penta— or hexachlorobenzene under
alkaline conditions.
P027
Discarded unused formulations containing tn—,
(H)
tetra- or pentachlorophenol or discarded unused
formulations containing compounds derived from these
chlorophenola.
(This listing does not include
formulations containing hexachlorophene synthesized
from prepurified 2,4,5—tnichlorophenol as the sole
component).
F028
Residues resulting from the incineration or thermal
(T)
treatment of soil contaminated with hazardous waste
numbers P020,
F021,
F022, F023,
P026 and F027.
P039
Leachate resulting from the treatment, storage or
.Lfl
disposal of wastes classified by more than one waste
code under Subpart D,
or from a mixture of wastes
classified under Subparts C and D.
(Leachate
resulting from the management of one or more of the
following USEPA hazardous wastes and no other
hazardous wastes retains its hazardous waste
code(s):
P020,
P021, F022, F023,
P026, P027 or
F028.)
(Board Note:BOARD NOTE:
The primary hazardous properties of these materials
have been indicated by the letters T
(Toxicity), R (Reactivity),
I
(Ignitability),
and C
(Corrosivity).
The letter H indicates Acute Hazardous
Waste.-)-
(Source:
Amended at
15
Ill.
Reg.
,
effective
Section 721.132
Hazardous Waste from Specific Sources
The following solid wastes are listed hazardous wastes from specific sources
unless they are excluded under 35
Ill. Ada.
Code 720.120 and 720.122 and
listed
in Appendix
I.
117—377

58
EPA
Hazardous
Hazard
Waste No.
Industry and Hazardous Waste
Code
Wood Preservation:
KOOI
Bottom sediment sludge from the treatment of waste-
(T)
waters from wood preserving processes that use
creosote and/or pentachlorophenol.
Inorganic Pigments:
1(002
Wastewater treatment sludge from the production of
(T)
chrome yellow and orange pigments.
K003
Wastewater treatment sludge from the production of
(T)
molybdate orange pigments.
1(004
Wastewater treatment sludge from the production of
(T)
zinc yellow pigments.
K005
Wastewater treatment sludge from the production of
(T)
chrome green pigments.
K006
Wastewater treatment sludge from the production of
(T)
chrome oxide green pigments (anhydrous and
hydrated).
K007
Wastewater treatment sludge from the production of
(T)
iron blue pigments.
1(008
Oven residue from the production of
chrome oxide
(T)
green pigments.
Organic Chemicals:
1(009
Distillation bottoms from the production of
(T)
acetaldehyde from ethylene.
1(010
Distillation side cuts from the production of
(T)
acetaldehyde from ethylene.
1(011
Bottom stream from the wastewater stripper in the
(R,T)
production of acrylonitrile.
K013
Bottom stream from the acetronitnile column in the
(T)
production of acrylonitrile.
1(014
Bottoms
from the acetontnile purification column in
(T)
the production of acrylonitrile.
117—378

59
.1(015
Still bottoms from the distillation of benzyl
(T)
chloride.
K016
Heavy ends or distillation residues from the
(T)
production of carbon tetrachloride.
1(017
Heavy ends (still bottoms) from the purification
(T)
column in the production of epichlorohydrin.
1(018
Heavy ends from the fractionation column in ethyl
(T)
chloride production.
1(019
Heavy ends from the distillation of ethylene di—
(T)
chloride in ethylene dichloride production.
K020
Heavy ends from the distillation of vinyl chloride
(T)
in vinyl chloride monomer production.
K02l
Aqueous spent antimony catalyst waste from
(T)
fluoromethanes production.
1(022
Distillation bottom tars from the production of
(T)
phenol/acetone from cumene.
1(023
Distillation light ends from the production of
(T)
phthalic anhydride from naphthalene.
1(024
Distillation bottoms from the production of phthalic
(T)
anhydride from naphthalene.
1(093
Distillation light ends from the production of
(T)
phthalic anhydride from ortho—xylene.
1(094
Distillation bottoms from the production of phthalic
(T)
anhydride from ortho—xylene.
1(025
Distillation bottoms from the production of
(T)
nitrobenzene by the nitration of benzene.
K026
Stripping still tails from the production of methyl
(T)
ethyl pyridines.
1(027
Centrifuge and distillation residues from toluene
(R,T)
diisocyanate production.
K028
Spent catalyst from the hydrochlorinator reactor in
(T)
the production of l,1,l—trichloroethane.
1(029
Waste
from the product stream stripper in the
(T)
production of
1,1,1—trichioroethane.
117—37 9

60
1(095
Distillation bottoms from the production of 1,1,1—
(T)
trichloroethane.
1(096
Heavy ends from the heavy ends column from the
(T)
production of
1,1,1-trichloroethane.
1(030
Column bottoms or heavy ends from the combined
(T)
production of trichloroethylene and perchloro—
ethylene.
K083
Distillation bottoms from aniline production.
(T)
1(103
Process residues from aniline extraction from the
(T)
production of~aniline.
1(104
Combined wastewater streams generated from
(T)
nitrobenzene/aniline production.
1(085
Distillation or fractionation column bottoms
(T)
from the production of chlorobenzenes.
Kb05
Separated aqueous stream from the reactor product
(T)
washing step
in the production of chlorobenzenes.
1(107
Column bottoms from product separation from the
(C,T~
production of 1,1—dimethylhydrazine
(UDMH)
from
carboxilic
acid hydrazides.
1(108
Condensed column overheads from product separation
(I,T)
and condensed reactor vent gases from the production
of l,l-dimethylhydrazine
(UDMH)
from carboxilic acid
hydrazides.
1(109
Spent filter cartridges from the product
purification from the production of l,1-di—
methylhydrazine
(UDMH)
from carboxilic acid
hydrazides.
1(110
Condensed column overheads from intermediate
IT.).
separation from the production of 1,l—di-
methylhydrazine
(UDMH~
from carboxilic acid
hydrazides.
1(111
Product wastewaters from the production of di—
(C,T)
nitrotoluene via nitration of toluene.
K112
Reaction by—product water
from the drying column in
(T)
the production of toluenediaxnine via hydrogenation
of dinitrotoluene.
117—380

61
1(113
Condensed liquid light ends from the purification of
(T)
toluenediamine in the production of toluenediamine
via hydrogenation of dinitroluene.
K114
Vicinals
from the purification of toluene—diamine in
(T)
the production of toluenediamine via hydrogenation
of dinitrotolune.
1(115
Heavy ends from the purification of toluenediamine
(T)
in the production of toluenediamine via
hydrogenation of dinitrotoluene.
1(116
Organic condensate from the solvent recovery column
(T)
in the production of toluene diisocyanate via
phosgenation of toluenediamine.
1(117
Wastewater from the reactor vent gas scrubber in the
(T)
production of ethylene dibromide via bromination of
ethene.
K118
Spent adsorbent solids from purification of ethylene
(T)
dibromide
in the production of ethylene dibromide
via bromination of ethene.
1(136
Still bottoms from the purification of ethylene di—
(T)
bromide in the production of ethylene dibromide via
bromination of ethene.
Inorganic Chemicals:
1(071
Brine purification muds from the mercury cell
(T)
process in chlorine production, where separately
prepurified brine is not used.
K073
Chlorinated hydrocarbon waste from the purification
(T)
step of the diaphragm cell process using graphite
anodes
in chlorine production.
1(106
Wastewater treatment sludge from the mercury cell
(T)
process in chlorine production.
Pesticides:
K031
By-product
salts generated
in the production of MSMA
(T)
and cacodylic acid.
1(032
Wastewater treatment sludge from the production of
(T)
chlordane.
K033
Wastewater and scrub water from the chlorination of
(T)
cyclopentadiene in the production of chlordane.
117—38 1

62
1(034
Filter solids from the filtration of hexachloro—
(T)
cyclopentadiene in the production of chlordane.
K097
Vacuum atripper discharge from the chiordane
(T)
chlorinator
in the production of chlordane.
1(035
Wastewater treatment sludges generated in the
(T)
production of creosote.
1(036
Still bottoms from toluene reclamation distillation
(T)
in the production of disulfoton.
1(037
Wastewater treatment sludges from the production of
(T)
disulfoton.
1(038
Wastewater from the washing and stripping of phorate
(T)
production.
K039
Filter cake from the filtration of diethyl—
(T)
phosphorodithioic acid in the production of phorate.
1(040
Wastewater treatment sludge from the production of
(T)
phorate.
1(041
Wastewater treatment sludge from the production of
(T)
toxaphene.
1(098
Untreated process wastewater from the production of
(T)
toxaphene.
1(042
Heavy ends or distillation residues from the
(T)
distillation of tetrachlorobenzene in the production
of 2,4,5—T.
1(043
2,6—Dichlorophenol waste from the production of 2,4—
(T)
B.
1(099
Untreated wastewater from the production of 2,4—B.
(T)
1(123
Process wastewater
(including supernates,
filtrates
(T)
and washwaters)
from the production of ethylenebis—
dithiocarbamic acid and its salts.
1(124
Reactor vent scrubber water from the production of
(C,T)
ethylenebisdithiocarbamic acid and its salts.
Kb25
Filtration, evaporation and centrifugation solids
(T)
from the production of ethylenebisdithiocarbamic
acid and
its salts.
117—382

63
1(126
Baghouse dust and floor sweepings in milling and
(T)
packaging operations from the production or
formulation of ethylenebisdithiocarbamic acid and
its salts.
K131
Wastewater from the reactor and spent sulfuric acid
(C,T)
from the acid dryer from the production of methyl
bromide.
Kl32
Spent absorbent and wastewater separator solids from
(T)
the production of methyl bromide.
Explosives:
1(044
Wastewater treatment
sludges from the manufacturing
(R)
and processing of explosives.
1(045
Spent carbon from the treatment of wastewater
(R)
containing explosives.
1(046
Wastewater treatment sludges from the manufacturing,
(T)
formulation and loading of lead-based initiating
compounds.
1(047
Pink/red water from TNT operations.
(R)
Petroleum Refining:
KO48
Dissolved air flotation
(DAF)
float from the
(T)
petroleum refining
industry.
1(049
Slop oil emulsion solids from the petroleum refining
(T)
industry.
K050
Heat exchanger bundle cleaning sludge from the
(T)
petroleum refining industry.
K05b
API
separator sludge from the petroleum refining
(T)
industry.
1(052
Tank bottoms
(leaded) from the petroleum refining
(T)
industry.
Iron and Steel:
K061
Emission control dust/sludge from the primary
(T)
production of steel in electric furnaces.
1(062
Spent pickle liquor generated by steel finishing
(C,T)
operations of facilities within the iron and steel
industry
(SIC Codes 331 and 332)
(as defined in 35
Ill. Adm.
Code 720.110).
117—383

64
Primary Copper:
K064
Acid plant blowdown slurry or sludge resulting from
(T)
the thickening of blowdown slurry from primary
copper production.
Primary Lead:
1(065
Surface impoundment solids .contained in and dredged
(T)
from surface impoundments at primary lead smelting
facilities.
Primary Zinc:
1(066
After June 30,
1990,
sludge from treatment of
(T)
process wastewater or acid plant blowdown from
primary zinc production.
Primary Aluminum:
1(088
Spent potliners from primary aluminum reduction.
(T)
Ferroalloys:
K090
Emission control dust or sludge from
(T)
ferrochromiumsilicon production.
1(091
Emission control dust or sludge from ferrochromium
(T)
production.
Secondary Lead:
1(069
Emission control dust/sludge from secondary lead
(T)
smelting.
1(100
Waste leaching solution from acid leaching of
(T)
emission control dust/sludge from secondary lead
smelting.
Veterinary Pharmaceuticals:
1(084
Wastewater treatment sludges generated during the
(T)
production of veterinary pharmaceuticals from
arsenic or organo—arsenic compounds.
1(101
Distillation tar residues from the distillation of
(T)
aniline-based compounds in the production of
veterinary pharmaceuticals from arsenic or organo—
arsenic compounds.
117—384

65
1(102
Residue from use of activated carbon for
(T)
decolorization in the production of veterinary
pharmaceuticals from arsenic or organo—arsenic
compounds.
Ink Formulation:
1(086
Solvent washes and sludges,
caustic washes and
(T)
aludg~s,or water washes and sludges from cleaning
tubs and equipment used
in the formulation of ink
from pigments, driers,
soaps and stabilizers
containing chromium and lead.
Coking:
1(060
Ammonia still
lime sludge from coking operations.
(T)
1(087
Decanter tank tar sludge from coking operations.
(T)
(Source:
Amended at
15
Ill. Reg.
,
effective
Section 721.133
Discarded Commercial Chemical Products,
Off—Specification
Species, Container Residues and Spill Residues Thereof
The following materials or items are hazardous wastes
if and when they are
discarded or intended to be discarded as described in Section
721.102(a)(2)(A), when they are mixed with waste oil or used oil or other
material and applied to the land for dust suppression or road treatment,
when
they are otherwise applied to the land in lieu of their original intended use
or when they are contained in products that are applied to land in lieu of
their original intended use,
or when,
in lieu of their original intended use,
they are produced for use as (or as
a component of)
a fuel,
distributed for
use as
a fuel,
or burned as a fuel.
a)
Any commercial chemical product,
or manufacturing chemical
intermediate having the generic name listed in subsections
(e) or
(f).
b)
Any off—specification commercial chemical product or manufacturing
chemical intermediate which,
if
it met specifications, would have
the generic name listed in subsections
(e)
or
(f).
C)
Any residue remaining in a container or inner
liner removed from a
container that has held any commercial chemical product or
manufacturing chemical intermediate having the generic name listed
in subsection
(e)
or
(f),
unless the container is empty as defined
in Section 72l.b07(b)(3).
BOARD
NOTE:
Unless the residue is being beneficially used or
reused, or
legitimately recycled or reclaimed,
or being
accumulated,
stored, transported or treated prior to such use,
117—385

66
reuse, recycling or reclamation,
the Board considers the residue
to be intended for discard, and thus a hazardous waste.
An
example of
a legitimate reuse of the residue would be where the
residue remains in the container and the container is used to hold
the same commercial chemical product or manufacturing chemical
intermediate
it previously held.
An example of the discard of the
residue would be where the drum is sent to a drum reconditioner
who reconditions the drum but discards the residue.
d)
Any residue or contaminated soil, water or other debris resulting
from the cleanup of
a spill,
into or on any land or water of any
commercial chemical product or manufacturing chemical intermediate
having the generic
name
listed in subsection
(a)
or
(f), or any
residue or contaminated soil,
water or other debris resulting from
the cleanup of
a spill,
into or on any land or water,
of any off—
specification chemical product or manufacturing chemical
intermediate which,
if
it met specifications, would have the
generic name listed
in subsection
(e)
or
(f).
BOARD NOTE:
The phrase “commercial chemical product or
manufacturing chemical intermediate having the generic name listed
in
...“
refers to
a chemical substance which is manufactured or
formulated
for commercial or manufacturing use which consists of
the commercially pure grade of the chemical,
any technical grades
of the chemical that are produced or marketed,
and all
formulations
in which the chemical
is the sole active ingredient.
It does not refer to a material,
such as
a manufacturing process
waste,
that contains any of the substances listed
in subsections
(e)
or
(f).
Where
a manufacturing process waste
is deemed to be a
hazardous waste because it contains a substance listed in
subsections
(e) or
(f),
such waste will be listed in either
Sections
721.131 or 721.132 or will be identified as a hazardous
waste by the characteristics set forth in Subpart C.
e)
The commercial chemical products,
manufacturing chemical
intermediates or off-specification commercial chemical products or
manufacturing chemical intermediates referred to in subsections
(a) through
(d),
are identified as acute hazardous waste
(H)
and
are subject to the small quantity exclusion defined in Section
721.105(e).
These wastes and their corresponding EPA Hazardous
Waste Numbers are:
BOARD NOTE:
For the convenience of the regulated community the
primary hazardous properties of these materials have been
indicated by the letters T (Toxicity), and R (Reactivity).
Absence of
a letter indicates that the compound only is listed
for
acute toxicity.
117—386

67
Chemical
Hazardous
Abstracts
Waste No.
No.
Substance
P023
107-20-0
Acetaldehyde, chboro—
P002
591-08-2
Acetamide, N—(aminothioxomethyl)
P057
640—19-7
Acetamide, 2—fluoro—
P058
62—74-8
Acetic acid,
fluoro—, sodium salt
P002
591—08-2
1—Acetyl—2—thiourea
P003
107—02—8
Acrolein
P070
116—06—3
Aldicarb
P004
309—00—2
Aidrin
P005
107—18—6
Allyl alcohol
P006
20859-73—8
Aluminum phosphide
(R,T)
P007
2763—96—4
5—(Aminomethyl
)
—3—isoxazolol
P008
504-24—5
4—Aminopyridine
P009
131-74—8
Ammonium picrate
(R)
P119
7803-55-6
Ammonium vanadate
P099
506—61-6
Argentate(1—), bis(cyano-C)—, potassium
P010
7778—39—4
Arsenic acid H3AsO4
P012
1327—53—3
Arsenic oxide As2O3
POll
1303—28—2
Arsenic oxide As205
P011
1303—28-2
Arsenic pentoxide
P012
1327—53—3
Arsenic trioxide
P038
692—42—2
Arsine, diethyl—
P036
696-28-6
Arsonous dichloride, phenyl-
P054
151—56—4
Aziridine
P067
75—55—8
Aziridine, 2—methyl
P013
542-62-1
Barium cyanide
P024
106-47—8
Benzenamine, 4-chloro—
P077
100-01-6
Benzenamine,
4—nitro—
P028
100-44-7
Benzene,
(chioromethyl)—
P042
51-43-4
l,2—Benzenediol, 4—(1—hydroxy—2—
(methylamino)ethyl-,
(R)-
P046
122-09-8
Benzeneethanamine, alpha,
alpha—di—
methyl-
P014
108-98-5
Benzenethiol
POOl
P81-81-2
2H—l-Benzopyran-2—one,
4-hydroxy-3—(3-
oxo-1-phenylbutyl)-, and salts, when
present at concentrations greater than
0.3
P028
100-44—7
Benzyl chloride
P015
7440-41—7
Beryllium
P017
598-31-2
Bromoacetone
P018
357-57—3
Brucine
P045
39196-18-6
2—Butanone, 3, 3—dimethyl—l—(methyl—
thio)-,
O-(methylamino)carbonyfl oxime
P021
592-01-8
Calcium cyanide
P021
592-01—8
Calcium cyanide Ca(CN)2
P022
75-15-0
Carbon disulfide
P095
75-44-5
Carbonic dichloride
P023
107-20—0
Chloroacetaldehyde
117—387

68
P024
106—47—8
p—Chloroaniline
P026
5344-82-1
1-(o-Chlorophenyl)thiourea
P027
542—76-7
3—Chloropropionitrile
P029
544-92-3
Copper cyanide
P029
544-92-3
Copper
cyanide CuCN
P030
Cyanides (soluble cyanide salts), not
otherwise specified
P031
460-19-5
Cyanogen
P033
506-77-4
Cyanogen chloride
P033
506-77-4
Cyanogen chloride
CNC1
P034
131-89-5
2—Cyclohexyl—4,6—dinitrophenol
P016
542-88-1
Dichloroaethyl ether
P036
696-28-6
Dichlorophenylaraine
P037
60—57—1
Dieldrin
P038
692—42—2
Diethylarsine
P041
311-45-5
Diethyl-p-nitropheriyl phosphate
P040
297-97-2
0,0—Diethyl 0-pyrazinyl
phosphorothioate
P043
55-91—4
Diisopropylfluorophosphate
(DFP)
P004
309—00-2
1,4,5,8—Dimethanonaphthalene,
1,2, 3,4,10, 10—hexachloro-
1,4,4a,5,8,Ba—hexahydro-,
(lalpha,
4alpha, 4abeta,
Salpha,
Balpha,
8abeta)-
P060
465-73-6
1,4, 5,8—Di—methanonaphthalene,
1,2,3,4,10, 1O—hexachloro—
1,4,4a,5,8,8a—hexahydro-,
(lalpha,
4alpha,
4abeta,
Sbeta,
Bbeta,
8abeta)—
P037
60-57-1
2,7:3,6—Dimethanonaphth(2,3—boxirene,
3,4,5,6,9,9—hexachloro-
la,2, 2a,3,6, 6a, 7, 7a—octahydro—,
(laalpha,
2beta, 2aalpha, 3beta,
6beta,
6aalpha, 7beta,
laalpha)—
P051
P72-20—8
2,7:3,6—Dimethanonaphth(2,3—boxirene,
3,4,5,6,9,9—hexachloro—
1a,2,2a,3,6,6a,7,7a—octahydro—,
(laalpha,
2beta, 2abeta,
3alpha,
6alpha,
6abeta,
7beta, 7aalpha)-,
and
metabolitea
P044
60-51-5
Dimethoate
P046
122-09-8
alpha,
alpha-Dimethylphenethylamine
P047
534-52—1
4,6—Dinitro—o-cresol and salts
P048
51-28—5
2,4—Dinitrophenol
P020
88—85—7
Dinoseb
P085
152-16-9
Diphosphoramide, octamethyl-
P111
107-49-3
Diphosphoric acid,
tetraethyl ester
P039
298—04—4
Disulfoton
P049
541—53-7
Dithiobiuret
P050
115—29—7
Endosulfan
P088
145—73—3
Endothall
P051
72—20—8
Endrin
P051
72-20-8
Endrin,
and metabolites
117—388

69
P042
51-43—4
Epinephrine
P031
460—19-5
Ethanedinitrile
P066
16752-77-5
Ethanimidothioic acid, N-((methyl—
amino)carbonyloxy)—,
methyl ester
P101
107-12-0
Ethyl cyanide
P054
151—56-4
Ethylenimine
P097
52-85-7
Famphur
P056
7782—41—4
Fluorine
P057
640—19-7
Fluoroacetamide
P058
62—74—8
Fluoroacetic acid,
sodium salt
P065
628—86-4
Fulminic acid, mercury
(2+)
salt
(R,T)
P059
76—44-8
Heptachlor
P062
757-58-4
Hexaethyl tetraphosphate
P116
79-19-6
Hydrazinecarbothioamide
P068
60-34-4
Hydrazine, methyl—
P063
74-90-8
Hydrocyanic acid
P063
74-90—8
Hydrogen cyanide
P096
7803—51-2
Hydrogen phosphide
P060
465—73-6
Isodrin
P007
2763—96—4
3(2H)—Isoxazolone,
5—(aininomethyl)—
P092
62—38-4
Mercury,
(acetato—O)phenyl—
P065
628—86—4
Mercury fulminate (R,T)
P082
62-75-9
Methanamine, N-methyl—N—nitroso—
P064
624—83-9
Methane,
isocyanato—
P016
542-88-1
Methane, oxybischloro—
P112
509-14-8
Methane, tetranitro-
(R)
P118
75-70-7
Methanethiol, trichloro—
P050
115-29-7
6,9—Methano—2,4,3—benzodioxathiepen,
6,7,8,9,10,10—hexachloro—1,5,5a,6,9,9a—
hexahydro—, 3-oxide
P059
76—44-8
4,7—Methano—1H—indene,
1,4,5,6,7,8,8—
heptachloro—3a, 4,7,7a—tetrahydro—
P066
16752-77—5
Methomyl
P068
60-34-4
Methyl hydrazine
P064
624-83-9
Methyl
isocyanate
P069
75—86-5
2—Methyllactonitrile
P071
298-00-0
Methyl parathion
P072
86-88-4
alpha—Naphthylthiourea
P073
13463—39—3
Nickel carbonyl
P073
13463—39-3
Nickel carbonyl Ni(CO)4,
(T—4)—
P074
557-19-7
Nickel cyanide
P074
557-19-7
Nickel cyanide Ni(CN)2
P075
54—11-5
Nicotine, and salts
P076
10102—43—9
Nitric oxide
P077
100—01—6
p—Nitroaniline
P078
10102-44—0
Nitrogen dioxide
P076
10102-43-9
Nitrogen oxide NO
P078
10102—44—0
Nitrogen oxide NO2
P081
55—63—0
Nitroglycerine
(R)
P082
62-75-9
N—Nitroaodimethylamine
P084
4549-40-0
N—Nitrosomethylvinylamine
P085
152-16-9
Octainethylpyrophosphoramide
117—389

70
P087
20816—12—0
Osmium oxide OSO4~ (T—4)—
P087
20816-12—0
Osmium tetroxide
P088
145-73-3
7—Oxabicyclo(2.2.1)heptane-2,3—di—
carboxylic acid
P089
56—38-2
Parathion
P034
131—89-5
Phenol,
2—cyclohexyl—4
,
6—dinitro—
P048
51-28—5
Phenol, 2,4—dinitro-
P047
P534-52-1
Phenol,
2—methyl—4,6—dinitro—,
and
salts
P020
88—85-7
Phenol,
2—(1—methylpropyl)—4,6-dinitro—
P009
131-74—8
Phenol,
2,4,6—trinitro—, ammonium salt
(H)
P092
62-38-4
Phenylmercury acetate
P093
103—85-5
Phenylthiourea
P094
298-02-2
Phorate
P095
75-44-5
Phosgene
P096
7803—51-2
Phosphine
P041
311—45-5
Phosphoric acid,
diethyl 4-nitrophenyl
ester
P039
298-04-4
Phosphorodithioic acid, O,O-diethyl S-
2—(ethylthio)ethyl)
ester
P094
298—02-2
Phosphorodithioic acid, O,O-diethyl S-
((ejhylthio)methyl
ester
P044
60-51-5
Phoaphorodithioic acid,
0,0-dimethyl
5-
2-
(methylarnino)—2-oxoethyl
ester
P043
55—91-4
Phosphorofluoridic acid,
bis(1—methyl—
ethyl)eater
P089
56-38-2
Phosphorothioic acid,
0,0-diethyl 0-
(4-nitrophenyl) ester
P040
297—97-2
Phosphorothioic acid, O,O-diethyl 0—
pyrazinyl ester
P097
52-85-7
Phosphorothioic acid, O—(4—
(dimethyl—
amino)sulfonyl) phenyl)
O,O-dimethyl
ester
P071
298-00-0
Phosphorothioic acid, O,O-dimethyl 0-
(4-nitrophenyl) ester
P110
78-00-2
Plumbane, tetraethyl—
P098
151-50-8
Potassium cyanide
P098
151-50-8
Potassium cyanide KCN
P099
506-61-6
Potassium silver cyanide
P070
116-06-3
Propanal, 2—methyl—2—(methylthio)—,
0-
((methylamino) carbonyl
3
oxime
P101
107-12—0
Propanenitrile
P027
542-76-7
Propanenitrile, 3—chloro-
P069
75-86-5
Propanenitrile, 2-hydroxy—2—methyl-
P081
55-63-0
1,2,3—Propanetriol, trinitrate-
(R)
P017
598-31—2
2—Propanone,
1—bromo—
P102
107—19-7
Propargyl alcohol
P003
107—02-8
2—Propenal
P005
107—18—6
2—Propen—1—ol
P067
75-55—8
1,2—Propylenimine
P102
107—19—7
2—Propyn—1—ol
117—390

71
P008
504—24—5
4—Pyridinamine
P075
P54—11—5
Pyridine,
3—(1—methyl—2—
pyrrolidinyl)-,
(S)— and salts
P114
12039—52—0
Selenioua acid, dithallium
(1+) salt
P103
630-10-4
Selenourea
P104
506-64—9
Silver cyanide
P104
506-64—9
Silver cyanide
AgCN
P105
26628—22—B
Sodium azide
P106
143-33—9
Sodium cyanide
P106
143-33-9
Sodium cyanide NaCN
P108
P57-24—9
Strychnidin—lO—one, and salts
P018
357-57-3
Strychnidin-lO-ona,
2,3—dimethoxy-
P108
P57—24—9
Strychnine and salts
P115
7446—18—6
Sulfuric acid,
dithalliunt
(1+)
salt
P109
3689—24-5
Tetraethyldithiopyrophosphate
P110
78-00-2
Tetraethyl lead
P111
107-49-3
Tetraethylpyrophosphate
P112
509—14-8
Tetranitromethane
(R)
P062
757-58-4
Tetraphoaphoric acid, hexaethyl ester
P113
1314—32—5
Thallic oxide
P113
1314—32—5
Thallium oxide Tl203
P114
12039—52—0
Thallium
(I)
selenite
P115
7446—18—6
Thallium
(I)
sulfate
P109
3689-24-5
Thiodiphosphoric acid, tetraethyl ester
P045
39196—18—4
Thiofanox
P049
541-53—7
Thioimidodicarbonic diamide
((H2N)C(S) ~2
P014
108-98-5
Thiophenol
P116
79-19—6
Thiosemicarbazide
P026
5344-82-1
Thiourea,
(2—chiorophenyl)-
P072
86-88-4
Thiourea,
1—naphthalenyl—
P093
103-85—5
Thiourea, phenyl—
P123
8001—35-2
Toxaphene
P118
75-70-7
Trichioromethanethiol
P119
7803—55-6
Vanadic acid, ammonium salt
P120
1314-62—1
Vanadium oxide V2O5
P120
1314-62-1
Vanadium pentoxide
P084
4549-40-0
Vinylamine, N-methyl—N-nitroso-
P001
P81-81-2
Warfarin,
and salts, when present at
concentrations greater than 0.3.
P121
557—21-b
Zinc cyanide
P121
557—21—1
Zinc cyanide Zn(CN)2
P122
1314—84-7
Zinc phoaphide Zn3P2, when present at
concentrations greater than 10
(R,T)
f)
The
commercial
chemical products,
manufacturing chemical
intermediates or off-specification commercial chemical products
referred to
in
subsections
(a)
through
(d),
are identified as
toxic wastes
(T)
unless otherwise designated and are subject to
the
small
quantity
exclusion
defined
in
Section 721.105(a)
and
(g).
These
wastes
and their corresponding EPA Hazardous Waste
Numbers
are:
117—391

72
BOARD
NOTE:
For the convenience of the regulated community, the
primary hazardous properties of these materials have been
indicated by the letters T
(Toxicity),
R (Reactivity),
I
(Ignitability) and C
(Corrosivity).
Absence of
a letter indicates
that the compound
is only listed for toxicity.
Chemical
Hazardous
Abstracts
Waste No.
No.
Substance
U001
75-07-0
Acetaldehyde
(I)
U034
75-87-6
Acetaldehyde, trichloro—
U187
62-44-2
Acetamide, N-(4-ethoxyphenyl)-
U005
53—96—3
Acetamide, N-9H—fluoren—2—yl—
13240
P 94—75-7
Acetic acid,
(2,4—dichlorophenoxy)—,
salts and esters
13112
141—78—6
Acetic acid,
ethyl ester
(I)
U144
301—04—2
Acetic acid,
lead
(2+)
salt
13214
563—68—8
Acetic acid, thallium
(1+)
salt
See F027
93—76—5
Acetic acid,
(2,4,5—trichiorophenoxy)—
U002
67—64—1
Acetone
(I)
UOO3
75—05—8
Acetonitrile
(I,T)
U004
98—86—2
Acetophenone
U005
53—96—3
2-Acetylaminofluorene
0006
75—36—5
Acetyl chloride (C,R,T)
0007
79—06—1
Acrylamide
U008
79—10—7
Acrylic acid
(I)
U009
107—13—1
Acrylonitrile
U011
61—82—5
Amitrole
13012
62—53—3
Aniline
(I,T)
13136
75—60—5
Arsinic acid,
dimethyl—
13014
492—80—8
Auramine
U015
115—02—6
Azaserine
13010
50—07—7
Azirino2~,3~:3,4)pyrrolo(1,2—aindole—
4,7—dione,
6—amino-8—
(
(aminocarbonyl)—
oxymethyl)
-1, la,2,8, 8a,8b—hexahydro—
8a—methoxy-5-methyl—,
1a—S—(laalpha,
8beta,
8aalpha, 8balpha)—
13157
56—49—5
Benzjaceanthrylene,
l,2—dihydro—3—
methyl-
U016
225—51—4
Benz(c)acridine
U0l7
98—87—3
Benzal chloride
U192
23950—58—5
Benzamide, 3,5—dichloro—N—(1, 1—di—
methyl-2-propynyl)
0018
56—55—3
Benzaanthracene
0094
57—97—6
Benza)anthracene,
7,12—dimethyl—
0012
62—53—3
Benzenamine
(I,T)
0014
492-80—8
Benzenamine,
4,4’—carbonimidoylbisN,N-
dimethyl-
U049
3165—93—3
Benzenamine,
4—chloro—2—methyl—,
hydrochloride
117—39 2

73
13093
60-11-7
Benzenamine,
N,N-dimethyl—4-(phenyl—
azo)—
13328
95-53-4
Benzenamine, 2—methyl—
U353
106-49-0
Benzenamine, 4—methyl—
U158
101-14-4
Benzenamine, 4,4’-methylenebis2—
chloro—
0222
636-21-5
Benzenamine,
2—methyl—, hydrochloride
U18l
99-55-8
Senzenamine,
2—methyl—5—nitro—
0019
71—43—2
Benzene
(I,T)
0038
510-15-6
Benzeneacetic acid,
4-chloro—alpha—(4-
chborophenyl
)
-alpha-hydroxy-, ethyl
ester
U030
101-55-3
Benzene, 1—bromo—4—phenoxy—
13035
305-03-3
Benzenebutanoic acid,
4—bis(2-chloro-
ethyl)amino)-
13037
108—90—7
Benzene, chloro—
13221
25376—45—B
Benzenediamine, ar—methyl—
13028
117-81—7
1,2—Benzenedicarboxylic acid, bis(2—
ethylhexyl)
eater
13069
84-74-2
1,2-Benzenedicarboxylic acid, dibutyl
ester
U088
84-66—2
1,2—Benzenedicarboxylic acid,
diethyl
ester
U102
131-11—3
1,2—Benzenedicarboxylic acid,
dimethyl
ester
13107
117—84—0
1,2—Benzenedicarboxylic acid, dioctyl
ester
13070
95-50-1
Benzene,
1,2—dichloro—
U07l
541-73-b
Benzene,
1,3—dichloro—
U072
106—46-7
Benzene, 1,4-dichioro—
U060
72—54—8
Benzene, 1,l’—(2,2—dichloroethyl—
idene)bia(4-chloro-
U0l7
98-87-3
Benzene,
(dichloromethyl)-
13223
26471-62-5
Benzene, 1,3—diisocyanatomethyl—
(R,T)
0239
1330-20—7
Benzene, dimethyl-
(I,T)
0201
108—46—3
1,3—Benzenediol
0127
118-74—1
Benzene, hexachloro—
0056
110-82-7
Benzene, hexahydro-
(I)
U220
108-88-3
Benzene, methyl—
U105
121-14-2
Benzene, 1-methyl—2,4-dinitro-
U106
606-20-2
Benzene, 2—methyl—1,3-dinitro-
U055
98—82—8
Benzene,
(1—methy.ethyl)—
(I)
13169
98—95—3
Benzene, nitro—
0183
608-93-5
Benzene, pentachloro—
13185
82-68-8
Benzene, pentachloronitro-
U020
98—09—9
Benzenesulfonic acid chloride
(C,R)
U020
98—09—9
Benzenesulfonyl chloride (C,R)
13207
95-94—3
Benzene,
1,2,4,5—tetrachloro—
13061
50-29—3
Benzene,
1,1’—(2,2,2—trichloroethyl—
idene)bis
(
4—chloro—
U247
72—43—5
Benzene, 1,1’—(2,2,2—trichloroethyl—
idene)bis4—methoxy-
117—393

74
U023
98-07—7
Benzene,
(trichloromethyl)—
13234
99—35—4
Benzene,
1,3,5—trinitro—
13021
92—87—5
Benzidene
13202
P 81—07—2
1,2—Benzisothiazol—3(2H)—one, 1,1—di-
oxide, and salts
13203
94—59—7
1,3—Benzodioxole,
S—(2—propenyl)—
Ul4l
120-58-1
1,3—Benzodioxole,
5—(1—propenyl)-
0090
94-58-6
1,3—Benzodioxole,
5-propyl—
0064
189-55—9
Benzo(ratpentaphene
U248
P 81-81-2
2H—1—Benzopyran—2—one, 4—hydroxy-3—(3-
oxo-1-phenylbutyl)-, and salts, when
present at concentrations of 0.3
or
less
U022
50-32-8
Benzo(apyrene
U197
106—51-4
p-Benzoquinone
13023
98-07-7
Benzotrichloride
(C,R,T)
13085
1464—53—5
2,2’—Bioxirane
13021
92—87—5
(1,1’—Biphenyl—4,4’—diamine
0073
91—94—1
1,1’—Biphenyl)—4,4’—diamine,
3,3’—di—
chloro—
0091
119—90—4
(1,1’—Biphenyl)—4,4 ‘—diamine,
3,3 ~—di—
methoxy-
0095
119—93—7
(1,1’—Biphenyl3—4,4’—diamine,
3,3’—di—
methyl-
U225
75-25—2
Bromoform
13030
101-55-3
4—Bromophenyl phenyl ether
13128
87—68—3
1,3—Butadiene, 1,1,2,3,4,4—hexachloro—
13172
924-16-3
1—Butanamine, N-butyl-N-nitroso—
13031
71—36—3
1—Butanol
(I)
U159
78-93-3
2—Butanone
(I,T)
Ul60
1338-23-4
2-Butanone, peroxide
(R,T)
U053
4170—30-3
2—Butenal
13074
764—41—0
2—Butene,
1,4—dichioro—
(I,T)
U143
303—34-4
2—Butenoic acid, 2—methyl—,
7—(2,3—
dihydroxy-2—
(
1—methoxyethyl
)
-3-methyl-
1-oxobutoxy)methyl
)
-2,3,5, 7a-tetra-
hydro-1H-pyrrolizin—1—yl ester,
iS-
(ialpha(Z),
7(2S*,3R*),
7aalphaJ—
0031
71-36-3
n-Butyl alcohol
(I)
0136
75—60—5
Cacodylic acid
13032
13765—19-0
Calcium chromate
U238
51-79-6
Carbaxnic acid,
ethyl eater
U178
615-53-2
Carbamic acid,
methylnitroso—, ethyl
ester
13097
79-44-7
Carbamic chloride, dimethyl-
0114
P 111—54-6
Carbamodithioic acid,
1,2—ethanediyl-
bis—,
salts and esters
13062
2303-16-4
Carbamothioic acid,
bis(1—methyl—
ethyl)—,
S—(2, 3-dichloro—2—propenyl)
ester
13215
6533—73—9
Carbonic acid, dithallium
(1+)
salt
13033
353—50-4
Carbonic difluoride
117—394

75
13156
79-22—b
Carbonochloridic acid,
methyl ester
(I,T)
U033
353-50-4
Carbon oxyfluoride
(R,T)
13211
56-23-5
Carbon tetrachloride
U034
75—87—6
Chloral
0035
305—03—3
Chiorambucil
U036
57—74-9
Chlordanealpha and gamma isomers
0026
494—03-1
Chlornaphazin
0037
108-90-7
Chlorobenzene
0038
510-15-6
Chlorobenzilate
U039
59—50-7
p—Chloro-m—cresol
13042
110-75-8
2—Chloroethyl vinyl ether
13044
67-66-3
Chloroform
13046
107-30-2
Chloromethyl methyl ether
0047
91—58—7
beta-Chloronaphthalene
13048
95-57-8
o—Chlorophenol
0049
3165-93-3
4-Chloro-o-toluidine,
hydrochloride
U032
13765—19-0
Chromic acid H2CrO4,
calcium salt
13050
218—01-9
Chrysene
U051
Creosote
U052
1319—77—3
Cresol
(Cresylic acid)
U053
4170—30-3
Crotonaldehyde
U055
98—82—8
Cumeme
(I)
U246
506-68-3
Cyanogen bromide CNBr
0197
106-51-4
2, 5—Cyclohexadiene—1,4—dione
0056
110—82—7
Cyclohexane
(I)
0129
58—89—9
Cyclohexane, i,2,3,4,5,6—hexachloro—,
(lalpha,2alpha, 3beta, 4alpha,Salpha, 6bet
a)—
13057
108—94-1
Cyclohexanone
(I)
13130
77—47—4
b,3—Cyclopentadiene,
1,2,3,4,5,5—hexa—
chloro—
0058
50-18-0
Cyclophosphamide
13240
F 94—75—7
2,4—B,
salts and esters
U059
20830—81—3
Daunomycin
U060
72—54—8
DDD
13061
50—29—3
DDT
13062
2303—16—4
Diallate
U063
53—70-3
Dibenz(a, hanthracene
U064
189—55—9
Dibenzo(a,ipyrene
U066
96-12-8
1, 2—Dibromo-3—chloropropane
U069
84—74-2
Dibuty.
phthalate
0070
95-50-1
o-Dichlorobenzene
0071
541-73—1
m—Dichlorobenzene
0072
106-46—7
p—Dichlorobenzene
13073
9 1—94—1
3,3’—Dichlorobenzidine
U074
764—41—0
b,4—Dichloro—2—butene
(I,T)
U07 5
75-71-8
Dichiorodifluoromethane
U078
75-35—4
1,l-Dichloroethylene
U079
156-60-5
1,2-Dichloroethylene
13025
111—44-4
Dichioroethyl ether
U027
108-60-1
Dichloroisopropyl ether
117—395

76
Dichloromethoxy ethane
2,4—Dichlorophenol
2, 6-Dichlorophenol
1,3-Dichloropropene
1,2:3,4—Diepoxybutane
(I,T)
1, 4-Diethyleneoxide
Diathylhexyl phthalate
N,
‘—Diethylhydrazine
0,0—Diethyl S—methyl dithiophosphate
Diethyl phthalate
Diethyistilbestrol
Dihydrosafro.e
3,3 ‘-Dimethoxybenzidine
Dimethylamine
(I)
p—Dimethylaminoazobenzene
7,12-Bimethylbenz(a anthracene
3,3w—Dimethylbenzidine
alpha, alpha-Dimethyl-
benzylhydroperoxide
(H)
Dimethylcarbamoyl chloride
1, 1-Dimethylhydrazine
1, 2-Dimethylhydrazine
2, 4-Dimethylphenol
Diniethyl phthalate
Dimethyl sulfate
2, 4-Dinitrotoluene
2, 6—Dinitrotoluene
Di-n-octyl phthalate
1, 4—Dioxane
1, 2-Diphenylhydrazine
Dipropylamine
(I)
Di-n-propylnitrosamine
Epichlorohydrin
Ethanal
(I)
Ethanamine, N—ethyl—N-nitroao-
1,2-Ethanediamine, N,N-dimethyl-N’ -2-
pyridinyl-N’
(
2-thienylmethyl
)
-
Ethane,
1, 2—dibromo—
Ethane,
Ethane,
Ethane,
Ethane,
chloro-
Ethane,
1,1’—oxybis—
(I)
Ethane,
1,1’—oxybis(2-chloro-
Ethane,
pentachloro—
Ethane,
1,1,1,2—tetrachloro—
Ethane, 1,1,2,2—tetrachloro—
Ethanethioaznide
Ethane,
Ethane,
Ethanol, 2-ethoxy-
U024
13081
U082
13084
13085
13108
0028
13086
13087
13088
13089
0090
13091
0092
0093
0094
0095
U096
U09 7
U098
U099
13101
0102
13103
13105
13106
0107
13108
13109
13110
13111
1304b
U00 1
13174
U155
0067
0076
0077
13131
0024
0117
U02 5
Ul84
0208
0209
U2 18
0226
U227
13359
111—91—1
120—83—2
87—65—0
542—75—6
1464—53—5
123—91—1
117—81—7
1615—80—1
3288—58—2
84—66—2
56—53—1
94—58—6
119—90—4
124—40—3
60—11 —7
57—97 —6
119—93—7
80— 15—9
79—44—7
57—14—7
540—73—8
105—67—9
131—11—3
77—78—1
121—14—2
606—20—2
117—84—0
123—91—1
122—66—7
142—84—7
621—64—7
106—89—8
75—07—0
55—18—5
91—80-5
106—93—4
75—34—3
107—06—2
67—72—1
111—91—1
60—29—7
111—44—4
76—01—7
630—20—6
79—34—5
62—55—5
71—55—6
79—00—5
110—80—5
1, 1—dichloro—
1, 2—dichloro—
hexachloro—
1,i’—(methylenebis(oxy)bis(2—
1,1, l—trichloro—
1,1,2—trichioro—
117—39 6

77
U173
1116—54—7
Ethanol,
2,2’—(nitrosoimino)bis—
13004
98-86-2
Ethanone,
1—phenyl—
13043
75-01—4
Ethene,
chloro—
U042
110-75-8
Ethene, (2—chloroethoxy)—
0078
75-35-4
Ethene,
1,1-dichloro—
0079
156—60-5
Ethene, 1,2—dich.oro—,
(E)—
13210
127-18-4
Ethene, tetrachloro-
0228
79-01—6
Ethene, trichloro—
13112
141—78—6
Ethyl acetate
(I)
0113
140—88—5
Ethyl acrylate
(I)
U238
51-79—6
Ethyl carbamate (urethane)
13117
60-29-7
Ethyl ether
13114
P 111—54-6
Ethylenebisdithiocarbamic acid,
salts
and esters
13067
106-93-4
Ethylene dibromide
0077
107—06-2
Ethylene dichloride
0359
110-80-5
Ethylene glycol monoethyl ether
0115
75-21—8
Ethylene oxide
(I,T)
0116
96—45—7
Ethylenethiourea
0076
75-34-3
Ethylidene dichloride
0118
97—63-2
Ethyl methacrylate
U119
62—50-0
Ethyl methanesulfonate
U120
206-44—0
Fluoranthene
13122
50-00-0
Formaldehyde
0123
64—18—6
Formic acid
(C,T)
0124
110—00—9
Furan
(I)
Ul25
98-01—1
2-Furancarboxaldehyde
(I)
13147
108—31—6
2,5—Furandione
13213
109-99—9
Furan, tetrahydro—
(I)
13125
98—01—1
Furfural
(I)
13124
110—00—9
Furfuran
(I)
13206
18883—66-4
Glucopyranose, 2—deoxy—2—(3—methyl—3—
riitrosoureido
)
—,
D—
0206
18883—66—4
D—Glucose,
2—deoxy—2—(
(methylnitroso—
amino)—carbonyl
amino)-
0126
765—34-4
Glycidylaldehyde
0163
70-25-7
Guanidine, N-methyl—N’-nitro-N—
nitroao—
0127
118-74-1
Hexachlorobenzene
U128
87-68-3
Hexachlorobutadiene
Ui 30
77—47-4
Hexachlorocyclopentadiene
0131
67-72-1
Hexachloroethane
13132
70-30-4
Hexachlorophene
0243
1888-71-7
Hexachloropropene
0133
302—01—2
Hydrazine
(R,T)
0086
1615—80—1
Hydrazine, 1,2—diethyl—
0098
57—14-7
Hydrazine, l,1—dimethyl—
0099
540-73-8
Hydrazine, 1,2—dimethyl-
13109
122-66—7
Hydrazine, 1,2—diphenyl-
0134
7664—39—3
Hydrofluoric acid
(C,T)
13134
7664-39-3
Hydrogen
fluoride
(C,T)
0135
7783—06—4
Hydrogen
sulfide
117—397

78
13135
7783—06—4
Hydrogen Bulfide H2S
13096
80-15-9
Hydroperoxide, 1—methyl-i-phenylethyl-
(R)
Ui16
96—45—7
2—Imidazolidinethione
13137
193—39—5
Indenoi,2
,
3—cdpyrene
13190
85-44—9
1,3—Isobenzofurandione
U140
78-83—1
Isobutyl alcohol (I,T)
U14l
120—58—i
Iaoaafrole
0142
143—50—0
1(epone
0143
303-34-4
Lasiocarpene
0144
301-04-2
Lead
acetate
Ui46
1335—32-6
Lead,
bis(acetato—0)tetrahydroxytri-
0145
7446-27-7
Lead phosphate
U146
1335—32—6
Lead aubacetate
0129
58-89-9
Lindane
U163
70—25—7
MNNG
U147
108—31—6
Maleic anhydride
0148
123-33—1
Maleic hydrazide
Ul49
109—77-3
Malononitrile
0150
148-82—3
Melphalan
0151
7439—97—6
Mercury
U152
126—98—7
Methacrylonitrile (I,T)
13092
124-40-3
Methanamine, N—methyl-
(I)
0029
74-83-9
Methane, bromo-
13045
74—87—3
Methane,
chloro—
(I,T)
13046
107—30—2
Methane, chloromethoxy-
0068
74-95-3
Methane, dibromo-
0080
75—09-2
Methane, dichloro—
0075
75-71-8
Methane, dichlorodifluoro—
0138
74—88—4
Methane, iodo-
0119
62—50-0
Methanesulfonic acid, ethyl ester
13211
56—23-5
Methane, tetrachloro-
13153
74—93—1
Methanethiol
(I,T)
13225
75-25—2
Methane,
tribromo—
13044
67-66—3
Methane, trichloro—
Ul21
75-69-4
Methane, trichlorofluoro—
0036
57—74—9
4,7—Methano—lH—indene,
1,2,4,5,6,7,8,8—
octachloro—2, 3, 3a, 4,7,7a—hexahydro—
13154
67-56—1
Methanol
(I)
13155
91—80-5
Methapyrilene
U142
143—50-0
1,3,4—Metheno—2H-cyclobutacd—
pentalen—2—one,
1, la, 3, 3a,4, 5,5, 5a,5b,6—decachloro—
octahydro—
0247
72—43—5
Methoxychior
13154
67—56-1
Methyl alcohol
(I)
U029
74—83-9
Methyl bromide
13186
504-60—9
1-Methylbutadiene
(I)
0045
74—87—3
Methyl chloride
(I,T)
Ul56
79-22—1
Methyl chlorocarbonate
(I,T)
U226
71-55—6
Methylchloroform
U157
56—49—5
3—Methylcholanthrene
117—3 98

79
0158
101—14—4
4,4’—Methylenebis(2—chloroaniline)
0068
74-95—3
Methylene bromide
0080
75-09-2
Methylene chloride
Ui59
78—93—3
Methyl ethyl ketone
(MEK)
(I,T)
0160
1338-23—4
Methyl ethyl ketone peroxide
(R,T)
U138
74-88-4
Methyl iodide
0161
108—10-1
Methyl isobutyl ketone
(I)
13162
80—62-6
Methyl methacrylate
(I,T)
U161
108-10-1
4-Methyl—2—pentanone
(I)
13164
56-04-2
Methylthiouracil
0010
50—07—7
Mitomycin C
U059
20830—81—3
5,12—Naphthacenedione,
8—acetyl—10—(3—
amino-2, 3,6-trideoxy)-alpha-L-lyxo-
hexapyranosyl
)
oxyl —7,8,9, iO—tetra-
hydro-6, 8, i1-trihydroxy—i-methoxy-,
(8S—cis)—
0167
134—32-7
1-Naphthalenamine
0168
91—59—8
2—Naphthalenamine
13026
494-03—1
Naphthaleneamine, N,N’—bis(2—chloro—
ethyl)—
13165
91—20-3
Naphthalene
0047
91-58-7
Naphthalene, 2—chloro-
U166
130—15-4
1,4-Naphthalenedione
U236
72-57—1
2,7—Naphthalenedisulfonic acid,
3,3’—
((3,3’—dimethyl—(l, i’—biphenyl—4,4’—
diyl)bis(azo)bia5—amino—4—hydroxy—,
tetrasodium salt
0166
130-15-4
1,4-Naphthoquinone
0167
134-32—7
alpha—Naphthylamine
0168
91-59-8
beta-Naphthylamine
0217
10102—45—1
Nitric acid, thallium
(1+) salt
0169
98—95—3
Nitrobenzene
(I,T)
0170
100-02—7
p—Nitrophenol
0171
79-46—9
2-Nitropropane
(I,T)
0172
924—16-3
N-N itrosodi—n—butylamine
0173
1116-54-7
N-Nitrosodiethanolaxnine
13174
55-18-5
N-Nitrosodiethylaznine
13176
759—73—9
N-Nitroso-N—athylurea
13177
684—93—5
N—Nitroao—N—methylurea
13178
615-53-2
N-Nitroao-N-methylurethane
0179
100-75—4
N—Nitrosopiperidine
Ui80
930—55—2
N-Nitrosopyrrolidine
0181
99-55—8
5—Nitro—o—toluidine
0193
1120—71-4
1,2—Oxathiolane, 2,2—dioxide
13058
50-18—0
2H—i,3,2—Oxazaphosphorin—2—amine,
N,N—
bis
(
2-chioroethyl
)
tetrahydro-, 2-oxide
UliS
75—21—8
Oxirane
(I,T)
Ul26
765—34-4
Oxiranecarboxyaldehyde
0041
106—89-8
Oxirane,
(chloromethyl)—
0182
123—63-7
Paraldehyde
U183
608—93-5
Pentachlorobenzene
13184
76-01—7
Pentachloroethane
117—399

80
13185
82-68-8
Pentachloronitrobenzene
(PCNB)
See F027
87—86-5
Pentachlorophenol
Ub61
108—10—1
Pentanol,
4—methyl—
U186
504—60—9
1,3—Pentadiene
(I)
U187
62-44-2
Phenacetin
0188
108—95—2
Phenol
U048
95—57—8
Phenol,
2—chioro—
U039
59—50—7
Phenol,
4—chloro—3—methyl—
0081
120—83—2
Phenol,
2,4—dichioro—
U082
87-65—0
Phenol,
2,6—dichloro—
U089
56—53—1
Phenol,
4,4’—(1,2—diethyl—1,2—
ethenediyl)bis-,
(B)—
UbOl
105—67—9
Phenol, 2,4—dimethyl—
0052
1319—77—3
Phenol, methyl—
0132
70—30—4
Phenol, 2,2’—methylenebis(3,4,6—tri—
chloro—
Ul70
100—02-7
Phenol,
4-nitro—
See F027
87-86—5
Phenol, pentachloro—
See F027
58-90—2
Phenol,
2,3,4,6—tetrachloro—
See F027
95—95—4
Phenol,
2,4,5—trichloro—
See F027
88—06—2
Phenol, 2,4,6—trichloro—
Ul50
148—82—3
L—Phenylalanine, 4—(bis(2—chloro—
ethyl)amino—
0145
7446—27—7
Phosphoric acid, lead
(2+)
salt
(2:3)
U087
3288—58-2
Phosphorodithioic acid,
0,0—diethyl 5—
methyl ester
U189
1314—80—3
Phosphorus sulfide
(R)
13190
85—44—9
Phthalic anhydride
0191
109—06-8
2—Picoline
0179
100—75-4
Piperidine,
1—nitroso—
0192
23950—58—5
Pronamide
0194
107—10-8
1—Propanamine (I,T)
0111
621—64-7
1-Propanamine, N-nitroso-N—propyl-
0110
142—84-7
l—Propanamine,
N—propyl—
(I)
13066
96-12-8
Propane, i,2—dibromo—3-chloro-
13083
78—87—5
Propane,
1,2—dichloro—
13149
109—77-3
P~opanedinitri1e
0171
79—46—9
Propane, 2—nitro—
(I,T)
0027
108-60—1
Propane, 2,2’—oxybis2—chloro—
See F027
93—72—b
Propanoic acid, 2—(2,4,5—trichloro—
phenoxy)-
0193
1120—71—4
1,3-Propane sultone
U235
126-72—7
i—Propanol,
2,3—dibromo—,
phosphate
(3:1)
U140
78—83—1
1—Propanol,
2—methyl— (I,T)
U002
67—64—1
2—Propanone
(I)
U007
79—06—~1
2—Propenamide
U084
542-75—6
1—Propene,
i,3—dichloro—
U243
1888—71—7
l—Propene, i,1,2,3,3,3—hexachloro—
U009
107—13—1
2—Propenenitrile
U152
126—98—7
2—Propenenitrile, 2—methyl—
(I,T)
0008
79—10—7
2—Propenoic acid
(I)
117—400

81
U113
140—88-5
2—Propenoic acid,
ethyl ester
(I)
0118
97-63-2
2—Propenoic acid,
2—methyl-, ethyl
ester
0162
80-62-6
2—Propenoic acid,
2—methyl-, methyl
ester
(I,T)
See P027
93—72—1
Propionic acid,
2—(2,4,5—trichloro—
phenoxy)
U194
107—10—8
n—Propylamine
(I,T)
U083
78—87-5
Propylene dich.oride
13148
123—33—1
3,6—Pyridazinedione,
1,2-dihydro-
13196
110—86—1
Pyridine
0191
109-06-8
Pyridine,
2—methyl-
U237
66—75—1
2,4—(1H,3H)—Pyrimidiaedione, 5—(bia(2—
chloroethyl)amino
U164
58-04—2
4(1H)—Pyrixnidinone,
2,3—dihydro—6—
methyl-2-thioxo-
U18O
930-55—2
Pyrrolidine, 1—nitroso—
13200
50—55—5
Reserpine
0201
108—46—3
Resorcinol
U202
P 81—07—2
Saccharin and salts
0203
94—59—7
Safrole
0204
7783—00—8
Selenious acid
13204
7783—00—B
Selenium dioxide
0205
7488—56—4
Selenium sulfide
0205
7488—56—4
Selenium sulfide SeS2
(R,T)
13015
115—02—6
L—Serine,
diazoacetate
(ester)
See F027
93—72—1
Silvex
(2,4,5—TP)
0206
18883—66—4
Streptozotocin
0103
77—78-1
Sulfuric acid,
dimethyl ester
U189
1314—80—3
Sulfur phosphide
(R)
See F027
93—76—5
2,4,5—T
U207
95—94-3
1,2,4,5—Tetrachlorobenzene
U208
630—20-6
1,1,1,2—Tetrachloroethane
0209
79-34—5
1,i,2,2—Tetrachloroethane
0210
127—18-4
Tetrachloroethylene
See F027
58—90-2
2,3,4,6—Tetrachlorophenol
0213
109—99—9
Tetrahydrofuran
(I)
13214
563—68—8
Thallium
(I) acetate
U215
6533—73-9
Thallium
(I) carbonate
13216
7791—12—0
Thallium
(I) chloride
U2l6
7791—12—0
Thallium chloride T1C1
U217
10102—45—1
Thallium
(I) nitrate
0218
62-55—5
Thioacetaxnide
0153
74-93—1
Thiomethanol
(I,T)
0244
137—26-8
Thioperoxydicarbonic diamide
((H2N)C(S) 2S2,
tetramethyl—
0219
62-56—6
Thiourea
0244
137—26—8
Thiram
0220
108-88-3
Toluene
0221
25376—45—B
Toluenediamine
0223
26471—62-5
Toluene diisocyanate
(R,T)
U328
95-53-4
o-Toluidine
117—40 1

82
13353
106—49—0
p—Toluidine
0222
636-21-5
o-Toluidine hydrochloride
UOli
61—82—5
1H—1, 2,4—Triazol—3—amine
0227
79—00-5
1,1,2-Trichioroethane
U228
79-01-6
Trichloroethylene
0121
75-69-4
Trichloromonofluoromethane
See F027
95—95—4
2,4,5—Trichiorophenol
See FO27
88—06-2
2,4,6-Trichlorophenol
0234
99—35—4
1,3,5—Trinitrobenzene
(R,T)
13182
123—63—7
1,3,5—Trioxane, 2,4,6—trimethyl—
13235
126—72—7
Tris(2,3—dibromopropyl) phosphate
U236
72—57—1
Trypan blue
U237
66—75—1
Uracil mustard
0176
759—73—9
Urea, N—ethyl—N—nitroao—
13177
684-93-5
Urea, N—methyl—N—nitroso-
U043
75—01—4
Vinyl chloride
U248
P 81-81—2
Warfarin,
and salts, when present at
concentrations of 0.3
or less
13239
1330—20—7
Xylene
(I)
13200
50—55—5
Yohimban—16—carboxylic acid,
11,17—di—
methoxy-18—((3,4, 5-trimethoxybenzoyl
) -
oxy—,
methyl ester,
(3beta, l6beta, l7alpha, i8beta,2oalpha)—
13249
1314—84-7
Zinb phosphide Zn3?2, when present at
concentrations of 10
or less
(Source:
Amended at
15
Ill. Reg.
,
effective
)
117—402

83
Section 721.Appendix C
Chemical Analysis Test Methods
The Board incorporates by reference 40 CFR 261, Appendix III
(1989),
as
amended
at
54
Fed.
Reg.
41407,
October
6,
1989,
and as amended at
55 Fed.
Reg.
8948, March
9,
1990 and at
55 Fed.
Req.
18496, May 2,
1990.
This Section
incorporates
no
future
editions
or
modifications.
(Source:
Amended at
15
Ill.
Reg.
,
effective
)
117—403

84
Section 72l.Appendix G
Basis for Listing Hazardous Wastes
EPA
Hazardous Constitutents for which Listed
Hazardous
Waste No.
FOOl
Tetrachloroethylene,
methylene chloride, trichioroethylene,
1,1,1-tn-
chioroethane, carbon tetrachloride, chlorinated fluorocarbons.
F002
Tetrachloroethylene,
methylene chloride,
trichloroethylene, 1,1,1-tn-
chioroethane,
1,1,2-trichloroethane, chlorobenzene,
1,1,2—trichioro-
1,2,2— tnifluoroethane, ortho—dichlorobenzene,
trichlorofluoromethane.
FOO3
N.A.
FOO4
Cresols and cresylic acid,
nitrobenzene.
F005
Toluene, methyl ethyl ketone,
carbon disulfide,
isobutanol,
pyridine,
2-
ethoxyethanol,
benzene, 2—nitropropane
F006
Cadmium, hexavalent chromium,
nickel, cyanide (complexed).
FOO7
Cyanide (salts).
FOOB
Cyanide (salts).
FOO9
Cyanide (salts).
POlO
Cyanide (salts).
FOil
Cyanide (salts).
FO12
Cyanide (complexed).
FO19
Hexavalent chromium,
cyanide
(complexed).
F020
Tetra- and pentachlorodibenzo-p-dioxins; tetra— and pentachlorodibenzo—
furans; tn—
and tetrachlorophenols and their chlorophenoxy derivative
acids, esters,
ethers,
amines and other salts.
FO21
Penta— and hexachlorodibenzo-p-dioxins; penta- and hexachlorodibenzo-
furans; pentachlorophenol and
its derivatives.
F022
Tetra—,
penta— and hexachlorodibenzo—p—dioxins;
tetra—, penta— and hexa—
chlorodibenzofurans.
F023
Tetra— and pentachlorodibenzo—p-dioxins;
tetra— and pentachlorodibenzo—
furans; tn— and tetra— chlorophenols and their chlorophenoxy derivative
acids,
esters,
ethers,
amines and other salts.
F024
Chloromethane, dichloromethane,
trichloromethane,
carbon tetrachloride,
chioroethylene,
1, 1-dichloroethane,
l,2—dichloroethane,
trans—1,2—di
117—404

85
ch.oroethylene,
1, b—dichloroethylene,
1,1,1—trichloroethane,
1,1,2—tn—
chioroethane,
trichioroethylene,
1,1,i,2—tetrachloroethane,
1,1,2,2—
tetrachloroethane, tetrachloroethylene,
pentachloroethane, hexachloro—
ethane,
allyl chloride (3—chloropropene),
dichioropropane, dichloro—
propene,
2—chloro—i, 3—butadiene,
hexachloro—.
,
3—butadiene, hexachloro—
cyclopentadiene,
hexachlorocyclohoxane, benzene,
chlorobenzene, di—
chlorobenzenes,
1, 2,4—trichlorobenzene,
tetrachlorobenzenes, penta—
chlorobenzene, hexachlorobenzene,
toluene, naphthalene.
F025
Chloromethane, dichloromethane,
tnichloromethane; carbon tetrachloride;
chloroethylene;
1, 1—dichloroethane;
1,2—dichloroethane;
trans—i, 2—di—
chloroethylene;
1, 1—dichloroethylene;
1,1,i—tnichloroethane;
1,1,2—tn—
chloroethane;
trichloroethylene;
1,1,1,2—tetrachloroethane; 1,1,2,2—
tetrachloroethane; tetrachloroethylene;
pentachloroethane; hexachloro-
ethane;
allyl chloride
(3—chioropropene); dichloropropane; dichloro-
propene;
2-chloro—l, 3-butadiene;
hexachloro—1, 3—butadiene; hexachloro—
cyclopentadiene; benzene;
chlorobenzene; dichlorobenzene;
1,2,4—tn—
chlorobenzene; tetrachlorobenzene; pentachlorobenzene; hexachloro—
benzene; toluene;
naphthalene.
P026
Tetra-, penta—,
and hexachlorodibenzo-p—dioxins; tetra—, penta—,
and
hexachlorodibenzofurans.
FO27
Tetra—,
penta—, and hexachlorodibenzo—p—dioxins; tetra—, penta—,
and
hexachlorodibenzofurans; tn-,
tetra-,
and pentachlorophenols and their
chlorophenoxy derivative acids,
esters, ethers,
amine and other salts.
F028
Tetra—, penta—,
and hexachlorodibenzo—p—dioxins; tetra—,
penta—,
and
hexachlorodibenzofurans; tn—,
tetra—,
and pentachlorophenols and their
chlorophenoxy derivative acids,
esters, ethers, amine and other salts.
F039
All constituents for which treatment standards are specified for multi—
source leachate
(wastewaters and non—wastewaters’ under 35 Ill.
Adm.
Code 728.Table
B
(Constituent Concentrations
in Waste~
KOOl
Pentachlorophenol, phenol,
2-chlorophenol,
p-chloro—ni—cresol, 2,4-di—
methylphenol,
2,4—dinitrophenol,
tnichlorophenols, tetrachlorophenols,
2,4—dinitrophenol,
cresosote, chrysene,
naphthalene, fluoranthene,
benzo(b)fluoranthene,
benzo(a)pyrene, indeno(1,2,3—cd)pyrene, benz(a)-
anthracene, dibenz(a)anthracene,
acenaphthalene.
K002
Hexavalent chromium,
lead.
K003
Hexavalent chromium,
lead.
KOO4
Hexavalent chromuim.
K005
Hexavalent chromium,
lead.
K006
Hexavalent chromium.
KOO7
Cyanide
(complexed), hexavalent chromium.
117—405

86
K008
Hexavalent chromium.
KOO9
Chloroform,
formaldehyde, methylene chloride,
methyl chloride,
paraldehyde,
formic acid.
KOlO
Chloroform, formaldehyde, methylene chloride, methyl chloride,
paraldehyde, formic acid,
chloroacetaldehyde.
KO11
Acnylonitrile, acetonitrile,
hydrocyanic acid.
K0i3
Hydro cyanic acid, acrylonitnile, acetonitnile.
K014
Acetonitnile,
acrylamide.
K015
Benzyl chloride,
chlorobenzene,
toluene, benzotnichlonide.
K016
Hexachlorobenzene,
hexachlorobutadiene, carbon tetrachloride,
hexa—
chloroethane, perchloroethylene.
KO17
Epichlorohydrin, chloroethers (bis(chlonomethyl)
ether and bis—(2-
chloroethyl)
ethers), trichloropropane, dichloropropanols.
KO18
1, 2-dichloroethane, trichloroethylene,
hexachlonobutadiene, hexachloro—
benzene.
KO19
Ethylene dichlonide,
I,
i,1—tnichloroethane,
1, i,2—tnichloroethane,
tetrachloroethanes
(1, 1,2, 2—tetrachloroethane and 1,1,1, 2—tetrachioro—
ethane), tnichloroethylene, tetrachioroethylene,
carbon tetrachlonide,
chloroform,
vinyl chloride,
vinylidene chloride.
K020
Ethylene dichlonide,
l,1,1—trichloroethane,
1, 1,2—tnichlonoethane,
tetrachloro-ethanes
(1,i,2,2—tetrachloroethane and 1,b,1,2—tetrachloro—
ethane),
trichloroethylene,
tetrachloroethylene, carbon tetrachlonide,
chloroform,
vinyl chloride, vinylidene chloride.
K021
Antimony,
carbon tetrachloride, chloroform.
K022
Phenol,
tars
(polycyclic aromatic hydrocarbons).
K023
Phthalic anhydride, maleic anhydride.
K024
Phthalic anhydride, 1,4-naphthoguinone.
K025
Meta-dinitrobenzene,
2, 4-dinitrotoluene.
K026
Paraldehyde, pyridines,
2—picoline.
KO27
Toluene diisocyanate,
toluene-2, 4—diamine.
K028
1,1,b—tnichloroethane, vinyl chloride.
117—406

87
K029
i,2-dichloroethane,
l,1,1—tnichloroethane, vinyl chloride, vinylidene
chloride, chloroform.
1(030
Hexachlorobenzene, hexachlorobutadiene,
hexachloroethane,
1,1,1,2—
tetrachloroethane,
1,1,2,2—tetnachloroethane, ethylene dichloride.
1(031
Arsenic.
1(032
Hexachlorocyclopentadiene.
K033
Hexachlorocyclopentadiene.
K034
Hexachlorocyclopentadiene.
K035
Creosote,
chrysene, naphthalene,
fluoranthene, benzo(b)
fluoranthene,
benzo(a)—pyrene,
indeno(1,2,3—cd) pyrene,
benzo(a)anthracene, dibenzo—
(a) anthracene,
acenaphthalene.
Toluene, phosphorodithioic and phosphorothioic acid esters.
Toluene, phosphorodithioic and phosphonothioic acid esters.
Phorate,
formaldehyde,
phosphorodithioic and phosphorothioic acid
esters.
Phosphorodithioic
and
phosphorothioic
acid
esters.
Phorate,
formaldehyde,
phosphorodithioic
and
phosphorothioic
acid
esters.
Toxaphene.
Hexachlorobenzene, ortho-dichlorobenzene.
2, 4—dichlorophenol,
2, 6-dichlorophenol, 2,4,6—tnichlorophenol.
N.A.
N.A.
Lead
N.A.
Hexavalent
chromium,
lead.
Hexavalent chromium,
lead.
Hexavalent chromium.
Hexavalent chromium,
lead.
1(036
1(037
1(03 B
1(039
1(040
K041
1(042
1(043
1(044
1(045
1(046
K04 7
KO48
1(049
1(050
1(051
117—407

88
1(052
Lead
1(060
Cyanide,
naphthalene,
phenolic compounds, arsenic.
1(061
Hexaválent chromium,
lead,
cadmium.
1(062
Hexavalent chromium,
lead.
1(064
Lead,
cadmium
1(065
Lead, cadmium
K066
Lead,
cadmium
KO69
Hexavalent chromium,
lead, cadmium.
1(071
Mercury.
1(073
Chloroform, carbon tetrachlonide, hexachlonoethane, trichloroethane,
tetrachloroethylene, dichloroethylene,
1,1,2,2-tetrachloroethane.
1(083
Aniline, diphenylamine, nitrobenzene, phenylenediamine.
1(084
Arsenic.
K085
Benzene, dichlorobenzenes,
trichlorobenzenes, tetrachlonobenzenes,
pentachlorobenzene,
hexachlorobenzene, benzyl chloride.
1(086
Lead,
hexavalent chromium.
1(087
Phenol, naphthalene.
1(088
Cyanide
(complexes)
1(090
Chromium
1(091
Chromium
1(093
Phthalic anhydride
tnaleic anhydride.
1(094
Phthalic anhydnide.
1(095
1,i,2-tnichlonoethane,
1,l,1,2—tetrachloroethane, 1,1,2,2—tetrachloro—
ethane.
1(096
1,2-dichloroethane,
1,1, 1,—tnichloroethane,
1,1,2—tnichloroethane.
K097
Chlordane, heptachlor.
1(098
Toxaphene.
1(099
2, 4—dichlorophenol,
2,4,6—trichlorophenol.
117—408

89
1(100
Hexavalent chromium,
lead,
cadmium.
KiOl
Arsenic.
1(102
Arsenic.
1(103
Aniline,
nitrobenzene, phenylenediamine.
1(104
Aniline,
benzene, diphenylamine, nitrobenzene,
phynylenediamine.
K105
Benzene, rnonochlorobenzene,
dichlorobenzenes,
2,4,6—trichlonophenol.
1(106
Mercury.
K107
1,i—Dimethylhydrazine
(UDMFfl
1(108
3.,i—Dimethylhydrazine
(UDMH)
1(109
i,l-Dimethylhydrazine
(UDMH~
KilO
1,l-Dimethylhydrazine
(UDMH)
1(111
2, 4—Dinitrotoluene.
1(112
2,4-Toluenediamine,
o—toluidine,
p-toluidine,
aniline.
1(113
2,4-Toluenediamine,
o-toluidine, p-toluidine,
aniline.
1(114
2,4—Toluenediamine,
o-toluidine,
p-toluidine.
1(115
2, 4-Toluenediamine.
1(116
Carbon tetrachloride, tetrachloroethylene,
chloroform,
phosgene.
1(117
Ethylene dibromide
1(118
Ethylene dibromide
K123
Ethylene thiourea
K124
Ethylene thiourea
K125
Ethylene thiourea
1(126
Ethylene thiourea
1(131
Dimethyl sulfate, methyl bromide
1(132
Methyl bromide
1(136
Ethylene dibromide
117—409

90
N.A.-—Waste is hazardous because it fails the test for the characteristic of
ignitability, corrosivity or reactivity.
(Source:
Amended at
15
Ill. Reg.
,
effective
117—4 10

91
TITLE
35:
ENVIRONMENTAL
PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER
I:
POLLUTION CONTROL BOARD
SUBCHAPTER
c:
HAZARDOUS
WASTE OPERATING REQUIREMENTS
PART 722
STANDARDS APPLICABLE TO GENERATORS OF
HAZARDOUS
WASTE
SUBPART A:
GENERAL
Section
722.110
Purpose, Scope and Applicability
722.111
Hazardous Waste Determination
722.112
USEPA Identification Numbers
SUBPART
B:
THE MANIFEST
Section
722.120
General Requirements
722.121
Acquisition of Manifests
722.122
Number of Copies
722.123
Use
of
the
Manifest
SUBPART
C:
PRE-TRANSPORT
REQUIREMENTS
Section
722.130
Packaging
722.131
Labeling
722.132
Marking
722.133
Placarding
722.134
Accumulation Time
SUBPART D:
RECORDKEEPING
AND
REPORTING
Section
722. 140
Recordkeeping
722.141
Annual Reporting
722.142
Exception Reporting
722.143
Additional Reporting
722.144
Special Requirements for Generators of between 100 and 1000
kilograms per month
SUBPART E:
EXPORTS OF HAZARDOUS WASTE
Section
722.150
Applicability
722.151
Definitions
722.152
General Requirements
722.153
Notification
of Intent to Export
722.154
Special Manifest Requirements
722.155
Exception Report
722.156
Annual Reports
722. 157
Recordkeeping
SUBPART
F:
IMPORTS
OF
HAZARDOUS
WASTE
Sect ion
722.160
Imports
of
Hazardous
Waste
117—411

92
SUBPART G:
FARMERS
Section
722.170
Farmers
Appendix A
Hazardous Waste Manifest
AUTHORITY:
Implementing Section 22.4 and authorized by Section 27 of the
Environmental Protection Act
(Ill. Rev.
Stat.
1989,
ch.
111 1/2, pars.
1022.4
and 1027).
SOURCE:
Adopted
in R81—22,
43 PCB 427,
at
5
Ill. Reg. 9781, effective as
noted in 35
Ill.
Adm.
Code 700.106; amended and codified in R81-22,
45 PCB
317,
at 6
Ill. Reg.
4828, effective as noted in 35
Ill.
Adm. Code 700.106;
amended in R82-18,
51 PCB 31,
at
7
Ill.
Reg.
2518,
effective February 22,
1983; amended
in R84—9 at 9
Ill. Reg.
11950, effective July 24,
1985;
amended
in R85—22 at 10 Ill. Reg.
1131, effective January 2,
1986;
amended in R86—i at
10
Ill. Reg.
14112, effective August 12,
1986;
amended in R86—19 at
10 Ill.
Reg.
20709, effective December 2,
1986;
amended in R86—46 at 11 Ill.
Reg.
13555, effective August
4,
1987;
amended in R87—5 at 11
Ill. Reg.
19392,
effective November
12,
1987;
amended in R87—39
at
12
Ill. Reg.
13129,
effective July 29,
1988;
amended in R88—16 at
13
Ill. Reg.
452, effective
December 27,
1988;
amended
in R89-l at
13
Ill.
Reg.
18523, effective November
13,
1989; amended
in R90-10 at
14
Ill. Reg.
,
effective September
25,
1990; amended in R90—ll
at
15
Ill. Reg.
,
effective
SUBPART
A:
GENERAL
Section 722.111
Hazardous Waste Determination
A person who generates
a solid waste,
as defined in
35
Ill.
Adm. Code 721.102,
shall determine if that waste
is
a hazardous waste using the following method:
a)
The person should first determine if the waste
is excluded from
regulation under 35
Ill.
Adm. Code 721.104.
b)
The person should then determine if the waste is listed as a
hazardous waste in 35
Ill. Adm. Code 721.Subpart
B.
(Board Note:
Even if
a waste
is listed, the generator still has
an opportunity under 35
Ill. Adm. Code 720.122 and 40 CFR 260.22
(1986) to demonstrate that the waste from the generator’s
particular facility or operation is not a hazardous waste.
C)
For purposes of compliance with 35
Ill. Adm. Code 728, or if~the
waste is not listed as a hazardous waste in 35
Ill. Adm. Code
721.Subpart
B,
the generator ehouldshall then determine whether
the waste
is identified
in
35 Ill.
Adin.
Code 72l.Subpart C by
either:
117—412

93
1)
Testing the waste according to the methods set forth in 35
Ill.
Adm.
Code 721.Subpart
C, or according to an equivalent
method approved by the Board under 35
Ill.
Adm.
Code
720.120; or
2)
Applying knowledge of the hazard characteristic of the waste
in light of the materials or processes used.
d)
If the generator determines that the waste is hazardous, the
generator shall refer to 35
Ill.
Adm.
Code 724,
725 and 728 for
possible exclusions or restrictions pertaining to the management
of the specific waste.
(Source:
Amended at
15
Ill. Reg.
,
effective
)
SUBPART
C:
PRE-TRANSPORT
REQUIREMENTS
Section 722.134
Accumulation Time
a)
Except as provided in subsections
(d),(e) or
(f),
a generator may
accumulate hazardous waste on—site for 90 days or less without
a
permit or without having interim status provided that:
1)
The waste is placed in containers and the generator complies
with 35
Ill.
Adm. Code 725.Subpart I or the waste is placed
in tanks and the generator complies with
35
Ill.
Adm.
Code
725.Subpart J except
35
Ill.
Adxn.
Code 725.297(c) and
725.300.
In addition,
such a generator is exempt from all
the requirements
in 35
Ill.
Adm.
Code 725.Subparts C and H,
except for 35
Ill.
Adin.
Code 725.211 and 725.214;
2)
The date upon which each period of accumulation begins
is
clearly marked and visible for inspection on each container;
3)
While being accumulated on—site, each container and tank is
labeled on marked clearly with the words,
“Hazardous Waste”,
and
4)
The generator complies with the requirements for owners or
operators in 35
Ill.
Adm.
Code 725.Subparts C and D~
~i~t4
with 35
Ill.
Adm.
Code 725.116 and 728.1O7(a~(4).
b)
A generator who accumulates hazardous waste for more than 90 days
is an operator of
a storage facility and
is subject to the
requirements of
35 Ill.
Adm.
Code 724 and 725 and the
permit
requirements of
35
Ill. Adm. Code 702, 703 and 705 unless the
generator has been granted an extension of the 90—day period.
If
hazardous wastes must remain on—site for longer than 90 days due
to unforeseen,
temporary, and uncontrollable circumstances, the
generator may seek an extension of up to 30 days by means of a
variance or provisional variance,
pursuant to Section 37 of the
Environmental Protection Act.
117—413

94
c)
Accumulation near point of generation.
1)
A generator may accumulate as much as
55 gallons of
hazardous waste or one quart of acutely hazardous waste
listed
in 35 Ill.
Adm.
Code 721.133(e)
in containers at or
near any point of generation where wastes initially
accumulate, which is under the control of the operator of
the process generating the waste, without
a permit or
interim status and without complying with paragraph
(a)
provided the generator:
A)
Complies with
35 Ill.
Adm.
Code 725.271,
725.272 and
725.273(a); and
B)
marks the generator’s containers either with the words
“Hazardous Waste” or with other words that identify
the contents of the containers.
2)
A generator who accumulates either hazardous waste or
acutely hazardous waste listed in 35 Ill. Adm. Code
721.133(e)
in excess of the amounts listed in subsection
(c)(1)
at or near any point of generation must, with respect
to that amount of excess waste,
comply within three days
with subsection
(a)
or other applicable provisions of this
chapter.
During the three day period the generator must
continue to comply with subsection
(c)(1).
The generator
must mark the container holding the excess accumulation of
hazardous waste with the date the excess amount began
accumulating.
d)
A generator who generates greater than 100 kilograms but less than
1000 kilograms of hazardous waste in a calendar month may
accumulate hazardous waste on—site for 180 days or less without a
permit or without having interim status provided that:
1)
The quantity of waste accumulated on—site never exceeds 6000
kilograms;
2)
The generator complies with the requirements of 35 Ill.
Adm.
Code 725.Subpart
I,
except the generator need not comply
with 35
Ill.
Adm.
Code 725.276;
3)
The generator complies with the requirements of
35
Ill.
Adm.
Code 725.301;
4)
The generator complies with the requirements of subsections
(a)(2)
and
(a)(3)
and the requirements of
35 Ill.
Adxn. Code
725.Subpart C;
and
5)
The generator complies with the following requirements:
117—414

95
A)
At all times there must be at least one employee
either on the premises or on call
(i.e., available to
respond
to an emergency by reaching the facility
within a short period of time) with the responsibility
for coordinating all emergency response measures
specified in subsection (d)(4)(D).
The employee is
the emergency coordinator.
B)
The generator shall poet the following
information
next to the telephone:
i)
The
name
and telephone number
of the emergency
coordinator:
ii)
Location of fire extinguishers and spill control
material,
and
if present,
fire alarm: and
iii)
The telephone number of the fire department,
unless the facility has a direct alarm.
C)
The generator shall ensure that all employees are
thoroughly
familiar
with proper waste handling and
emergency procedures, relevant to their
responsibilities during normal
facility operations and
emergencies:
D)
The emergency coordinator or designee shall respond to
any emergencies that arise.
The applicable responses
are as follows:
1)
In
the
event
of a fire,
call the fire department
or attempt to extinguish it using a fire
extinguisher:
ii)
In
the
event
of
a spill,
contain the flow of
hazardous waste to the extent possible, and as
soon as
is practicable,
clean up the hazardous
waste and any contaminated materials or soil:
iii)
In the event of a fire, explosion or other
release which could threaten human health
outside the facility or when the generator has
knowledge that a spill has reached surface
water,
the generator shall immediately notify
the National Response Center (using
its 24-hour
toll free number 800/424—8802).
The report must
include the following information:
the name,
address and USEPA identification number
(35
Ill.
Adm. Code 722.112) of the generator; date, time
and type of incident
(e.g.,
spill or fire);
quantity
and
type
of hazardous waste involved
in
the incident;
extent of injuries,
if any; and,
117—415

96
estimated quantity and disposition of
recoverable materials, if any.
e)
A generator who generates greater than 100 kilograms but less than
1000 kilograms of hazardous waste in a calendar month and who must
transport the waste, or offer the waste for transportation, over a
distance of 200 miles or more for off—site treatment,
storage or
disposal may accumulate hazardous waste on—site for 270 days or
less without a permit or without having interim status provided
that the generator complies with the requirements of subsection
(d).
f)
A generator who generates greater than 100 kilograms but leBs than
1000 kilograms of hazardous waste in a calendar month and who
accumulates hazardous waste
in quantities exceeding 6000 kg or
accumulates hazardous waste for more than 180 days
(or for more
than 270 days
if the generator must transport the waste,
or offer
the waste for transportation, over
a distance of 200 miles or
more)
is an operator of a storage facility and is subject to the
requirements of
35
Ill. Adm.
Code 724 and 725 and the permit
requirements of
35
Ill.
Adm.
Code 703 unless the generator has
been granted an extension to the 180—day (or 270—day
if
applicable) period.
If
hazardous wastes must remain on—site for
longer than 180 days
(or 270 days
if applicable) due to
unforeseen, temporary and uncontrollable circumstances, the
generator may seek an extension of up to 30 days by means of
variance or provisional variance pursuant to Section 37 of the
Environmental Protection Act.
(Source:
Amended
at
15
Ill.
Reg.
,
effective
)
117—4 16

97
TITLE
35:
ENVIRONMENTAL
PROTECTION
SUBTITLE
G:
WASTE
DISPOSAL
CHAPTER
I:
POLLUTION CONTROL BOARD
SUBCHAPTER
C:
HAZARDOUS
WASTE OPERATING REQUIREMENTS
PART 724
STANDARDS
FOR
OWNERS
AND
OPERATORS
OF
HAZARDOUS
WASTE
TREATMENT, STORAGE AND DISPOSAL FACILITIES
SUBPART
A:
GENERAL
PROVISIONS
Section
724.101
Purpose, Scope and Applicability
724.103
Relationship to Interim Status Standards
SUBPART B:
GENERAL FACILITY STANDARDS
Section
724.110
Applicability
724.111
Identification Number
724.112
Required Notices
724.113
General Waste Analysis
724.114
Security
724.115
General Inspection Requirements
724.116
Personnel Training
724.117
General Requirements for Ignitable,
Reactive or Incompatible
Wastes
724.118
Location
Standards
SUBPART
C:
PREPAREDNESS
AND
PREVENTION
Section
724.130
Applicability
724.131
Design
and
Operation
of
Facility
724.132
Required Equipment
724.133
Testing
and
Maintenance
of
Equipment
724.134
Access
to
Communications
or
Alarm
System
724.135
Required
Aisle
Space
724.137
Arrangements
with
Local
Authorities
SUBPART
B:
CONTINGENCY
PLAN
AND
EMERGENCY PROCEDURES
Sect ion
724.150
Applicability
724.151
Purpose and Implementation of Contingency Plan
724.152
Content of Contingency Plan
724.153
Copies
of
Contingency
Plan
724.154
Amendment of Contingency Plan
724.155
Emergency Coordinator
724.156
Emergency
Procedures
SUBPART
E:
MANIFEST
SYSTEM, RECORDKEEPING
AND
REPORTING
Section
724.170
Applicability
724.171
Use
of
Manifest
System
724.172
Manifest
Discrepancies
117—4 17

98
724.173
Operating Record
724.174
Availability,
Retention and Disposition of Records
724.175
Annual Report
724.176
Unmanifested Waste Report
724.177
Additional Reports
SUBPART F:
RELEASES FROM SOLID WASTE MANAGEMENT UNITS
Sect ion
724.190
Applicability
724.191
Required Programs
724.192
Groundwater Protection Standard
724.193
Hazardous Constituents
724.194
Concentration Limits
724.195
Point of Compliance
724.196
Compliance Period
724.197
General Groundwater Monitoring Requirements
724.198
Detection Monitoring Program
724.199
Compliance Monitoring Program
724.200
Corrective Action Program
724.201
Corrective Action for Solid Waste Management Units
SUBPART C:
CLOSURE AND POST-CLOSURE
Section
724.210
Applicability
724.211
Closure Performance Standard
724.212
Closure Plan;
Amendment of Plan
724.213
Closure; Time Allowed For Closure
724.214
Disposal or Decontamination of Equipment, Structures and Soils
724.215
Certification of Closure
724.216
Survey Plat
724.217
Post—closure Care and Use of Property
724.218
Post—closure Plan; Amendment of Plan
724.219
Post—closure Notices
724.220
Certification of Completion of Post—closure Care
SUBPART
H:
FINANCIAL REQUIREMENTS
Section
724.240
Applicability
724.241
Definitions of Terms As Used In This Subpart
724.242
Cost Estimate for Closure
724.243
Financial Assurance for Closure
724.244
Cost Estimate for Post—closure Care
724.245
Financial Assurance for Post—closure Care
724.246
Use of
a Mechanism for Financial Assurance of Both Closure and
Post—closure Care
724.247
Liability Requirements
724.248
Incapacity
of
Owners
or Operators, Guarantors or Financial
Inst itutions
724.251
Wording of the Instruments
117—418

99
SUBPART
I:
USE
AND
MANAGEMENT OF CONTAINERS
Section
724.270
Applicability
724.271
Condition of Containers
724.272
Compatibility of Waste With Container
724.273
Management of Containers
724.274
Inspections
724.275
Containment
724.276
Special Requirements for Ignitable or Reactive Waste
724.277
Special Requirements for Incompatible Wastes
724.278
Closure
SUBPART
J:
TANK SYSTEMS
Section
724.290
Applicability
724.291
Assessment of Existing Tank System’s Integrity
724.292
Design and Installation of New Tank Systems or Components
724.293
Containment and Detection of Releases
724.294
General Operating Requirements
724.295
Inspections
724.296
Response to Leaks or Spills and Disposition of Leaking or
urifit—
for—use Tank Systems
724.297
~Closure and Post—Closure Care
724.298
Special Requirements for Ignitable or Reactive Waste
724.299
Special Requirements for Incompatible Wastes
724.300
Special Requirements for Hazardous Wastes F020, P021,
P022,
F023,
F026 and P027
SUBPART K:
SURFACE IMPOUNDMENTS
Section
724.320
Applicability
724.321
Design and Operating Requirements
724.322
Double—lined Surface Impoundments:
Exemption from Subpart
F:
Ground—water Protection Requirements (Repealed)
724.326
Monitoring and Inspection
724.327
Emergency Repairs; Contingency Plans
724.328
Closure and Post-closure Care
724.329
Special Requirements for Ignitable or Reactive Waste
724.330
Special Requirements for Incompatible Wastes
724.331
Special Requirements for Hazardous Wastes F020, P021, P022,
P023,
FO26 and P027
SUBPART L:
WASTE PILES
Section
724.350
Applicability
724.351
Design and Operating Requirements
724.352
Double-lined Piles:
Exemption from Subpart F:
Ground—water
Protection Requirements
(Repealed)
724.353
Inspection of Liners:
Exemption from Subpart
F:
Ground—water
Protection Requirements
(Repealed)
724.354
Monitoring and Inspection
724.356
Special Requirements for Ignitable or Reactive Waste
117—419

100
724.357
Special Requirements for Incompatible Wastes
724.358
Closure and Post-closure Care
724.359
Special Requirements for Hazardous Wastes F020,
F021, P022,
P023,
FO26 and F027
SUBPART M:
LAND
TREATMENT
Section
724.370
Applicability
724.371
Treatment Program
724.372
Treatment Demonstration
724.373
Design and Operating Requirements
724.376
Food—chain Crops
724.378
Unsaturated Zone Monitoring
724.379
Recordkeeping
724.380
Closure and Post—closure Care
724.381
Special Requirements for Ignitable or Reactive Waste
724.382
Special Requirements for Incompatible Wastes
724.383
Special Requirements for Hazardous Wastes FO2O,
F021,
F022, F023,
F026 and FO27
SUBPART
N:
LANDFILLS
Section
724.400
Applicability
724.401
Design and Operating Requirements
724.402
Double—lined Landfills:
Exemption from Subpart F:
Ground—water
Protection Requirements
(Repealed)
724.403
Monitoring and Inspection
724.409
Surveying and Recordkeeping
724.410
Closure and Post—closure Care
724.412
Special Requirements for Ignitable or Reactive Waste
724.413
Special Requirements for Incompatible Wastes
724.414
Special Requirements for Bulk and Containerized Liquids
724.415
Special Requirements for Containers
724.416
Disposal of Small Containers of Hazardous Waste in Overpacked
Drums
(Lab Packs)
724.417
Special Requirements for Hazardous Wastes F02O, FO21,
F022,
F023,
F026 and F027
SUBPART
0:
INCINERATORS
Section
724.440
Applicability
724.441
Waste Analysis
724.442
Principal Organic Hazardous Constituents
(POHC8)
724.443
Performance Standards
724.444
Hazardous Waste Incinerator Permits
724.445
Operating Requirements
724.447
Monitoring and Inspections
724.451
Closure
SUBPART X:
MISCELLANEOUS UNITS
Section
724.701
Applicability
117—4 20

101
724.701
Environmental Performance Standards
724.702
Monitoring, Analysis,
Inspection,
Response, Reporting and
Corrective Action
724.703
Post—closure Care
SUBPART AA:
AIR EMISSION STANDARDS
FOR
PROCESS
VENTS
Section
724.930
Applicability
724.931
Definitions
724.932
Standards:
Process Vents
724.933
Standards:
Closed-vent Systems and Control Devices
724.934
Test methods and procedures
724.935
Recordkeeping reguirements
724.936
Reporting Rrequirements
SUBPART BB:
AIR EMISSION STANDARDS FOR EQUIPMENT LEAKS
Section
724.950
Applicability
724.951
Definitions
724.952
Standards:
Pumps
in Light Liquid Service
724.953
Standards:
Compressors
724.954
Standards:
Pressure Relief Devices in Gas/Vapor Service
724.955
Standards:
Sampling Connecting Systems
724.956
Standards:
Open—ended Valves or Lip~B
724.957
Standards:
Valves in Gas/Vapor or Light Liquid Service
724.958
Standards:
Pumps, Valves. Pressure Relief Devices and Other
Connectors
724.959
Standards:
Delay of Repair
724.960
Standards:
Closed—vent
Systems and Control Devices
724.961
Alternative Percentage Standard for Valves
724.962
Skip Period Alternative for Valves
724.963
Test Methods and Procedures
724.964
Recordkeeping Requirements
724.965
Reporting Requirements
Appendix A
Recordkeeping Instructions
Appendix B
EPA Report Form and Instructions
(Repealed)
Appendix D
Cochran’s Approximation to the Behrens-Pisher Student’s T-Test
Appendix E
Examples of Potentially Incompatible Waste
Appendix
I
Groundwater Monitoring List
AUTHORITY:
Implementing Section 22.4 and authorized by Section 27 of the
Environmental Protection Act
(Ill. Rev.
Stat.
1989,
ch.
ill
1/2, pars.
1022.4
and 1027).
SOURCE:
Adopted
in R82—19,
53 PCB
131, at 7
Ill.
Reg. 14059,
effective
October
12,
1983;
amended in R84—9 at 9
Ill. Reg.
11964,
effective July 24,
1985;
amended
in R85—22 at 10
Ill.
Reg.
1136,
effective January 2,
1986;
amended
in R86-l at
10
Ill. Reg.
14119, effective August
12,
1986;
amended in
R86—28
at
11
Ill.
Reg.
6138, effective March 24,
1987; amended in R86—28 at
11
Ill.
Reg. 8684,
effective April 21,
1987;
amended in R86—46 at
11
Ill.
Reg.
13577, effective August
4,
1987;
amended
in R87—5 at 11
Ill. Reg.
19397,
117—42 1

102
effective November
12,
1987;
amended in R87—39
at 12
Ill. Reg.
13135,
effective July 29,
1988;
amended in R88—16 at
13
Ill. Reg.
458, effective
December 28,
1988;
amended in R89—1 at 13 Ill. Reg.
18527, effective November
13,
1989; amended
in R90—2 at
14
Ill.
Reg.
14511, effective August 22,
1990;
amended
in R90-10 at 14
Ill. Reg.
16658, effective September 25,
1990;
amended
in R90—11 at 15
Ill.
Reg.
,
effective
SUBPART B:
GENERAL
FACILITY
STANDARDS
Section 724.113
General Waste Analysis
a)
Analysis:
1)
Before an owner or operator treats,
stores or disposes of
any hazardous waste, or non—hazardous waste if applicable
under Section 724.213(d),
the owner or operator shall obtain
a detailed chemical and physical analysis of
a
representative sample of the waste.
At
a minimum, this
analysis must contain all the information which must be
known to treat,
store or dispose of the waste in accordance
with the requirements of this Part or 35
Ill. Adm. Code 728,
or with the conditions of
a permit issued under
35
Ill. Adm.
Code
702,
703 and 705.
2)
The analysis may include data developed under 35
Ill.
Adm.
Code 721, and existing published or documented data on the
hazardous waste or on hazardous waste generated from similar
processes.
BOARD NOTE:
For example,
the facility’s records of analyses
performed on the waste before the effective date of these
regulations,
or studies conducted on hazardous waste
generated from processes similar to that which generated the
waste to be managed at the facility,
may be included
in the
data base required to comply with subsection
(a)(1).
The
owner or operator of an off—site facility may arrange for
the generator of the hazardous waste to supply part or all
of the information required by subsection
(a)(1). except as
otherwise specified in 35
Ill. Adm.
Code 728.1071b~and
(C).
If the generator does not supply the information, and the
owner or operator chooses to accept a hazardous waste, the
owner or operator is responsible
for obtaining the
information required to comply with this Section.
3)
The analysis must be repeated as necessary to ensure that
it
is accurate and up to date.
At a minimum, the analysis must
be repeated:
A)
When the owner or operator is notified, or has reason
to believe, that the process or operation generating
117—422

103
the hazardous waste,
or non—hazardous waste
if
applicable under Section 724.213(d),
has changed; and
B)
For off-site facilities, when the results of the
inspection required in subsection (a)(4) indicate that
the hazardous waste received at the facility does not
match the waste designated on the accompanying
manifest or shipping paper.
4)
The owner or operator of an off—site facility shall inspect
and,
if necessary, analyze each hazardous waste movement
received at the facility to determine whether
it matches the
identity of the waste specified on the accompanying manifest
or shipping paper.
b)
The owner or operator shall develop and follow a written waste
analysis plan which describes the procedures which
it
will carry
out to comply with subsection
(a).
The owner or operator shall
keep this plan at the facility.
At a minimum, the plan must
specify:
1)
The parameters for which each hazardous waste,
or non—
hazardous waste
if
applicable under Section 724.213(d), will
be analyzed and the ratIonale for the selection of these
parameters
(i.e.,
how analysis
for these parameters will
provide sufficient information on the waste’s properties to
comply with subsection
(a)).
2)
The test methods which will be used to test for these
parameters.
3)
The sampling method which will be used to obtain a
representative sample of the waste to be analyzed.
A
representative sample may be obtained using either:
A)
One of the sampling methods described in
35
Ill.
Adm.
Code 721.Apperidix A;
or
B)
An equivalent sampling method.
BOARD
NOTE:
See 35
Ill.
Adm.
Code 720.121 for related
discussion.
4)
The frequency with which the initial analysis of the waste
will be reviewed or repeated to ensure that the analysis is
accurate and up to date.
5)
For off—site facilities, the waste analyses that hazardous
waste generators have agreed to supply.
6)
Where applicable, the methods which will be used to meet the
additional waste analysis requirements for specific waste
117—423

104
management methods as specified in Sections 724.117,
724.414.~and 724.441, 724.934~d)and 724.963(d),
and 35
Ill.
Adm.
Code 728.107.
And,
7)
For surface impoundments exempted from land disposal
restrictions under 35 Ill.
Adin.
Code 728.104(a), the
procedures and schedules
for:
A)
The sampling of impoundment contents;
B)
The analysis of teBt data; and,
C)
The annual removal of residues which are not deliated
under 35
Ill.
Adm.
Code 720.122 or which exhibit a
characteristic of hazardous waste,
and either:
i)
Do not meet applicable treatment standards of
35
Ill.
Adm.
Code 728.Subpart
D; or
ii)
Where no treatment standards have been
established:
Such residues are prohibited from
land disposal under
35
Ill.
Adm.
Code 728.132 or
728.139;
or such residues are prohibited from
land disposal under 35
Ill.
Adm.
Code
728.133(f).
C)
For off-Bite facilities,
the waste analysis plan required in
subsection
(b) must also specify the procedures which will be used
to inspect and,
if necessary, analyze each movement of hazardous
waste received at the facility to ensure that
it matches the
identity of the waste designated on the accompanying manifest or
shipping paper.
At
a minimum, the plan must describe:
1)
The procedures which will be used to determine the identity
of each movement of waste managed at the facility; and
2)
The sampling method which will be used •to obtain a
representative sample of the waste to be identified,
if the
identification method includes sampling.
BOARD
NOTE:
35
Ill.
Adm. Code 703, requires that the waste
analysis plan be submitted with Part B of the
permit
application.
(Source:
Amended at 15
Ill.
Reg.
,
effective
Section 724.115
General
Inspection Requirements
a)
The owner or operator shall conduct inspections often enough to
identify problems in time to correct them before they harm human
health or the environment.
The owner or operator shall
inspect
117—424

105
the facility for malfunctions and deterioration, operator errors
and discharges which may be causing, or may lead to:
1)
Release of hazardous waste constituents to the environment;
or
2)
A threat to human health.
b)
Inspection schedule.
1)
The owner or operator shall develop and follow a written
schedule for inspecting monitoring equipment,
safety and
emergency equipment, security devices and operating and
structural equipment
(Such as dikes and sump pumps) that are
important to preventing, detecting or responding to
environmental or human health hazards.
2)
The owner or operator shall keep this schedule at the
facility.
3)
The schedule must identify the types of problems
(e.g.,
malfunctions or deterioration) which are to be looked for
during the inspection
(e.g.,
inoperative sump pump,
leaking
fitting,
eroding dike, etc.).
4)
The frequency of inspection may vary for the items on the
schedule.
However,
it should be based on the rate of
possible deterioration of the equipment and the probability
of an environmental or
human
health incident
if the
deterioration, malfunction or any operator error goes
undetected between inspections.
Areas
subject to spills,
such as loading and unloading areas, must be inspected daily
when in use.
At
a minimum, the inspection schedule must
include the terms and frequencies called for in Sections
724.274,
724.294,
724.326,
724.353,
724.354,
724.403,
724.447k and 724.702,
724.933,
724.952,
724.953 and 724.958,
where applicable.
BOARD
NOTE:
35
Ill.
Adm.
Code 703 requires the inspection
schedule to be submitted with Part
a
of the permit
application.
The Agency will evaluate the schedule along
with
the
rest
of
the
application
to
ensure
that
it
adequately protects human health and the environment.
As
part of this review, the Agency may modify or amend the
schedule as may be necessary.
c)
The owner or operator shall remedy any deterioration or
malfunction of equipment or structures which the
inspection
reveals on a schedule which ensures that the problem does not lead
to an environmental or human health hazard.
Where a hazard
is
imminent or has already occurred,
remedial action must be taken
immediately.
117—425

106
d)
The owner or operator shall record inspections
in an inspection
log or summary.
The owner or operator shall keep these records
for at least three years from the date of inspection.
At
a
minimum, these records must include the date and time of the
inspection,
the name of the inspector,
a notation of the
observations made and the date and nature of any repairs or other
remedial actions.
(Source:
Amended at 15
Ill.
Reg.
,
effective
)
SUBPART E:
MANIFEST SYSTEM, RECORDKEEPING
AND
REPORTING
Section 724.173
Operating Record
a)
The owner or operator shall keep a written operating record at the
facility.
b)
The following information must be recorded, as it becomes
available,
and maintained in the operating record until closure of
the facility:
1)
A description and the quantity of each hazardous waste
received, and the methodor methods and date or dates of its
treatment,
storage or disposal at the facility as required
by Appendix A;
2)
The location of each hazardous waste within the facility and
the quantity at each location.
For disposal facilities,
the
location and quantity of each hazardous waste must be
recorded on a map or diagram of each cell or disposal area.
For all facilities,
this information must include cross—
references to specific manifest document numbers,
if the
waste was accompanied by
a manifest;
BOARD NOTE:
See Section 724.219 for related requirements.
3)
Records and results of waste analyses performed as specified
in Sections 724.113,
724.117, 724.4l4~.and 724.441,
724.934,
724.963, and
in 35
Ill.
Adm. Code 728.104(a) and 728.107;
4)
Summary reports and details of all incidents that require
implementing the contingency plan as specified in Section
724.156(j);
5)
Records and results of inspections as required by Section
724.115(d)
(except these data need to be kept only three
years);
6)
Monitoring, testing or analytical data and corrective action
where required by Subpart F or Sections 724.326,
724.353,
117—426

107
724.354,
724.376,
724.378,
724.380,
724.403,
724.409,
724.447~,.e?—724.702.
724.934(c) through
(f).
724.935,
724.963(d) through
(i)
or 724.964.
7)
For off—site facilities,
notices to generators as specified
in Section 724.112(b);
8)
All closure cost estimates under Section 724.242 and,
for
disposal
facilities,
all
post—closure
cost
estimates
under
Section
724.244;
9)
A
certification
by
the
permittee,
no
less
often
than
annually:
that the permittee has
a program in place to
reduce
the
volume
and
toxicity
of
hazardous
waste
that
the
permittee
generates,
to
the
degree
the
permittee
determines
to
be
economically
practicable;
and
that
the
proposed
method
of treatment, storage or disposal
is that practicable method
currently
available
to
the
permittee
which
minimizes
the
persent and future threat to human health and the
environment;
10)
Records of the quantities
(and date of placement) for each
shipment of hazardous waste placed in land disposal units
under an extension of the effective date of any land
disposal restriction granted pursuant to 35 Ill.
Adm.
Code
728.105,
a petition pursuant to 35 Ill.
Adm.
Code 728.106 or
a certification under
35
Ill.
Adm.
Code 728.108, and the
applicable notice required of
a generator under 35
Ill.
Adm.
Code 728.107(a);
11)
For an off—site treatment facility,
a copy of the notice,
and the certification and demonstration,
if applicable,
required of the generator or the owner or operator under
35
Ill.
Adm.
Code 728.107 or 728.108;
12)
For an on—site treatment facility, the information contained
in the notice (except the manifest number), and the
certification and demonstration,
if applicable, required of
the generator or the owner or operator under 35
Ill.
Adm.
Code 728.107 or 728.108;
13)
For an off—site land disposal facility, a copy of the
notice,
and the certification and demonstration,
if
applicable, required of the generator or the
owner
or
operator
of
a
treatment
facility
under
35
Ill.
Adm.
Code
728.107
or
728.108,
whichever
is
applicable;
and
14)
For an on—site land disposal facility, the information
contained
in
the
notice
required
of
the
generator
or
owner
or operator of a treatment facility under 35
Ill.
Adm.
Code
728.107, except
for the manifest number,
and the
117—427

108
certification
and
demonstration
if
applicable,
required
under 35
Ill. Adm.
Code 728.108, whichever is applicable.
15)
For an off-site storage facility,
a copy of the notice, and
the certification and demonstration if applicable, required
of the generator or the owner or operator under 35 Ill.
Adni.
Code 728.107 or 728.108; and,
16)
For an on—site storage facility, the information contained
in the notice (except the manifest number), and the
certification and demonstration if applicable, required of
the generator or the owner or operator under 35 Ill.
Adm.
Code 728.107 or 728.108.
(Source:
Amended at
15
Ill.
Reg.
,
effective
Section 724.177
Additional Reports
In addition to submitting the annual report and unmanifeated waste reports
described
in Sections 724.175 and 724.176, the owner or operator muatshall
also report to the Agency:
a)
Releases,
fires and explosions
as specified in Section 724.156(j);
b)
Facility closures specified in Section 724.215;
and
C)
As otherwise required by Subparts
r
and K NF, K throuch
N,
AA and
BB.
(Source:
Amended at
15
Ill. Reg.
,
effective
SUBPART K:
SURFACE IMPOUNDMENTS
Section 724.321
Design and Operating Requirements
a)
Any s&urface impoundment that
it not covered by subsection
(C)
or
35
Ill.
Adm. Code 725.321 must have a liner for all portions of
the impoundment
(except
for existing portions of such
impoundment).
The liner must be designed,
constructed and
installed to prevent any migration of wastes out of the
impoundment
to the adjacent subsurface soil or ground
watergroundwater or surface water at any time during the active
life (including the closure period) of the impoundment.
The liner
may be constructed of materials that may allow wastes to migrate
into
the
liner
(but
not
into
the
adjacent
subsurface
soil
or
~
or surface water)
during the active life
of
the
facility,
provided
that
the
impoundment
is
closed
in
accordance with Section 724.328(a)(l).
For impoundments that will
be closed in accordance with Section 724.328(a)(2), the liner must
be
constructed
of
materials
that
can
prevent
wastes
from
migrating
into the liner during the active life of the facility.
The liner
must be:
117—428

109
1)
Constructed of materials that have appropriate chemical
properties and sufficient strength and thickness to prevent
failure due to pressure gradients (including static head and
external hydrogeologic forces), physical contact with the
waste or leachate to which they are exposed, climatic
conditions, the stress of installation and the stress of
daily operation;
2)
Placed upon a foundation or base capable of providing
support to the liner and resistance to pressure gradients
above and below the liner to prevent failure of the liner
due to settlement, compression or uplift; and
3)
Installed to cover all surrounding earth likely to be in
contact with the waste or leachate.
b)
The owner or operator will be exempted from the requirements of
subsection
(a)
if the Board finds, based on a demonstration by the
owner or operator,
in a variance and/or site—specific rulemaking,
that alternate design and operating practices,
together with
location characteristics, will prevent the migration of any
hazardous constituents
(see Section 724.193)
into the ground
~
or surface water at any future time.
In deciding
whether to grant an exemption, the Board.will consider:
1)
The nature and quantity of
the wastes;
2)
The proposed alternate design and operation;
3)
The hydrogeologic setting of the facility,
including the
attenuative capacity and thickness of the liners and soils
present between the impoundment and ~
or surface water;
and
4)
All other factors which would influence the quality and
mobility of the leachate produced and the potential for it
to migrate to ~
ter or surface water.
C)
The owner or operator of each new surface impoundment, each new
surface impoundment unit at an existing facility, each replacement
of
an existing surface impoundment unit and each lateral expansion
of an existing surface impoundment unit, must install two or more
liners and a leachate collection system between Buch liners.
The
liners and leachate collection
system must protect human health
and the environment.
The requirements of this subsection shall
apply with respect to all waste received after the issuance of the
permit
for units where Fart B of the permit application is
received by the Agency or USEPA after November
8,
1984.
The
requirement for the installation of two or more liners in this
subsection may be satisfied by the installation of a top liner
designed~operated and constructed of materials to prevent the
117—429

110
migration
of any constituent into such liner during the period
such facility remains in operation
(including any post—closure
monitoring period),
and a lower liner designed,
operated and
constructed to prevent the migration of any constituent through
such
liner
during
such
period.
For
the
purpose
of
the
preceding
sentence,
a lower liner shall be deemed to satisfy such
requirement
if it
is constructed of at least a 3—foot thick layer
of recompacted clay or other natural material with a permeability
of no more than 1 x l0~ centimeter per second.
d)
Subsection
(C)
will not apply if the owner or operator
demonstrates to the Agency and the Agency finds for such surface
impoundment,
that
alternative
design
and
operating
practices,
together with location characteristics, will prevent the migration
of any hazardous constituent
into the
~
or
surface water at least as effectively as such liners and leachate
collection systems.
e)
The double liner requirement set forth in subsection
(c) may be
waived by the Agency for any monofill,
if:
1)
The monofill contains only hazardous wastes from foundry
furnace emission controls or metal casting molding sand, and
such wastes do not contain constituents which would render
the wastes hazardous
for reasons other than the EP—toxicity
characteristice in 35 Ill.
Adm. Code 721.124; ~
2)
Design and location.
A)
Liner,
location and groundwater monitoring.
i)
The monofill has at least one liner for which
there
is no evidence that such liner is leaking.
For the purposes of this subsection, the term
“liner” means
a liner designed,
constructed,
installed and operated to prevent hazardous
waste from passing into the liner at any time
during the active life of the facility, or a
liner designed, constructed,
installed and
operated to prevent hazardous waste from
migrating beyond the liner to adjacent
subsurface soil,
groundwater or surface water at
any time during the active life of the facility.
In the case of any surface impoundment which has
been exempted from the requirements of
subsection
(C)
on the basis of a liner designed,
constructed,
installed and operated to prevent
hazardous waste from passing beyond the liner,
at the closure of such impoundment, the owner or
operator must remove or decontaminate all waste
residues,
all contaminated liner material and
contaminated
soil,
to
the
extent
practicable.
If
117—430

111
all contaminated soil is not removed or
decontaminated, the owner or operator of such
impoundment
will
comply
with
appropriate
post-
closure requirements,
including but not limited
to groundwater monitoring and corrective action;
ii)
The
monof ill
is
located
more
than
one—quarter
mile from an underground source of drinking
water
(as that term is defined in 35 Ill. Adm.
Code 702.110 and
iii)
The monofill is in compliance with generally
applicable ~
monitoring
requirements for facilities with
permits
or
B)
FtCflA
The
owner
or
operator
demonstrates
to
the
Board
that
the monofill is located, designed and operated so as
to assure that there will be no migration of any
hazardous
constituent
into
~
or
surface water at any future time.
f)
A surface impoundment must be designed,
constructed, maintained
and operated to prevent overtopping resulting from normal or
abnormal operations; overfilling;
wind and wave action;
rainfall;
run—on; malfunctions of level controllers,
alarms and other
equipment; and human error.
g)
A surface impoundment must have dikes that are designed,
constructed and maintained with sufficient structural integrity to
prevent massive failure of the dikes.
In ensuring structural
integrity,
it must not be presumed that the liner system will
function without leakage during the active life of the unit.
h)
The Agency will specify in the permit all design and operating
practices
that
are
necessary
to
ensure
that
the
requirements
of
this Section are satisfied.
(Source:
Amended at 15
Ill. Reg.
,
effective
)
Section 724.329
Special Requirements for Ignitable or Reactive Waste
Ignitable or reactive waste must not be placed in a surface
impoundment,
unless the waste and impoundment satisfy all applicable requirements of
35
Ill. Adm.
Code 728,
and:
a)
The waste is treated,
rendered or mixed before or immediately
after placement
in the impoundment
so that:
117—43 1

112
1)
The resulting waste, mixture or dissolution of material no
longer meets the definition of ignitable or reactive waste
under 35
Ill.
Adm.
Code 721.121 or 721.123;
and
2)
Section 724.117(b)
is complied with; or
b)
The waste is managed in such a way that it is protected from any
material or conditions which may cause it to ignite or react; or
c)
The surface impoundment is used solely for emergencies.
(Source:
Amended at
15 Ill. Reg.
,
effective
)
SUBPART L:
WASTE PILES
Section 724.356
Special Requirements for Ignitable or Reactive Waste
Ignitable or reactive waste must not be placed
in
a waste pile,
unless the
waste and waste pile satisfy all applicable requirements of
35
Ill.
Adm. Code
728,
and:
a)
The waste
is treated,
rendered or mixed before or immediately
after placement in the pile so that:
1)
The resulting waste, mixture or dissolution of material no
longer meets the definition of ignitable or reactive waste
under
35
Il.
Mm. Code 721.121 or 721.123;
and
2)
Section 724.117(b)
is complied with;
or
b)
The waste
is managed
in such a way that it
is protected from any
material
or
conditions
which
may
cause
it
to
ignite
or
react.
(Source:
Amended
at
15
Ill.
Reg.
,
effective
SUBPART
M:
LAND
TREATMENT
Section
724.381
Special
Requirements
for
Ignitable
or
Reactive
Waste
The
owner
or operator must not apply ignitable or reactive waste to the
treatment zone, unless the waste and and the treatment
zone satisfy all
applicable requirements of
35
Ill. Adm. Code
728,
and:
a)
The waste is immediately incorporated into the soil so that:
1)
The resulting waste, mixture or dissolution of material no
longer
meets
the
definition
of
ignitable
or
reactive
waste
under 35
Ill. Adm. Code 721.121 or 721.123; and
2)
Section 724.117(b)
is complied with;
or
117—43 2

113
b)
The waste
is managed in such a way that it is protected from any
material or conditions which may cause it to ignite or react.
(Source:
Amended at 15
Ill. Reg.
,
effective
)
SUBPART N:
LANDFILLS
Section 724.401
Design and Operating Requirements
a)
Any landfill that is not covered by subsection
(C) or 35
Ill. Adm.
Code 725.401(a) must have a liner Bystem for all portions of the
landfill (except for existing portions of such landfill).
The
liner system must have:
1)
A liner that
is designed,
constructed and installed to
prevent any migration of wastes out of the landfill to the
adjacent subsurface soil or groundwater or surface water at
any time during the active life (including the closure
period)
of the landfill.
The liner must be constructed of
materials that prevent wastes from passing into the liner
during the active life of the facility.
The liner must be:
A)
Constructed of materials that have appropriate
chemical properties and sufficient strength and
thickness to prevent failure due to pressure gradients
(including static head and external hydrogeologic
forces), physical contact with the waste or leachate
to which they are exposed,
climatic conditions, the
stress of installation and the stress of daily
operation;
B)
Placed upon a foundation or base capable of providing
support to the liner and resistance to pressure
gradients above and below the liner to prevent failure
of the liner due to settlement,
compression or uplift;
and
C)
Installed to cover all surrounding earth likely to be
in contact with the waste or leachate;
and
2)
A leachate collection and removal system immediately above
the liner that
is designed,
constructed, maintained and
operated to collect and remove leachate from the landfill.
The Agency will specify design and operating conditions in
the permit to ensure that the leachate depth over the liner
does not exceed 30 cm
(one foot).
The leachate collection
and removal system must be:
A)
Constructed of materials that are:
117—433

114
i)
Chemically resistant to the waste managed in the
landfill and the leachate expected to be
generated;
and
ii)
Of sufficient strength and thickness to prevent
collapse under the pressures exerted by
overlying wastes, waste cover materials and by
any equipment used at the landfill;
and
B)
Designed and operated to function without clogging
through the scheduled closure of the landfill.
b)
The owner or operator will be exempted from the requirements of
subsection
(a)
if the Board finds, based on a demonstration by the
owner or operator,
in a variance and/or site—specific rulemaking,
that alternative design and operating practices, together with
location characteristics, will prevent the migration of any
hazardous constituents
(see Section 724.193)
into the groundwater
or surface water at any future time.
In deciding whether to grant
an exemption, the Board will consider:
1)
The nature and quantity of the wastes;
2)
The proposed alternate design and operation;
3)
The hydrogeologic Betting of the facility,
including the
attenuative capacity and thickness of the liners and soils
present between the landfill and groundwater or surface
water;
and
4)
All other factors which would influence the quality and
mobility of the leachate produced and the potential
for it
to migrate to groundwater or surface water.
c)
The owner or oprator of each new landfill,
each new landfill unit
at an existing facility, each replacement of an existing landfill
unit and each lateral expansion of an existing landfill unit, must
install two or more liners and a leachate collection system
above
and between the liners.
The liners and leachate collection
systems must protect human health and the environment.
This
subsection applies with respect to all waste received after
issuance of the permit for units where Part
B of the
permit
application is received by the Agency or USEPA after November 8~
1984.
The requirement
for the installation of two or more liners
in this subsection may be satisfied by the installation of a top
liner designed,
operated and constructed of materials to prevent
the migration of any constituent into such liner during the period
such facility remains
in operation (including any post—closure
monitoring period),
and a lower liner designed,
operated and
constructed to prevent the migration of any constituent through
such liner during such period.
For the purpose of the preceding
sentence,
a lower liner shall be deemed to satisfy such
117—434

115
requirement
if
it
is constructed
of
at least a 3—foot thick layer
of recompacted clay or other natural material with a permeability
of no more than
1
x ~
centimeter per second.
d)
Subsection
(c)
will not apply
if the owner or operator
demonstrates to the Agency, and the Agency finds for such
landfill, that alternative design and operating practices,
together with location characteristics, will prevent the migration
of any hazardous constituent into the groundwater or surface water
at least
as effectively
as such liners and leachate collection
systems.
e)
The double liner requirement set forth in subsection
(c) be waived
by the Agency for any monofill,
if:
1)
The monofill contains only hazardous wastes
from
foundry
furnace emission controls or metal casting molding sand,
and
such wastes do not contain constituents which would render
the wastes hazardous for reasons other than the toxicity
characteristic in
35 Ill. Adm.
Code 721.124, with USEPA
hazardous waste numbers D004 through D017;
and
2)
No migration demonstration.
A)
Design and location requirements.
i)
The monofill has at least one liner for which
there
is no evidence that such liner
is leaking.
ii)
The monofill
is located more than one—quarter
mile from an underground source of drinking
water
(as that term is defined in 35
Ill.
Adm.
Code
702.110.
iii)
The monofill is in compliance with generally
applicable groundwater monitoring requirements
for facilities with
RCRA
permits; or
B)
The owner or operator demonstrates to the Board that
the monof ill
is located, designed and operated so as
to assure that there will be no migration of any
hazardous
constituent into groundwater or surface
water at any future time.
f)
The owner or operator must design,
construct, operate and maintain
a run—on control system capable of
preventing flow onto the active
portion of the landfill during peak discharge from at least a 25-
year storm.
g)
The owner or operator must design,
construct, operate and maintain
a run—off management system to collect and control at
least the
water volume resulting from a 24 hour, 25—year storm.
117—435

116
h)
Collection and holding facilities
(e.g., tanks or basins)
associated with run—on and run-off control systems must be
emptied
or otherwise managed expeditiously after storms to maintain design
capacity of the system.
i)
If the landfill contains any particulate matter which may be
subject to wind dispersal,
the owner or operator must cover or
otherwise manage the landfill to control wind dispersal.
j)
The Agency will specify in the permit all design and operating
practices that are necessary to ensure that the requirements of
this Section are satisfied.
(Source:
Amended at 15
Ill. Reg.
,
effective
)
Section 724.412
Special Requirements for Ignitable or Reactive Waste
a)
Except as provided in paragraphsubsection
(b)
and in Section
724.416,
ignitable or reactive waste must not be placed in a
landfill, unless the waste and landfill meet all applicable
requirements of
35
Ill.
Adm. Code
728,
and the waste is treated,
rendered or mixed before or immediately after placement in a
landfill so that:
1)
The resulting waste, mixture or dissolution of material no
longer meets the definition of ignitable or reactive waste
under
35
111.
Adm. Code 721.121 or 721.123;
and
2)
Section 724.117(b)
is complied with.
b)
-lExcept for prohibited wastes which remain subiect to treatment
standards in 35
Ill. Adm.
Code.Subpart D,
ignitable waste
in
containers may be landfilled without meeting the requirements of
paragraphsubsection
(a)
provided that the wastes are disposed of
in such a way that they are protected from any material or
conditions which may cause-them to ignite.
At a minimum,
ignitable wastes must be disposed of in non—leaking containers
which are carefully handled and placed so as to avoid heat,
sparks,
rupture or any other condition that might cause ignition
of the wastes; must be covered daily with soil or other non—
combustible material to minimize the potential for ignition of the
wastes; and must not be disposed of in cells that contain or will
contain other wastes which may generate heat sufficient to cause
ignition
of
the
waste.
(Source:
Amended at
15
Ill.
Reg.
,
effective
)
117—436

117
Section 724.416
Disposal of Small Containers of Hazardous Waste in
Overpacked Drums (Lab Packs)
Small containers of hazardous waste in overpacked drums
(lab packs) may be
placed in a landfill if the following requirements are met:
a)
Hazardous waste must be packaged in non—leaking inside containers.
The inside containers must be of a design and constructed of a
material that will not react dangerously with, be decomposed by or
be ignited by the contained waste.
The inside containers must be
tightly and securely sealed.
The inside containers must be of the
size and type specified in the Department of Transportation
(DOT)
hazardous materials regulations (49 CFR 173, 178 and 179),
if
those regulations specify
a particular inside container for the
waste.
b)
The inside containers must be overpacked in an open head DOT—
specification metal shipping container (49 CFR 178 and 179) of no
more than 416 liter
(110 gallon) capacity and surrounded by, at a
minimum,
a sufficient quantity of absorbent material to completely
absorb all of the liquid contents of the inside containers.
The
metal outer container must be full after packing with inside
containers and absorbent material.
C)
In accordance with Section 724.117(b),
the absorbent material used
must not be capable of reacting dangerously with, being decomposed
by or being ignited by the contents of the inside containers.
d)
Incompatible waste,
as defined in 35 Ill. Adm. Code 720.110, must
not be placed in the same outside container.
e)
Reactive wastes, other than cyanide- or sulfide—bearing waste as
defined in 35
Ill. Adm. Code 721.123(a) (5), must be treated or
rendered non—reactive prior to packaging in accordance with
paragraphsubsections
(a)
through
(d).
Cyanide- and sulfide—
bearing reacitve waste may be packed in accordance with
paragrapheubsections
(a) through
(d) without first being treated
or rendered non—reactive.
~J,,
Such disposal
is
in compliance with 35 Ill. Adm. Code 728.
Persons who incinerate lab packs according to
35 Ill. Mm.
Code
728.142(c) (1) may use fiber drums in place of metal outer
containers.
Such fiber drums must meet the DOT specifications
in
49 CFR 173.12 and be overpacked according to the requirements of
subsection
(b).
g)
Pursuant to 35
Ill. Adm. Code 729.312, the use of labpacks for
disposal of liquid wastes or wastes containing free liquids
allowed under this Section is restricted to labwaste and non—
periodic waste,
as those terms are defined in that Part.
(Source:
Amended at
15
Ill. Reg.
,
effective
117—437

118
SUBPART AR:
AIR EMISSION
STANDARDS
FOR PROCESS
VENTS
Section 724.930
Applicability
a)
This Subpart applies to owners and operators of facilities that
treat,
store or dispose of hazardous wastes (except as provided in
Section 724.101).
b)
Except for Sections 724.934(d) and 724.935(e), this Subpart
applies to process vents associated with distillation,
fractionation, thin—film evaporation, solvent extraction,
or air
or steam stripping operations that manage hazardous wastes with
organic concentrations of at least
10
ppmw
(parts
per
million by
weight),
if these operations are conducted in:
1)
Units that are subject to the permitting requirements of 35
Ill.
Adm.
Code 703; or
2)
Hazardous waste recycling units that are located on
hazardous waste management facilities otherwise subject to
the permitting requirements of 35
Ill. Mm. Code 703.
C)
If the owner or operator of process vents subject to the
requirements of Sections 724.932 through 724.936 has received a
RCRA
permit prior to December 21,
1990,
the requirements of
Sections 724.932 through 724.936 must be incorporated when the
permit
is reissued under 35 Ill. Mm.
Code 705.201 or reviewed
under
35 Ill. Mm.
Code 702.161.
BOARD
NOTE:
The requirements of Sections 724.932 through 724.936
apply to process vents on hazardous waste recycling units
previously exempt under 35 Ill.
Adm.
Code 721.106(c)(1).
Other
exemptions under 35
Ill. Mm.
Code 721.104, 722.134 and 724.101(g)
are
not affected by these requirements.
(Source:
Added at 15
Ill. Reg.
,
effective
Section 724.931
Definitions
As used in this Subpart,
all terms not defined in the Subpart have the meaning
given them
in the Resource Conservation and Recovery Act and 35
Ill.
Adsi.
Code
720 through 726.
Air stripping operation
is a desorption operation employed to
transfer one or more volatile components from a liquid mixture
into a gas
(air) either with or without the application of heat to
the liquid.
Packed towers,
spray towers and bubble—cap, sieve, or
valve—type plate towers are among the process configurations used
for contacting the air and
a liquid.
117—438

119
Bottoms receiver means
a container or tank used to receive and
collect the heavier bottoms fractions of the distillation feed
stream that remain in the liquid phase.
BTU means British thermal unit.
Closed—vent system means a system that is not open to the
atmosphere and that is composed of piping, connections,
and,
if
necessary, flow—inducing devices that transport gas or vapor from
a piece or pieces of equipment to a control device.
Condenser means
a heat—transfer device that reduces a
thermodynamic fluid from its vapor phase to its liquid phase.
Connector means flanged, screwed, welded or other joined fittings
used to connect two pipelines or
a pipeline and a piece of
equipment.
For the purposes of reporting and recordkeeping,
connector means flanged fittings that are not covered by
insulation or other materials that prevent location of the
fittings.
Continuous recorder means
a data—recording device recording an
instantaneous data value at least once every 15 minutes.
Control device means an enclosed combustion device,
vapor recovery
system, or flare.
Any device the primary function of which is the
recovery or capture of solvents or other organics for use, reuse,
or sale
(e.g.,
a primary condenser on
a solvent recovery unit)
is
not a control device.
Control device shutdown means the cessation of operation of a
control device for any purpose.
Distillate receiver means a container or tank used to receive and
collect liquid material
(condensed) from the overhead condenser of
a distillation unit and from which the condensed liquid
is pumped
to larger storage tanks or other process units.
Distillation operation means an operation, either batch or
continuous,
separating one or more feed stream(s)
into two or more
exit streams, each exit stream having component concentrations
different from those
in the feed stream(s).
The separation is
achieved by the redistribution of the components between the
liquid
and
vapor
phase
as
they
approach
equilibrium
within
the
distillation unit.
Double block and bleed system means two block valves connected in
series with
a bleed valve or line that can vent the line between
the two block valves.
Equipment
means
each
valve,
pump,
compressor, pressure relief
device,
sampling connection system, open—ended valve or line,
or
117—439

120
flange,
and any control devices or systems required by this
Subpart.
Flame zone means the portion of the combustion chamber in a boiler
occupied by the flame envelope.
Flow indicator means a device that indicates whether gas flow is
present in a vent stream.
First attempt at repair means to take rapid action for the purpose
of stopping or reducing leakage of organic material to the
atmosphere using best practices.
Fractionation operation means a distillation operation or method
used to separate a mixture of several volatile components of
different boiling points in successive stages,
each stage removing
from the mixture some proportion of one of the components.
ft means foot.
h means hour.
Hazardous waste management unit shutdown means
a work practice or
operational procedure that stops operation of a hazardous waste
management unit or part of a hazardous waste management unit.
An
unscheduled work practice or operational procedure that stops
operation of a hazardous waste management unit or part of a
hazardous waste management unit for less than 24 hours
is not
a
hazardous waste management unit shutdown.
The use of spare
equipment and technically feasible bypassing of equipment without
stopping operation are not hazardous waste management unit
shutdowns.
Hot well means a container for collecting condensate as in a steam
condenser serving a vacuum—jet or steam—jet ejector.
In gas—vapor service means that the piece of equipment contains or
contacts
a hazardous waste stream that
is in the gaseous state at
operating conditions.
In heavy liquid service means that the piece of equipment
is not
in gas/vapor service or in light liquid service.
In light liquid service means that the piece of equipment contains
or contacts
a waste stream where the vapor pressure of one or more
of the components
in the stream
is greater than 0.3 kilopascals
(kPa) at 20 C, the total concentration of the pure components
having
a vapor pressure greater than 0.3 kPa at 20 C is equal to
or greater than 20 percent by weight,
and the fluid is a liquid
at
operating conditions.
117—440

121
In situ sampling systems means nonextractive samplers on in—line
samplers.
In vacuum service means that equipment
is operating at an internal
pressure that is at least 5 kPa below ambient pressure.
Kg means kilogram.
kPa means kilopascals.
lb means pound.
m means meter.
Mg means Megagrams,
or metric tonnes.
MJ means Megajoules,
or ten to the sixth Joules.
MW means Megawatts.
Malfunction means any sudden failure of a control device or a
hazardous waste management unit or failure of
a hazardous waste
management unit to operate in
a normal or usual manner, so that
organic emissions are increased.
Open—ended valve or line means any valve,
except pressure relief
valves,
having one side of the valve seat in contact with process
fluid and one side open to the atmosphere, either directly or
through open piping.
ppmv means parts per million by volume.
ppmw meant parts per million by weight.
Pressure release means the emission of materials resulting from
the system pressure being greater than the set pressure of the
pressure relief device.
Process heater means
a device that transfers heat liberated by
burning fuel to fluids contained in tubes, including all fluids
except water that are heated to produce steam.
Process vent means any open—ended pipe or stack that is vented to
the atmosphere either directly,
through a vacuum—producing system,
or through a tank (e.g.,
distillate receiver,
condenser, bottoms
receiver,
surge control tank,
separator tank,
or hot well)
associated with hazardous waste distillation,
fractionation, thin—
film evaporation, solvent extraction, or air or steam stripping
operations.
Repaired means that equipment is
adjusted, or otherwise altered,
to eliminate a leak.
117—44 1

122
s means second.
scm means standard cubic meter.
scft meant standard cubic foot.
Sensor means a device that measures a physical quantity or the
change in
a physical quantity,
such as temperature,
pressure,
flow
rate,
pH, or liquid level.
Separator tank means a device used for separation of two
immiscible liquids.
Solvent extraction operation means an operation or method of
separation in which a solid or solution is contracted with a
liquid solvent
(the two being mutually insoluble) to
preferentially dissolve and transfer one or more components into
the solvent.
Startup means the setting
in operation of
a hazardous waste
management unit or control device for any purpose.
Steam stripping operation means
a distillation operation in which
vaporization of the volatile constituents of a liquid mixture
takes place by the introduction of steam directly in to the
charge.
Surge control tank means
a large—sized pipe or storage reservoir
sufficient to contain the surging liquid discharge of the process
tank to which
it is connected.
Thin—film evaporation operation means
a distillation operation
that employs a heating surface consisting of
a large diameter tube
that may be either straight or tapered,
horizontal or vertical.
Liquid
is spread on the tube wall by a rotating assembly of blades
that maintain a close clearance from the wall or actually ride on
the film of liquid on the wall.
Vapor incinerator means any enclosed combustion device that
is
used for destroying organic compounds and does not extract energy
in the form of steam or process heat.
Vented means discharged through an opening, typically an open-
ended pipe or stack,
allowing the passage of a stream of liquids,
gases, or fumes into the atmosphere.
The passage of liquids,
gases,
or fumes is caused by mechanical means such as compressors
or vacuum—producing
systems or by process—related means such as
evaporation produced by heating and not caused by tank loading and
unloading
(working losses) or by natural means such as diurnal
temperature changes.
117—442

123
yr means year.
(Source:
Added at
15 Ill. Reg.
,
effective
Section 724.932
Standards: Process Vents
a)
The owner or operator of a facility with process vents associated
with distillation, fractionation, thin-film evaporation, solvent
extraction, or air or steam stripping operations managing
hazardous wastes with organic concentrations of at least 10
ppmw
shall either:
1)
Reduce total organic emissions
from
all affected process
vents at the facility below 1.4
kg/h
(3
lb/h)
and
2.8
Mg/yr
(3.1 tons/yr); or
2)
Reduce, by use of
a control device, total organic emissions
from all affected process vents at the facility by
95 weight
percent.
b)
If the owner or operator installs a closed—vent system and control
device to comply with the provisions of subsection
(a),
the
closed—vent system and control device must meet the requirements
of Section 724.933.
c)
Determinations of vent emissions and emission reductions or total
organic compound concentrations achieved by add—on control devices
must be either based on engineering calculations or performance
tests.
If performance tests are used to determine vent emissions,
emission reductions,
or total organic compound concentrations
achieved by add-on control devices, the performance tests must
conform with the requirements of Section 724.934(c).
d)
When an owner or operator and the Agency do not agree on
determinations of vent emissions or emission reductions or total
organic compound concentrations achieved by add—on control devices
based on engineering calculations, the procedures
in Section
724.934(c) must be used to resolve the disagreement.
(Source:
Added at 15 Ill. Reg.
,
effective
)
Section 724.933
Standards: Closed—vent Systems and Control Devices
a)
Compliance Required.
1)
Owners or operators of closed—vent systems and control
devices used to comply with provisions of this Part shall
comply with the provisions of this Section.
2)
The owner or operator of an existing facility who cannot
install
a closed—vent system and control device to comply
with the provisions of this Subpart on the effective date
117—443

124
that the facility becomes subject to the provisions of this
Subpart shall prepare an implementation schedule that
includes dates by which the closed—vent system and control
device will be installed and in operation.
The controls
must be
installed as soon as possible,
but
the
implementation schedule may allow up to 18 months after the
effective date that the facility becomes subject to this
Subpart for installation and startup.
All units that begin
operation after December 21,
1990, must comply with the
rules immediately (i.e., must have control devices installed
and operating on startup of the affected unit); the 2-year
implementation schedule does not apply to these units.
b)
A control device involving vapor recovery (e.g., a condenser or
adsorber) must be designed and operated to recover the organic
vapors vented to it with an efficiency of 95 weight percent or
greater unless the total organic emission limits of Section
724.932(a)(1)
for all affected process vents
is attained at an
efficiency less than 95 weight percent.
c)
An enclosed combustion device
(e.g.,
a vapor incinerator, boiler
or process heater) must be designed and operated to reduce the
organic emissions vented to it by 95 weight percent or greater; to
achieve a total organic compound concentration of 20 ppmv,
expressed as the sum of the actual compounds, not carbon
equivalents, on a dry basis corrected to
3 percent oxygen; or to
provide a minimum residence time of
0.50 seconds at
a minimum
temperature
of
760 C.
If a boiler or process heater is used as
the control device, then the vent stream must be introduced into
the flame zone of the boiler or process heater.
d)
Flares
1)
A flare must be designed for and operated with no visible
emissions as determined by the methods specified in
subsection (e)(1)
except
for periods not to exceed a total
of
5 minutes during any
2
consecutive hours.
2)
A flare must be operated with a flame present at all times,
as determined by the methods specified in subsection
(f) (2) (c).
3)
A flare must be used only if the net heating value of the
gas being combusted is 11.2 MJ/scm (300 Btu/scf)
or greater
if the flare
is steam—assisted or air—assisted;
or if the
net heating value of the gas being combusted is 7.45 143/scm
(200 Btu/scf) or greater
if the flare is nonassisted.
The
net heating value of the gas being combusted must be
determined by the methods specified in subsection
(e)(2).
4)
Exit Velocity.
117—444

125
A)
A steam—assisted or nonassisted flare must be designed
for an operated with an exit velocity,
as determined
by the methods specified in subsection
(e)(3), less
than 18.3
rn/s
(60 ft/a),
except as provided in
subsections
(d)(4)(B) and
(C).
B)
A steam—assisted or nonassisted flare designed for and
operated with
an
exit
velocity,
as
determined
by
the
methods specified
in subsection (e)(3), equal to or
greater than 18.3 m/s
(60 ft/a)
but less than 122
rn/a
(400 ft/s)
is allowed if the net heating value of the
gas
being
combuated
is
greater
than
37.3
143/scm
(1000
Btu/Bcf).
C)
A
steam—assisted
or
nonassisted
flare
designed
for
and
operated with an exit velocity,
as determined by the
methods specified in subsection (e)(3),
less than the
velocity, V as determined by the method specified in
subsection
(e)(4) and less than 122
rn/s (400 ft/s)
is
allowed.
5)
An air—assisted flare must be designed and operated with an
exit velocity less than the velocity, V as determined by the
method specified in subsection
(e)(5).
6)
A flare used to comply with this Section must be steam-
assisted,
air—assisted or nonasaisted.
e)
1)
Reference Method 22 in 40 CFR 60,
incorporated by reference
in 35
Ill.
Adm. Code 720.111, must be used to determine the
compliance of
a flare with the visible emission provisions
of this Subpart.
The observation period is 2 hours and must
be used according to Method 22.
2)
The net heating value of the gas being combusted in a flare
must be calculated using the following equation:
H
=
K
*
SUM(Ci
*
Hi)
Where:
H is the net heating value of the sample in 143/scm;
where the net enthalpy per mole of offgas is based on
combustion
at
25
C
and
760
mm
Hg,
but
the
standard
temperature for determining the volume corrersponding
to 1 mole
is 20 C.
K
=
1.74 E —7
(l/ppm)(g mol/scm)(MJ/kcal)
where
standard temperature for
(g mol/scm) 20 C.
StJM(Xi) means the sum of the values of X for each
component
i,
from
i=1
to
n.
117—445

126
Ci is the concentration of sample component i in ppm
on a wet basis,
as measured for organics by Reference
Method 18 in 40 CFR 60,
and for carbon monoxide,
by
ASTH D1946,
incorporated by reference in 35
Ill.
Adzn.
Code 720.111.
Hi
is the net heat of combustion of sample component
i,
kcal/gmol at 25 C and 760 mm Mg.
The heats of
combustion must be determined using ASTM D2382,
incorporated by reference in
35 Ill. Adm. Code
720.111,
if published values are not available or
cannot be calculated.
3)
The actual exit velocity of
a flare must be determined by
dividing the volumetric flow rate (in units of standard
temperature and pressure),
as determined by Reference
Methods 2,
2A,
2C,
or 2D in 40 CFR 60,
incorporated by
reference in 35 Ill. Adm. Code 720.111,
as appropriate,
by
the unobstructed
(free) cross—sectional area of the flare
tip.
4)
The maximum allowed velocity in rn/a,
V for a flare complying
with subsection (d)(4)(C) must be determined by the
following equation:
LOG(V)
=
(H
+
28.8)
/
31.7
Where:
LOG
means
logarithm
to
the base 10
H
is the net heating value as determined in subsection
(e) (2).
5)
The maximum allowed velocity in rn/a,
V
for an air—assisted
flare must be determined by the following equation:
V
=
8.706
+
0.7084H
Where:
H is the net heating value as determined in subsection
(e) (2)
f)
The owner or operator shall monitor and inspect each control
device required to comply with this Section to ensure proper
operation and maintenance of the control device by implementing
the following requirements:
1)
Install,
calibrate, maintain and operate according to the
manufacturer’s specifications a flow indicator that provides
117—44 6

127
a record of stream flow from each affected process vent to
the control device at least once every hour.
The flow
indicator sensor must be installed in the vent stream at the
nearest feasible point to the control device inlet but
before the point at which the vent streams are combined.
2)
Install,
calibrate, maintain and operate according to the
manufacturer’s specifications a device to continuously
monitor control device operation as specified below:
A)
For a thermal vapor incinerator,
a temperature
monitoring device equipped with a continuous recorder.
The device must have accuracy of ~ 1 percent of the
temperature being monitored
in C or
±
C, whichever is
greater.
the temperature sensor must be installed at
a location in the combustion chamber downstream of the
-combustion
zone.
B)
For a catalytic vapor incinerator,
a temperature
monitoring device equipped with a continuous recorder.
The device must be capable of monitoring temperature
at two locations and have an accuracy of ±1 percent
of the temperature being monitored in C or ±0.5
C,
whichever
is greater.
One temperature sensor must be
installed in the vent stream at the nearest feasible
point to the catalyst bed inlet and a second
temperature sensor must be installed in the vent
stream
at the nearest feasible point to the catalyst
bed outlet.
C)
For a flare,
a heat sensing monitoring device equipped
with a continuous recorder that indicates the
continuous ignition of the pilot flame.
D)
For
a boiler or process heater having a design heat
input capacity less than 44 MW,
a temperature
monitoring device equipped with a continuous recorder.
The device must have an accuracy of
±
1 percent of the
temperature being monitored in C or
+
0.5
C, whichever
is greater.
The temperature sensor must be installed
at a location in the furnace downstream of the
combustion
zone.
E)
For a boiler or process heater having a design heat
input capacity greater than or equal to 44 MW,
a
monitoring device equipped with a continuous recorder
to measure a parameter(s)
that indicates good
combustion operating practices are being used.
F)
For a condenser,
either:
117—447

128
i)
A monitoring device equipped with a continuous
recorder to measure the concentration level of
the organic compounds in the exhaust vent stream
from the condenser;
or
ii)
A temperature monitoring device equipped with
a
continuous recorder.
The device must be capable
of monitoring temperature at two locations and
have an accuracy of ±1 percent of the
temperature being monitored in C or ±0.5 C,
whichever is greater.
One temperature sensor
must be installed at
a location in the exhaust
vent stream from the condenser, and a second
temperature sensor must be installed at a
location in the coolant fluid exiting the
condenser.
G)
For
a carbon adsorption system that regenerates the
carbon bed directly in the control device such as a
fixed—bed carbon adsorber, either:
i)
A monitoring device equipped with a continuous
recorder to measure the concentration level of
the organic compounds
in the exhaust vent stream
from the carbon bed, or
ii)
A monitoring device equipped with a continuous
recorder to measure a parameter that indicates
the carbon bed
is regenerated on a regular,
predetermined time cycle.
3)
Inspect
the readings from each monitoring device required by
subsection
(f)(1)
and
(2)
at least once each operating day
to check control device operation and,
if necessary,
immediately implement the corrective measures necessary to
ensure the control device operates in compliance with the
requirements of this Section.
g)
An owner or operator using a carbon adsorption system such as a
fixed-bed carbon adsorber that regenerates the carbon bed directly
onsite in the control device shall replace the existing carbon in
the control device with fresh carbon at a regular, predetermined
time interval that
is no longer than the carbon service life
established as a requirement of Section 724.935(b)(4) (C) (vi).
h)
An owner or operator using
a carbon adsorption system such as a
carbon canister that does not regenerate the carbon bed directly
onsite
in the control device shall replace the existing carbon in
the control device with fresh carbon on a regular basis by using
one of the following procedures:
117—448

129
1)
Monitor the concentration level of the organic compounds in
the exhaust vent stream from the carbonadsorption system on
a regular schedule,
and replace the existing carbon with
fresh carbon immediately when carbon breakthrough is
indicated.
The monitoring frequency must be daily or at an
interval no greater than 20 percent of the time required to
consume the total carbon working capacity established as a
requirement
of Section .724.935(b) (4) (C) (vii), whichever is
longer.
2)
Replace the existing carbon with fresh carbon at a regular,
predetermined time interval that is less than the design
carbon replacement interval established as a requirement of
Section 724.935(b) (4) (C(vii).
i)
An alternative operational or process parameter may be monitored
if the operator demonstrates that the parameter will ensure that
the control device is operated in conformance with these standards
and the control device’s design specifications.
j)
An owner or operator of an affected facility seeking to comply
with the provisions of this Part by using a control device other
than
a thermal vapor
incinerator, catalytic vapor incinerator,
flare,
boiler,
process heater,
condenser or carbon adsorption
system
is required to develop documentation including sufficient
information to describe the control device operation and identify
the process parameter or parameters that indicate proper operation
and maintenance of the control device.
k)
Closed vent systems.
1)
Closed—vent systems must be designed for and operated with
no detectable emissions,
as indicated by an instrument
reading of less than 500 ppm above background and by visual
inspections,
as determined by the methods specified at
Section 724.934(b).
2)
Closed—vent systems must be monitored to determine
compliance with this Section during the initial leak
detection monitoring,
which must be conducted by the date
that the facility becomes Bubject to the provisions of this
Section annually,
and at other times as specified in the
RCRA
permit.
3)
Detectable emissions,
as
indicated by an instrument reading
greater than 500 ppm and visual inspections, must be
controlled as soon as practicable,
but not later than 15
calendar days after the emission is detected.
4)
A first attempt at repair must be made no later than
5
calendar days after the emission is detected..
117—449

130
1)
Closed—vent systems and control devices used to comply with
provisions of this Subpart must be operated at all times when
emissions may be vented to them.
(Source:
Added at 15
Ill.
Reg.
,
effective
Section 724.934
Test methods and procedures
a)
Each owner or operator subject to the provisions of this Subpart
shall comply with the teat methods and procedures requirements
provided in this Section
b)
When
a closed—vent
system is tested for compliance with no
detectable emissions, as required in Section 724.933(k), the test
must comply with the following requirements:
1)
Monitoring must comply with Reference Method 21 in 40 CFR
60,
incorporated by reference in 35
Ill.
Adm. Code 720.111.
2)
The detection instrument must meet the performance criteria
of Reference Method 21.
3)
The instrument must be calibrated before use on each day of
its use by the procedures specified in Reference Method 21.
4)
Calibration gases must be:
A)
Zero air (less than 10 ppm of hydrocarbon
in air).
B)
A mixture of methane or n-hexane and air at a
concentration of approximately, but less than,
10,000
ppm methane or n—hexane.
5)
The background level must be determined as set forth in
Reference Method 21.
6)
The instrument probe must be traversed around all potential
leak interfaces as close to the interface as possible as
described in Reference Method 21.
7)
The arithmetic difference between the maximum concentration
indicated by the instrument and the background level
is
compared with 500 ppm for determining compliance.
C)
Performance tests to determine compliance with Section 724.932(a)
and with the total organic compound concentration limit of Section
724.933(c) must comply with the following:
1)
Performance tests to determine total organic compound
concentrations and mass flow rates entering and exiting
control devices must be conducted and data reduced in
117—450

131
accordance with the following reference methods and
calculation procedures:
A)
Method 2 in 40 CFR 60 for velocity and volumetric flow
rate.
B)
Method
18 in 40 CFR 60 for organic content.
C)
Each performance test must consist of three separate
runs, each run conducted for at least
1 hour under the
conditions that exist when the hazardous waste
management unit is operating at the highest load or
capacity level reasonably expected to occur.
For the
purpose of determining total organic compound
concentrations and mass flow rates, the average of
results of all runs applies.
The average must be
computed on
a time—weighed basis.
D)
Total organic mass flow rates must be determined by
the following equation:
F
=
K
*
Q
*
SUM(Ci
*
MWi)
Where:
F is the total organic mass flow rate,
kg/h.
K
=
4.16
E —8, conversion factor for molar
volume,
kg—mol/cubic m,
at 293 K and 760 mm Hg.
Q
=
volumetric flow rate of gases entering or
exiting control device, dscm/h,
as determined by
Method 2 in 40 CFR 60,
incorporated by reference
in 35
Ill. Adm.
Code 720.111.
SUM(Xi) means the sum of the values of X for
each component
i,
from i=.
to n.
n
=
number
of
organic
compounds
in
the
vent
gas.
Ci
is the organic concentration in ppm,
dry
basis, of compound i in the vent gas,
as
determined
by
Method
18
in
40
CFR
60.
MWi is the molecular weight of organic compound
i in the vent gas,
kg/kg—mol.
E)
The annual total organic emission rate must be
determined by the following equation:
A
=
F
*
HOURS
117—451

132
Where:
A is total organic emission rate, kg/y.
F is the total organic
mass
flow rate,
kg/h,
as
calculated in subsection (c)(1)(D).
HOURS is the total annual hours of operation for
the affected unit.
F)
Total organic emissions from all affected process
vents at the facility must be determined by
summing
the hourly total organic mass emissions rates
(F as
determined in subsection (c)(1)(D)) and by
summing
the
annual total organic mass emission rates
(A as
determined in subsection
(c)(1)(E))
for all affected
process vents at the facility.
2)
The owner or operator shall record such process information
as
is
necessary
to
determine
the
conditions
of
the
performance
tests.
Operations
during
periods
of
startup,
shutdown and malfunction do not constitute representative
conditions for the purpose of a performance test.
3)
The owner or operator of an affected facility shall provide,
or cause to be provided, performance testing facilities as
follows:
A)
Sampling ports adequate for the test methods specified
in subsection (c)(1).
B)
Safe sampling platform(s).
C)
Safe access to sampling platform(s).
D)
Utilities for sampling and testing equipment.
4)
For the purpose of making compliance determinations, the
time—weighted average of the results of the three runs must
apply.
In the event that a sample is accidentally lost or
conditions occur in which one of the three runs must be
discontinued
because
of
forced
shutdown,
failure
of
an
irreplaceable portion of the sample train, extreme
meteorological conditions or other circumstances beyond the
owner or operator’s control, compliance may, upon the
Agency’s approval,
be determined using the average of the
results of the two other runs.
d)
To show that a process vent associated with a hazardous waste
distillation, fractionation, thin—film evaporation,
solvent
extraction, or air or steam stripping operation
is not subject to
the requirements of this Subpart, the owner or operator shall make
117—452

133
an initial determination that the time—weighted,
annual average
total organic concentration of the waste managed by the waste
management unit is less than 10 ppmw using one of the following
two methods:
1)
Direct measurement of the organic concentration of the waste
using the following procedures:
A)
The owner or operator shall take a minimum of four
grab samples of waste for each wastestream managed in
the affected unit under process conditions expected to
cause the maximum waste organic concentration.
B)
For waste generated onaite, the grab samples must be
collected at a point before the waste is exposed to
the atmosphere such as in an enclosed pipe or other
closed system that
is used to transfer the waste after
generation to the first affected distillation,
fractionation, thin—film evaporation,
solvent
extraction,
or air or steam stripping operation.
For
waste generated offsite, the grab samples must be
collected at the inlet to the first waste management
unit that receive~the waste provided the waste has
been transferred to the facility in a closed system
such as a tank truck and the.waste
is not diluted or
mixed with other waste.
C)
Each sample must be analyzed and the total organic
concentration of the sample must be computed using
Method 9060 or 8240 of SW-846
(incorporated by
reference under 35
Ill. Adm. Code 720.111.
D)
The arithmetic mean of the results of the analyses of
the four samples apply for each wastestreazu managed in
the unit in determining the time-weighted, annual
average total organic concentration of the waste.
The
time-weighted average
is to be calculated using the
annual quantity of each waste stream processed and the
mean organic concentration of each wastestream managed
in the unit.
2)
Using knowledge of the waste to determine that its total
organic concentration is
less that 10 ppmw.
Documentation
of the waste determination
is required.
Examples of
documentation that must be used to support
a determination
under this subsection include:
A)
Production process information documenting that no
organic compounds are used.
B)
Information that the waste is generated by a process
that
is identical to a process at the same or another
117—453

134
facility that has previously been demonstrated by
direct measurement to generate a wastestream having a
total organic content less than
10 ppmw,
or
C)
Prior speciation analysis results on the same
wastestream where it
is also documented that no
process changes have occurred since that analysis that
could affect the waste total organic concentration.
e)
The determination that distillation, fractionation, thin-film
evaporation, solvent extraction, or air or steam stripping
operations which manage hazardous wastes with time—weighted,
annual average total organic concentrations less than 10 ppmw must
be made as follows:
1)
By the effective date that the facility becomes subject to
the provisions of this Subpart or by the date when the waste
is first managed in
a waste management unit,
whichever
is
later; and
2)
For continuously generated waste,
annually; or
3)
Whenever there
is a change in the waste being managed or a
change in the process that generates or treats the waste.
f)
When an owner or operator and the Agency do not agree on whether a
distillation,
fractionation, thin—film evaporation, solvent
extraction, or air or steam stripping operation manages a
hazardous waste with organic concentrations of at least 10 ppmw
based on knowledge of the waste,
the procedures in Method 8240 in
SW—846,
incorporated by reference in 35
Ill.
Adrn. Code 720.111,
must be used to resolve the dispute.
(Source:
Added
at 15 Ill.
Reg.
,
effective
)
Section 724.935
Recordkeeping requirements
a)
Compliance Required.
1)
Each owner or operator subject to the provisions of thiB
Subpart shall comply with the recordkeeping requirements of
this Section.
2)
An owner or operator of more than one hazardous waste
management unit subject to the provisions of this Subpart
may comply with the recordkeeping requirements for these
hazardous waste management units in one recordkeeping system
if
the system identifies each record by each hazardous waste
management unit.
b)
Owners
and operators shall record the following information in the
facility operating record:
117—454

135
1)
For facilities that comply with the provisions of Section
724.933(a) (2),
an implementation schedule that includes
dates by which the closed—vent system and control device
will be installed and
in operation.
The schedule must also
include a rationale of why the installation cannot be
completed at an earlier date.
The implementation schedule
must be in the facility operating record by the effective
date that the facility becomes subject to the provisions of
this Subpart.
2)
Up—to—date documentation of compliance with the process vent
standards in Section 724.932, including:
A)
Information and data identifying all affected process
vents, annual throughput and operating hours of each
affected unit, estimated emission rates for each
affected vent and for the overall facility
(i.e., the
total emissions for all affected vents at the
facility), and the approximate location within the
facility of each affected unit (e.g., identify the
hazardous waste management units on a facility plot
plan).
B)
Information and data supporting determination of vent
emissions and emission reductions achieved by add—on
control devices based on engineering calculations or
source tests.
For the purpose of determining
compliance, determinations of vent emissions and
emission reductions must be made using operating
parameter values
(e.g.,
temperatures, flow rates,
or
vent stream organic compounds and concentrations)
that
represent the conditions that result in maximum
organic emissions,
such
as when the waste management
unit
is operating at the highest
load or capacity
level reasonably expected to occur.
If the owner or
operator takes any action (e.g., managing a waste of
different composition or increasing operating hours of
affected waste management units) that would result in
an increase in total organic emissions from affected
process vents at the facility, then a new
determination is required.
3)
Where an owner or operator chooses to use test date to
determine the organic removal efficiency or total organic
compound concentration achieved by the control device,
a
performance test plan.
The test plan must include:
A)
A description of how it
is determined that the planned
test is going to be conducted when the hazardous waste
management unit is operating at the highest load or
capacity level reasonably expected to occur.
This
117—455

136
must include the estimated or design flow rate and
organic content of each vent stream and define the
acceptable operating ranges of key process and control
device parameters during the test program.
B)
A detailed engineering description of the closed-vent
system and control device including:
i)
Manufacturer’s name and model number of control
device.
ii)
Type of control device.
iii)
Dimensions of the control device.
iv)
Capacity.
v)
Construction materials.
C)
A detailed description of sampling and monitoring
procedures,
including sampling and monitoring
locations in the system, the equipment to be used,
sampling and monitoring frequency,
and planned
analytical procedures
for sample analysis.
4)
Documentation of compliance with Section 724.933 must
include the following information:
A)
A list of all information references and sources used
in preparing the documentation.
B)
Records including the dates of each compliance test
required by Section 724.933(k).
C)
If engineering calculations are used,
a design
analysis, specifications, drawings,
schematics, and
piping and instrumentation diagrams based on the
appropriate sections of APTI Course 415
(incorporated
by reference
in 35
Ill.
Adm. Code 720.111)
or other
engineering texts, approved by the Agency, that
present basic control device design information.
Documentation provided by the control device
manufacturer or vendor that describes the control
device design in accordance with subsections
(b)(4)(C)(i) through
(vii)
may be used to comply with
this requirement.
The design~analysis must address
the vent stream characteristics and control device
operation parameters as specified below.
i)
For a thermal vapor incinerator,
the design
analysis must consider the vent stream
composition,
constituent concentrations and flow
117—456

137
rate.
The design analysis must also establish
the design minimum and average temperature in
the combustion zone and the combustion zone
residence time.
ii)
For
a catalytic vapor incinerator, the design
analysis must consider the vent
stream
composition,
constituent concentrations, and
flow rate.
The design analysis must also
establish the design minimum and average
temperatures
across
the
catalyst bed inlet and
outlet.
iii)
For a boiler or process heater, the design
analysis must consider the vent stream
composition,
constituent
concentrations
and
flow
rate.
The
design
analysis
must
also
establish
the design minimum and average flame zone
temperatures,
combustion
zone
residence
time
and
description
of
method
and
location
where
the
vent stream is introduced into the combustion
zone.
iv)
For a flare, the design analysis must consider
the vent stream composition,
constituent
concentrations,
and
flow
rate.
The
design
analysis
must
also
consider
the
requirements
specified
in
Section
724.933(d).
v)
For a condenser,
the design analysis must
consider
the
vent
stream
composition,
constituent
concentrations,
flow
rate,
relative
humidity
and
temperature.
The
design
analysis
must
also
establish
the
design
outlet
organic
compound
concentration
level,
design
average
temperature of the condenser exhaust vent stream
and design average temperatures of the coolant
fluid at the condenser inlet and outlet.
vi)
For a carbon adsorption system such as a fixed—
bed adsorber that regenerates the carbon bed
directly onsite in the control device,
the
design analysis must consider the vent stream
composition,
constituent concentrations, flow
rate,
relative humidity and temperature.
The
design
analysis
must
also
establish
the
design
exhaust vent stream organic compound
concentration level, number and capacity of
carbon beds,
type and working capacity of
activated carbon used for carbon beds, design
total steam flow over the period of each
complete carbon bed regeneration cycle, duration
117—457

138
of the carbon bed steaming and cooling/drying
cycles, design carbon bed temperature after
regeneration, design carbon bed regeneration
time and design service life of carbon.
vii)
For a carbon adsorption system such as a carbon
canister that does not regenerate the carbon bed
directly onsite in the control device,
the
design analysis must consider the vent stream
composition,
constituent concentrations, flow
rate,
relative .humidity and temperature.
The
design analysis must also establish the design
outlet organic concentration level, capacity of
carbon bed, type and working capacity of
activated carbon used for carbon bed and design
carbon replacement interval based on the total
carbon
working
capacity
of
the
control
device
and source operating schedule.
D)
A statement signed and dated by the owner or operator
certifying
that
the
operating
parameters
used
in
the
design
analysis
reasonably
represent
the
conditions
that
exist
when
the
hazardous
waste
management
unit
is
or would be operating at the highest load or capacity
level reasonably expected to occur.
E)
A
statement
signed
and
dated
by
the
owner
or
operator
certifying that the control device is designed to
operate at an efficiency of 95 percent or greater
unless
the
total
organic
concentration
limit
of
Section 724.932(a)
is achieved at an efficiency less
than 95 weight percent or the total organic emission
limits
of
Section
724.932(a)
for
affected
process
vents at the facility are attained by
a control device
involving vapor recovery
at an efficiency less than 95
weight percent.
A statement provided by the control
device manufacturer or vendor certifying that the
control equipment meets the design specifications may
be used to comply with this requirement.
F)
If
performance
tests
are
used
to
demonstrate
compliance,
all test results.
C)
Design documentation and monitoring operating and inspection
information for each closed-vent system and control device
required to comply with the provisions of this Part must be
recorded and kept up—to-date
in the facility operating record.
The
information
must
include:
1)
Description
and
date
of
each
modification
that
is
made
to
the
closed—vent
system
or
control
device
design.
117—458

139
2)
Identification of operating parameter, description of
monitoring device, and diagram of monitoring sensor location
or locations used to comply with Section 724.933(f)(1)
and
(2).
3)
Monitoring,
operating
and
inspection
information
required
by
Section 724.933(f) through
(k).
4)
Date,
time and duration of each period that occurs while the
control device is operating when any monitored parameter
exceeds the value established in the control device design
analysis as specified below:
A)
For
a thermal vapor incinerator designed to operate
with a minimum residence time of 0.50 second at
a
minimum temperature of 760 C, any period when the
-combustion
temperature
is
below
760
C.
B)
For a thermal vapor incinerator designed to operate
with
an
organic
emission
reduction
efficiency
of
95
weight
percent
or
greater,
any
period
when
the
combustion zone temperature is more than 28 C below
the design average combustion zone temperature
established
as
a
requirement
of
subsection
(b) (4) (C) (i)
C)
For a catalytic vapor incinerator,
any period when:
i)
Temperature
of
the
vent
stream
at
the
catalyst
bed inlet is more than 28 C below the average
temperature of the inlet vent stream established
as a requirement
of subsection
(b) (4) (C) (ii); or
ii)
Temperature
difference
across
the
catalyst
bed
is less than 80 percent of the design average
temperature difference established as a
requirement
of
subsection
(b)
(4) (C) (ii).
D)
For a boiler or process heater,
any period when:
i)
Flame
zone
temperature
is
more
than
28
C
below
the design average flame zone temperature
established as a requirement of subsection
(b)(4)(C)(iii); or
ii)
Position
changes
where
the
vent
stream
is
introduced to the combustion zone from the
location established as a requirement of
subsection
(b)
(4)(C) (iii).
E)
For a flare, period when the pilot flame is not
ignited.
117—459

140
F)
For a condenser that complies with Section
724.933(f)(2)(F)(i),
any period when the organic
compound concentration level or readings of organic
compounds in the exhaust vent stream from the
condenser are more than 20 percent greater than the
design outlet organic compound concentration level
established as a requirement of subsection
(b)
(4) (C)
(v)
G)
For
a
condenser
that
complies
with
Section
724.933(f)(2)(F)(ii),
any
period
when:
i)
Temperature of the exhaust vent stream from the
condenser
is
more
than
6
C
above
the
design
average exhaust vent stream temperature
established as a requirement of subsection
(b) (4) (C) (v)
ii)
Temperature of the coolant fluid exiting the
condenser is more than 6 C above the design
average coolant fluid temperature
at the
condenser outlet established as a requirement of
subsection (b)(4)(C)(v).
H)
For
a carbon adsorption system such as a fixed—bed
carbon adsorber that regenerates the carbon bed
directly onsite
in the control device and complies
with Section 724.933(f)(2QG)(i),
any period when the
organic
compound
concentration
level
or
readings
of
organic
compounds
in
the
exhaust
vent
stream
from
the
carbon bed are more than 20 percent greater than the
design exhaust vent stream organic compound
concentration level established as
a requirement of
subsection
(b) (4) (C) (vi).
I)
For a carbon adsorption system such as
a fixed—bed
carbon
adsorber
that
regenerates
the
carbon
bed
directly onsite in the control device and complies
with Section 724.933(f)(2)(G)(ii), any period when the
vent stream continues to flow through the control
device
beyond
the
predetermined
carbon
bed
regeneration time established
as a requirement of
subsection
(b)
(4) (C) (vi).
5)
Explanation for each period recorded under subsection
(c)(4)
of the cause for control device operating parameter
exceeding the design value and the measures implemented to
correct the control device operation.
6)
For
a carbon adsorption system operated subject to
requirements specified
in Section 724.933(g)
or
(h)(2), any
117—460

141
date when existing carbon in the control device is replaced
with fresh carbon.
7)
For a carbon adsorption system operated subject to
requirements specified
in Section 724.933(h)(1), a log that
records:
A)
Date and time when control device
is monitored for
carbon breakthrough and the monitoring device reading.
B)
Date when existing carbon in the control device is
replaced with fresh carbon.
8)
Date of each control device startup and shutdown.
d)
Records of the monitoring, operating and inspection
information
required by subsections
(c)(3) through
(8) need be kept only 3
years.
e)
For a control device other than a thermal vapor incinerator,
catalytic vapor incinerator,
flare, boiler, process heater,
condenser or carbon adsorption system,
the Agency shall specify
the appropriate recordkeeping requirements.
f)
Up-to—date information and data used to determine whether or not
a
process vent is subject to the requirements in Section 724.932,
including supporting documentation
as required by Section
724.934(d)(2), when application of the knowledge of the nature of
the hazardous wastestream or the process by which
it was produced
is used,
must be recorded in a log that is kept
in the facility
operating record.
(Source: Added at 15
Ill.
Reg.
,
effective
)
Section 724.936
Reporting Requirements
a)
A semiannual report must be submitted by owners and operators
subject to the requirements of this Subpart to the Agency by dates
specified in the RCRA permit.
The report must include the
following
information:
1)
The tJSEPA identification number
(35
Ill. Adm. Code 722.112),
name,
and address of the facility.
2)
For each month during the semiannual reporting period:
a)
Dates when the control device:
i)
Exceeded or operated outside of the design
specifications as defined in Section
724.935(c)(4)
and
117—461

142
ii)
Such exceedances were not corrected within 24
hours, or that a flare operated with visible
emissions as defined by Method 22 monitoring
B)
The duration and cause of each exceedance or visible
emissions, and
C)
Any corrective measures taken.
b)
If
during the
semiannual
reporting
period, the control device does
not exceed or operate outside of the design specifications as
defined in Section 724.935(c)(4)
for more than 24 hours or
a flare
does not operate with visible emissions as defined in Section
724.933(d),
a report to the Agency is not required.
(Source:
Added at
15
Ill. Reg.
,
effective
SUBPART
BB:
AIR EMISSION
STANDARDS
FOR EQUIPMENT LEAKS
Section 724.950
Applicability
a)
The regulations
in this Subpart apply to owners and operators of
facilities that treat, store, or dispose of hazardous wastes
(except as provided in Section 724.101).
b)
Except as provided in Section 724.964(k), this Subpart applies to
equipment that contains or contacts hazardous wastes with organic
concentrations of at least
10 percent by weight that are managed
in:
1)
Units
that
are subject to the RCRA permitting requirements
of 35
Ill. Adm. Code 703,
or
2)
Hazardous waste recycling units that are located on
hazardous waste management facilities otherwise subject to
the permitting requirements of
35
Ill. Adm. Code 703.
c)
If the owner or operator of equipment subject to the requirements
of Sections 724.952 through 724.965 has received a RCRA permit
prior to December 21, 1990,
the requirements of Sections 724.952
through 724.965 must be incorporated when the permit is reissued
under 35
Ill. Adm. Code 705.201 or reviewed under 35
Ill. Adm.
Code 702.161.
d)
Each
piece of equipment to which this Subpart applies must be
marked in such a manner that
it can be distinguished readily from
other pieces of equipment.
e)
Equipment that
is in vacuum service is excluded from the
requirements of Sections 724.952 to 724.960,
if it is identified
as required
in Section 724.964(g)(5).
117—462

143
BOARD NOTE:
The requirements of Sections 724.952 through 724.965
apply to equipment associated with hazardous waste recycling units
previously exempt under 35
Ill. Adm. Code 721.106(c)(1).
Other
exemptions under 35 Ill.
Adm. Code 721.104,
722.134 and 724.101(g)
are not affected by these requirements.
(Source:
Added at
15 Ill. Reg.
,
effective
)
Section 724.951
Definitions
As used
in this Subpart, all terms have the meaning given them in Section
724.931, the Resource Conservation and Recovery Act and 35 Ill. Adm. Code 720
through 726.
(Source:
Added at
15
Ill. R~g.
,
effective
Section 724.952
Standards:
Pumps in Light Liquid Service
a)
Monitoring
1)
Each pump in light liquid service must be monitored monthly
to detect leaks by the methods specified
in Section
724.963(b), except
as provided in subsections
(d),
(e) and
(f).
2)
Each pump in light
liquid service must be checked by visual
inspection each calendar week for indications of liquids
dripping from the pump seal.
b)
Leaks
1)
If an instrument reading of
10,000 ppm or greater is
measured,
a leak is detected.
2)
If there are indications of liquids dripping from the pump
seal,
a leak is detected.
c)
Repairs
1)
When a leak is detected,
it must be repaired as soon as
practicable, but not later than 15 calendar days after
it
is
detected,
except as provided in Section 724.959.
2)
A first attempt
at repair
(e.g., tightening the packing
gland) must be made no later than 5 calendar days after each
leak is detected.
d)
Each pump equipped with a dual mechanical seal system that
includes
a barrier fluid system
is exempt from the requirements of
subsection
(a),
provided the following requirements are met:
117—463

144
1)
Each dual mechanical seal system must be:
A)
Operated with the barrier fluid at
a pressure that
is
at all times greater than the pump stuffing box
pressures;
or
B)
Equipped with
a barrier fluid degassing reservoir that
is connected by a closed—vent system to a control
device that complies with the requirements of Section
724.960;
or
C)
Equipped with a system that purges the barrier fluid
into a hazardous wastestream with no detectable
emissions to the atmosphere.
2)
The barrier fluid system must not be a hazardous waste with
organic concentrations
10 percent or greater by weight.
3)
Each barrier fluid system must be equipped with a sensor
that will detect failure of the seal system, the barrier
fluid system, or both.
4)
Each pump must be checked by visual inspection,
each
calendar week,
for indications of liquids dripping from the
pump seals.
5)
Alarms
A)
Each sensor as described in
subsection (d)(3) must be
checked daily or be equipped with an audible alarm
that must be checked monthly to ensure that it is
functioning
properly.
B)
The owner or operator shall determine, based on design
considerations
and
operating
experience,
a
criterion
that indicates failure of the seal system, the barrier
fluid system,
or both.
6)
Leaks
A)
If there are indications of liquids dripping from the
pump seal or the sensor
indicates failure of the seal
system, the barrier fluid system, or both based on the
criterion determined
in subsection (d)(5)(B),
a leak
is detected.
B)
When a leak
is detected,
it must be repaired as soon
as practicable, but not later than 15 calendar days
after
it is detected, except as provided in Section
724.959.
117—464

145
C)
A first attempt at repair
(e.g., relapping the seal)
must be made no later than
5 calendar days after each
leak is detected.
e)
Any pump that is designated,
as described in Section
724.964(g)(2),
for no detectable emissions, as indicated by an
instrument reading of less than 500 ppm above background,
is
exempt
from the requirements of subsections
(a),
(c) and
(d),
if
the pump meets the following requirements:
1)
Must have no externally actuated shaft penetrating the pump
housing.
2)
Must operate with no detectable emissions as indicated by an
instrument reading of less than 500 ppm above background as
measured by the methods specified in Section 724.963(c).
3)
Must be tested for compliance with subsection
(e)(2)
initially upon designation,
annually and at other times as
specified in the RCRA permit.
f)
If any pump is equipped with a closed-vent system capable of
capturing and transporting any leakage from the seal or seals to a
control device that complies with the requirements of Section
724.960,
it
is exempt from the requirements of subsections
(a)
through
(e).
(Source:
Added at
15
Ill.
Reg.
,
effective
)
Section 724.953
Standards: Compressors
a)
Each compressor must be equipped with a seal system that includes
a barrier fluid system and that prevents leakage of total organic
emissions to the atmosphere,
except as provided in subsections
(h)
and
(i).
b)
Each compressor seal system as required in subsection
(a) must be:
1)
Operated
with
the barrier fluid at
a pressure that is at all
times greater than the compressor stuffing box pressure; or
2)
Equipped with a barrier fluid system that
is connected by a
closed—vent system to a control device that complies with
the requirements of Section 724.960; or
3)
Equipped with a system that purges the barrier fluid into a
hazardous wastestream with no detectable emissions to
atmosphere.
C)
The barrier fluid must not be a hazardous waste with organic
concentrations
10
percent
or
greater
by
weight.
117—465

146
d)
Each barrier fluid system
as described in subsections
(a) through
(c) must be equipped with a sensor that will detect failure of the
seal system, barrier fluid system,
or both.
e)
1)
Each sensor as required in subsection
(d) must be checked
daily or must be equipped with an audible alarm that must be
checked monthly to ensure that it is functioning properly
unless the compressor
is located within the boundary of an
unmanned plant site,
in which case the sensor must be
checked daily.
2)
The owner or operator shall determine, based on design
considerations and operating experience,
a criterion that
indicates failure of the seal system, the barrier fluid
system,
or both.
f)
If
the
sensor
indicates
failure
of
the
seal
system,
the
barrier
fluid system, or both based on the criterion determined under
subsection
(e)(2),
a leak is detected.
g)
Repairs
1)
When
a leak
is detected,
it must be repaired as soon as
practicable, but not later than 15 calendar days after it
is
detected,
except as provided in Section 724.959.
2)
A first attempt at repair (e.g., tightening the packing
gland)
must be made no later than
5 calendar days after each
leak is detected.
h)
A compressor is exempt from the requirements of subsections
(a)
and
(b)
if
it
is equipped with a closed-vent system capable of
capturing and transporting any leakage from the seal to
a control
device that complies with the requirements of Section 724.960,
except as provided in subsection
(i).
i)
Any
compressor
that
is
designated,
as
described
in
Section
724.964(g)(2),
for no detectable emission as indicated by an
instrument reading of less than 500 ppm above background,
is
exempt from the requirements of subsections
(a) through
(h)
if the
compressor:
1)
Is
determined
to
be
operating
with
no
detectable
emissions,
as indicated by an instrument reading of less than 500 ppm
above background,
as measured by the method specified in
Section 724.963(c).
2)
Is tested for compliance with subsection
(i)(1)
initially
upon designation,
annually and other times as specified in
the RCRA permit.
(Source:
Added
at
15
Ill.
Reg.
,
effective
117—466

147
Section
724.954
Standards:
Pressure
Relief
Devices
in
Gas/Vapor
Service
a)
Except
during
pressure
releases,
each
pressure
relief
device
in
gas/vapor
service
must
be
operated
with
no
detectable
emissions,
as indicated by an instrument reading of less than 500 ppm above
background as measured by the method specified in Section
724.963(c).
b)
Actions following pressure release.
1)
After each pressure release, the pressure relief device must
be returned to a condition of no detectable emissions, as
indicated by an instrument reading of less than 500 ppm
above background,
as soon
as practicable,
but no later than
5 calendar days after each pressure release, except as
provided in Section 724.959.
2)
No later than
5 calendar days after the pressure release,
the pressure relief device must be monitored to confirm the
condition of no detectable emissions,
as indicated by an
instrument reading of less than 500 ppm above background,
as
measured by the method specified in Section 724.963(c).
c)
Any pressure relief device that
is equipped with a closed-vent
system capable of capturing and transporting leakage from the
pressure relief device to a control device as described in Section
724.960
is exempt from the requirements of subsections
(a)
and
(b).
(Source:
Added at
15
Ill. Reg.
,
effective
Section 724.955
Standards:
Sampling Connecting Systems
a)
Each sampling connection system must be equipped with a closed
purge
system
or
closed-vent
system.
b)
Each closed—purge system or closed—vent
system as required in
subsection
(a)
must:
1)
Return
the
purged
hazardous
waste
stream
directly
to
the
hazardous
waste
management
process
line
with
no
detectable
emissions to atmosphere; or
2)
Collect and recycle the purged hazardous waste stream with
no detectable emissions to atmosphere;
or
3)
Be designed and operated to capture and transport all the
purged hazardous wastestream to a control device that
complies with the requirements of Section 724.960.
117—467

148
C)
In situ sampling systems are exempt
from the requirements of
subsections
(a)
and
(b).
(Source:
Added at
15
Ill.
Reg.
,
effective
)
Section 724.956
Standards:
Open—ended Valves or Lines
a)
Equipment.
1)
Each open-ended valve or line must be equipped with a cap,
blind flange, plug or a second valve.
2)
The cap, blind flange, plug or second valve must seal the
open end at all times except during operations requiring
hazardous wastestream flow through the open—ended valve or
line.
b)
Each open—ended valve or line equipped with
a second valve must be
operated
in
a
manner
such
that
the
valve
on
the
hazardous
wastestream end is closed before the second valve
is closed.
C)
When a double block and bleed system is being used,
the bleed
valve or line may remain open during operations that require
venting the line between the block valves but must comply with
subsection
(a)
at
all
other
times.
(Source:
Added at
15
Ill.
Reg.
,
effective
Section 724.957
Standards:
Valves in Gas/Vapor or Light Liquid Service
a)
Each valve in gas/vapor or light liquid service must be monitored
monthly to detect leaks by the methods specified in Section
724.963(b)
and must comply with subsections
(b) through
(e),
except
as
provided
in
subsections
(f),
(g)
and
(h),
and
in
Section
724.961 and 724.962.
b)
If an instrument reading of 10,000 ppm or greater is measured,
a
leak is detected.
C)
Monitoring Frequency
1)
Any valve for which a leak is not detected for two
successive months must be monitored the first month of every
succeeding quarter, beginning with the next quarter, until
a
leak
is detected.
2)
If
a leak is detected, the valve must be monitored monthly
until
a
leak
is
not
detected
for
two
successive
months,
d)
1)
When a leak is detected,
it must be repaired as
soon as
practicable,
but no later than 15 calendar days after the
leak is detected, except as provided
in Section 724.959.
117—468

149
2)
A
first
attempt
at
repair
must
be
made
no
later
than
5
calendar
days
after
each
leak
is
detected.
e)
First
attempts
at
repair
include,
but
are
not
limited
to
the
following best practices where practicable:
1)
Tightening
of
bonnet
bolts.
2)
Replacement
of
bonnet
bolts.
3)
Tightening
of
packing
gland
nuts.
4)
Injection
of
lubricant
into
lubricated
packing.
f)
Any valve that
is designated,
as described in Section
724.964(g)(2),
for no detectable emissions,
as indicated by an
instrument reading of less than 500 ppm above background,
is
exempt from the requirements of subsection
(a)
if the valve:
1)
Has no external actuating mechanism in contact with the
hazardous wastestream.
2)
Is
operated
with
emissions
less
than
500
ppm
above
background
as
determined
by
the
method
specified
in
Section
724.963(c).
3)
Is tested for compliance with subsection (f)(2)
initially
upon
designation,
annually,
and
at
other
times
as
specified
in the RCRA permit.
g)
Any valve that is designated, as described in Section
724.964(h)(1),
as an unsafe—to—monitor valve is exempt from the
requirements of subsection
(a),
if:
1)
The
owner
or
operator
of
the
valve
determines
that
the
valve
is unsafe to monitor because monitoring personnel would be
exposed
to
an
immediate
danger
as
a
consequence
of
complying
with
subsection
(a).
2)
The
owner
or
operator
of
the
valve
adheres
to
a
written
plan
that
requires
monitoring
of
the
valve
as
frequently
as
practicable
during
safe-to-monitor
times.
h)
Any valve that is designated,
as described in Section
724.964(h) (2), as
a difficult-to-monitor valve
is exempt from the
requirements of subsection
(a),
if:
1)
The owner or operator of the valve determines that the valve
cannot be monitored without elevating the monitoring
personnel more than
2 meters above a support surface;
117—469

150
2)
The hazardous waste management unit within which the valve
is located was in operation before June 21,
1990; and
3)
The owner or operator of the valve follows a written plan
that requires monitoring of the valve at least once per
calendar year.
(Source:
Added at 15
Ill. Reg.
,
effective
)
Section 724.958
Standards:
Pumps, Valves, Pressure Relief Devices and Other
Connectors
a)
Pumps
and
valves
in
heavy
liquid
service,
pressure
relief
devices
in
light
liquid
or
heavy
liquid
service
and
flanges
and
other
connectors must be monitored within
5 days by the method specified
in Section 724.963(b),
if evidence of
a potential leak
is found by
visual,
audible,
olfactory,
or any other detection method.
b)
If an
instrument reading of 10,000 ppm or greater is measured,
a
leak
is detected.
C)
Repairs
1)
When a leak is detected,
it must be repaired as soon as
practicable,
but
not
later
than
15
calendar
days
after
it
is
detected,
except as provided in Section 724.959.
2)
The first attempt at repair must be made no later than
S
calendar days after each leak is detected.
d)
First attempts at repair include, but are not limited to, the best
practices
described
under
Section
724.957(e).
(Source:
Added at 15
Ill. Reg.
,
effective
)
Section 724.959
Standards:
Delay of Repair.
a)
Delay of repair of equipment for which leaks have been detected is
allowed
if the repair is technically infeasible without a
hazardous waste management unit shutdown.
In such a case,
repair
of this equipment must occur before the end of the next hazardous
waste
management
unit
shutdown.
b)
Delay of repair of equipment for which leaks have been detected is
allowed
for
equipment
that
is
isolated
from
the
hazardous
waste
management unit and that does not continue to contain or contact
hazardous
waste
with
organic
concentrations
at
least
10
percent
by
weight.
C)
Delay of repair for valves is allowed if:
117—470

151
1)
The owner or operator determines that emissions of purged
material resulting from immediate repair are greater than
the emissions likely to result from delay of repair.
2)
When repair procedures are effected, the purged material
is
collected and destroyed or recovered in a control device
complying with Section 724.960.
d)
Delay of repair for pumps
is allowed if:
1)
Repair requires the use of a dual mechanical seal system
that includes
a barrier fluid system.
2)
Repair is completed as soon as practicable, but not later
than 6 months after the leak was detected.
e)
Delay of repair beyond a hazardous waste management ~unitshutdown
is allowed for
a valve
if valve assembly replacement is necessary
during the hazardous waste management unit shutdown,
valve
assembly supplies have been depleted,
and valve assembly supplies
had been sufficiently stocked before the supplies were depleted.
Delay of repair beyond the next hazardous waste management unit
shutdown
is not allowed unless the next hazardous waste management
unit shutdown occurs sooner than 6 months after the first
hazardous waste management unit shutdown.
(Source:
Added at 15
Ill.
Reg.
,
effective
Section 724.960
Standards:
Closed—vent Systems and Control Devices
Owners or operators of closed—vent systems and control devices shall comply
with the provisions of Section 724.933.
(Source:
Added at
15
Ill.
Reg.
,
effective
)
Section 724.961
Alternative Percentage Standard for Valves
a)
An owner or operator subject to the requirements of Section
724.957 may elect to have all valves within a hazardous waste
management unit comply with an alternative standard which allows
no greater than
2 percent of the valves to leak.
b)
The following requirements must be met
if an owner or operator
decides to comply with the alternative standard of allowing 2
percent of valves to leak:
1)
An owner or operator shall notify the Agency that the owner
or operator has elected to comply with the requirements of
this Section.
117—47 1

152
2)
A performance test
as specified in subsection
(c)
must be
conducted initially upon designation, annually and other
times specified in the
RCRA
permit.
3)
If a valve
leak is detected it must be repaired in
accordance with Section 724.957(d)
and
(e).
C)
Performance tests must be conducted in the following manner:
1)
All
valves subject to the requirements in Section 724.957
within the hazardous waste management unit must be monitored
within
1 week by the methods specified in Section
724.963(b).
2)
If an instrument reading of 10,000 ppm or greater is
measured,
a leak
is detected.
3)
The leak percentage must be determined by dividing the
number
of valves subject to the requirements in Section
724.957 for which leaks are detected by the total number of
valves
subject
to
the
requirements
in
Section
724.957
within
the hazardous waste management unit.
d)
If
an owner or operator decides to comply with this Section no
longer, the owner or operator shall notify the Agency
in writing
that the work practice standard described
in Section 724.957(a)
through
(e) will be followed.
(Source:
Added at
15
Ill.
Reg.
,
effective
Section 724.962
Skip Period Alternative for Valves
a)
Election
1)
An owner or operator subject to the requirements of
Section
724.957 may elect for all valves within a hazardous waste
management unit to comply with one of the alternative work
practices specified in subsections
(b)(2) and
(3).
2)
An owner or operator shall notify the Agency before
implementing one of the alternative work practices.
b)
Reduced Monitoring
1)
An owner or operator shall comply with the requirements for
valves,
as described in Section 724.957, except as described
in subsection
(b)(2)
and
(3).
2)
After two consecutive quarterly leak detection periods with
the percentage of valves leaking equal to or less than 2
percent,
an owner or operator may begin to skip one of the
117—472

153
quarterly leak detection periods for the valves subject to
the requirements in Section 724.957.
3)
After five consecutive quarterly leak detection periods with
the percentage of valves leaking equal to or less than 2
percent, an owner or operator may begin to skip three of the
quarterly
leak detection periods for the valves subject to
the requirements in Section 724.957.
4)
If the percentage of valves leaking is greater than 2
percent, the owner or operator shall monitor monthly in
compliance with the requirements in Section 724.957, but may
again elect to use thia Section after meeting the
requirements of Section 724.957(c)(1).
(Source:
Added at 15
Ill. Reg.
,
effective
Section 724.963
Test Methods and Procedures
a)
Each owner or operator subject to the provisions of this Subpart
shall comply with the test methods and procedures requirements
provided in this Section.
b)
Leak detection monitoring,
as required in Sections 724.952 through
724.962, must comply with the following requirements:
1)
Monitoring must comply with Reference Method 21 in 40 CFR
60,
incorporated by reference in 35
Ill. Adm. Code 720.111.
2)
The detection instrument must meet the performance criteria
of Reference Method 21.
3)
The instrument must be calibrated before use on each day of
its use by the procedures specified in Reference Method
21.
4)
Calibration gases must be:
A)
Zero air (less than 10 ppm of hydrocarbon in air).
B)
A mixture of methane or n-hexane and air at
a
concentration of approximately, but less than 10,000
ppm methane or n—hexane.
5)
The instrument probe must be traversed around all potential
leak interfaces as close to the interface as possible as
described in Reference Method
21.
c)
When equipment is tested for compliance with no detectable
emissions,
as required in Sections 724.952(e),
724.953(i),
724.954
and 724.957(f), the test must comply with the following
requirements:
117—473

154
1)
The requirements of subsections (b)(1) through
(4)
apply.
2)
The background level must be determined as set forth in
Reference Method 21.
3)
The instrument probe must be traversed around all potential
leak interfaces as close to the interface as possible as
described in Reference Method 21.
4)
This arithmetic difference between the maximum concentration
indicated by the instrument and the background level
is
compared with 500 ppm for determining compliance.
d)
In accordance with the waste analysis plan required by Section
724.113(b), an owner or operator of
a facility shall determine,
for each piece of equipment, whether the equipment contains or
contacts a hazardous waste with organic concentration that equals
or exceeds 10 percent by weight using the following:
1)
Methods described in ASTM Methods D 2267,
E 169,
E
168,
E
260 incorporated by reference in 35
Ill. Adm.
Code
720.111;
2)
Method 9060 or 8240 of SW—846,
incorporated by reference in
35
Ill. Adm. Code 720.111; or
3)
Application of the knowledge of the nature of the hazardous
wastestream or the process by which
it was produced.
Documentation
of
a
waste
determination
by
knowledge
is
required.
Examples
of
documentation
that
must
be
used
to
support
a
determination
under
this
provision
include
production process information documenting that no organic
compounds are used,
information that the waste is generated
by a process that
is identical to a process at the same or
another facility that has previously been demonstrated by
direct measurement to have a total organic content
less than
10 percent,
or prior speciation analysis results on the same
wastestream where it is also documented that no process
changes have occurred since that analysis that could affect
the waste total organic concentration.
e)
If an owner or operator determines that a piece of equipment
contains or contacts
a hazardous waste with organic concentrations
at least 10 percent by weight,
the determination can be revised
only after following the procedures in subsection (d)(1) or
(2).
f)
When an owner or operator and the Agency do not agree on whether
a
piece of equipment contains or contacts
a hazardous waste with
organic concentrations at least
10 percent by weight, the
procedures in subsection (d)(1) or
(2)
must be used to resolve the
dispute.
117—474

155
g)
Samples used in determining the percent organic content must be
representative of the highest total organic content hazardous
waste that is expected to be contained in or contact the
equipment.
h)
To determine if pumps or valves are in light liquid service, the
vapor pressures of constituents must either be obtained from
standard reference texts or be determined by ASTM D—2879
incorporated by reference in 35
Ill. Adm. Code 720.111.
i)
Performance
tests
to
determine
if
a
control
device
achieves
95
weight percent organic emission reduction must comply with the
procedures of Section 724.934(c)(l)
through
(4).
(Source:
Added at
15
Ill. Reg.
,
effective
)
Section 724.964
Recordkeeping Requirements
a)
Lumping Units
1)
Each owner or operator subject to the provisions of this
Subpart shall comply with the recordkeepirig requirements of
this Section.
2)
An owner or operator of more than one hazardous waste
management unit subject to the provisions of this Subpart
may comply with the recordkeeping requirements for these
hazardous waste management units in one recordkeeping system
if the system identifies each record by each hazardous waste
management unit.
b)
Owners
and operators shall record the following
information
in the
facility operating record:
1)
For each piece of equipment to which this Subpart applies:
A)
Equipment identification number and hazardous waste
management unit identification.
B)
Approximate locations within the facility (e.g.,
identify the hazardous waste management unit on a
facility plot plan).
C)
Type of equipment
(e.g., a pump or pipeline valve).
D)
Percent—by-weight total organics
in the hazardous
wastestream at the equipment.
E)
Hazardous waste state
at the equipment (e.g.,
gas/vapor or
liquid).
117—475

156
F)
Method of compliance with the standard
(e.g.,
“monthly
leak detection and repair” or “equipped with dual
mechanical seals”).
2)
for facilities than comply with the provisions of Section
724.933(a)(2),
an implementation schedule as specified in
that Section.
3)
Where an owner or operator chooses to use test data to
demonstrate the organic
removal efficiency or total organic
compound concentration achieved by the control device, a
performance test plan as specified in Section 724.935(b) (3).
4)
Documentation of compliance with Section 724.960, including
the detailed design documentation or performance teat
results specified
in Section 724.935(b) (4).
c)
When each leak is detected as specified in Sections 724.952,
724.953, 724.957 or 724.958, the following requirements apply:
1)
A
weatherproof and readily visible identification, marked
with the equipment identification number,
the date evidence
of
a potential leak was found in accordance with Section
724.958(a), and the date the leak was detected,
must be
attached to the leaking equipment.
2)
The identification on equipment except on a valve, may be
removed after it has been repaired.
3)
The identification on a valve may be removed after
it has
been monitored for 2 successive months
as specified in
Section 724.957(c) and no leak has been detected during
those
2 months.
d)
When each leak is detected as specified in Sections 724.952,
724.953,
724.957 or 724.958, the following information must be
recorded in an inspection log and must be kept in the facility
operating record:
1)
The instrument and operator identification numbers and the
equipment
identification
number.
2)
The date evidence of a potential leak was found in
accordance with Section 724.958(a).
3)
The
date
the
leak
was
detected
and
the
dates
of
each
attempt
to repair the leak.
4)
Repair methods applied in each attempt to repair the leak.
117—476

157
5)
“Above 10,000”,
if the maximum instrument reading measured
by the methods specified in Section 724..963(b)
after each
repair attempt is equal to or greater than 10,000 ppm.
6)
“Repair delayed” and the reason for the delay if
a leak is
not repaired within 15 calendar days after discovery of the
leak.
7)
Documentation supporting the delay of repair of
a. valve in
compliance with Section 724.959(c).
8)
The signature of the owner or operator (or designate) whose
decision it was that repair could not be effected without a
hazardous waste management unit shutdown.
9)
The expected date of successful repair of the leak if
a leak
is not repaired within 15
calendar days.
10)
The date of successful repair of the leak.
e)
Design documentation and monitoring, operating and inspection
information for each closed—vent system and control device
required to comply with the provisions of Section 724.960 must be
recorded and kept up-to—date in the facility operating record as
specified in Section 724.935(c)(l)
and
(2), and monitoring,
operating and inspection information
in Section 724.935(c) (3)
through
(8).
f)
For a control device other than
a thermal vapor incinerator,
catalytic vapor incinerator,
flare, boiler, process heater,
condenser,
or carbon adsorption Bystem, the Agency shall specify
the appropriate recordkeeping requirements,
indicating proper
operation and maintenance of the control device, in the RCRA
permit.
g)
The following information pertaining to all equipment subject to
the requirements
in Sections 724.952 through 724.960 must be
recorded in a log that is kept in the facility operating record:
1)
A list of identification numbers
for equipment
(except
welded fittings)
subject to the requirements of this
Subpart.
2)
List of Equipment
A)
A list of identification numbers
for equipment that
the owner or operator elects to designate for no
detectable emissions,
as indicated by an instrument
reading of less than 500 ppm above background, under
the provisions of Sections 724.952(e),
724.953(i) and
724.957(f).
117—477

158
B)
The designation of this equipment as subject to the
requirements of Sections 724.952(e),
724.953(i) or
724.957(f) must be signed by the owner or operator.
3)
A list of equipment identification numbers for pressure
relief devices required to comply with Section 724.954(a).
4)
Compliance teats.
A)
The dates of each compliance test required in Sections
724.952(e), 724.953(i),
724.954 and 724.957(f).
B)
The background level measured during each compliance
test.
C)
The maximum instrument reading measured at the
equipment during each compliance test.
5)
A
list of identification numbers for equipment in vacuum
service.
h)
The following information pertaining to all valves subject to the
requirements
of
Section
724.957(g)
and
(h)
must
be
recorded
in
a
log that
is kept in the facility operating record:
1)
A list of identification numbers for valves that are
designated as unsafe to monitor,
an explanation for each
valve stating why the valve is unsafe to monitor, and the
plan for monitoring each valve.
2)
A list of identification numbers for valves that are
designated
as difficult to monitor,
an explanation for each
valve stating why the valve
is difficult to monitor, and the
planned schedule for monitoring each valve.
i)
The following information must be recorded in the facility
operating record for valves complying with Section 724.962:
1)
A schedule of monitoring.
2)
The percent of valves found leaking during each monitoring
period.
j)
The following information must be recorded in a log that is kept
in the facility operating record:
1)
Criteria required in Section 724.952(d)(5)(B) and
724.953(e) (2)
and an explanation of the design criteria.
2)
Any changes to these criteria and the reasons for the
changes.
117—47 8

159
k)
The following information must be recorded in a log that
is kept
in the facility operating record for use in determining exemptions
as provided in Section 724.950 and other specific Subparts:
1)
An analysis determining the design capacity of the hazardous
waste management unit.
2)
A statement listing the hazardous waste influent to and
effluent from each hazardous waste management unit subject
to the requirements in Sections 724.960 and an analysis
determining whether these hazardous wastes are heavy
liquids.
3)
An up-to—date analysis and the supporting information and
data used to determine whether or not equipment is subject
to the requirements in Sections 724.952 through 724.960.
The record must include supporting documentation as required
by Section 724.963(d) (3) when application of the knowledge
of the nature of the hazardous wastestream or the process by
which
it was produced
is used.
If the owner or operator
takes any action
(e.g., changing the process that produced
the waste)
that could result in an increase in the total
organic
content
of
the
waste
contained
in
or
contacted
by
equipment determined not to be subject to the requirements
in Sections 724.952 through 724.960, then a new
determination is required.
1)
Records of the equipment leak information required by subsection
(d) and the operating information required by subsection
(e) need
be kept only
3 years.
rn)
The owner or operator of any facility that
is subject to this
Subpart and to regulations
at 40 CFR 60,
Subpart VV, or 40 CFR 61,
Subpart V,
incorporated by reference in
35 Ill. Adm. Code 720.111,
may elect to determine compliance with this Subpart by
documentation
either
pursuant
to
Section
724.964,
or
pursuant
to
those provisions of 40 CFR 60 or 61,
to the extent that the
documentation under the regulation at 40 CFR 60 or 61 duplicates
the documentation required under this Subpart.
The documentation
under the regulation at 40 CFR 60 or 61 must be kept with or made
readily available with the facility operating record.
(Source:
Added at
15
Ill.
Reg.
,
effective
)
Section 724.965
Reporting Requirements
a)
A semiannual report must be submitted by owners and operators
subject to the requirements of this Subpart to the Agency by dates
specified
in
the
RCRA permit.
The report must include the
following information:
117—479

160
1)
The USEPA identification number
(35 Ill. Adm. Code 722.112),
name, and address of the facility.
2)
For each month during the semiannual reporting period:
A)
The equipment identification number of each valve for
which a leak was not repaired as required in Section
724.957(d).
B)
The eqi~iipmentidentification number of each pump for
which a leak was not repaired as required in Sections
724.952(c) and (d)(6).
C)
The
equipment
identification
number
of
each
compressor
for
which
a
leak
was
not
repaired
as
required
in
Section
724.953(g),
3)
Dates
of
hazardous
waste
management
unit
shutdowns
that
occurred
within
the
semiannual
reporting
period.
4)
For
each
month
during
the
semiannual
reporting
period,
dates
when
the
control
device
installed
as
required
by
Sections
724.952,
724.953,
724.954
or
724.955,
exceeded
or
operated
outside
of
the
design
specifications
as
defined
in
Section
724.964(e)
and
as
indicated
by
the
control
device
monitoring
required
by
Section
724.960
and
was
not
corrected
within
24
hours,
the
duration
and
cause
of
each
exceedance,
and
any
corrective
measures
taken.
b)
If,
during
the
semiannual
reporting
period,
leaks
from
valves,
pumps and compressors are repaired as required in Sections
724.957(d),
724.952(c) and (d)(6),
and 724.953(g), respectively,
and the control device does not exceed or operate outside of the
design specifications as defined
in Section 724.964(e)
for more
than 24 hours,
a report to the Agency is not required.
(Source:
Added at 15
Ill. Reg.
,
effective
)
117—480

161
TITLE 35:
ENVIRONMENTAL PROTECTION
SUBTITLE
G:
WASTE
DISPOSAL
CHAPTER
I:
POLLUTION
CONTROL
BOARD
SUBCHAPTER
c:
HAZARDOUS
WASTE
OPERATING
REQUIREMENTS
PART
725
INTERIM
STATUS
STANDARDS FOR
OWNERS
AND
OPERATORS
OF
HAZARDOUS
WASTE TREATMENT, STORAGE
AND
DISPOSAL
FACILITIES
SUBPART A:
GENERAL
PROVISIONS
Sect ion
725.101
Purpose,
Scope
and
Applicability
725.104
Imminent
Hazard
Action
SUBPART
B:
GENERAL
FACILITY
STANDARDS
Section
725.110
Applicability
725.111
USEPA
Identification
Number
725.112
Required Notices
725.113
General Waste Analysis
725.114
Security
725.115
General Inspection Requirements
725.116
Personnel Training
725.117
General Requirements
for Ignitable, Reactive or Incompatible
Wastes
725.118
Location Standards
SUBPART C:
PREPAREDNESS
AND
PREVENTION
Section
725.130
Applicability
725.131
Maintenance and Operation of Facility
725.132
Required Equipment
725.133
Testing
and
Maintenance
of
Equipment
725.134
Access
to
Coffimunications
or
Alarm
System
725.135
Required Aisle Space
725.137
Arrangements with Local Authorities
SUBPART D:
CONTINGENCY PLAN
AND
EMERGENCY PROCEDURES
Sect ion
725.150
Applicability
725.151
Purpose
and
Implementation
of
Contingency
Plan
725.152
Content
of
Contingency
Plan
725.153
Copies of Contingency Plan
725.154
Amendment of Contingency Plan
725.155
Emergency Coordinator
725.156
Emergency
Procedures
SUBPART
E:
MANIFEST SYSTEM, RECORDKEEPING AND REPORTING
Section
725.170
Applicability
725.171
Use
of
Manifest
System
725.172
Manifest
Discrepancies
117—48 1

162
725.173
Operating Record
725.174
Availability,
Retention and Disposition of Records
725.175
Annual Report
725.176
Unmanifested Waste Report
725.177
Additional Reports
SUBPART F:
GROUNDWATER MONITORING
Section
725.190
Applicability
725.191
Groundwater Monitoring System
725.192
Sampling and Analysis
725.193
Preparation,
Evaluation and Response
725.194
Recordkeeping and Reporting
SUBPART G:
CLOSURE AND POST-CLOSURE
Section
725.210
Applicability
725.211
Closure Performance Standard
725.212
Closure Plan; Amendment of Plan
725.213
Closure; Time Allowed for Closure
725.214
Disposal or Decontamination
of Equipment, Structures and Soils
725.215
Certification of Closure
725.216
Survey Plat
725.217
Post-closure Care and Use of Property
725.218
Post—closure Plan; Amendment of Plan
725.219
Post-Closure Notices
725.220
Certification of Completion of Post-Closure Care
SUBPART H:
FINANCIAL REQUIREMENTS
Section
725.240
Applicability
725.241
Definitions of Terms as Used in this Subpart
725.242
Cost Estimate for Closure
725.243
Financial Assurance for Closure
725.244
Cost Estimate for Post-closure Care
725.245
Financial Assurance for Post—closure Monitoring and Maintenance
725.246
Use of a Mechanism for Financial Assurance of Both Closure and
Post-closure Care
725.247
Liability Requirements
725.248
Incapacity of Owners or Operators, Guarantors or Financial
Institutions
725.251
Promulgation of Forms
(Repealed)
SUBPART
I:
USE
AND
MANAGEMENT OF CONTAINERS
Section
725.270
Applicability
725.271
Condition of Containers
725.272
Compatibility of Waste with Container
725.273
Management of Containers
725.274
Inspections
725.276
Special Requirements for Ignitable or Reactive Waste
725.277
Special Requirements for Incompatible Wastes
117—482

163
SUBPART J:
TANK SYSTEMS
Section
725.290
Applicability
725.291
Assessment of Existing Tank System’s Integrity
725.292
Design and Installation of New Tank Systems or Components
725.293
Containment and Detection of Releases
725.294
General Operating Requirements
725.295
Inspections
725.296
Response to leaks or spills and disposition of Tank Systems
725.297
Closure and Post—Closure Care
725.298
Special Requirements for Ignitable or Reactive Waste
725.299
Special Requirements for Incompatible Wastes
725.300
Waste Analysis and Trial Tests
725.301
Generators of 100 to 1000 kg/mo.
SUBPART K:
SURFACE IMPOUNDMENTS
Section
725.320
Applicability
725.321
Design Requirements
725.322
General Operating Requirements
725.323
Containment System
725.325
Waste Analysis and Trial Tests
725.326
Inspections
725.328
Closure and Post—Closure Care
725.329
Special Requirements for Ignitable or Reactive Waste
725.330
Special Requirements for Incompatible Wastes
SUBPART L:
WASTE PILES
Section
725.350
Applicability
725.351
Protection from Wind
725.352
Waste Analysis
725.353
Containment
725.354
Design Requirements
725.356
Special Requirements
for Ignitable or Reactive Waste
725.357
Special Requirements for Incompatible Wastes
725.358
Closure and Post-Closure Care
SUBPART H:
LAND TREATMENT
Section
725.370
Applicability
725.372
General Operating Requirements
725.373
Waste Analysis
725.376
Food Chain Crops
725.378
Unsaturated Zone (Zone of Aeration) Monitoring
725.379
Recordkeeping
725.380
Closure and Post—closure
725.381
Special Requirements for Ignitable or Reactive Waste
725.382
Special Requirements for Incompatible Wastes
117—483

164
SUBPART N:
LANDFILLS
Section
725.400
Applicability
725.401
Design Requirements
725.402
General Operating Requirements
725.409
Surveying and Recordkeeping
725.410
Closure and Post—Closure
725.412
Special Requirements for Ignitable or Reactive Waste
725.413
Special Requirements for Incompatible Wastes
725.414
Special Requirements for Liquid Wastes
725.415
Special Requirements for Containers
725.416
Disposal of Small Containers of Hazardous Waste in Overpacked
Drums
(Lab Packs)
SUBPART 0:
INCINERATORS
Section
725.440
Applicability
725.441
Waste Analysis
725.445
General Operating Requirements
725.447
Monitoring and Inspection
725.451
Closure
725.452
Interim Status Incinerators Burning Particular Hazardous Wastes
SUBPART
P:
THERMAL TREATMENT
Section
725.470
Other Thermal Treatment
725.473
General Operating Requirements
725.475
Waste Analysis
725.477
Monitoring and Inspections
725.481
Closure
725.482
Open Burning; Waste Explosives
725.483
Interim Status Thermal Treatment Devices Burning Particular
Hazardous Waste
SUBPART Q:
CHEMICAL, PHYSICAL AND BIOLOGICAL TREATMENT
Section
725.500
Applicability
725.501
General Operating Requirements
725.502
Waste Analysis and Trial Tests
725.503
Inspections
725.504
Closure
725.505
Special Requirements for Ignitable or Reactive Waste
725.506
Special Requirements for Incompatible Wastes
SUBPART R:
UNDERGROUND INJECTION
Section
725. 530
Applicability
Appendix A
Recordkeeping Instructions
Appendix B
EPA Report Form and Instructions (Repealed)
Appendix C
EPA Interim Primary Drinking Water Standards
Appendix D
Tests for Significance
117—484

165
Appendix E
Examples of Potentially Incompatible Waste
AUTHORITY:
Implementing Section 22.4 and authorized by Section 27 of the
Environmental
Protection
Act
(Ill.
Rev.
Stat.
1989,
ch.
111—1/2,
pars.
1022.4
and 1027).
SOURCE:
Adopted in R81—22, 43 PCB 427,
at
5 Ill. Reg. 9781, effective as
noted in 35
Ill.
Adrn.
Code
700.106;
amended
and
codified
in
R81—22,
45
PCB
317,
at 6
Ill. Reg.
4828, effective as noted in 35 Ill. Adm. Code 700.106;
amended in R82—18,
51 PCB 831,
at
7
Ill. Reg. 2518,
effective February 22,
1983;
amended
in
R82—l9,
53
PCB
131,
at
7
Ill.
Reg.
14034,
effective
October
12,
1983; amended in R84—9,
at 9 Ill.
Reg.
11869, effective July 24,
1985;
amended in R85-22 at 10
Ill.
Reg.
1085, effective January
2,
1986;
amended in
R86-1
at
10
Ill.
Reg.
14069, effective August
12,
1986; amended in R86—28 at
11
Ill. Reg.
6044,
effective March 24,
1987;
amended
in R86—46 at
11
Ill. Reg.
13489, effective August 4, 1987;
amended
in R87-5 at
11
Ill.
Reg.
19338,
effective November 10,
1987;
amended in R87-26 at 12
111. Reg.
2485, effective
January 15,
1988; amended
in R87—39 at
12
Ill. Reg.
13027,
effective July 29,
1988;
amended in R88—16
at
13
Ill. Reg.
437, effective December 28, 1988;
amended
in R89—1 at
13
Ill. Reg.
18354, effective November 13,
1989;
amended
in R90—2 at
3.4
Ill.
Reg.
14447, effective August 22,
1990;
amended in R90—lO
at 14
Ill.
Reg.
16498, effective September 25,
1990;
amended in R90—11
at
15
Ill.
Reg.
,
effective
SUBPART
A:
GENERAL PROVISIONS
Section 725.101
PurpoBe, Scope and Applicability
a)
The purpose of this Part
is to establish minimum standards which
define the acceptable management of hazardous waste during the
period of interim status and until certification of final closure
or,
if the facility is
subject to post—closure requirements,
until
post-closure responsibilities are fulfilled.
b)
The standards in this Part apply to owners and operators of
facilities which treat,
store or dispose of hazardous waste who
have fully complied with the requirements for interim status under
Section
3005(e)
of
the
Resource
Conservation
and
Recovery
Act
(RCRA)
(42 U.S.C.
6901 et seq.)
and 35 Ill.
Adm. Code 703, until
either a permit
is issued under Section 3005 of the Resource
Conservation and Recovery Act or Section 21(f)
of the
Environmental Protection Act, or until applicable closure and
post-closure responsibilities under this Part are fulfilled,
and
to those owners and operators of facilities
in existence on
November
19,
1980,
who have failed to provide timely notification
as required by Section 3010(a) of RCRA,
or failed to file Part A
of the Permit Application as required by 40 CFR 270.10(e)
and
(g)
or 35 Ill.
Adm. Code 703.150 and 703.152.
These standards apply
to all treatment,
storage or disposal of hazardous waste at these
facilities after November
19,
1980,
except as specifically
provided otherwise in this Part or
35
Ill.
Adni. Code 721;
117—485

166
BOARD NOTE:
As stated in Section 3005(a) of RCRA,
after
the
effective
date
of
regulations
under
that
Section,
i.e.,
40
CFR
270
and
124,
the
treatment,
storage
or
disposal
of
hazardous
waste
is
prohibited except in accordance with a permit.
Section 3005(e) of
RCRA provides for the continued operation of an existing facility
which meets certain conditions until final administrative
disposition of the owner’s and operator’s permit application is
made.
35 Ill. Adm. Code 703.140 et
seq. provide that
a permit is
deemed issued under Section 2l(f)(1)
of the Environmental
Protection Act under conditions similar to federal
interim status.
c)
The requirements of this Part do not apply to:
1)
A person disposing of hazardous waste by means of ocean
disposal subject to a permit issued under the Marine
Protection, Research
and
Sanctuaries Act
(16 U.S.C.
1431—
1434;
33 U.S.C.
1401);
BOARD
NOTE:
This Part applies to the treatment or storage
of hazardous waste before
it
is loaded into an ocean vessel
for incineration or disposal at
sea,
as provided in
subsection
(b).
3)
The
owner
or operator of a POTW (publicly owned treatment
works) which treats,
stores or disposes of hazardous waste;
BOARD NOTE:
The owner or operator of a facility under
subsections
(c)(1) through (c)(3)
is subject to the
requirements of
35
Ill. Adm. Code 724 to the extent they are
included in a permit by rule granted to such
a person under
35
Ill.
Adm. Code 702 and 703 or are required by 35
Ill.
Adm. Code 704.Subpart
F.
5)
The owner or operator of
a facility permitted,
licensed or
registered by Illinois to manage municipal or industrial
solid waste,
if the only hazardous waste the facility
treats,
stores or disposes of
is excluded from regulation
under this Part by
35
Ill.
Adm. Code 721.105;
6)
The owner or operator of a facility managing recyclable
materials described
in
35
Ill.
Adm. Code 72l.106(a)(2)
and
(3)
(except to the extent that requirements of this Part are
referred to in 35
Ill. Adm.
Code 726.Subparts C,
D,
F or G;
7)
A generator accumulating waste on-site in compliance with 35
Ill. Adm. Code 722.134,
except to the extent the
requirements are included in 35
Ill. Adm.
Code 722.134;
8)
A farmer disposing of waste pesticides
from the farmer’s own
use in compliance with
35
Ill.
Adm. Code 722.170;
117—486

167
9)
The owner or operator of
a totally enclosed treatment
facility,
as defined in 35
Ill.
Adm. Code 720.110;
10)
The owner or operator of an elementary neutralization unit
or
a wastewater treatment unit as defined in 35
Ill. Adm.
Code 720.110;
11)
Immediate response:
A)
Except as provided in subsection (c)(11)(B),
a person
engaged in treatment or containment activities during
immediate response to any of the following situations:
i)
A discharge of
a hazardous waste;
ii)
An imminent and substantial threat of
a
discharge of
a hazardous waste;
iii)
A discharge of
a material which, when
discharged, becomes
a hazardous waste.
B)
An owner or operator of
a. facility otherwise regulated
by this Part must comply with all applicable
requirements of Subparts C and D.
C)
Any person who
is covered by subsection
(c)(11)(A) and
who continues or initiates hazardous waste treatment
or containment activities after the
immediate
response
is over
is subject to all applicable requirements of
this Part and
35
Ill.
Adm. Code 702, 703 and 705 for
those activities.
12)
A transporter storing manifested shipments of hazardous
waste
in containers meeting the requirements of 35 Ill. Adm.
Code 722.130 at a transfer facility for a period of ten days
or less.
13)
The addition of absorbent material to waste in a container
(as defined in 35
Ill.
Adni. Code 720.110), or the addition
of waste to the absorbent material in a container, provided
that these actions occur at the time waste is first placed
in the containers; and Sections 725.117(b),
725.271 and
725.272 are complied with.
d)
The following hazardous wastes must not be managed at facilities
subject to regulation under this Part:
hazardous waste numbers
F020,
F021, F022,
P023,
F026 or F027 unless:
1)
The wastewater treatment sludge is generated in a surface
impoundment as part of the plant’s wastewater treatment
system;
117—487

168
2)
The waste is stored in tanks or containers;
3)
The waste
is stored or treated in waste piles that meet the
requirements of 35
Ill.
Adrn.
Code 724.350(c)
as well as all
other applicable requirements of Subpart L;
4)
The waste is burned in incinerators that are certified
pursuant to the standards and procedures in Section 725.452;
or
5)
The waste is burned in facilities that thermally treat the
waste in a device other than an incinerator and that are
certified pursuant to the standards and procedures in
Section 725.483.
e)
This Part applies to owners and operators of facilities which
treat,
store
or
dispose
of
hazardous
wastes
referred
to
in
35
Ill.
Adm. Code 728, and the
35
Ill.
Adm. Code 728 standards are
considered material conditions or requirements of the interim
status standards of this Part.
f)
35
Ill.
Adm. Code 700 contains rules concerning application of
other Board regulations.
(Source:
Amended at 15
Ill.
Reg.
,
effective
)
SUBPART
B:
GENERAL FACILITY STANDARDS
Section 725.113
General Waste Analysis
a)
Waste analysis:
1)
Before an owner or operator treats,
stores or disposes of
any hazardous waste,
or non-hazardous waste
if applicable
under Section 725.213(d),
the owner or operator shall obtain
a detailed chemical and physical analysis of
a
representative sample of the waste.
At a minimum, this
analysis must contain all
the information which must be
known to treat,
store or dispose of the waste in accordance
with the requirements of this Part and 35 Ill. Adm. Code
728.
2)
The analysis may include data developed under 35
Ill. Adm.
Code 721 and existing published or documented data on the
hazardous waste or on waste generated from similar
processes.
BOARD NOTE:
For example, the facility’s record of analyses
performed on the waste before the effective date of these
regulations or studies conducted on hazardous waste
generated from processes similar to that which generated the
117—488

169
waste to be managed at the facility may be included in the
data base required to comply with subsection (a)(1). except
as otherwise specified in 35
Ill.
Adni. Code 728.107(b~and
idì.
The owner or operator of an off—site facility may
arrange for the generator of the hazardous waste to supply
part or all of the information required by subsection
(a)(1).
If the generator does not supply the information
and the owner or operator chooses to accept
a hazardous
waste,
the owner or operator
is responsible for obtaining
the information required to comply with this Section.
3)
The analysis must be repeated as necessary to ensure that it
is accurate and up to date.
At a minimum, the analysis must
be repeated:
A)
When the owner or operator is notified, or has reason
to believe,
that the process or operation generating
the hazardous waste, or non—hazardous waste if
applicable under Section 725.213(d),
has changed;
and
B)
For off—site facilities, when the results of the
inspection required
in subsection
(a)(4) indicate that
the hazardous waste received at the facility does not
match the waste designated on the accompanying
manifest or shipping paper.
4)
The owner or operator of an off-site facility shall inspect
and,
if necessary,
analyze each hazardous waste movement
received at the facility to determine whether
it matches the
identity of the waste specified on the accompanying manifest
or shipping paper.
b)
The owner or operator shall develop and follow a written waste
analysis plan which describes the procedures which the owner or
operator will carry out to comply with subsection
(a).
The owner
or operator shall keep this plan at the facility.
At
a minimum,
the plan must specify:
1)
The parameters for which each hazardous waste, or non—
hazardous waste
if applicable under Section 725.213(d),
will
be analyzed and the rationale for the selection of these
parameters (i.e., how analysis for these parameters will
provide sufficient information
on the waste’s properties to
comply with subsection
(a).
2)
The test methods which will be used to test for these
parameters.
3)
The sampling method which will be used to obtain a
representative sample of the waste to be analyzed.
A
representative sample may be obtained using either:
117—489

170
A)
One of the sampling methods described in 35
Ill. Adm.
Code 721.Appendix A or
B)
An equivalent sampling method.
BOARD NOTE:
See 35
Ill. Adm. Code 720.120(c)
for
related discussion.
4)
The frequency with which the initial analysis of the waste
will be reviewed or repeated to ensure that the analysis
is
accurate and up—to—date.
5)
For off—site facilities, the waste analyses that hazardous
waste generators have agreed to supply.
6)
Where applicable,
the methods which will be used to meet the
additional waste analysis requirements for specific waste
management methods as specified in Sections 725.293,
725.325,
725.352, 725.373,
725.414,
725.441, 725.475~er~4
725.502,
725.934(d)
and 725.963(d),
and 35
Ill.
Adm.
Code
728.107.
And,
7)
For surface impoundments exempted from land disposal
restrictions under
35
Ill.
Adm.
Code 728.104(a), the
procedures
and
schedules
for:
A)
The sampling of impoundment contents;
B)
The analysis of test data; and,
C)
The annual removal of residues which are not delisted
under
35
Ill.
Adm.
Code 720.122 or which exhibit
a
characteristic of hazardous waste,
and either:
i)
Do not meet applicable treatment standards of 35
Ill. Adm. Code 728.Subpart
D; or
ii)
Where no treatment standards have been
established:
Such residues are prohibited from
land
disposal
under
35
Ill.
Adm. Code 728.132 or
728.139;
or
such
residues
are
prohibited
from
land disposal under 35
Ill.
Adni.
Code
728.133(f).
C)
For off—site facilities,
the waste analysis plan required in
subsection
(b)
must also specify the procedures which will be used
to inspect and,
if necessary,
analyze each movement of hazardous
waste received at the facility to ensure that
it matches the
identity of the waste designated on the accompanying manifest or
shipping paper.
At
a minimum,
the plan must describe:
117—490

171
1)
The procedures which will be used to determine the identity
of each movement of waste managed at the facility;
and
2)
The sampling method which will be used to obtain a
representative sample of the waste to be identified,
if the
identification method includes sampling.
(Source:
Amended at
15
Ill.
Reg.
,
effective
)
Section 725.115
General Inspection Requirements
a)
The owner or operator shall inspect the facility for malfunctions
and deterioration, operator errors and discharges which may be
causing
——
or may lead to
——
the conditions listed below.
The
owner or operator shall conduct these inspections often enough to
identify problems in time to correct them before they harm human
health or the environment.
1)
Release of hazardous waste constituents to the environment
or
2)
A threat to human health.
b)
1)
The owner or operator shall develop and follow a written
schedule for inspecting all monitoring equipment, safety and
emergency equipment,
security devices and operating and
structural equipment
(such as dikes and sump pumps)
that are
important to preventing, detecting or responding to
environmental or human health hazards.
2)
The owner or operator shall keep this schedule at the
facility.
3)
The schedule must identify the types of problems (e.g.,
malfunctions or deterioration) which are to be looked for
during the inspection
(e.g.,
inoperative sump pump,
leaking
fitting, eroding dike,
etc.).
4)
The frequency of inspection may vary for the items on the
schedule.
However,
it should be based on the rate of
possible deterioration of the equipment and the probability
of an environmental or human health incident
if the
deterioration or malfunction or any operator error goes
undetected between inspections.
Areas subject to spills,
such as loading and unloading areas, must be inspected daily
when
in use.
At
a minimum, the inspection schedule must
include the items and frequencies called
for in Sections
725.274,
725.293, 725.295,
725.326, 725.447, 725.477~~.ei~ê
725.503,
725.933,
725.952,
725.953 and 725.958.
c)
The owner or operator shall remedy any deterioration or
malfunction of equipment or structure which the inspection reveals
117—491

172
on a schedule which ensures that the problem does not lead to an
environmental or human health hazard.
Where a hazard is
imminent
or has already occurred,
remedial action must be taken
immediately.
d)
The owner or operator shall record inspections in an inspection
log or summary.
The owner or operator shall keep these records
for at least three years from the date of inspection.
At a
minimum, these records must include the date and
time
of the
inspection, the name of the inspector,
a notation of the
observations made and the date and nature of any repairs or other
remedial actions.
(Source:
Amended at
15
Ill. Reg.
,
effective
)
SUBPART
E:
MANIFEST SYSTEM,
RECORDKEEPING
AND
REPORTING
Section 725.173
Operating Record
a)
The owner or operator shall keep
a written operating record at the
facility.
b)
The following information must be recorded as it becomes available
and maintained in the operating record until closure of the
facility.
1)
A description and the quantity of each hazardous waste
received and the method or methods and date or dates of its
treatment,
storage or disposal
at the facility as required
by Appendix A;
2)
The location of each hazardous waste within the facility and
the quantity at each location.
For disposal facilities the
location and quantity
of each hazardous waste must be
recorded on a map or
diagram
of
each cell or disposal area.
For all facilities this information must include cross-
references to specific manifest document
numbers
if the
waste was accompanied by a manifest;
BOARD NOTE:
See Sections 725.219,
725.379 and 725.409 for
related requirements.
3)
Records and results of waste analysis and trial tests
performed
as specified
in Sections 725.113,
725.293,
725.325,
725.352,
725.373,
725.414,
725.441,
725.475., e~
725.502,
725.934 and 725.963 and 35
Ill. Adm. Code
728.104(a)
and 728.107;
4)
Summary reports and details of all incidents that require
implementing the contingency plan as 8pecified in Section
725.156(j);
117—492

173
5)
Records and results of inspections
as required by Sections
725.115(d)
(except these data need be kept only three
years);
6)
Monitoring, testing or analytical data where required by
Sections 725.190,
725.194, 725.291,
725.293,
725.295,
725.376,
725.378,
725.380(d)(1), 725.447~ei~4725.477k
725.934c~ through
(f),
725.935, 725.963(d) through
(i)
and
725.964
BOARD NOTE:
As required by Section 725.194, monitoring data
at disposal facilities must be kept throughout the post—
closure period.
7)
All closure cost estimates under Section 725.242 and,
for
disposal
facilities,
all
post—closure
cost
estimates
under
Section
725.244;
8)
Records of the quantities
(and date of placement) for each
shipment of hazardous waste placed In land disposal units
under an extension of the effective date of any land
disposal restriction granted pursuant to 35
Ill. Adm. Code
728.105,
a petition pursuant to 35 Ill. Adm. Code 728.106 or
a certification under 35
Ill. Adm.
Code 728.108, and the
applicable notice required of
a generator under 35
Ill. Adm.
Code 728.107(a);
9)
For an off—site treatment facility,
a copy of the notice,
and the certification and demonstration,
if applicable,
required of the generator or the owner or operator under 35
Ill. Adm.
Code 728.107 or 728.108;
10)
For an on-site treatment facility, the information contained
in the notice
(except the manifest
number),
and
the
certification and demonstration,
if applicable, required of
the generator or the owner or operator under 35
Ill. Adm.
Code 728.107 or 728.108;
11)
For
an
off—site
land
disposal
facility,
a
copy
of
the
notice,
and the certification and demonstration,
if
applicable,
required of the generator or the
owner
or
operator of a treatment facility under 35
Ill.
Adm. Code
728.107 or 728.108, whichever
is applicable;
and
12)
For an on—site land disposal facility, the information
contained in the notice required of the generator or owner
or operator of
a treatment facility under 35
Ill.
Adm. Code
728.107,
except
for the manifest number, and the
certification and demonstration,
if applicable, required
under 35
Ill.
Adni.
Code 728.108, whichever is applicable.
117—493

174
13)
For an off—site storage facility,
a copy of the notice,
and
the certification and demonstration if applicable, required
of the generator or the owner or operator under 35
Ill.
Adni.
Code 728.107 or 728.108;
and,
14)
For an on-site storage facility,
the information contained
in the notice
(except the manifest number), and the
certification and demonstration if applicable, required of
the generator or the owner or operator under
35 Ill. Adm.
Code 728.107 or 728.108.
(Source:
Amended at
15 Ill. Reg.
,
effective
Section 725.177
Additional Reports
In addition to submitting the annual report and unnianifestèd waste reports
described in ~Sections
725.175 and 725.176, the owner or operator mustshall
also report to the DirectorAgency:
a)
Releases,
fires and explosions
as specified in SSection
725.156(j);
b)
Groundwater contamination and monitoring data as specified in
ffSection 725.193 and 725.194;
er’~4
C)
Facility closure as specified in ~Section 725.215~-; and
~j.
As otherwise required by Subparts AA and BB.
(Source:
Amended at
15 Ill. Reg.
,
effective
SUBPART K:
SURFACE IMPOUNDMENTS
Section 725.329
Special Requirements for Ignitable or Reactive Waste
Ignitable or reactive waste must not be placed in a surface impoundment,
unless the waste and impoundment satisfy all applicable requirements of
35
Ill.
Adm. Code
728,
and:
a)
The waste is treated, rendered or mixed before or immediately
after placement in the impoundment
so that
1)
The resulting waste,
mixture or dissolution of material no
longer meets the definition of ignitable or reactive waste
under 35
Ill.
Adm. Code 721.121 or 721.123;
and
2)
Section 725.117(b)
is complied with;
or
117—494

175
b)
Management conditions.
1)
The waste
is managed in such a way that
it
is protected from
any material or conditions which may cause it to ignite or
react; and
2)
The owner or operator obtains a certification from a
qualified chemist or engineer that, to the best of the
chemist or engineer’s knowledge and opinion, the design
features or operating plans of the facility will prevent
ignition or reaction;
and
3)
The certification and the basis for it are maintained at the
facility;
or
c)
The surface
impoundment
is used solely for emergencies.
(Source:
Amended at
15
Ill.
Reg.
,
effective
SUBPART L:
WASTE PILES
Section 725.356
Special Requirements for Ignitable or Reactive Waste
Ignitable or reactive wastee must not be placed in a pile unless the waste and
pile meet all
applicable requirements of
35
Ill.
Adrn. Code 728,
and:
a)
Addition of the waste to an existing pile~
1)
Results in the waste or mixture no longer meeting the
definjtion of
ignitable or reactive waste under ~35
Ill.
Adm. Code 721.121 or 721.123k and
2)
Complies with S~Section725.117(b); or
b)
The waste is managed in such a way that
it
is protected from any
material or conditions which may cause
it to ignite or react.
(Source:
Amended
at
15
Ill.
Reg.
,
effective
)
SUBPART M:
LAND TREATMENT
Section 725.381
Special Requirements for Ignitable or Reactive Waste
Ignitabic or reactive wastes must not be land troeted unlcee:The owner or
operator shall not a~~lvignitable or reactive waste to the treatment zone
unless unless the waste and treatment zone meet all
applicable requirements of
35
Ill.
Adni.
Code 728,
and:
a)
The waste is immediately incorporated into the soil so that:
117—495

176
1)
The resulting waste,
mixture or dissolution of material no
longer meets the definition of ignitable or reactive waste
under Cectign 725.121 or 35 Ill. Adm. Code 721.121 or
721.123; and
2)
Section ~&ij4.1l7(b)
is complied with; or
b)
The waste
is managed in such a way that it
is protected from any
material or conditions which may cause
it to ignite or react.
(Source:
Amended at
15 Ill. Reg.
,
effective
)
SUBPART N:
LANDFILLS
Section 725.412
Special Requirements for Ignitable or Reactive Waste
a)
Except as provided in peragraphsubsection
(b) and in Section
725.416,
ignitable or reactive waste must not be placed in a
landfill, unless the waste and landfill meets all applicable
requirements of
35
Ill. Adm. Code 728,
and the waste
is treated,
rendered or mixed before or immediately after placement in a
landfill
so that:
1)
The resulting waste, mixture or dissolution of material no
longer meets the definition of ignitable or reactive waste
under 35
Ill. Adm. Code 721.121 or 721.123;
and
2)
Section 725.117(b)
is
complied with.
b)
~Except for prohibited wastes which remain subiect to treatment
standards
in 35
Ill. Adm.
Code 728.Subpart D,
ignitable waste
in
containers may be landfilled without meeting the requirements of
paragraphsubsection
(a),
provided that the wastes are disposed of
in such a way that they are protected from any material or
conditions which may cause them to ignite.
At a minimum,
ignitable
wastes
must
be
disposed
of
in
non—leaking
containers
which are carefully handled and placed so as to avoid heat,
sparks, rupture or any other condition that might cause ignition
of the wastes; must be covered daily with soil or other non—
combustible
material
to
minimize
the
potential
for
ignition
of
the
wastes; and must not be disposed in cells that contain or will
contain other wastes which may generate heat sufficient to cause
ignition of the waste.
(Source:
Amended at
15 Ill. Reg.
,
effective
)
Section
725.416
Disposal
of
Small
Containers
of
Hazardous
Waste
in
Overpacked Drums
(Lab Packs)
Small
containers
of
hazardous
waste
in
overpacked
drums
(lab
packs)
may
be
placed
in
a
landfill
if
the
following
requirements
are
met:
117—49 6

177
a)
Hazardous waste must be packaged
in non—leaking inside containers.
The inside containers must be of
a design and constructed of a
material that will not react dangerously with,
be decomposed by or
be ignited by the contained waste.
The inside containers must be
tightly and securely Bealed.
The inside containers must be of the
size and
type
specified in the Department of Transportation
(DOT)
hazardous materials regulations
(49 CFR 173, 178 and l79.~.
incorporated by reference
in 35
Ill.
Adm. Code 720.111),
if those
regulations specify a particular inside container for the waste.
b)
The inside containers must be overpacked in an open head DOT—
specification metal shipping container
(49 CFR 178 and 179)
of no
more than 416 liter (110 gallon)
capacity and surrounded by,
at a
minimum,
a sufficient quantity of absorbent material to completely
absorb all of the liquid contents of the inside containers.
The
metal outer container must be full after packing with inside
containers and absorbent material.
C)
In accordance with Section 725.117(b), the absorbent material used
must not be capable of reacting dangerously with,
being decomposed
by or being ignited by the contents of the inside containers.
d)
Incompatible waste,
as defined
in
35
Ill.
Adm. Code 720.110, must
not be placed
in the same outside container.
e)
Reactive wastes,
other than cyanide— or sulfide—bearing waste as
defined in 35
Ill. Adm. Code 721.123(a)(5), must be treated or
rendered non—reactive prior to packaging in accordance with
paragraphsubsections
(a) through
(d).
Cyanide- and sulfide—
bearing reacitve waste may be packed in accordance with
paragraphsubsections
(a) through
(d) without first being treated
or rendered non—reactive.
£1
Such disposal
is in compliance with the requirements of 35
Ill.
Adm. Code 728.
Persons who incinerate lab packs according to the
requirements of
35
Ill. Adm.
Code 728.142(c)(1) may use fiber
drums
in place of metal outer containers.
Such fiber drums must
meet the DOT specifications in 49 CFR 171.12
and be overpacked
according to subsection
(b).
9)
Pursuant to 35
Ill. Adm. Code 729.312, the use of labpacks for
disposal of liquid wastes or wastes containing free liquids
allowed under this Section is restricted to labwaste and non-
periodic waste,
as those terms are defined in that Part.
(Source:
Amended at
15
Ill. Reg.
,
effective
)
117—49 7

178
SUBPART
AR:
AIR
EMISSION
STANDARDS FOR PROCESS
VENTS
Section 725.930
Applicability
a)
This Subpart applies to owners and operators of
facilities that
treat,
store or dispose of hazardous wastes
(except as provided in
Section 725.101).
b)
Except for Sections 725.934(d)
and 725.935(e), this Subpart
applies to process vents associated with distillation,
fractionation,
thin—film evaporation,
solvent extraction,
or air
or steam stripping operations that manage hazardous wastes with
organic concentrations of
at least 10 ppmw (parts per million by
weight),
if these operations are conducted in:
1)
Units that are subject to the permitting requirements of
35
Ill.
Adni.
Code 703; or
2)
Hazardous waste recycling units that are located on
hazardous waste management facilities otherwise subject to
the permitting requirements of
35
Ill.
Adni.
Code 703.
BOARD NOTE:
The requirements of Sections
725.932 through
725.936 apply to process vents on hazardous waste recycling
units previously exempt under
35 Ill. Adm. Code
72l.106(c)(1).
Other exemptions under 35
Ill. Adm. Code
721.104,
722.134 and 725.101(c) are not affected by these
requirements.
c)
Agency decisions pursuant to this Part must be made in writing,
are in the nature of permit decisions pursuant to Section 39 of
the Environmental Protection Act and may be appealed to the Board
pursuant to
35
Ill.
Adm.
Code
105.
(Source:
Added at
15
Ill.
Reg.
,
effective
Section 725.931
Definitions
As
used
in
this
Subpart,
all
terms
not
defined
in
the
Subpart
have
the
meaning
given them in
35
Ill.
Adm. Code 724.931,
the Resource Conservation and
Recovery Act and 35
Ill.
Adni. Code 720 through 726.
BTU means British thermal unit.
ft means foot.
h means hour.
kg means kilogram.
kPa means kilopascals.
117—498

179
lb means pound.
m means meter.
Mg means Megagrams,
or metric tonnes.
MJ means Megajoules,
or ten to the sixth Joules.
MW means Megawatts.
ppmv means parts per million by volume.
ppmw meant parts per million by weight.
s means second.
scm means standard cubic meter.
scft meant standard cubic foot.
yr means year.
(Source:
Added at
15
Ill. Reg.
,
effective
Section 725.932
Standards: Process Vents
a)
The owner or operator of
a facility with process vents associated
with distillation, fractionation, thin-film evaporation, solvent
extraction, or air or steam stripping operations managing
hazardous wastes with organic concentrations of at least 10 ppmw
shall either:
1)
Reduce total organic emissions
from all affected process
vents at the facility below 1.4 kg/h
(3 lb/h)
and 2.8 Mg/yr
(3.1 tons/yr); or
2)
Reduce,
by use of
a control device,
total organic emissions
from all affected process vents at the facility by 95 weight
percent.
b)
If the owner or operator installs a closed—vent system and control
device to comply with the provisions of subsection
(a), the
closed—vent
system and control device must meet the requirements
of Section 725.933.
c)
Determinations
of vent emissions and emission reductions or total
organic compound concentrations achieved by add—on control devices
must be based on either engineering calculations or performance
tests.
If performance tests are used to determine vent emissions,
emission reductions, or total organic compound concentrations
achieved by add—on control devices, the performance tests must
conform with the requirements of Section 725.934(c).
117—499

180
d)
When an owner or operator and the Agency do not agree on
determinations of vent emissions or emission reductions or total
organic compound concentrations achieved by add—on control devices
based on engineering calculations,
the test methods in Section
725.934(c) must be used to resolve the disagreement.
(Source:
Added at
15 Ill. Reg.
,
effective
)
Section 725.933
Standards: Closed-vent Systems and Control Devices
a)
Compliance Required.
1)
Owners
or operators of closed—vent systems and control
devices used to comply with provisions of this Part Bhall
comply with the provisions of
this Section.
2)
The owner or operator of
an existing facility who cannot
install a closed—vent system and control device to comply
with the provisions of this Subpart on the effective date
that the facility becomes subject to the provisions of this
Subpart shall prepare an implementation schedule that
includes dates by which the closed—vent
system and control
device will be installed and in operation.
The controls
must be installed as soon as possible, but the
implementation schedule may allow up to
18 months after the
effective date that the facility becomes subject to this
Subpart for installation and startup.
All units that begin
operation after December 21,
1990, must comply with the
rules immediately
(i.e.,
must have control devices installed
and operating on startup of the affected unit);
the 2—year
implementation schedule does not apply to these units.
b)
A control device involving vapor recovery
(e.g.,
a condenser or
adsorber)
must be designed and operated to recover the organic
vapors vented to it with an efficiency of 95 weight percent or
greater unless the total organic emission limits of Section
725.932(a)(1)
for all affected process vents
is attained at an
efficiency less than 95 weight percent.
C)
An enclosed combustion device
(e.g.,
a vapor incinerator,
boiler
or process heater) must be designed and operated to reduce the
organic emissions vented to
it by 95 weight percent or greater;
to
achieve a total organic compound concentration of 20
ppmv,
expressed as the sum of the actual compounds,
not carbon
equivalents,
on a dry basis corrected to 3 percent oxygen; or to
provide a minimum residence time of 0.50 seconds at
a minimum
temperature of 760 C.
If
a boiler or process heater
is used as
the control device, then the vent stream must be introduced into
the flame combustion zone of the boiler or process heater.
117—500

181
d)
Flares
1)
A flare must be designed for and operated with no visible
emissions as determined by the methods specified in
subsection (e)(1) except
for periods not to exceed a total
of 5 minutes during any
2 consecutive hours.
2)
A flare must be operated with
a flame present at all times,
as determined by the methods specified in subsection
(f) (2) (c).
3)
A flare must be used only if the net heating value of the
gas being combusted is 11.2 MJ/scm (300 Stu/scf)
or greater
if the flare is steam—assisted or air—assisted; or
if the
net heating value of the gas being combusted is 7.45 14J/scm
(200 Btu/scf)
or greater
if the flare
is nonassisted.
The
net heating value of the gas being combusted must be
determined by the methods specified in subsection (e)(2).
4)
Exit Velocity.
A)
A steam—assisted or nonassisted flare must be designed
for an operated with an exit velocity, as determined
by the methods specified
in subsection
(e)(3),
less
than 18.3 rn/s
(60 ft/s),
except as provided
in
subsections
(d)(4)(B)
and
(C).
B)
A steam—assisted or nonassisted flare designed for and
operated with an exit velocity,
as determined by the
methods specified in subsection
(e)(3), equal to or
greater than 18.3
rn/s
(60 ft/s) but less than 122 m/s
(400 ft/s)
is allowed
if the net heating value of the
gas being combusted is greater than 37.3 MJ/scm (1000
Btu/scf).
C)
A steam—assisted or nonassisted flare designed for and
operated with an exit velocity,
as determined by the
methods specified in subsection
(e)(3),
less than the
velocity,
V as determined by the method specified in
subsection
(e)(4)
and less than 122 m/s (400 ft/s)
is
allowed.
5)
An air-assisted flare must be designed and operated with an
exit velocity less than the velocity,
V as determined by the
method specified in subsection
(e)(5).
6)
A flare used to comply with this Section must be
steam—
assisted,
air—assisted or nonassisted.
e)
1)
Reference Method
22 in 40 CFR 60,
incorporated by reference
in
35
Ill.
Adm. Code 720.111, must be used to determine the
compliance of
a flare with the visible emission provisions
117—501

182
of this Subpart.
The observation period is
2 hours and must
be used according to Method 22.
2)
The net heating value of the gas being combusted in a flare
must be calculated using the following equation:
H
K
*
SUM(Ci
*
Hi)
Where:
H is the net heating value of the sample in MJ/scm;
where the net enthalpy per mole of offgas is based on
combustion at 25 C and 760 mm Hg,
but the standard
temperature for determining the volume corrersponding
to 1 mole is 20
C.
K
=
1.74
E —7
(1/ppm)(g mol/scm)(MJ/kcal)
where
standard temperature for
(g mol/scm)
20 C.
SUM(Xi) means the sum of the values of X for each
component
i, from i=1 to n.
Ci is the concentration of sample component i
in ppm
on a wet basis,
as measured for organics by Reference
Method 18 in 40 CFR 60,
and for carbon monoxide,
by
ASTM D1946, incorporated by reference in 35
Ill. Adm.
Code 720.111.
Hi
is the net heat of combustion of sample component
i,
kcal/gmol at 25
C and 760 mm Hg.
The heatB of
combustion must be determined using ASTM D2382,
incorporated by reference
in
35
Ill. Adm. Code
720.111,
if published values are not available or
cannot be calculated.
3)
The actual exit velocity of
a flare must be determined by
dividing the volumetric flow rate (in units of standard
temperature and pressure),
as determined by Reference
Methods
2,
2A,
2C, or 2D in 40 CFR 60,
incorporated by
reference
in 35
Ill. Adm.
Code 720.111,
as appropriate, by
the unobstructed
(free) cross—sectional area of the flare
tip.
4)
The maximum allowed velocity
in m/s, V far a flare complying
with subsection
(d)(4)(C) must be determined by the
following equation:
LOG(V)
=
(H
+
28.8)
/
31.7
Where:
LOG
means logarithm to the base 10
117—502

183
H is the net heating value as determined in subsection
(e) (2).
5)
The maximum allowed velocity in m/s, V for an air-assisted
flare must be determined by the following equation:
V
8.706
+
0.7084H
Where:
H
iB
the net heating value as determined in subsection
(e) (2)
f)
The owner or operator shall monitor and inspect each control
device required to comply with this Section to ensure proper
operation and maintenance of the control device by implementing
the following requirements:
1)
Install,
calibrate, maintain and operate according to the
manufacturer’s specifications
a flow indicator that provides
a record of vent stream flow from each affected process vent
to the control device at least once every hour.
The flow
indicator sensor must be installed in the vent stream at the
nearest feasible point to the control device inlet but
before being combined with other vent streams.
2)
Install,
calibrate, maintain and operate according to the
manufacturer’s specifications a device to continuously
monitor control device operation as specified below:
A)
For a thermal vapor incinerator,
a temperature
monitoring device equipped with a continuous recorder.
The device must have accuracy of±1 percent of the
temperature being monitored in C or ±C, whichever is
greater.
the temperature sensor must be installed at
a location in the combustion chamber downstream of the
combustion zone.
B)
For a catalytic vapor incinerator,
a temperature
monitoring device equipped with a continuous recorder.
The device must be capable of monitoring temperature
at two locations and have an accuracy of ±1percent of
the temperature being monitored in C or ±0.5 C,
whichever
is greater.
One temperature sensor must be
installed in the vent stream at the nearest feasible
point to the catalyst bed inlet and
a second
temperature sensor must be installed in the vent
stream at the nearest feasible point to the catalyst
bed outlet.
117—503

184
C)
For a flare,
a heat sensing monitoring device equipped
with a continuous recorder that indicates the
continuous
ignition of the pilot
flame.
D)
For a boiler or process heater having a design heat
input capacity less than 44 MW,
a temperature
monitoring device equipped with a continuous recorder.
The device must have an accuracy of ±1 percent of the
temperature being monitored in C or ±0.5
C, whichever
is greater.
The temperature sensor must be installed
at a location in the furnace downstream of the
combustion zone.
E)
For a boiler or process heater having a design heat
input capacity greater than or equal to 44
MW,
a
monitoring device equipped with a continuous recorder
to measure a parameter(s) that indicates good
combustion operating practices are being used.
F)
For a condenser,
either:
i)
A monitoring device equipped with
a continuous
recorder to measure the concentration level of
the organic compounds in the exhaust vent stream
from the condenser;
or
ii)
A temperature monitoring device equipped with a
continuous recorder.
The device must be capable
of monitoring temperature at two locations and
have an accuracy of ~
1 percent of the
temperature being monitored in C or ±0.5
C,
whichever is greater.
One temperature sensor
must be installed
at
a location in the exhaust
vent stream from the condenser,
and a second
temperature sensor must be installed at a
location
in the coolant fluid exiting the
condenser.
G)
For a carbon adsorption system such as a fixed—bed
carbon adsorber that regenerates the carbon bed
directly
in the control device, either:
I)
A monitoring device equipped with a continuous
recorder to measure the concentration level of
the organic compounds in the exhaust vent stream
from the carbon bed; or
ii)
A monitoring device equipped with a continuous
recorder to measure a parameter that indicates
the carbon bed
is regenerated on a regular,
predetermined time cycle.
117—504

185
3)
Inspect the readings from each monitoring device required by
subsection (f)(1)
and
(2) at least once each operating day
to check control device operation and,
if necessary,
immediately implement the corrective measures necessary to
ensure the control device operates in compliance with the
requirements of this Section.
g)
An owner or operator using a carbon adsorption system such as
a
fixed—bed carbon adsorber that regenerates the carbon bed directly
onsite in the control device shall replace the existing carbon in
the control device with fresh carbon at a regular, predetermined
time interval that is no longer than the carbon service life
established as a requirement of Section 725.935(b)(4)(C)(vi).
h)
An owner or operator using a carbon adsorption system such as a
carbon canister that does not regenerate the carbon bed directly
onsite
in the control device shall replace the existing carbon in
the control device with fresh carbon on a regular basis by using
one of the following procedures:
1)
Monitor the concentration level of the organic compounds in
the exhaust vent stream from the carbon adsorption system on
a regular schedule, and replace the existing carbon with
fresh carbon immediately when carbon breakthrough is
indicated.
The monitoring frequency must be daily or at an
interval no greater than 20 percent of the time required to
consume the total carbon working capacity established as a
requirement of Section 725.935(b) (4) (C) (vii), whichever is
longer.
2)
Replace the existing carbon with fresh carbon at a regular,
predetermined time Interval that
is less than the design
carbon replacement interval established as a requirement of
Section 725.935(b) (4) (C) (vii).
i)
An owner or operator of an affected facility seeking to comply
with the provisions of this Part by using
a control device other
than a thermal vapor incinerator, catalytic vapor incinerator,
flare,
boiler,
process heater,
condenser or carbon adsorption
system is required to develop documentation including sufficient
information to describe the control device operation and identify
the process parameter or parameters that indicate proper operation
and maintenance of the control device.
j)
Closed vent systems.
1)
Closed-vent systems must be designed
for and operated with
no detectable emissions,
as indicated by an instrument
reading of less than 500 ppm above background and by visual
inspections,
as determined by the methods specified at
Section 725.934(b).
117—505

186
2)
Closed—vent systems must be monitored to determine
compliance with this Section during the initial leak
detection monitoring, which must be conducted by the date
that the facility becomes subject to the provisions of this
Section annually,
and at other times as specified by the
Agency pursuant to Section 725.930(c).
3)
Detectable emissions,
as indicated by an instrument reading
greater than 500 ppm and visual inspections, must be
controlled as soon as practicable, but not later than 15
calendar days after the emission is detected.
4)
A first attempt at repair must be made no later than 5
calendar days after the emission is detected..
k)
Closed—vent systems and control devices used to comply with
provisions of this Subpart must be operated at all times when
emissions may be vented to them.
(Source:
Added at
15
Ill. Reg.
,
effective
Section 725.934
Test Methods
and Procedures
a)
Each owner or operator subject to the provisions of this Subpart
shall comply with the test methods and procedures requirements
provided in this Section
b)
When a closed—vent system
is tested for compliance with no
detectable emissions,
as required in Section 725.933(j),
the test
must comply with the following requirements:
1)
Monitoring must comply with Reference Method 21
in 40 CFR
60,
incorporated by reference in
35
Ill. Adm. Code 720.111.
2)
The detection instrument must meet the performance criteria
of Reference Method
21.
3)
The instrument must be calibrated before use on each day of
its use by the procedures specified
in Reference Method 21.
4)
Calibration gases must be:
A)
Zero air
(less than 10 ppm of hydrocarbon in air).
B)
A mixture of methane or n—hexane and air at a
concentration of approximately, but less than, 10,000
ppm methane or n—hexane.
5)
The background level must be determined
as set forth in
Reference Method 21.
117—506

187
6)
The instrument probe must be traversed around all potential
leak interfaces as close to the interface as possible as
described
in
Reference
Method
21.
7)
The arithmetic difference between the maximum concentration
indicated by the instrument and the background level
is
compared with 500 ppm for determining compliance.
c)
Performance tests to determine compliance with Section 725.932(a)
and with the total organic compound concentration limit of Section
725.933(c) must comply with the following:
1)
Performance tests to determine total organic compound
concentrations and
mass
flow rates entering and exiting
control devices must be conducted and data reduced in
accordance with the following reference methods and
calculation procedures:
A)
Method
2
in 40 CFR 60 for velocity and volumetric flow
rate.
B)
Method 18
in 40 CFR 60 for organic content.
C)
Each performance test must consist of three separate
runs,
each run conducted for at least
1 hour under the
conditions that exist when the hazardous waste
management unit
is operating at the highest load or
capacity level reasonably expected to occur.
For the
purpose of determining total organic compound
concentrations and mass flow rates, the average of
results of all runs applies.
The average must be
computed on a time-weighed basis.
D)
Total organic mass flow rates must be determined by
the following equation:
F
=
K
*
Q
*
SUM(Ci
*
MWi)
Where:
F is the total organic mass flow rate,
kg/h.
K
=
4.16 E —8,
conversion factor for molar
volume, kg-mol/cubic
in,
at 293 K and 760 mm Hg.
Q
=
volumetric flow rate of gases entering or
exiting control device,
dscm/h,
as determined by
Method
2
in 40 CFR 60,
incorporated by reference
in 35
Ill.
Adm. Code 720.111.
SUN(Xi) means the sum of the values of X
for
each component
i,
from i=1 to n.
117—507

188
n
=
number
of
organic
compounds
in
the
vent
gas.
Ci
is the organic concentration in ppm, dry
basis, of compound
i in the vent gas, as
determined
by
Method
18
in
40 CFR 60.
MWi is the molecular weight of organic compound
i in the vent gas, kg/kg—mol.
E)
The annual total organic emission rate must be
determined
by
the
following
equation:
A
=
F
*
HOURS
Where:
A is total organic emission rate, kg/y.
F
is
the
total
organic
mass
flow
rate,
kg/h,
as
calculated
in
subsection
(c)(1)(D).
HOURS
is the total annual hours of operation for
the
affected
unit.
F)
Total
organic
emissions
from
all
affected
process
vents at
the facility must be determined by summing
the hourly total organic mass emissions rates
(F as
determined in subsection
(c)(1)(D)) and by summing the
annual total organic mass emission rates
(A
as
determined
in
subsection
(c)(1)(E))
for
all
affected
process vents at the facility.
2)
The owner or operator shall record such process information
as is necessary to determine the conditions of the
performance tests.
Operations during periods of startup,
shutdown
and
malfunction
do
not
constitute
representative
conditions for the purpose of a performance test.
3)
The owner or operator of
an affected
facility shall provide,
or cause to be provided, performance testing facilities as
follows:
A)
Sampling ports adequate for the test methods specified
in subsection
(c)(1).
B)
Safe sampling platform(s).
C)
Safe access to sampling platform(s).
D)
Utilities for sampling and testing equipment.
117—508

189
4)
For the purpose of making compliance determinations, the
time—weighted average of the results of the three runs must
apply.
In the event that a sample is accidentally lost or
conditions occur in which one of the three runs must be
discontinued because of forced shutdown,
failure of an
irreplaceable portion of the sample train,
extreme
meteorological conditions or other circumstances beyond the
owner or operator’s control, compliance may, upon the
Agency’s approval, be determined using the average of the
results of the two other runs.
d)
To show that
a process vent associated with a hazardous waste
distillation,
fractionation, thin—film evaporation, solvent
extraction,
or air or steam stripping operation is not subject to
the requirements of this Subpart, the owner or operator shall make
an initial determination that the time-weighted, annual average
total organic concentration of the waste managed by the waste
management unit
is less than 10 ppmw using one of the following
two methods:
1)
Direct measurement of the organic concentration of the waste
using the following procedures:
A)
The owner or operator shall take a minimum of
four
grab samples of waste for each wastestream managed in
the affected unit under process conditions expected to
cause the maximum waste organic concentration.
B)
For waste generated onsite,
the grab samples must be
collected at a point before the waste is exposed to
the atmosphere such as in an enclosed pipe or other
closed system that is used to transfer the waste after
generation to the first affected distillation,
fractionation, thin—film evaporation,
solvent
extraction, or air or steam stripping operation.
For
waste generated offsite, the grab samples must be
collected at the inlet to the first waste management
unit that receives the waste provided the waste has
been transferred to the facility in a closed system
such as a tank truck and the waste
is not diluted or
mixed with other waste.
C)
Each sample must be analyzed and the total organic
concentration of the sample must be computed using
Method 9060 or 8240 of SW—846
(incorporated by
reference under 35
Ill. Mm.
Code 720.111.
D)
The arithmetic mean of the results of the analyses of
the four samples apply for each wastestream managed
in
the unit in determining the time—weighted, annual
average total organic concentration of the waste.
The
time—weighted average is to be calculated using the
117—509

190
annual quantity of each waste stream processed and the
mean organic concentration of each wastestream managed
in the unit.
2)
Using knowledge of the waste to determine that
itB
total
organic concentration is
less that
10 ppmw.
Documentation
of the waste determination is required.
Examples of
documentation that must be used to support
a determination
under this subsection include:
A)
Production process information documenting that no
organic compounds are used.
B)
Information that the waste is generated by a process
that is identical to a process at the same or another
facility that has previously been demonstrated by
direct measurement to generate a wastestream having
a
total organic content less than 10 ppmw,
or
C)
Prior speciation analysis results on the same
wastestream where it
is documented that no process
changes have occurred since that analysis that could
affect the waste total organic concentration.
e)
The determination that distillation,
fractionation, thin—film
evaporation,
solvent extraction, or air or steam Btripping
operations which manage hazardous wastes with time—weighted,
annual average total organic concentrations less than 10 ppmw must
be made as follows:
1)
By the effective date that the facility becomes subject to
the provisions of this Subpart or by the date when the waste
is first managed
in a waste management unit,
whichever is
later;
and
2)
For continuously generated waste, annually; or
3)
Whenever there
is
a change in the waste being managed or a
change
in the process that generates or treats the waste.
f)
When an owner or operator and the Agency do not agree on whether a
distillation,
fractionation, thin—film evaporation, solvent
extraction, or air or steam stripping operation manages a
hazardous waste with organic concentrations of at least
10 ppmw
based on knowledge of the waste, the procedures in Method 8240 in
SW—846,
incorporated by reference
in 35
Ill. Adm.
Code 720.111,
must be used to resolve the dispute.
(Source:
Added at
15
Ill.
Reg.
,
effective
117—5 10

191
Section 725.935
Recordkeeping Requirements
a)
Compliance Required.
1)
Each owner or operator subject to the provisions of this
Subpart shall comply with the recordkeeping requirements of
this Section.
2)
An
owner
or operator of more than one hazardous waste
management unit subject to the provisions of this Subpart
may comply with the recordkeeping requirements for these
hazardous waste management units in one recordkeeping system
if the system identifies each record by each hazardous waste
management unit.
b)
Owners and operators shall record the following information in the
facility operating record:
1)
For facilities that comply with the provisions of Section
725.933(a)(2),
an implementation schedule that includes
dates by which the closed-vent system and control device
will be installed and in operation.
The schedule must also
include a rationale of why the installation cannot be
completed at an earlier date.
The implementation schedule
must be in the facility operating record by the effective
date that the facility becomes subject to the provisions of
this Subpart.
2)
Up—to-date documentation of compliance with the process vent
standards in Section 725.932,
including:
A)
Information and data identifying all affected process
vents,
annual throughput and operating hours of each
affected unit, estimated emission rates for each
affected vent and for the overall facility (i.e.,
the
total emissions for all affected vents at the
facility),
and the approximate location within the
facility of
each affected unit
(e.g.,
identify the
hazardous waste management units on a facility plot
plan).
B)
Information and data supporting determination of vent
emissions
and
emission
reductions
achieved
by
add—on
control devices based on engineering calculations or
source tests.
For the purpose of determining
compliance, determinations of vent emissions and
emission reductions must be made using operating
parameter values
(e.g., temperatures, flow rates, or
vent stream organic compounds and concentrations)
that
represent the conditions that result in maximum
organic emissions,
such as when the waste management
unit
is operating at the highest load or capacity
117—511

192
level reasonably expected to occur.
If the owner or
operator takes any action (e.g., managing a waste of
different composition or increasing operating hours of
affected waste management units)
that would result in
an increase in total organic emissions from affected
process vents at the facility,
then a new
determination is required.
3)
Where an owner or operator chooses to use teat date to
determine the organic removal efficiency or total organic
compound
concentration achieved by the control device,
a
performance test plan.
The test plan must include:
A)
A description of how it
is determined that the planned
test is going to be conducted when the hazardous waste
management unit is operating at the highest load or
capacity level reasonably expected to occur.
This
must include the estimated or design flow rate and
organic content of each vent stream and define the
acceptable operating ranges of key process and control
device parameters during the test program.
B)
A detailed engineering description of the closed-vent
system and control device including:
i)
Manufacturer’s name and model number of control
device.
ii)
Type of control device.
iii) Dimensions of the control device.
iv)
Capacity.
v)
Construction materials.
C)
A detailed description of sampling and monitoring
procedures, including sampling and monitoring
locations
in
the
system,
the
equipment
to
be
used,
sampling
and
monitoring
frequency,
and
planned
analytical procedures for sample analysis.
4)
Documentation of compliance with Section 725.933 must
include the following information:
A)
A list of all information references and sources used
in preparing the documentation.
B)
Records including the dates of each compliance test
required
by
Section
725.933(j).
117—512

193
C)
If engineering calculations are used,
a design
analysis,
specifications, drawings,
schematics, and
piping and instrumentation diagrams based on the
appropriate
sections
of
APTI
Course
415
(incorporated
by reference in 35 Ill. Adm. Code 720.111)
or other
engineering texts, approved by the Agency, that
present basic control device design information.
Documentation provided by the control device
manufacturer or vendor that describes the control
device design in accordance with Bubsections
(b)(4)(C)(i)
through
(vii) may be used to comply with
this requirement.
The design analysis must address
the vent stream characteristics and control device
operation parameters as specified below.
i)
For a thermal vapor incinerator, the design
analysis must consider the vent stream
composition,
constituent concentrations and flow
rate.
The design analysis must also establish
the design minimum and average temperature in
the combustion zone and the combustion zone
residence time.
ii)
For a catalytic vapor
incinerator, the design
analysis must consider the vent stream
composition,
constituent concentrations, and
flow rate.
The design analysis must also
establish the design minimum and average
temperatures across the catalyst bed inlet and
outlet.
iii)
For a boiler or process heater,
the design
analysis must consider the vent stream
composition,
constituent concentrations and flow
rate.
The design analysis must also establish
the design minimum and average flame zone
temperatures,
combustion zone residence time and
description of method and location where the
vent stream is introduced into the combustion
zone.
iv)
For a flare, the design analysis must consider
the vent stream composition,
constituent
concentrations,
and flow rate.
The design
analysis must also consider the requirements
specified in Section 725.933(d).
v)
For a condenser, the design analysis must
consider the vent stream composition,
constituent concentrations, flow rate,
relative
humidity and temperature.
The design analysis
must also establish the design outlet organic
117—513

194
compound concentration level, design average
temperature of the condenser exhaust vent stream
and design average temperatures of the coolant
fluid at the condenser inlet and outlet.
vi)
For a carbon adsorption system such as a fixed—
bed adsorber that regenerates the carbon bed
directly onBite in the control device, the
design analysis must consider the vent stream
composition,
constituent concentrations,
flow
rate,
relative
humidity
and temperature.
The
design analysis must also establish the design
exhaust vent stream organic compound
concentration level,
number
and capacity of
carbon beds,
type and working capacity of
activated carbon used for carbon beds, design
total steam flow over the period of each
complete carbon bed regeneration cycle, duration
of the carbon bed steaming and cooling/drying
cycles, design carbon bed temperature after
regeneration,
design carbon bed regeneration
time and design service life of carbon.
vii)
For a carbon adsorption system such as a carbon
canister that does not regenerate the carbon bed
directly onsite
in the control device,
the
design analysis must consider the vent stream
composition, constituent concentrations,
flow
rate,
relative humidity and temperature.
The
design analysis must also establish the design
outlet organic concentration level, capacity of
carbon bed, type and working capacity of
activated carbon used for carbon bed and design
carbon replacement interval based on the total
carbon working capacity of the control device
and source operating schedule.
D)
A statement signed and dated by the owner or operator
certifying that the operating parameters used in the
design analysis reasonably represent the conditions
that exist when the hazardous waste management unit is
or would be operating at the highest load or capacity
level reasonably expected to occur.
E)
A statement signed and dated by the owner or operator
certifying that the control device is designed to
operate at an efficiency of 95 percent or greater
unless the total organic concentration limit of
Section 725.932(a)
is achieved at an efficiency less
than 95 weight percent or the total organic emission
limits
of
Section
725.932(a)
for
affected
process
vents at the facility are attained by a control device
117—514

195
involving vapor recovery at
an efficiency less than
95
weight percent.
A statement provided by the control
device manufacturer or vendor certifying that the
control equipment meets the design specifications may
be used to comply with this requirement.
F)
If performance tests are used to demonstrate
compliance,
all test results.
C)
Design documentation and monitoring operating and inspection
information
for
each
closed—vent
system
and
control
device
required to comply with the provisions of this Part must be
recorded and kept up—to—date in the facility operating record.
The information must include:
1)
Description and date of each modification that is made to
the closed—vent system or control device design.
2)
Identification of operating parameter,
description of
monitoring device, and diagram of monitoring sensor location
or locations used to comply with Section 725.933(f)(1)
and
(2).
3)
Monitoring, operating and inspection information required by
Section 725.933(f) through
(k).
4)
Date,
time and duration of each period that occurs while the
control device
is operating when any monitored parameter
exceeds the value established in the control device design
analysis as specified below:
A)
For a thermal vapor incinerator designed to operate
with a minimum residence time of 0.50 second at
a
minimum temperature of 760
C,
any period when the
combustion temperature
is below 760 C.
B)
For a thermal vapor incinerator designed to operate
with an organic emission reduction efficiency of 95
percent or greater, any period when the combustion
zone temperature
is more than 28 C below the design
average combustion zone temperature established as a
requirement
of subsection (b)(4)(C)(i).
C)
For a catalytic vapor incinerator,
any period when:
i)
Temperature of the vent stream at the catalyst
bed inlet is more than 28
C below the average
temperature of the inlet vent stream established
as
a requirement of subsection (b)(4)(C)(ii);
or
ii)
Temperature difference across the catalyst bed
is less than 80 percent of the design average
117—5 15

196
temperature difference established as a
requirement of subsection (b)(4)(C)(ii).
D)
For a boiler or process heater,
any period when:
i)
Flame zone temperature
is
more
than
28
C
below
the design average flame zone temperature
established as a requirement
of subsection
(b)(4)(C)(iii); or
ii)
Position changes where the vent stream is
introduced to the combustion zone from the
location
established
as
a
requirement
of
subsection
(b) (4) (C) (iii).
E)
For a flare, period when the pilot
flame is not
ignited.
F)
For
a condenser that complies with Section
725.933(f)(2)(F)(i),
any period when the organic
compound concentration level or readings of organic
compounds in the exhaust vent stream from the
condenser are more than 20 percent greater than the
design
outlet
organic
compound
concentration
level
established as a requirement
of subsection
(b) (4) (C) (v).
G)
For a condenser that complies with Section
725.933(f)(2)(F)(ii),
any period when:
i)
Temperature of the exhaust vent stream from the
condenser is more than 6 C above the design
average exhaust vent stream temperature
established as a requirement
of subsection
(b) (4) (C) (v).
ii)
Temperature of the coolant fluid exiting the
condenser
is more than
6 C above the design
average coolant fluid temperature
at the
condenser
outlet
established
as
a
requirement
of
subsection
(b) (4) (C) (v).
H)
For
a
carbon
adsorption
system
such
as
a
fixed—bed
carbon adsorber that regenerates the carbon bed
directly onsite in the control device and complies
with Section 725.933(f)(2)(G)(i),
any period when the
organic compound concentration level or readings of
organic compounds in the exhaust vent stream from the
carbon
bed
are
more
than
20
percent
greater
than
the
design exhaust vent stream organic compound
concentration level established
as
a requirement of
Bubsection
(b) (4) (C) (vi).
117—5 16

197
I)
For
a
carbon
adsorption
Bystem
such
as
a
fixed—bed
carbon
adsorber
that
regenerates
the
carbon
bed
directly
onsite
in
the
control
device
and
complies
with
Section
725.933(f)(2)(G)(ii),
any
period
when
the
vent
stream
continues
to
flow
through
the
control
device
beyond
the
predetermined
carbon
bed
regeneration
time
established
as
a
requirement
of
subsection
(b) (4) (C) (vi).
5)
Explanation
for
each
period
recorded
under
subsection
(c)(4)
of
the
cause
for
control
device
operating
parameter
exceeding
the
design
value
and
the
measures
implemented
to
correct
the
control
device
operation.
6)
For carbon adsorption systems operated subject to
requirements specified in Section 725.933(g)
or (h)(2),
any
date when existing carbon in the control device
is replaced
with
fresh
carbon.
7)
For
carbon
adsorption
systems
operated
subject
to
requirements specified in Section 725.933(h) (1),
a
log that
records:
A)
Date
and
time
when
control
device
is
monitored
for
carbon breakthrough and the monitoring device reading.
B)
Date
when
existing
carbon
in
the
control
device
is
replaced with fresh carbon.
8)
Date
of
each
control
device
startup
and
shutdown.
d)
Records
of
the
monitoring,
operating
and
inspection
information
required
by
subsections
(c)(3)
through
(8)
need
be
kept
only
3
years.
e)
For
a control device other than a thermal vapor incinerator,
catalytic vapor incinerator,
flare,
boiler, process heater,
condenser or carbon adsorption system, monitoring and inspection
information indicating proper operation and maintenance of the
control
device
must
be
recorded
in
the
facility
operating
record.
f)
Up—to—date
information
and
data
used
to
determine
whether
or
not
a
process
vent
is
Bubject
to
the
requirements
in
Section
725.932,
including supporting documentation as required by Section
725.934(d)
(2),
when
application
of
the
knowledge
of
the
nature
of
the
hazardous
wasteatream
or
the
process
by
which
it
was
produced
is
used,
must
be
recorded
in
a
log
that
is
kept
in
the
facility
operating
record.
(Source: Added at
15 Ill. Reg.
,
effective
117—5 17

198
SUBPART SB:
AIR EMISSION STANDARDS FOR EQUIPMENT LEANS
Section 725.950
Applicability
a)
The regulations
in this Subpart apply to owners and operators of
facilities that treat,
store,
or dispose of hazardous wastes
(except as provided in Section 725.101).
b)
Except as provided in Section 725.964(j),
this Subpart applies to
equipment that contains or contacts hazardous wastes with organic
concentrations of
at least
10 percent by weight that are managed
in:
1)
Units that are subject to the RCRA permitting requirements
of
35
Ill. Adm.
Code 703, or
2)
Hazardous waste recycling units that are located on
hazardous waste management facilities otherwise subject to
the permitting requirements of 35 Ill. Adm. Code 703.
C)
Each piece of equipment to which this Subpart applies must be
marked in such
a manner that
it can be distinguished readily from
other pieces of equipment.
d)
Equipment that is in vacuum service is excluded from the
requirements of Sections 725.952 to 725.960,
if
it
is identified
as required
in Section 725.964(g) (5).
BOARD NOTE:
The requirements of Sections 725.952 through 725.964
apply to equipment associated with hazardous waste recycling units
previously exempt under 35 Ill.
Adin. Code 721.106(c)(1).
Other
exemptions under
35
Ill.
Adm. Code 721.104, 722.134 and 725.101(e)
are not affected by these requirements.
e)
Agency decisions pursuant to this Part must be made in writing,
are in the nature of permit decisions pursuant to Section 39 of
the Environmental Protection Act and may be appealed to the Board
pursuant to
35
Ill.
Adrn. Code
105.
(Source:
Added at
15
Ill.
Reg.
,
effective
Section 725.951
Definitions
As used in this Subpart,
all terms have the meaning given them in Section
725.931, the Resource Conservation and Recovery Act and 35
Ill. Adm. Code 720
through 726.
(Source:
Added at
15
Ill.
Reg.
,
effective
117—518

199
Section 725.952
Standards:
Pumps in Light Liquid Service
a)
Monitoring
1)
Each pump in light liquid service must be monitored monthly
to detect leaks by the methods specified in Section
725.963(b),
except as provided in subsections
(d),
(e) and
(f).
2)
Each pump in light liquid service must be checked by visual
inspection each calendar week for
indications of liquids
dripping from the pump seal.
b)
Leaks
1)
If an instrument reading of 10,000 ppm or greater is
measured,
a leak is detected.
2)
If there are indications of liquids dripping from the pump
seal,
a leak is detected.
C)
Repairs
1)
When a leak
is detected,
it must be repaired as soon as
practicable,
but not later than
15. calendar days after
it
is
detected,
except as provided in Section 725.959.
2)
A first attempt at repair
(e.g., tightening the packing
gland)
must be made no later than
5 calendar days after each
leak is detected.
d)
Each pump equipped with
a dual mechanical seal system that
includes a barrier fluid system is exempt from the requirements of
subsection
(a),
provided the following requirements are met:
1)
Each dual mechanical seal system must be:
A)
Operated with the barrier fluid at a pressure that
is
at all times greater than the pump stuffing box
pressures; or
B)
Equipped with a barrier fluid degasBing reservoir that
is connected by a closed-vent
system to a control
device that complies with the requirements of Section
725.960; or
C)
Equipped with a system that purges the barrier fluid
into a hazardous wastestream with no detectable
emissions to the atmosphere.
2)
The barrier fluid system must not be a hazardous waste with
organic concentrations
10 percent or greater by weight.
117—5 19

200
3)
Each barrier fluid system must be equipped with a sensor
that will detect failure of the seal system,
the barrier
fluid system,
or both.
4)
Each pump must be checked by visual inspection, each
calendar week,
for indications of liquids dripping from the
pump seals.
5)
Alarms
A)
Each sensor as described in subBection (d)(3) must be
checked daily or be equipped with an audible alarm
that must be checked monthly to ensure that
it
is
functioning properly.
B)
The owner or operator shall determine, based on design
considerations and operating experience,
a criterion
that indicates failure of the seal system, the barrier
fluid system, or both.
6)
Leaks
A)
If there are indications of liquids dripping from the
pump seal or the sensor indicates failure of the seal
system, the barrier fluid system,
or both based on the
criterion determined in subsection
(d)(5)(B),
a leak
is detected.
B)
When a leak is detected,
it must be repaired as soon
as practicable, but not later than 15 calendar days
after it
is detected,
except as provided in Section
725.959.
C)
A first attempt
at repair
(e.g., relapping the seal)
must be made no later than 5 calendar days after each
leak is detected.
e)
Any pump that is designated, as described in Section
725.964(g) (2),
for no detectable emissions,
as indicated by an
instrument reading of less than 500 ppm above background,
is
exempt from the requirements of subsections
(a),
(c) and
(d),
if
the pump meets the following requirements:
1)
Must have no externally actuated shaft penetrating the pump
housing.
2)
Must operate with no detectable emissions as
indicated by an
instrument reading of less than 500 ppm above background as
measured by the methods specified
in Section 725.963(c).
117—520

201
3)
Must be tested for compliance with subsection (a)(2)
initially upon designation,
annually and at other times as
specified by the Agency pursuant to Section 725.950(e).
f)
If any pump
is equipped with a closed-vent
system capable of
capturing
and
transporting any leakage from the seal or seals to
a
control device that complies with the requirements of Section
725.960,
it is exempt from the requirements of subsections
(a)
through
(a).
(Source:
Added at
15
Ill.
Req.
,
affective
)
Section 725.953
Standards: Compressors
a)
Each compressor must be equipped with a seal system that includes
a barrier fluid system and that prevents leakage of total organic
emissions to the atmosphere,
except as provided in subsections
(h)
and
(i).
b)
Each compressor seal system as required in subsection
(a) must be:
1)
Operated with the barrier fluid at a pressure that
is at all
times greater than the compressor stuffing box pressure;
or
2)
Equipped with a barrier fluid system that
is connected by a
closed—vent system to
a control device that complies with
the requirements of Section 725.960; or
3)
Equipped with
a system that purges the barrier fluid into a
hazardous wastestrearn with no detectable emissions to
atmosphere.
C)
The barrier fluid must not be
a hazardous waste with organic
concentrations 10 percent or greater by weight.
d)
Each barrier fluid system
as described in subsections
(a) through
(C)
must be equipped with a sensor that will detect failure of the
seal system, barrier fluid system, or both.
e)
1)
Each sensor as required in subsection
(d) must be checked
daily or must be equipped with an audible alarm that must be
checked monthly to ensure that
it is functioning properly
unless the compressor is located within the boundary of an
unmanned plant site,
in which case the sensor must be
checked daily.
2)
The owner or operator shall determine, based on design
considerations and operating experience,
a criterion that
indicates failure of the seal system, the barrier fluid
system,
or both.
117—52 1

202
f)
If the sensor indicates failure of the seal system, the barrier
fluid system, or both based on the criterion determined under
subsection
(e)(2),
a leak is detected.
g)
Repairs
1)
When a leak is detected,
it must be repaired as soon as
practicable, but not later than 15
calendar days after it is
detected, except as provided in Section 725.959.
2)
A first attempt at repair
(e.g., tightening the packing
gland)
must be made no later than
5 calendar days after each
leak
is detected.
h)
A compressor is exempt from the requirements of subsections
(a)
and
(b)
if
it
is equipped with a closed-vent system capable of
capturing and transporting any leakage from the seal to a control
device that complies with the requirements of Section 725.960,
except as provided in subsection
(i).
i)
Any compressor that
is designated,
as described in Section
725.964(g) (2),
for no detectable emission as indicated by an
instrument reading of less than 500 ppm above background,
is
exempt from the requirements of subsections
(a) through
(h)
if the
compressor:
1)
Is determined to be operating with no detectable emissions,
as indicated by an instrument reading of less than 500 ppm
above background,
as measured by the method specified in
Section 725.963(c).
2)
Is tested for compliance with subsection
(i)(l)
initially
upon designation,
annually and other times as specified by
the Agency pursuant to Section 725.950(e).
(Source:
Added at
15
Ill.
Reg.
,
effective
Section 725.954
Standards:
Pressure Relief Devices in Gas/Vapor Service
a)
Except during pressure releases,
each pressure relief device in
gas/vapor service must be operated with no detectable emissions,
as indicated by an instrument reading of less than 500 ppm above
background as measured by the method specified in Section
725.963(c).
b)
Actions following pressure release.
1)
After each pressure release, the pressure relief device must
be returned to a condition of no detectable emissions, as
indicated by an instrument reading of less than 500 ppm
above background,
as soon as practicable, but no later than
117—522

203
5 calendar days after each pressure release,
except as
provided in Section 725.959.
2)
No later than 5 calendar days after the pressure release,
the pressure relief device must be monitored to confirm the
condition of no detectable emissions,
as indicated by an
instrument reading of less than 500 ppm above background,
as
measured by the method specified in Section 725.963(c).
C)
Any pressure relief device that is equipped with a closed—vent
system capable of capturing and transporting leakage from the
pressure relief device to a control device as deBcribed in Section
725.960 is exempt from the requirements of subsections
(a) and
(b).
(Source:
Added at
15 Ill. Reg.
,
effective
)
Section 725.955
Standards:
Sampling Connecting Systems
a)
Each sampling connection system must be equipped with a closed
purge system or closed—vent system.
b)
Each closed—purge system or closed—vent system as required
in
subsection
(a) must:
1)
Return the purged hazardous waste stream directly to the
hazardous waste management process line with no detectable
emissions to atmosphere;
or
2)
Collect and recycle the purged hazardous waste stream with
no detectable emissions to atmosphere;
or
3)
Be designed and operated to capture and transport all the
purged hazardous wastestream to a control device that
complies with the requirements of Section 725.960.
c)
In situ sampling systems are exempt from the requirements of
subsections
(a)
and
(b).
(Source:
Added at
15 Ill. Reg.
,
effective
Section 725.956
Standards:
Open—ended Valves or Lines
a)
Equipment.
1)
Each open-ended valve or line must be equipped with a cap,
blind flange,
plug or
a second valve.
2)
The cap, blind flange, plug or second valve must seal the
open end at all times except during operations requiring
hazardous wastestream flow through the open—ended valve or
line.
117—523

204
b)
Each open—ended valve or line equipped with a second valve must be
operated in a manner such that the valve on the hazardous
wastestream end is closed before the second valve
is closed.
C)
When a double block and bleed system is being used,
the bleed
valve
or
line
may
remain
open
during
operations
that
require
venting
the
line
between
the
block
valves
but
must
comply
with
subsection
(a) at all other times.
(Source:
Added at
15
Ill. Reg.
,
effective
)
Section 725.957
Standards:
Valves in Gas/Vapor or Light Liquid Service
a)
Each valve in gas/vapor or light liquid service must be monitored
monthly to detect leaks by the methods specified
in Section
725.963(b)
and must comply with subsections
(b) through
(e),
except as provided in subsections
(f),
(g)
and
(h), and in Section
725.961 and 725.962.
b)
If an instrument reading of 10,000 ppm or greater is measured,
a
leak is detected.
c)
Monitoring Frequency
1)
Any valve for which a leak is not detected for two
successive months must be monitored the first month of every
succeeding quarter, beginning with the next quarter,
until
a
leak is detected.
2)
If
a leak is detected, the valve must be monitored monthly
until
a leak is not detected for two successive months,
d)
1)
When a leak is detected,
it must be repaired as soon as
practicable,
but no later than 15 calendar days after the
leak is detected,
except as provided in Section 725.959.
2)
A first attempt at repair must be made no later than 5
calendar days after each leak is detected.
e)
First attempts at repair include,
but are not limited to the
following best practices where practicable:
1)
Tightening of bonnet bolts.
2)
Replacement of bonnet bolts.
3)
Tightening
of packing gland nuts.
4)
Injection of lubricant
into lubricated packing.
117—524

205
f)
Any valve that is designated,
as described in Section
725.964(g)(2),
for no detectable emissions,
as indicated by an
instrument reading of less than 500 ppm above background,
is
exempt from the requirements of subsection
(a)
if the valve:
1)
Has no external actuating mechanism in contact with the
hazardous
wastestreani.
2)
Is operated with emissions less than 500 ppm above
background as determined by the method specified in Section
725.963(c).
3)
Ia tested for compliance with subsection (f)(2) initially
upon designation, annually,
and at other times as specified
by the Agency pursuant to Section 725.950(e).
g)
Any valve that is designated, as described in Section
725.964(h) (1),
as an unsafe-to—monitor valve is exempt
from the
requirements of subsection
(a),
if:
1)
The owner or operator of the valve determines that the valve
is unsafe to monitor because monitoring personnel would be
exposed to an immediate danger as a consequence of Complying
with subsection
(a).
2)
The owner or operator of the valve adheres to
a written plan
that requires monitoring of the valve as frequently as
practicable during safe—to-monitor times.
h)
Any valve that
is designated,
as described in Section
725.964(h)(2),
as a difficult—to-monitor valve is exempt from the
requirements of subsection
(a),
if:
1)
The owner or operator of the valve determines that the valve
cannot be monitored without elevating the monitoring
personnel more than 2 meters above
a support surface;
2)
The
hazardous
waste
management
unit
within
which
the
valve
is
located
was
in
operation
before
June
21,
1990;
and
3)
The
owner
or
operator
of
the
valve
follows
a
written
plan
that
requires
monitoring
of
the
valve
at
least
once
per
calendar
year.
(Source:
Added at 15
Ill. Reg.
,
effective
Section 725.958
Standards:
Pumps, Valves, Pressure Relief Devices,
Flanges
and
other
Connectors
a)
Pumps and valves in heavy liquid service, pressure relief devices
in light liquid or heavy liquid service and flanges and other
connectors must be monitored within
5 days by the method specified
117—525

206
in Section 725.963(b),
if evidence of a potential leak is found by
visual,
audible,
olfactory,
or
any
other
detection
method.
b)
If
an
instrument
reading
of
10,000
ppm or greater
is
measured,
a
leak
is
detected.
c)
Repairs
1)
When a
leak
is
detected,
it
must
be
repaired
as
soon
as
practicable,
but
not
later
than
15
calendar
days
after
it
is
detected,
except as provided in Section 725.959.
2)
The first attempt at repair must be made no later than 5
calendar
days
after
each
leak
is
detected.
d)
First attempts
at repair include, but are not limited to,
the best
practices described under Section 725.957(e).
(Source:
Added at
15 Ill.
Reg.
,
effective
Section 725.959
Standards:
Delay of Repair
a)
Delay of repair of equipment for which leaks have been detected is
allowed if the repair is technically infeasible without a
hazardous waste management unit shutdown.
In such a case,
repair
of this equipment must occur before the end of the next hazardous
waste management unit shutdown.
b)
Delay of repair of equipment for which leaks have been detected is
allowed for equipment that is isolated from the hazardous waste
management unit and that does not continue to contain or contact
hazardous waste with organic concentrations at
least
10 percent by
weight.
c)
Delay of repair
for valves
is allowed if:
1)
The owner or operator determines that emissions of purged
material resulting from immediate repair are greater than
the emissions likely to result from delay of repair.
2)
When repair procedures are effected, the purged material
is
collected and destroyed or recovered in
a control device
complying with Section 725.960.
d)
Delay of repair
for pumps
is allowed if:
1)
Repair requires the use of a dual mechanical seal system
that includes a barrier fluid system.
2)
Repair
is completed as soon as practicable, but not later
than 6 months after the leak was detected.
117—526

207
e)
Delay of repair beyond a hazardous waste management unit shutdown
is allowed for
a valve if valve assembly replacement
is necessary
during the hazardous waste management unit shutdown, valve
assembly supplies have been depleted,
and valve assembly supplies
had been sufficiently stocked before the supplies were depleted.
Delay of repair beyond the next hazardous waste management unit
shutdown is not allowed unless the next hazardous waste management
unit
shutdown
occurs
sooner
than
6
months
after
the
first
hazardous waste management unit shutdown.
(Source:
Added at 15
Ill. Reg.
,
effective
)
Section 725.960
Standards:
Closed—vent Systems and Control Devices
Owners or operators of closed—vent systems and control devices shall comply
with the provisions of Section 725.933.
(Source:
Added at
15
Ill.
Reg.
,
effective
)
Section 725.961
Percent Leakage Alternative for Valves
a)
An owner or operator subject to the requirements of Section
725.957 may elect to have all valves within a hazardous waste
management unit comply with an alternative standard which allows
no greater than 2 percent of the valves to leak.
b)
The following requirements must be met
if an owner or operator
decides to comply with the alternative standard of allowing 2
percent of valves to leak:
1)
An owner or operator shall notify the Agency that the owner
or operator has elected to comply with the requirements of
this Section.
2)
A performance test as specified in subsection
(c) must be
conducted initially upon designation,
annually and other
times as specified by the Agency pursuant to Section
725.950(e).
3)
If a valve leak is detected it must be repaired in
accordance with Section 725.957(d) and
(e).
C)
Performance tests must be conducted in the following manner:
1)
All valves subject to the requirements in Section 725.957
within the hazardous waste management unit must be monitored
within 1 week by the methods specified
in Section
725.963(b).
2)
If an instrument reading of 10,000 ppm or greater is
measured,
a leak is detected.
117—527

208
3)
The leak percentage must be determined by dividing the
number of valves subject
to
the
requirements
in
Section
725.957
for
which
leaks
are
detected
by
the
total
number
of
valves
subject
to
the
requirements
in
Section
725.957
within
the
hazardous
waste
management
unit.
d)
If
an
owner
or
operator
decides
no
longer
to
comply
with
this
Section,
the
owner
or
operator
shall
notify
the
Agency
in
writing
that
the
work
practice
standard
described
in
Section
725.957(a)
through
(e) will be followed.
(Source:
Added
at
15
Ill.
Reg.
,
effective
)
Section
725.962
Skip
Period
Alternative
for
Valves
a)
Election
1)
An owner or operator subject to the requirements of Section
725.957 may elect for all valves within a hazardous waste
management unit to comply with one of the alternative work
practices specified in subsections
(b)(2)
and
(3).
2)
An owner or operator shall notify the Agency before
implementing one of the alternative work practices.
b)
Reduced Monitoring
1)
An owner or operator shall comply with the requirements for
valves,
as described in Section 725.957, except
as described
in subsection (b)(2) and
(3).
2)
After two consecutive quarterly leak detection periods with
the percentage of valves leaking equal to or less than
2
percent,
an owner or operator may begin to skip one of the
quarterly leak detection periods for the valves subject to
the requirements in Section 725.957.
3)
After five consecutive quarterly leak detection periods with
the percentage of valves
leaking
equal
to
or
less
than
2
percent, an owner or operator may begin to skip three of the
quarterly leak detection periods for the valves subject to
the requirements
in Section 725.957.
4)
If the percentage of valves leaking is greater than
2
percent,
the owner or operator shall monitor monthly
in
compliance with the requirements
in Section 725.957,
but may
again elect to use this Section after meeting the
requirements of
Section 725.957(c)(1).
(Source:
Added at 15
Ill.
Reg.
,
effective
117—528

209
Section 725.963
Test Methods and Procedures
a)
Each
owner
or
operator
subject
to
the
provisions
of
this
Subpart
shall comply with the test methods and procedures requirements
provided
in
this
Section.
b)
Leak detection monitoring,
as
required
in
Sections
725.952
through
725.962,
must
comply
with
the
following
requirements:
1)
Monitoring must comply with Reference Method 21
in 40 CFR
60,
incorporated
by
reference
in
35
Ill.
Adm. Code 720.111.
2)
The detection instrument must meet the performance criteria
of
Reference
Method
21.
3)
The instrument must be calibrated before use on each day of
its use by the procedures specified in Reference Method 21.
4)
Calibration
gases
must
be:
A)
Zero air
(less than 10 ppm of hydrocarbon in air).
B)
A mixture of methane or n—hexane and air at
a
concentration of approximately,
but less than 10,000
ppm methane or n-hexane.
5)
The
instrument
probe
must
be
traversed
around
all
potential
leak interfaces as close to the interface
as possible as
described in Reference Method 21.
c)
When equipment
is tested for compliance with no detectable
emissions,
as required in Sections 725.952(e),
725.953(i),
725.954
and 725.957(f),
the test must comply with the following
requirements:
1)
The requirements of subsections
(b)(1) through
(4)
apply.
2)
The
background
level
must
be
determined
as
set
forth
in
Reference
Method
21.
3)
The
instrument
probe
must
be
traversed
around
all
potential
leak interfaces as close to the interface as possible as
described
in
Reference
Method
21.
4)
This arithmetic difference between the maximum concentration
indicated by the instrument and the background level is
compared with 500 ppm for determining compliance.
d)
In accordance with the waste analysis plan required by Section
725.113(b),
an owner or operator of
a facility shall determine,
for each piece of equipment, whether the equipment contains or
117—529

210
contacts a hazardous waste with organic concentration that equals
or exceeds
10 percent by weight using the following:
1)
Methods
described
in
ASTM
Methods
D
2267,
E
169,
E
168,
E
260 incorporated by reference in 35
Ill.
Adm.
Code
720.111;
2)
Method
9060
or
8240
of
SW—846,
incorporated
by
reference
in
35
Ill.
Mm.
Code 720.111; or
3)
Application of the knowledge of the nature of the hazardous
wasteatream
or
the
processby
which
it
was
produced.
Documentation of a waste determination by knowledge is
required.
Examples
of
documentation
that
must
be
used
to
support
a
determination
under this provision include
production
process
information
documenting
that
no
organic
compounds are used,
information that the waste
is generated
by a process that
is identical to a process at the same or
another facility that has previously been demonstrated by
direct measurement to have a total organic content less than
10 percent,
or prior speciation analysis results on the same
wastestream where
it
is also documented that no process
changes have occurred since that analysis that could affect
the waste total organic concentration.
e)
If an owner or operator determines that
a piece of equipment
contains or contacts
a hazardous waste with organic concentrations
at least 10 percent by weight,
the determination can be revised
only after following the procedures in subsection (d)(1)
or
(2).
f)
When an owner or operator and the Agency do not agree on whether a
piece of equipment contains or contacts a hazardous waste with
organic concentrations at least 10 percent by weight,
the
procedures in subsection
(d)(1) or
(2)
must be used to resolve the
dispute.
g)
Samples used in determining the percent organic content must be
representative of the highest total organic content hazardous
waste that
is expected to be contained in or contact the
equipment.
h)
To determine
if pumps or valves are in light liquid service, the
vapor pressures of constituents must either be obtained from
standard reference texts or be determined by ASTM D-2879
incorporated by reference in 35
Ill. Mm. Code 720.111.
i)
Performance tests to determine
if a control device achieves 95
weight percent organic emission reduction must comply with the
procedures of Section 725.934(c)(l)
through
(4).
(Source:
Added at
15
Ill.
Reg.
,
effective
117—5 30

211
Section 725.964
Recordkeeping Requirements
a)
Lumping Units
1)
Each owner or operator subject to the provisions of this
Subpart shall comply with the recordkeeping requirements of
this
Section.
2)
An
owner
or
operator
of
more
than
one
hazardous
waste
management
unit
subject
to
the
provisions
of
this
Subpart
may comply with the recordkeeping requirements for these
hazardous waste management units in one recordkeeping system
if the system identifies each record by each hazardous waste
management unit.
b)
Owners and operators shall record the following information
in the
facility operating record:
1)
For each piece of equipment to which this Subpart applies:
A)
Equipment identification number and hazardous waste
management unit identification.
B)
Approximate locations within the facility (e.g.,
identify the hazardous waste management unit on a
facility plot plan).
C)
Type of equipment (e.g.,
a pump or pipeline valve).
D)
Percent—by—weight total organics in the hazardous
wastestream at the equipment.
E)
Hazardous waste state at the equipment
(e.g. gas/vapor
or liquid).
F)
Method of compliance with the standard
(e.g.
“monthly
leak detection and repair” or “equipped with dual
mechanical seals”).
2)
for facilities than comply with the provisions of Section
725.933(a)(2),
an implementation schedule as specified in
that Section.
3)
Where an owner or operator chooses to use test data to
demonstrate the organic removal efficiency or total organic
compound concentration achieved by the control device,
a
performance test plan as specified in Section 725.935(b) (3).
4)
Documentation of compliance with Section 725.960, including
the detailed design documentation or performance test
results specified in Section 725.935(b)(4).
117—53 1

212
c)
When each leak is detected as specified in Sections 725.952,
725.953,
725.957 or 725.958, the following requirements apply:
1)
A weatherproof and readily visible identification,
marked
with the equipment identification number,
the date evidence
of a potential leak was found in accordance with Section
725.958(a), and the date the leak was detected, must be
attached to the leaking equipment.
2)
The identification on equipment except on a valve, may be
removed after
it has been repaired.
3)
The identification on a valve may be removed after
it has
been monitored for 2 successive months as specified in
Section 725.957(c) and no leak has been detected during
those 2 months.
d)
When each leak is detected as specified
in Sections 725.952,
725.953,
725.957 or 725.958, the following information must be
recorded in
an inspection log and must be kept in the facility
operating record:
1)
The instrument and operator identification numbers and the
equipment identification number.
2)
The date evidence of a potential leak was found
in
accordance with Section 725.958(a).
3)
The date the leak was detected and the dates of each attempt
to repair the leak.
4)
Repair methods applied in each attempt to repair the leak.
5)
“Above 10,000”,
if the maximum instrument reading measured
by the methods specified in Section 725.963(b) after each
repair attempt is equal to or greater than 10,000 ppm.
6)
“Repair delayed” and the reason for the delay if a leak is
not repaired within 15 calendar days after discovery of the
leak.
7)
Documentation supporting the delay of repair of a valve in
compliance with Section 725.959(c).
8)
The signature of the owner or operator (or designate) whose
decision it was that repair could not be effected without a
hazardous waste management unit shutdown.
9)
The expected date of successful repair of the leak if
a leak
is not repaired within 15 calendar days.
10)
The date of successful repair of the leak.
117—532

213
e)
Design documentation and monitoring,
operating and inspection
information for each closed—vent system and control device
required to comply with the provisions of Section 725.960 must be
recorded and kept up—to—date in the facility operating record as
specified in Section 725.935(c)(1)
and
(2), and monitoring,
operating and inspection information in Section 725.935(c) (3)
through
(8).
f)
For
a
control
device
other
than
a
thermal
vapor
incinerator,
catalytic
vapor
incinerator,
flare,
boiler,
process
heater,
condenser,
or
carbon
adsorption
system,
monitoring and inspection
information
indicating
proper
operation
and
maintenance
of
the
control
device
must
be
recorded
in
the
facility
operating
record.
g)
The following information pertaining to all equipment subject to
the requirements in Sections
725.952 through 725.960 must be
recorded in a log that
is kept
in the facility operating record:
1)
A list of identification numbers for equipment
(except
welded fittings)
subject to the requirements of this
Subpart.
2)
List of Equipment
A)
A list of identification numbers for equipment that
the owner or operator elects to designate for no
detectable emissions,
as indicated by an instrument
reading
of
less
than
500
ppm
above
background,
under
the provisions of Sections 725.952(e),
725.953(i)
and
725.957(f).
B)
The
designation
of
this
equipment
as
subject
to
the
requirements of Sections 725.952(e),
725.953(i) or
725.957(f) must be signed by the owner or operator.
3)
A list of equipment identification numbers for pressure
relief
devices
required
to
comply
with
Section
725.954(a).
4)
Compliance
tests.
A)
The
dates
of
each
compliance
test
required
in
Sections
725.952(e),
725.953(i),
725.954
and
725.957(f).
B)
The background level measured during each compliance
test.
C)
The
maximum
instrument
reading
measured
at
the
equipment during each compliance test.
5)
A
list
of
identification
numbers
for
equipment
in
vacuum
service.
117—533

214
h)
The
following
information
pertaining
to
all
valves
subject
to
the
requirements
of
Section
725.957(g)
and
(h)
must
be
recorded
in
a
log
that
is
kept
in
the
facility
operating
record:
1)
A
list
of
identification
numbers
for
valves
that
are
designated
as
unsafe
to
monitor,
an
explanation
for
each
valve
stating
why
the
valve
is
unsafe
to
monitor,
and
the
plan
for
monitoring
each
valve.
2)
A
list
of
identification
numbers
for
valves
that
are
designated
as
difficult
to
monitor,
an
explanation
for
each
valve
stating
why
the
valve
is
difficult
to
monitor,
and
the
planned
schedule
for
monitoring
each
valve.
i)
The following information must be recorded in the facility
operating record
for valves complying with Section 725.962:
1)
A
schedule
of
monitoring.
2)
The
percent
of
valves
found
leaking
during
each
monitoring
period.
j)
The following information must be recorded in a log that is kept
in the facility operating record:
1)
Criteria required
in Section 725.952(d)(5)(B) and
725.953(e)(2)
and an explanation of the criteria.
2)
Any changes to these criteria and the reasons for the
changes.
k)
The following information must be recorded in a log that
is kept
in the facility operating record for use in determining exemptions
as provided in Section 725.950 and other specific Subparts:
1)
An analysis determining the design capacity of the hazardous
waste management unit.
2)
A statement listing the hazardous waste influent to and
effluent from each hazardous waste management unit subject
to the requirements
in Sections 725.960 and an analysis
determining whether these hazardous wastes are heavy
liquids.
3)
An up—to-date analysis and the supporting information and
data used to determine whether or not equipment is subject
to the requirements
in Sections 725.952 through 725.960.
The record must include supporting documentation as required
by
Section
725.963(d)
(3)
when
application
of
the
knowledge
of
the
nature
of
the
hazardous
wastestream
or
the
process
by
which
it was produced is used.
If the owner or operator
117—5 34

215
takes any action
(e.g., changing the process that produced
the waste) that could result
in an increase
in the total
organic content of the waste contained in or contacted by
equipment determined not to be subject to the requirements
in Sections 725.952 through 725.960, then a new
determination is required.
1)
Records of the equipment leak information required by subsection
(d) and the operating information required by subsection
(e) need
be kept only
3 years.
m)
The owner or operator of any facility that
is subject to this
Subpart and to regulations at 40 CFR 60,
Subpart VV, or 40 CFR 61,
Subpart V,
incorporated by reference in 35 Ill. Adm. Code 720.111,
may elect to determine compliance with this Subpart by
documentation either pursuant to Section 725.964, or pursuant to
those provisions of 40 CFR 60 or 61,
to the extent that the
documentation under the regulation at 40 CFR 60 or
61 duplicates
the documentation required under this Subpart.
The documentation
under the regulation at 40 CFR 60 or 61 must be kept with or made
readily available with the facility operating record.
(Source:
Added at
15
Ill. Reg.
,
effective
117—535

216
TITLE
35:
ENVIRONMENTAL
PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER
I:
POLLUTION CONTROL BOARD
SUBCHAPTER
c:
HAZARDOUS
WASTE
OPERATING
REQUIREMENTS
PART
726
STANDARDS FOR THE
MANAGEMENT
OF SPECIFIC HAZARDOUS WASTE
AND SPECIFIC TYPES OF HAZARDOUS WASTE MANAGEMENT FACILITIES
SUBPART C:
RECYCLABLE MATERIALS USED IN A
MANNER
CONSTITUTING DISPOSAL
Section
726.120
Applicability
726.121
Standards applicable to generators and transporters of materials
used in a manner that constitutes disposal
726.122
Standards applicable to storers, who are not the ultimate users,
of materials that are to be used in a manner that constitutes
disposal
726.123
Standards applicable to users of materials that are used in
a
manner that constitutes disposal
SUBPART
D:
HAZARDOUS WASTE BURNED FOR ENERGY RECOVERY
Section
726.130
Applicability
726.131
Prohibitions
726.132
Standards applicable to generators of hazardous waste fuel
(Repealed)
726.133
Standards applicable to transporters of
hazardous waste fuel
726.134
Standards applicable to marketers of hazardous waste fuel
726.135
Standards applicable to burners
of hazardous waste fuel
726.136
Conditional exemption for spent materials and by—products
exhibiting a characteristic of hazardous waste
SUBPART E:
USED OIL BURNED FOR ENERGY RECOVERY
Section
726.140
Applicability
726. 141
Prohibitions
726.142
Standards applicable to generators of used oil burned for energy
recovery
726.143
Standards applicable to marketers of used oil burned for energy
recovery
726.144
Standards applicable to burners of used oil burned
for energy
recovery
SUBPART
F:
RECYCLABLE MATERIALS UTILIZED FOR PRECIOUS
METAL
RECOVERY
Section
726.170
Applicability and requirements
SUBPART
G:
SPENT LEAD-ACID BATTERIES BEING RECLAIMED
Section
726.180
Applicability and requirements
117—536

217
AUTHORITY:
Implementing Section 22.4 and authorized by Section 27 of the
Environmental Protection Act
(Ill.
Rev. Stat.
1989,
ch.
111 1/2,
pars.
1022.4
and 1027).
SOURCE:
Adopted in R85—22
at
10 Ill. Reg.
1162,
effective January 2, 1986;
amended in R86-1
at 10 Ill.
Reg.
14156, effective August
12,
1986; amended in
R87—26
at
12
Ill. Reg.
2900,
effective January
15,
1988;
amended in R89-l at
13
Ill.
Reg.
18606, effective November 13,
1989; amended
in R90—2 at
14 Ill.
Reg.
14533, effective August 22,
1990;
amended in R90-ll at
15
Ill.
Reg.
effective
SUBPART D:
HAZARDOUS WASTE BURNED FOR ENERGY RECOVERY
Section 726.132
Standards applicable to generators of hazardous waste fuel
(Repealed)
a)
Generatora of
hazardous waste fuel are subj?ct to the requirements
of
35
Ill.
Adm.
Code 722 except that Cection 726.136 exempts
eartain ~ipentmaterials and by products from these provisions;
b)
Generators who are marketers also shall comply with Gection
726.134;
C)
Generators who are burners also shell comply with Cection 726.135.
(Source:
Repealed at
15
Ill. Reg.
,
effective
117—537

218
TITLE
35:
ENVIRONMENTAL PROTECTION
SUBTITLE G:
WASTE DISPOSAL
CHAPTER
I:
POLLUTION CONTROL
BOARD
SUBCHAPTER
c:
HAZARDOUS WASTE OPERATING REQUIREMENTS
PART 728
LAND
DISPOSAL RESTRICTIONS
SUBPART A:
GENERAL
Section
728.101
Purpose,
Scope and Applicability
728.102
Definitions
728.103
Dilution Prohibited as a Substitute for Treatment
728.104
Treatment Surface Impoundment Exemption
728.105
Procedures for case—by—case Extensions to an Effective Date
728.106
Petitions to Allow Land Disposal of
a Waste Prohibited under
Subpart C
728.107
Waste Analysis and Recordkeeping
728.108
Landfill and Surface Impoundment Disposal Restrictions
728.109
Special Rules for Characteristic Wastes
SUBPART C:
PROHIBITION
ON LAND DISPOSAL
Section
728.130
Waste Specific Prohibitions
-—
Solvent Wastes
728.131
Waste Specific Prohibitions
——
Dioxin—Containing Wastes
728.132
Waste Specific Prohibitions
——
California List Wastes
728.133
Waste Specific Prohibitions
——
First Third Wastes
728.134
Waste Specific Prohibitions
——
Second Third Wastes
728.135
Waste Specific Prohibitions
——
Third Third Wastes
728.139
Statutory Prohibitions
SUBPART
D:
TREATMENT STANDARDS
Section
728.140
Applicability
of
Treatment Standards
728.141
Treatment Standards expressed as Concentrations in Waste Extract
728.142
Treatment
Standards expressed as Specified Technologies
728.143
Treatment Standards expressed
as Waste Concentrations
728.144
Adjustment of Treatment Standard
SUBPART
E:
PROHIBITIONS ON STORAGE
Section
728.150
Prohibitions on Storage of Restricted Wastes
Appendix A
Toxicity Characteristic Leaching Procedure
(TCLP)
Appendix
B
Treatment Standards
(As concentrations
in the Treatment Residual
Extract)
Appendix C
List of Halogenated Organic Compounds
Appendix D
Organometallic Lab Packs
Appendix E
Organic Lab Packs
Appendix
F
Technologies to Achieve Deactivation of Characteristics
Appendix G
Federal Effective Dates
Appendix H
National Capacity LDR Variances for UIC Wastes
117—538

219
Table A
Constituent Concentrations in Waste Extract
(CCWE)
Table B
Constituent Concentrations in Wastes
(CCW)
Table
C
Technology Codes and Description of Technology—Based Standards
Table
D
Technology-Based Standards by RCRA Waste Code
Table E
Standards
for Radioactive Mixed Waste
AUTHORITY:
Implementing Section 22.4 and authorized by Section 27 of the
Environmental Protection Act
(Ill. Rev.
Stat.
1989,
ch. 111
1/2, pars.
1022.4
and 1027).
SOURCE:
Adopted in R87—5 at
11
Ill. Reg.
19354, effective November
12,
1987;
amended
in R87—39 at 12
Ill.
Reg.
13046, effective July 29,
1988;
amended in
R89—1 at
13
Ill.
Reg.
18403, effective November 13,
1989;
amended in R89—9 at
14
Ill.
Reg.
6232,
effective April
16,
1990;
amended in R90—2 at
14
Ill.
Reg.
14470, effective August 22,
1990;
amended
in R90—lO
at
14
Ill.
Reg.
16508,
effective September
25,
1990;
amended in R90-1l at
15
Ill.
Reg.
effective
SUBPART
A:
GENERAL
Section 728.101
Purpose,
Scope and Applicability
a)
This Part identifies hazardous wastes that are restricted from
land disposal and defines those limited circumstances under which
an otherwise prohibited waste may continue to be land disposed.
b)
Except as specifically provided otherwise in this Part or
35 Ill.
Adm. Code 721,
the requirements of this Part apply to persons who
generate or transport hazardous waste and to owners and operators
of hazardous waste treatment, storage and disposal
facilities.
C)
Restricted wastes may continue to be land disposed as
follows:
1)
Where persons have been granted an extension to the
effective date of
a prohibition under Subpart C or pursuant
to Section 728.105, with respect to those wastes covered by
the extension;
2)
Where persons have been granted an exemption from a
prohibition pursuant to a petition under Section 728.106,
with respect to those wastes and units covered by the
petition;
~j
Wastes that are hazardous only because they exhibit
a
hazardous characteristic,
and which are otherwise prohibited
from land disposal under this Part,
are not prohibited from
land disposal
if the wastes:
117—539

220
~j
Are disposed into a nonhazardous or hazardous waste
in)ection well as defined
in
35 Ill. Adm. Code
704.106(a):
and
~j
Do not exhibit any prohibited characteristic of
hazardous waste at the point of injection.
5)
rrior to hay
8,
1990,
in a landfill or surface impoundment
unit where all applicable persons are in compliance with the
requirements of Cection 728.108, with respect to wastes
which are not subject to the treatment standards set forth
in Cubpart
D,
and which are not subject to the prohibitions
728.132 ~
728.130
d)
This
Part
does
not
affect
the
availability
of
a
waiver
under
Section 121(d) (4)
of the Comprehensive Environmental Response,
Compensation,
and Liability Act of 1980 (CERCLA)
(42 U.S.C. 9601
et seq).
e)
The following hazardous wastes are not subject to any provision of
this Part:
1)
Wastes generated by small quantity generators of less than
100 kg of non—acute hazardous waste or less than 1 kg of
acute hazardous waste per month,
as defined in 35
Ill.
Adm.
Code 721.105;
2)
Waste pesticides that
a farmer disposes of pursuant to 35
Ill.
Adm.
Code 722.170;
3)
Wastes identified or listed as hazardous after November
8,
1984,
for which USEPA has not promulgated land disposal
prohibitions or treatment standards.
f)
This Part
is cumulative with the land disposal restrictions of
35
Ill. Adm.
Code
729.
The Environmental Protection Agency (Agency)
shall not issue a wastestream authorization pursuant to 35
Ill.
Adm. Code 709 or Sections 22.6 or 39(h)
of the Environmental
Protection Act
(Ill. Rev.
Stat.
1987, ch.
111
1/2,
pars.
1022.6 or
1039(h)) unless the waste meets the requirements of this Part as
well as 35
Iii.
Adm. Code 729.
(Source:
Amended at
15
Ill. Reg.
,
effective
Section 728.102
Definitions
a)
When used in this Part the following terms have the meanings given
belowi-.
All other terms have the meanings given under
35
Ill.
Adm. Code 702.110,
720.110, 720.102 or 721.103.
“Agency” means the Illinois Environmental Protection Agency.
117—540

221
“Board” means the Illinois Pollution Control Board.
“CERCLA” means the Comprehensive Environmental Response,
Compensation,
and Liability Act of 1980
(42 U.S.C.
9601 et seq.)
“Halogenated organic compounds” or
“HOCs” means those compounds
having
a carbon-halogen bond which are listed under Appendix C.
“Hazardous constituent
or constituents” means those constituents
listed
in 35
Ill.
Adm. Code 72l.Appendix H.
Inorganic Solid Debris are nonfriable inorganic solids that
are
incapable of passing through a 9.5 mm standard sieve, and that
require cutting, or crushing and grinding,
in mechanical sizing
equipment prior to stabilization, limited to the following
inorganic
or metal materials:
Metal slags (either dross or scoria).
Glassified slag.
Glass.
Concrete
(excluding cementitious or pozzolanic stabilized
hazardous wastes).
Masonry and refractory bricks.
Metal cans,
containers,
drums or tanks.
valves,
appliances or
Metal
nuts,
bolts, pipes,
pumps,
industrial eguipment.
Scrap metal as defined
in 35
Iii. Adm. Code 721.10l(c)6).
“Land disposal” means placement in or on the land and includes,
but
is not limited to,
placement in a landfill,
surface
impoundment, waste pile,
injection well,
land treatment facility,
salt dome formation,
salt bed formation, underground mine or cave,
or placement
in a concrete vault or bunker intended for disposal
purposes.
“Nonwastewaters” are wastes that do not meet the criteria for
“wastewaters”
in this Section.
~‘Polychlorinatedbiphenyls” or “PCBs”
are halogenated organic
compounds defined
in accordance with 40 CFR 761.3, incorporated by
reference in 35
Ill. Adm.
Code 720.111
“ppm” means parts per million.
117—54 1

222
“RCRA
corrective action” means corrective action taken under
35
Ill. Adm. Code 724.200 or 725.193,
40 CFR 264.100 or 265.93
(1987), or
similar regulations in other States with RCRA programs
authorized by USEPA pursuant to 40 CFR 271 (1986~j.
“USEPA” means the United States Environmental Protection Agency.
“Wastewaters” are wastes that contain less than
1
by weight total
organic_carbon
(TOC)
and less than
1
by weight total suspended
solids
(TSS), with the following exceptions:
FOOl,
F002,~F003,
F004,
FOOS solvent—water mixtures that
contain less than 1
by weight TOC or less than 1
by weight
total FOOl,
F002, F003,
F004, F005 solvent constituents
listed
in Table
A.
K011,
K013, K014 wastewaters
(as generated)
that contain
less than 5
by weight TOC and
less than
1
by weight TSS.
K103 and Kl04 wastewaters contain less than 4
by weight TOG
and
less than
1
by weight TSS.
b)
~.A11other terms have the meanings given under
35
Ill.
Adxn.
Code
702.110,
720.110,
720.102 or
721.103.
(Source:
Amended at 15
Iii. Reg.
,
effective
Section 728.103
Dilution Prohibited
as
a Substitute for Treatment
~
Except
as provided
in subsection
(b),
nNo generator,
transporter,
handler or owner or operator of a treatment, storage or disposal
facility shall
in any way dilute
a restricted waste or the
residual from treatment
of
a restricted waste as a substitute for
adequate treatment to achieve compliance with Subpart
D,
to
circumvent the effective date of a prohibition in Subpart
C, to
otherwise avoid a prohibition
in Subpart
C.
~.j
Dilution of wastes that are hazardous only because they exhibit
a
characteristic
in
a treatment system which treats wastes
subsequently discharged to a water of the State pursuant to
an
NPDES permit issued under 35
Ill.
Adm. Code 309 or which treats
wastes
for purposes of pretreatment requirements under 35
Ill.
Adm. Code 310
is not impermissible dilution for purposes of this
Section unless
a method has been specified as the treatment
standard
in Section 728.142.
(Source:
Amended at
15
Iii.
Reg.
,
effective
)
Section 728.105
Procedures
for case—by—case Extensions to an Effective Date
a)
The Board incorporates by reference 40 CFR 268.5
(1989),
as
amended
at
54 Fed. Reg 36970,
September
6,
1989,
and
at
55 Fed.
117—542

223
Req.
23935,
June
13,
1990.
This Part incorporates no future
editions or amendments.
b)
Persons may apply to USEPA for extensions of effective dates
pursuant to 40 CFR 268.5.
Extensions which are granted by USEPA
will be deemed extensions
of dates specified in the derivative
Board rule.
(Source:
Amended at
15 Ill. Reg.
,
effective
Section 728.107
Waste Analysis and Recordkeeping
a)
Except as specified
in Section 728.132 or 728.143, the generator
shall test the generator’s waste,
or test an extract developed
using the test method described in Appendix A, or use knowledge of
the waste,
to determine if the waste is restricted from land
disposal under this Part.
1)
If
a generator determines that the generator is managing
a
restricted waste under this Part and determines that the
waste does not meet the applicable treatment standards
set
forth in Subpart D or exceeds the applicable prohibition
levels set
forth in Section 728.132 or 728.139, with each
shipment of waste the generator shall notify the treatment
or storage facility in writing of the appropriate treatment
standard set forth
in Subpart D and any applicable
prohibition
levels set forth in Section 728.132 or 728.139.
The notice must include the following information:
A)
USEPA Hazardous Waste Number;
B)
The corresponding treatment standards for wastes
FOO1—F005,
FO39 and wastes prohibited pursuant to
Section 728.132 or Section 3004(d)
of the Resource
Conservation and Recovery Act, referenced
in Section
728.139.
Treatment standards
for all other restricted
wastes must either be referenced as above,
or by
including on the notification the subcategory of the
waste,
the treatability group(s)
of the waste(s),
and
the Section and subsection where the treatment
standards appear.
Where the applicable treatment
standards are expressed as
specified technologies
in
Section 728.142,
the applicable five—letter treatment
code found
in Table C (e.g.,
INCIN,
WETOX) also must
be listed on the notification.
and all applicable
standards set
forth in Cection
728.132 or 728.139~
C)
The manifest number associated with the shipment of
waste;
and
D)
Waste analysis data, where available.
117—54 3

224
2)
If
a generator determines that the generator is managing
a
restricted waste under this Part,
and determines that the
waste can be land disposed without
further treatment, with
each shipment of waste the generator shall submit,
to the
treatment,
storage or land disposal facility,
a notice and a
certification stating that the waste meets the applicable
treatment standards set forth in Subpart D and the
applicable prohibition levels set forth in Section 728.132
or 728.139.
A)
The notice must include the following information:
i)
USEPA Hazardous Waste Number;
ii)
The corresponding treatment standards
for wastes
FOO1—F005,
FO39 and wastes prohibited pursuant
to Section 728.132 or Section 3004(d) of the
Resource Conservation and Recovery Act,
referenced in Section 728.139.
Treatment
standards
for all other restricted wastes must
either be referenced
as above, or by including
on the notification the subcategory of the
waste,
the treatability group(s)
of the
waste(s), and the Section and subsection where
the treatment
standards appear.
Where the
applicable treatment standards are expressed
as
specified technologies
in Section 728.142, the
applicable five-letter treatment code found
in
Table
C
(e.g., INCIN,
WETOX)
also must be listed
on the notification.--
iii)
The manifest number associated with the shipment
of waste;
iv)
Waste analysis data, where available.
B)
The certification must be signed by an authorized
representative and must state the following:
I certify under penalty of law that
I personally
have examined and am familiar with the waste
through analysis and testing or through
knowledge of the waste to support this
certification that the waste complies with the
treatment standards specified
in 35 Ill.
Adm.
Code 728.Subpart D and all applicable
prohibitions set forth in 35
Ill.
Adm. Code
728.132,
728.139 or
Section 3004(d) of the
Resource Conservation and Recovery Act.
I
believe that the information
I submitted
is
true,
accurate and complete.
I am aware that
there are significant penalties
for submitting a
117—544

225
false certification, including the possibility
of a fine and imprisonment.
3)
If
a generator’s waste
is subject to an exemption from a
prohibition on the type of land disposal method utilized for
the waste
(such
as, but not limited to,
a case—by—case
extension under Section 728.105, an exemption under Section
728.106,
an extension under Section 728.lOl(c)(3)
or
a
nationwide capacity variance under 40 CFR 268.Subpart C
(1989),
with each shipment of waste, the generator shall
submit
a notice with the waste to the facility receiving the
generator’s waste, stating that the waste is not prohibited
from land disposal.
The notice must include the following
information:
A)
EPA hazardous waste number:
B)
The corresponding treatment standards for wastes
FOO1-F005, F039 and wastes prohibited pursuant to
Section 728.132 or Section 3004(d)
of the Resource
Conservation and Recovery Act, referenced in Section
728.139.
Treatment standards for
all other restricted
wastes must either be referenced as above, or by
includino on the notification the eubcategory of the
waste, the treatability group(s) of the waste(s),
and
the
Section and
subsection where the treatment
standards appear.
Where the applicable treatment
standards are expressed as specified technologies
in
Section 728.142, the applicable five—letter treatment
code found
in Table C
(e.g.,
INCIN,
WETOX)
also must
be listed on the notification.
and all applicable
prohibitions set forth in Cection 728.132 or 728.139
C)
The manifest number associated with the shipment
of waste;
D)
Waste analysis data, where available, and
E)
The date the waste
is subject to the prohibitions.
4)
If
a generator determines that the generator is managing
a
prohibited waste
in tanks or containers regulated under
35
Ill.
Adm. Code 722.134,
and
is treating such waste
in such
tanks or containers to meet applicable treatment standards
under Subpart
D,
the generator shall develop and follow
a
written waste analysis plan which describes the procedures
the generator will carry out to comply with the treatment
standards.
The ~1an must be kept on—site in the generator’s
records,
and the following requirements must be met:
that
is
subject to the prohibitions under Section 728.133(f)
(including wastes that are disposed of in disposal units
other than landfills or surface impoundments)
and is
not
117—545

226
subject to the prohibitions set
forth in Section 728.132,
with each shipment of waste,
the generator shall notify the
treatment storage or disposal
facility,
in writing,
of any
applicable prohibitions set forth in Section 728.133(f).
The notice must include the following information~
A)
UCEPA hazardous waste number;
D)
The applicable prohibitions set forth in Section
728.133(f);
C)
The manifest number associated with the shipment of
waste; and
Waste
r1nn1~-sis
data where availabl
~j
The waste analysis plan must be based on a detailed
chemical and physical analysis of
a representative
sample of the prohibited waste(s) being treated,
and
contain all information necessary to treat the
waste(s)
in accordance with the requirements of this
Part,
including the selected testing frequency.
~j.
Such plan must be filed with the Agency a minimum
of
30 days prior to the treatment activity, with delivery
verified.
~j
Wastes shipped off—site pursuant to this
subsection
must comply with the notification requirements of
Section 728.107(a) (2).
5)
If
a generator determines whether the waste
is restricted
based solely on the generator’s knowledge of the waste,
the
generator shall retain all supporting data used to make this
determination on—site
in the generator’s
files.
If a
generator determines whether the waste is restricted based
on testing the waste or
an extract developed using the test
method described
in Appendix A,
the generator shall retain
all waste analysis data on site in the generator’s files.
6)
Generators shall retain on—site a copy of all notices,
certifications, demonstrations,
waste analysis data and
other documentation produced pursuant to this Section for
at
least five years from the date that the waste that is the
subject of such documentation was last sent to on—site or
off—site treatment storage or disposal.
The five year
record retention period
is automatically extended during the
course of any unresolved enforcement action regarding the
regulated activity or
as requested by the Agency.
fl
If a
generator is managing
a lab pack that contains wastes
identified
in Appendix
D and wishes
to use the alternative
117—546

227
treatment standard under Section 728.142, with each shipment
of waste the generator shall submit
a notice to the
treatment facility
in accordance with subsection
(a)(l).
The generator shall also comply with the requirements
in
subsections
(a)(5)
and (a)(6),
and shall submit the
following certification, which must be signed by an
authorized representative:
I certify under penalty of law that
I personally have
examined and am familiar with the waste and that the
lab pack contains only the wastes specified in 35
Ill.
Adm. Code 728.Appendix
D or solid wastes not subject
to regulation under
35
Ill.
Adm. Code 721.
I am aware
that there are significant penalties for submitting
a
false certification, including the possibility of fine
or
imprisonment.
~j.
If
a generator
is managing a lab pack that contains organic
wastes specified
in Appendix
E and wishes to use the
alternate treatment
standards under Section 728.142, with
each
shipment of waste the generator shall submit a notice
to the treatment facility
in accordance with subsection
(a)(1).
The generator also shall comply with the
requirements
in subsections
(a)(5)
and
(a)(6),
and shall
submit the following certification which must be signed by
an authorized
representative:
I certify under penalty of law that
I personally have
examined and am familiar with the waste throuah
analysis and testing or through knowledge of the waste
and
that
the lab pack contains only organic waste
specified in 35
Ill. Adm. Code 728.Appendix E or solid
wastes not subject to regulation under
35
Ill. Adm.
Code 721.
I am aware that there are significant
penalties for submitting
a false certification,
including the possibility
of fine or imprisonment.
~j
Small quantity generators with tolling agreements pursuant
to_35_Ill._Adm. Code 722.120(e) shall comply with the
applicable notification and certification requirements of
subsection
(a)
for the initial shipment of the waste subject
to the agreement.
Such generators
shall retain on—site a
copy of the notification and certification, together with
the tolling agreement,
for
at
least three years after
termination or expiration
of
the
agreement.
The three—year
record retention period
is automatically extended following
notification pursuant to Section 31(d)
of the Environmental
Protection Act, until either any subsequent enforcement
action
is resolved,
or the Agency notifies the generator
documents need no be retained,
117—547

228
b)
Treatment
facilities shall test their wastes according to the
frequency specified in their waste analysis plans as required by
35
Ill.
Adm.
Code 724.113 or 725.113.
Such testing must be
performed as provided in subsections
(b)(1),
(b)(2) and (b)(3).
1)
For wastes with treatment standards expressed
as
concentrations in the waste extract
(Section 728.141),
the
owner or operator of the treatment facility shall test the
treatment residues or an extract of such residues developed
using the test method described in Appendix A to assure that
the treatment residues or extract meet the applicable
treatment standards.
2)
For wastes prohibited under Section 728.132 or 728.139 which
are not subject to any treatment standards under Subpart D,
the owner or operator of the treatment facility shall test
the treatment residues according to the generator testing
requirements specified
in Section 728.132 to assure that the
treatment residues comply with the applicable prohibitions.
3)
For wastes with treatment standards expressed as
concentrations
in the waste (Section 728.143), the owner or
operator
of the treatment
facility shall test the treatment
residues
(not
an extract of such residues) to assure that
the treatment residues meet the applicable treatment
standards.
4)
A notice must be sent to the land disposal facility which
includes the following information:
A)
USEPA Hazardous Waste Number;
B)
The corresponding treatment standards
for wastes
FO0l—FOO5,
F039 and wastes prohibited pursuant to
Section 728.132 or Section 3004(d)
of the Resource
Conservation and Recovery Act, referenced in Section
728.139.
Treatment standards
for all other restricted
wastes must either be referenced as above,
or by
including on the notification the subcategory
of the
waste,
the treatability group(s)
of the waste(s),
and
the Section and subsection where the treatment
standards appear.
Where the applicable treatment
standards are expressed as specified technologies
in
Section 728.142,
the applicable five—letter treatment
code found
in Table C
(e.g.,
INCIN, WETOX)
also must
be listed on the notification.
and all applicable
prohibitions set forth in Cection 720.132 or 723.139.
C)
The manifest number associated with the shipment of
waste;
and
D)
Waste analysis data, where available,
117—548

229
5)
The treatment facility shall
submit a certification with
each shipment of waste or treatment residue of
a restricted
waste to the land disposal facility stating that the waste
or treatment residue has been treated in compliance with the
treatment standards specified
in Subpart D and the
applicable prohibitions
set forth in Section 728.132 or
728.139.
A)
For wastes with treatment standards expressed as
concentrations in the waste extract or
in the waste
(Sections 728.141 or 728.143),
or for wastes
prohibited under Section 728.132 or 728.139 which are
not subject to any treatment
standards under Subpart
D,
the certification must be signed by an authorized
representative and must state the following:
I certify under penalty of
law that
I have
personally examined and am familiar with the
treatment technology and operation of the
treatment process used to support this
certification and that, based on my inquiry of
those
individuals immediately responsible for
obtaining this information,
I believe that the
treatment process has been operated and
maintained properly so as to comply with the
performance levels
specified
in 35
Ill.
Adm.
Code 728.Subpart
D and all applicable
prohibitions set forth in 35
Ill. Adm. Code
728.132 or 728.139
or section 3004(d) of the
Resource Conservation and Recovery Act without
impermissible dilution of the prohibited waste.
I am aware that there are significant penalties
for submitting a false certification,
including
the possibility of fine and imprisonment.
B)
For wastes with treatment standards expressed as
technologies
(Section 728.142),
the certification must
be signed by an authorized representative and must
state the following:
I certify under penalty of law that the waste
has been treated in accordance with the
requirements of
35
Ill.
Adm.
Code 728.142.
I am
aware that there are significant penalties
for
submitting a false certification, including the
possibility of fine and imprisonment.
QJ
For wastes with treatment standards expressed
as
concentrations in the waste pursuant to Section
728.143,
if compliance with the treatment standards
in
Subpart D
is based
in part or
in whole on the
117—549

230
analytical detection limit alternative specified in
Section 728.143(c), the certification also must
state
the following:
I certify under penalty of law that
I have
personally examined and am familiar with the
treatment technology and operation of the
treatment process used to support this
certification and that, based on my inquiry of
those individuals immediately responsible for
obtaining this
information,
I believe that the
nonwastewater organic constituents have been
treated by incineration
in units operated in
accordance with 35
111.
Adm. Code 724.Subpart
0)
or
35
Ill. Adm. Code 725.Subpart
0, or by
combustion
in fuel substitution units operating
in accordance with applicable technical
requirements,
and
I have been unable to detect
the nonwastewater organic constituents despite
having used best good
faith efforts to analyze
for such constituents.
I am aware that there
are significant penalties for submitting
a false
certification, including the possibility of
fine
and imprisonment.
6)
If the waste or treatment residue will be further managed at
a different treatment or storage facility,
the treatment,
storage or disposal facility sending the waste or treatment
residue off-site must comply with the notice and
certification requirements applicable to generators under
this Section.
7)
For wastes that are subject to the prohibitions under
~ection 728.133(f)
anu arc not suoject to tne proni~i~ion~
set
forth
in Section 728.132, with each shipment of such
waste the owner or operator shall notify any subsequent
treatment, storage or disposal facility
in writing,
of any
applicable prohibitions
in writing,
of any applicable
prohibitions
set forth in Section 723.133(f).
The notice
must
include the following information~-
A)
UCEPA hazardous waste number;
B)
The applicable prohibitions set forth in Section
728.133(f);
C)
The manifest number associated with the shipment
of
‘-I
waste;
and
117—550

231
~2.)
Where the wastes are recyclable materials used in a manner
constituting disposal subject to the provisions of
35 Ill.
Adm. Code 726.120(b),
regarding treatment standards and
prohibition levels,
the owner or operator of a treatment
facility
(i.e. the recycler)
is not required to notify the
receiving facility pursuant to subsection
(b)(4).
With each
shipment of such wastes the owner or operator of the
recycling facility shall submit a certification described in
subsection
(b)(5),
and a notice which includes the
information listed
in subsection
(b)(4)
(except the manifest
number)
to the Agency.
The recycling facility also shall
keep records of the name and location of each entity
receiving the hazardous waste—derived product.
c)
Except where the owner or operator is disposing of any waste that
is
a recyclable material used
in
a manner constituting disposal
pursuant to
35
Ill.
Adm. Code 726.120(b), the ~4~eowner or
operator of any land disposal facility disposing any waste subject
to restrictions under this Part shall:
1)
Have copies of the notice and certification specified in
subsection
(a)
or
(b),
and the certification specified in
Section 728.108
if applicable.
2)
Test the waste,
or an extract of the waste or treatment
residue developed using the test method described in
Appendix A or using any methods required by generators under
Section 728.132, to assure that the wastes or treatment
residues are
in compliance with the applicable treatment
standards
set forth
in Subpart D and all applicable
prohibitions set forth in Sections 728.132 or 728.139.
Such
testing must be performed according to the frequency
specified in the facility’s waste analysis plan as required
by
35
Ill. Adm.
Code 724.113 or 725.113.
3)
Where the owner or operator
is disposing of
any waste that
is subject to the prohibitions under Section 728.133(f)
but
not subject to the prohibitions set forth
in Section
728.132, the owner or operator shall ensure that such waste
is the subject of
a certification according to the
requirements
of Section 728.108 prior to disposal in a
landfill or surface impoundment unit, and that such disposal
is
in accordance with the requirements of Section
728.1O5(h)(2).
The same requirement applies to any waste
that
is subject to the prohibitions under Section 728.133(f)
and also
is subject to the statutory prohibitions in the
codified prohibitions in Section 728.139 or Section 728.132
4)
Where the owner or operator
is disposing of any waste that
is
a recyclable material used in
a manner constituting
disposal subject to the provisions of
35
Ill. Adm. Code
117—55 1

232
726.120(b),
the owner or operator
is not subject to
subsections
(c)(1) through
(3) with respect to such waste.
(Source:
Amended at
15
Ill.
Reg.
,
effective
)
Section 728.108
Landfill and Surface Impoundment Disposal Restrictions
(Repealed)
The Board incorporates by reference
40
cm
268.8
(1989),
as amended at ~4 Fed.
fleg.
36970,
September
6,
1989.
This Section incorporates no future editions
or
amendments.
Prior to l~ay8,
1990, wastes which
are
otherwise
prohibited
from land disposal under Section 728.133(f) may be disposed
in a landfill or
surface impoundment which
is in compliance with the requirements of 40
0111
268.5(h)(2),
incorporated by reference in Section 728.105, provided the
requirements of
40
0111 268.8 are
met.
(Source:
Repealed at
15
Ill. Reg.
,
effective
Section 728.109
Special Rules for Characteristic Wastes
~j
The initial generator of a solid waste shall determine each waste
code applicable to the waste
in order to determine the applicable
treatment standards under Subpart B.
For purposes of part
268,
the waste will carry
a waste code designation for any applicable
listing under
35
Ill. Adm.
Code 721.Subpart B,
and also one or
more waste code designations under
35
Ill.
Adm. Code 721.Subpart
C
where
the
waste exhibits the relevant characteristic.
~
Where
a prohibited waste
is both
listed under
35
Ill.
Adm.
Code
72l.Subpart
D and exhibits
a characteristic under
35
Ill.
Adm.
Code 72l.Subpart
C,
the treatment standard for the waste code
listed in 35
Iii. Adm. Code 721.Subpart B will operate
in lieu of
the standard
for the waste code under
35
Ill.
Adm. Code
721.Subpart
C,
provided that the treatment standard for the listed
waste includes
a treatment standard for the constituent that
causes the waste to exhibit the characteristic.
Otherwise,
the
waste must meet the treatment standards
for all applicable listed
and characteristic waste codes.
~j.
In addition to any applicable standards determined
from the
initial point of generation,
no prohibited waste which exhibits
a
characteristic under
35
Ill. Mm.
Code 72l.Subpart
C shall be land
disposed unless the waste complies with the treatment standards
under Subpart
D.
~j
Wastes that exhibit a characteristic are also subject to Section
728.107 requirements,
except that
once the waste
is no
longer
hazardous,
for each shipment of such wastes to a non—hazardous
waste facility,
regulated under
35
Ill.
Adm. Code 807 or 811
through 815,
or exempted under Section 21(d)(l)(i)
of the
Environmental Protection Act,
or similarly regulated in other
States,
the initial generator or the treatment facility need not
117—552

233
send a Section 728.107 notification to such facility.
In such
circumstances,
a notification and certification must be sent to
the Agency,
or,
for out—of—State shipments, to the appropriate
USEPA Regional Administrator or State authorized, pursuant to 40
CFR 271, to implement 40 CFR 268 reauiremente,
fl
The notification must include the following information:
~j..
The name and address
of
the
non—hazardous
waste
facility receiving the waste shipment
~j
A
description
of
the
waste
as initially generated,
including the a~~licableUSEPA Hazardous Waste
Number(s) and treatability group(s):
~j
The treatment standards applicable to the waste at the
initial point of generation.
21
The certification must be signed by an authorized
representative and must state the language found in Section
728.107(b) (5) (A).
(Source:
Added at 15
Ill. Reg.
,
effective
)
SUBPART C:
PROHIBITIONS ON LAND DISPOSAL
Section 728.135
Waste Specific Prohibitions—-Third Third wastes.
~
The following wastes are prohibited from land disposal.
fl
The wastes specified
in
35
Ill.
Adm. Code 721.131
as EPA
Hazardous Waste Numbers:
F006
(wastewaters),
FO19
F039 (wastewaters)
21
The wastes specified in
35
Ill.
Adm.
Code
721.132
as
EPA
Hazardous Waste Numbers:
K002
K003
K004 (wastewaters)
K005
(wastewaters)
K006
1(008 (wastewaters)
1(011 (wastewaters)
1(013
(wastewaters)
1(014
(wastewaters)
1(017
1(021 (waste~~br~j
117—553

234
1(022
(wastewaters)
1(025
(wastewaters)
1(026
1(029
(wastewaters)
1(031
(wastewaters)
1(032
KO33
1(034
1(035
1(041
1(042
1(046
(wastewaters)
K048
(wastewaters)
1(049
(wastewaters)
1(050
(wastewaters)
1(05.
(wastewaters)
1(052
(wastewaters)
K060
(wastewaters)
1(061
(wastewaters)
1(069
(wastewaters)
1(073
1(083
(wastewaters)
1(084
(wastewaters)
1(085
1(095
(wastewaters)
1(096
(wastewaters)
1(097
1(098
KlOO
(wastewatersj
KlOl
(wastewaters)
1(102
(wastewaters)
1(105
1(106
(wastewaters)
~j
The wastes specified
in
35
Iii. Mm.
Code 721.133(e)
as EPA
Hazardous Waste Numbers:
Pool
P002
P003
P004
P005
P006
P007
P008
P009
POlO
(wastewaters)
POll
(wastewaters)
P012
(wastewaters)
P014
P015
P016
117— 554

235
P017
P018
P020
P022
P023
P024
P027
P028
P031
P033
P034
P036
(wastewaters)
P037
P038
P042
P045
P046
P047
P048
P049
P050
P051
P054
P056
P057
P058
P059
P060
P064
P065
(wastewaters)
P066
P067
P068
P069
P070
P072
P073
P075
P076
P077
P078
P081
P082
P084
P088
P092
P093
P095
P096
P101
P102
P103
117—555

236
P105
P108
P109
P110
P112
P113
P114
P115
P116
P118
P119
P120
P122
P123
j)
The wastes specified
in
35
Ill.
Adm. Code 721.133(f)
as EPA
Hazardous Waste Numbers:
U00 1
U002
1.1003
UOO4
U005
U006
1.3007
U008
U009
Uolo
U011
U012
U014
U015
UO16
U017
UO 18
1.1019
U020
U021
U02 2
U023
U02 4
U02 5
U026
U02 7
UO2 9
UO30
1.3031
UO32
U03 3
U034
U03 5
U036
117—556

237
0037
0038
0039
0041
0042
0044
2241
2241
0047
0048
0049
0050
0051
0052
0053
0055
0056
0057
0059
0060
0061
0062
0063
0064
0066
0067
0068
0070
0071
0072
0073
0074
0075
0076
0077
0078
0079
0080
0081
0082
0083
0084
0085
0089
0090
U091
0092
0093
0094
QQfl
117—557
238
13096
13097
13098
U099
13101
13103
U105
13106
13108
u109
UIi0
Ui”
13112
13113
Ui14
U115
U116
13117
Ui18
13119
U120
U121
13122
13123
13124
13125
Ui26
13127
U128
13129
U130
13131
U132
13133
13134
U135
U136 (wastewaters~
13137
13138
13140
13141
13142
13143
13144
UI45
13146
13147
13148
13149
Ui50
U151 (wastewaters~
13152
117-558

239
U153
13154
13155
13156
13157
13158
13159
Ui60
13161
13169
13170
13171
13172
13173
13174
13176
13177
13178
Ui79
1)180
13181
13182
13183
U184
13185
Ui86
U187
13188
13196
13197
13200
11201
13202
U203
15204
13205
13206
U208
117—559

240
13210
13211
13213
U214
13215
13216
U217
U218
U219
13220
13222
13225
13226
U2 27
U228
U2 34
13236
13237
13238
13239
13240
1.3243
13244
U246
1.3247
U248
13249
The following wastes identified as hazardous based on a
characteristic alone:
BOO.
D002
D003
D004
(wastewaters)
DOOS
D006
D007
DOO8
(except
for lead materials stored before
secondary smelting)
DOO9
(wastewaters)
DOlO
DOll
DO12
DO13
D014
DO15
DO?6
D017
117—560

241
~
The following wastes are prohibited from land disposal.
The
wastes specified
in 35
Ill. Adm. Code 721.132 as EPA Hazardous
Waste Numbers:
1(048
(nonwastewaters)
1(049
(nonwastewaters)
1(050 (nonwastewaters)
1(051
(nonwastewaters)
1(052
(nonwastewaters)
.~j.
Effective May 8,
1992, the following wastes
are prohibited from
land disposal:
fl
The wastes specified
in
35
Ill. Mm.
Code 721.131 as EPA
Hazardous Waste Numbers:
F039
(nonwastewaters)
21
The wastes specified in
35
111.
Adm. Code 721.132 as EPA
Hazardous Waste Numbers:
1(031
(nonwastewaters)
1(084
(nonwastewaters)
1(101
(nonwastewatérs)
1(102
(nonwastewaters)
1(106
(nonwastewaters)
.~J.
The wastes specified
in 35
Ill. Adm. Code 721.133(e)
as EPA
Hazardous Waste Numbers:
P010 (nonwastewaters)
POll (nonwastewaters)
P012
(nonwastewaters)
P036
(nonwastewaters)
P038
(nonwastewaters)
P065
(nonwastewaters)
P087
(nonwastewaters)
P092
(nonwastewaters)
j)
The wastes specified
in
35
Ill.
Adm. Code 721.133(f)
as EPA
Hazardous Waste Numbers:
U136
(nonwastewaters)
U151
(nonwastewatera)
~1
The following wastes identified
as hazardous based on a
characteristic alone:
DOO4
(nonwastewaters)
D008
(lead materials stored before secondary smelting)
D009
(nonwastewaters)
117—561

242
~j
Inorganic solids debris as defined in
35 Ill.
Adm.
Code
728.102(a)(7)
(which also applies to chromium refractory
bricks carrying the EPA Hazardous Waste Numbers 1(048-1(052)
fl
RCRA
hazardous wastes that contain naturally occurring
radioactive materials.
~j.
Effective May
8.
1992. hazardous wastes listed in 40
CFR 268.12
that are mixed radioactive/hazardous wastes are prohibited from
land
disposal.
.~j.
Effective
May
8,
1992,
the
wastes
specified j~this Section having
a treatment standard in Subpart D based on incineration, mercury
retorting or vitrification,
and which are contaminated soil or
debris,
are prohibited from land disposal.
~J
Between May
8,
1990,
and May 8,
1992, wastes included in
subsections
(c),
(d)
and
(e)
shall be disposed of in a landfill or
surface impoundment only if
such unit is
in compliance with the
requirements specified in Section 728.105(h)(2).
jj.
The requirements of subsections
(a),
(b),
(c),
(d)
and
(e) do not
apply
if:
fl
The wastes meet the applicable standards specified in
Subpart D
21
Persons have been granted an exemption from a prohibition
pursuant to a petition under Section 728.106, with respect
to those wastes and units covered by the petition
~
The wastes meet the a~~licablealternate standards
established pursuant to a petition granted under Section
728.144
4j.
Persons have been granted an extension to the effective date
of
a prohibition pursuant to Section 728.105, with respect
to these wastes covered by the extension.
jJ.
To determine whether a hazardous waste listed
in 40 CFR 268.10,
268.11 and 268.12 exceeds the applicable treatment standards
specified
in Sections 728.141 and 728.143,
the initial generator
shall either test
a representative
sample
of the waste extract or
the entire waste,
depending on whether the treatment standards are
expressed as concentrations in the waste extract or the waste,
or
use knowledge of the waste.
If the waste contains constituents
in
excess of the applicable Subpart D levels, the waste
is prohibited
from land disposal,
and all requirements of this Part are
applicable,
except as otherwise specified.
117—562

243
SUBPART
B:
TREATMENT
STANDARDS
Section
728.140
Applicability
of
Treatment
Standards
a)
A restricted waste identified in Section 728.141 may be land
disposed without further treatment only if an extract of the waste
or of the treatment residue of the waste developed using the test
method Appendix A does not exceed the value
shown
in Table A for
any hazardous constituent listed in Table A for that waste, with
the followino exceptions: D004.
D008,
1(031.
1(084,
1(101.
1(102,
POlO,
P011,
P012.
P036.
P038 and U136.
Wastes D004, D008.
1(031,
1(084,
1(101,
1(102, POlO.
P03.1, P012.
P036,
P038 and U136 may be
land dis~sedonly if an extract of the waste or of the treatment
residue of the waste develo~dusina either the test method in 35
Ill.
Adm. Code 721.Appendix A or the test method in 35 Ill. Adm.
Code 728.Appendix B does not exceed the value shown
in Table
B for
any hazardous constituent listed
in Table A for that waste.
b)
A restricted waste for which a treatment technology is specified
under Section 728.142(a) may be land disposed after it is treated
using that specified technology or an equivalent treatment method
approved by the Agency under the procedures
set forth in Section
728.142(b).
C)
ExcePt as otherwise specifies
in Section 728.143(c), aA restricted
waste identified
in Section 728.143 may be land disposed only if
the constituent concentrations in the waste or treatment residue
of the waste do not exceed the value shown in Table
B for any
hazardous constituent listed in Table
B for that waste.
(Source:
Amended at
15
Ill.
Reg.
,
effective
Section 728.141
Treatment Standards expressed as Concentrations in Waste
Extract
a)
Table A identifies the restricted wastes and the concentrations of
their associated hazardous constituents which may not be exceeded
by the extract of a waste or waste treatment residual developed
using
the
test
method
in
Appendix
A
for
the
allowable
land
disposal of such waste, with the exception of wastes D004.
D008.
1(031,
1(084,
1(101.
1(102.
P03.0,
POll,
p03.2,
P036, P038 and
13136.
Table A identifies the restricted wastes D004, D008.
1(031.
1(084,
K101,
1(102,
POlO, P011,
P012,
p036,
P038 and U136 and the
concentrations of their associated constituents which shall
not be
exceeded by the extract of a waste or waste treatment residual
developed using the test method in 35
Ill. Mm.
Code 721.Appendix
A or B for the allowable land disposal of such wastes.
(Appendix
B provides guidance on treatment methods that have been shown to
achieve the Table A levels for the respective wastes.
Appendix B
is not a regulatory requirement but is provided to assist
generators and owners or operators in their selection of
117—563

244
appropriate treatment methods.) Compliance with these
concentrations
is required based on grab samples.
b)
When wastes with differing treatment standards for a constituent
of concern are combined for purposes of treatment, the treatment
residue must meet the lowest treatment standard for the
constituent of concern.
Section 728.142
Treatment Standards expressed as Specified Technologies
a)
The following wastes in subsections
(a)(1)
and
(2) and Table D and
Emust
be treated using the identified technology or technologies
specified
in subsections
(a)(1)
and
(2)
and Table C.,
or an
~tmiyR1~nt
method approvcd undcr subsection
(b1.
1)
Liquid hazardous wastes containing PCBs at concentrations
greater than or equal to
50 ppm but less than 500 ppm must
be incinerated
in accordance with technical requirements at
40 CFR 761.70,
incorporated by reference in 35
Ill.
Adm.
Code 720.111, or burned in high efficiency boilers in
accordance with the technical requirements of 40 CFR 761.60.
Liquid hazardous wastes containing PCBs at
concentrations
greater than or equal to 500 ppm must be incinerated in
accordance with the technical requirements of 40 CFR 761.70.
Thermal treatment
in accordance with this Section must be
in compliance with applicable regulations
in 35
Ill. Adm.
Code
724,
725 and
726.
2)
Nonliquid hazardous wastes containing halogenated organic
compounds
(HOC5)
in total concentrations greater than or
equal to 1000 mg/kg and liquid HOC-containing wastes that
are prohibited under Section 728.132(e)(l) must be
incinerated in accordance with the requirements of
35
Ill.
Adm. Code 724.Subpart 0 or
35 Ill.
Adm.
Code 725.Subpart O~-
or
in boilers or industrial
furnaces,
as defined
in
35
Ill.
Mm.
Codc 720,
burning in accordance wi~.3~Ill. Mm.
Code
~7-26.These treatment standards do not apply where the waste
is subject to a Subpart C treatment
standard for a specific
HOC (such as
a hazardous waste chlorinated solvent for which
a treatment standard
is established under Section
728.141(a)).
3)
The
must be incinerated
in accordance with the requirements of
35
Ill.
r.dm. Code 724.Oubpart
0,
or
35
Ill. Mm.
Code
~-25.Cubpart 0, or burned
in boilers or industrial furnace3,
as defined
in
35
Ill. Mm.
Codc
720,
in accordance with 35
Til
-
(‘r~r~
7~.
KO2 7
1(030
1(113
117—564

245
1(114
1(115
1(116
P040
P041
ro43
I~O~4
4
r062
P035
P100
P111
13058
13087
13221
13223
4)
Thc wastewater form of the following hatardous wastes must
be treated by carbon adsr~rr~tion,or incineration,
or
oretreatment followed
by
carbon
~
KO-2
7
1(030
1(113
1(114
1(115
1(116
P040
P041
P043
P044
P062
roes
P100
Pill
U058
13221
13223
b)
Any person may submit an application to the Agency demonstrating
that an alternative treatment method can achieve a level of
performance equivalent to that achievable by methods specified in
subsections
(a),
(c)
and
(d).
The applicant shall submit
information demonstrating that the applicant’s treatment method
is
in compliance with federal and state requirements,
including this
Part,
35
Iii. Adm. Code 709,
724,
725,
726 and 729 and Sections
22.6 and 39(h)
of the Environmental Protection Act
(Ill.
Rev.
Stat.
1987,
oh.
111
1/2,
pars.
1022.6 and 1039(h)), and
is
protective of
human health or the environment.
On the basis of
such information and any other available information, the Agency
shall approve the use of the alternative treatment method
if the
Agency finds that the alternative treatment method provides a
117—565

246
measure of performance equivalent to that achieved by methods
specified in subsections
(a),
(C)
and
(d).
Any approval must be
stated
in writing and may contain such provisions and conditions
as the Agency determines to be appropriate.
The person to whom
such approvalcertification is issued shall comply with all
limitations contained in such determination.
~J.
As an alternative
to the otherwise applicable Subpart
B treatment
standards,
lab packs are eligible for land disposal provided the
following requirements are met:
li
The lab packs comply with the applicable provisions of 35
Ill. Adm.
Code 724.416 and 725.416;
BOARD NOTE:
35
Iii.
Adm. Code 729.301 and 729.312 include
additional restrictions on the use of lab packs.
21
All hazardous wastes contained in such lab packs are
specified
in Appendix B or Appendix E
.~j.
The
lab packs are incinerated
in accordance with the
requirements of
35
Ill. Mm.
Code 724.Subpart
0 or
35
III.
Adm. Code 725.Subpart 0;
and
jj
Any incinerator residues
from lab packs containing DOO4,
D005,
DOO6, D007, D008,
BOb
and DOll are treated in
compliance with the applicable treatment standards specified
for
such wastes
in Subpart D.
~j
Radioactive hazardous mixed wastes with treatment standards
specified
in Table E are not
sub-eject to any treatment standards
specified in Section 728.141,
Section 728.143 or Table
D.
Radioactive hazardous mixed wastes
not subiect to treatment
standards
in Table E remain
sub-sect to all applicable treatment
standards specified
in Section 728.141,
Section 728.143 and Table
D.
(Source:
Amended at
15
Ill.
Reg.
,
effective
Section 728.143
Treatment Standards expressed as Waste Concentrations
a)
Table
B identifies the restricted wastes and the concentrations of
their associated hazardous constituents which must not be exceeded
by the waste or treatment residual
(not an extract of such waste
or treatment residual)
for the allowable land disposal of such
waste or residual.
Compliance with these concentrations
is
required based upon grab samples,
unless otherwise noted in Table
B.
The wastewpter and nonwastewater treatment
standards in Table
ti
are oaaco on analysis or grao samples exccpt tne wastewatcr
treatment standards that are based on analysis
of composite
samplca for wastes,
1(000,
1(010,
1(036,
1(038,
1(040,
P030,
P071,
117—566

247
b)
When wastes with different treatment standards for a constituent
of concern are combined for purposes of treatment,
the treatment
residue must meet the lowest treatment standard for the
constituent
of concern.
Qj
Notwithstanding the prohibitions specified
in subsection
(a)
and
Table
B,
treatment
and disposal facilities may demonstrate
(and
certify pursuant to Section 728.107(b)(5))
compliance with the
treatment standards
for organic constituents specified in this
Section and Table
B by satisfying the following conditions:
jj
The treatment
for the organic constituents were established
based on incineration
in units operated
in accordance with
the technical requirements
of
35
Ill. Mm.
Code 724.Subpart
o
or
35
Ill.
Adm.
Code 725.Subpart 0,
or based on combustion
in fuel substitution units operating
in accordance with
applicable technical requirements
21
The organic constituents have been treated using the methods
referenced
in
subsection
(c)(1);
and
~j
The treatment or disposal
facility has been unable to detect
the organic constituents despite using
its best good—faith
efforts
as defined by applicable standards.
Until such
standards are developed,
such good—faith efforts may be
demonstrated by showing that the treatment or disposal
facility has detected the organic constituents at
levels
less than ten times the treatment standard specified
in this
Section.
(Source:
Amended at
15
Ill. Reg.
,
effective
117—567

248
Section 728.Appendix B
Organometallic Lab Packs
Hazardous waste with the following EPA waste codes may be placed in an
“organometallic”
or “Appendix D lab pack:”
FOOl,
F002,
F003,
FOO4,
F005,
FOO6, FOb,
F020,
F021,
F023,
F024,
F026,
F027,
F028
1(001,
1(002,
1(008,
1(009,
1(010,
1(011,
1(013,
1(014,
1(015,
1(016,
1(017,
1(018,
1(019,
1(020,
1(021,
1(022,
1(023,
1(024,
1(025,
1(026,
1(027,
1(028,
1(029,
1(030,
K031,
KO32,
1(033,
1(034,
1(035,
1(036,
1(037,
1(038,
1(039,
1(040,
1(041,
1(042,
1(043,
K044,
1(045,
1(046,
1(047,
1(048,
1(049,
1(050,
1(051,
1(052,
1(054,
1(060,
1(061,
1(064,
KO65,
1(066,
1(069,
1(071,
1(073,
K083,
1(084,
1(085.
1(086,
1(087,
1(093,
1(094,
1(095,
1(096,
K097,
1(098,
1(099,
1(101,
K102,
1(103,
1(104,
1(105,
1(111,
1(112, Kl13,
1(114,
1(115,
1(116,
1(117,
1(118,
1(123,
1(124,
1(125,
1(126,
1(136
DOOl,
B002, D003,
D004,
D005,
DOO6,
D007,
D008, BOb,
DOll,
D012,
DO13,
D014,
D015,
D016, D017
13032, U136,
13144,
13145,
0146,
U163, U214,
U215,
U216,
U217
BOARD NOTE:
35
Iii. Adm.
Code 729.301 and 729.312
include additional
limitations on the use of
lab packs.
P001.
P002,
P003,
P004,
P005,
P006.
P007,
P008,
P009,
P013,
P014,
P015,
P016,
P017,
P018.
P020,
P022.
P023.
P024, P025,
P026,
P027,
P028,
P031,
P034,
P036,
P037, P038.
P039,
P040,
P041,
P042,
P043,
P044,
P045, P047,
P048, P049,
P050,
P051, P054,
P056,
P057,
P058, P059,
P060,
P062.
P063, P064,
P065,
P066, P067,
P068. P069,
p070,
P071, P072, P073,
P074, P075,
P07’), P081,
P082,
P084, P085,
P087,
P088,
P089,
P092, P093,
P094, P095, P096,
P097, P098,
P099,
P101, P102,
P103,
P104,
P105,
P108,
P109,
P110,
P112,
P113, P114, P115,
P116,
P118.
P119,
P120,
P122,
P123
13004,
13005, 0006,
0007,
U008,
U009,
UO10,
13011, 0012,
U014,
0001, 0002,
13003,
0017,
U0l8,
13019,
13020,
13021. UO22,
13023,
U024,
0025, 0026,
0027,
0031,
U032,
U033,
0034, 0035,
13036,
13037,
0038, U039,
0041,
0045,
0046,
U047,
13048, 0049,
0050,
0051,
0052, 0053,
0055,
0015,
0028,
0042,
13056,
13070,
0083,
0096,
U111,
13124,
0137,
13148,
0161,
0176,
0189,
0205,
0219,
0238,
0016,
0029,
0043,
13057,
13071,
13084,
0097,
0112,
13125,
0136,
0149,
13162,
0177,
0190,
0206,
13220,
13239,
0030,
0044,
0058,
0072,
0085,
0098,
13113,
13126,
U137,
U150,
0164,
0178
0191
1.3207
U221,
13240.
0061,
U075,
13088,
0102,
13116,
13129,
0140,
U153,
Ul67,
U181,
13194,
ti2lfL
13059,
0060,
0073, 0074,
0086, UO87,
13099, 0101,
U114, 0115,
0127,
0128,
0138,
U139.
13152,
13154,
U165,
13166,
0179,
0180,
0192,
0193,
0208,
0209,
0222,
0223,
0243,
13244.
13062,
0063, U064,
0066,
U076,
0077,
0078,
0079,
0089, U090,
UO91, 0092,
U103, 0105,
0106, 0107,
0117, 0118,
0119, 0120,
13130,
0131, U132,
13133,
1.3141,
0142, 0143,
0144,
U154,
0155, 0156,
0157,
U168, 0169, 0170,
0171,
0182,
0183,
U184,
0185.
0196,
U197,
13200,
U201,
11211
U21~L 11214.
11215.
0067, 0068,
U080, 0081,
U093, 0094,
0108, 0109,
0121, 0122,
0134, 0135,
0145,
0146,
0158,
U159,
U172,
0173,
13186,
U187.
0202,
13203
U216,
0217
T12~c
t121~i
0069,
0082,
0095,
0110,
13123,
0136,
0147,
U160,
13174,
0188,
0204,
0218,
U2
37
0246,
0247,
0248,
13249, U328,
0353, 0359
0225,
0226, 0227, U228, U234,
~
~
117—568

249
(Source:
Added at
15
Ill. Reg.
,
effective
117—569

250
Section 728.Appendix E
Organic Lab Packs
Hazardous wastes with the following EPA Hazardous Waste Code No. may be placed
in an “organic” or “Appendix E”
lab pack:
POOl,
P002,
p003,
P004,
P005,
p006,
P007,
P008, P009,
P013,
P014,
P015.
P016,
P017,
P018, P020, P022,
P023,
P025,
P024,
P026,
P027,
P028,
P031, P034,
P036,
P037,
P038, P039, P040,
P041,
P042,
P043,
p044,
P045, P046,
P047, P048,
P049,
p050,
P051,
P054,
P057,
P058,
P059,
P060,
P062,
P063, P064,
P064, P065,
P066,
P067,
P068.
p069,
P070,
P071.
P072,
P073, P074,
P075,
P077,
P081, P082,
P084,
P085,
p087,
p088,
P089,
P092,
P093,
P094,
P095,
P096, P097,
P098, P099,
P101,
P102,
P103,
P104,
P105,
P108,
P109, P110, P111,
P112,
P113,
P114,
P115.
P116.
P118. P119,
P120,
P122,
P123
U001,
U002,
0003,
0004,
0005,
U006,
0007,
0008, 0009,
0010,
0011,
0012,
0014,
U015,
0016, 0017,
0018,
0019,
0020,
0021,
0022,
0023,
0024,
13025, 0026,
13027,
0028, 0029,
0030,
0031,
13033, U034,
0035,
0036,
U037, U038,
0039, 0041,
U042,
0043,
0044,
0045,
0046,
0047,
0048,
0049, 0050,
0051, 0052,
0053,
0055,
0056,
0057, 0058,
0059,
0060,
0061,
0062,
U063, 0064,
U066,
0067,
0068,
0069,
0070,
0071, 0072,
U073, 0074,
UO75,
0076,
0077, 0078,
0079,
0080,
0081,
0082,
0083,
0084, U085,
0086,
0087,
0088,
0089,
0090,
0091,
0092,
0093,
0094,
0095,
0096,
0097, U098,
0099,
0101,
0102,
0103,
0105,
0106,
0107,
0108,
0109,
0110,
Ubll,
0112, 0113,
0114,
Ul15,
13116, 0117,
0118,
0119,
0120,
0121,
0122,
0123,
0124,
0125,
Ub26, U127,
0128,
0129,
0130,
0131,
0132,
0133,
0135,
0137, 0138,
0139L
0140,
0141, 0142,
U143,
1.3147,
U148,
0149,
13150,
13153,
01S4,
0155, 0156,
U157L
0158,
13159,
13160,
0161,
0162,
0163,
0164,
0165,
0166,
0167,
0168, 0169, U170,
0171,
13172, 0173,
0174,
0176,
13177, U178, U179,
0180, 0181,
0182, 0183,
0184,
0185,
13186,
0187, 0188,
0189, 0190,
0191, 0192,
0193,
U194,
0196, 0197, U20O~
0201, 0202,
0203,
13205,
0206,
13207,
13208,
0209, 0210,
13211, 0213, 0214,
U218,
0219,
0220,
0221,
U222,
0223,
0225,
0226,
13227, 0228,
0234,
U235,
0236, U237L
U238,
0239, 0240,
U243,
0244,
0246,
13247, 0248,
13249,
0328,
0353,
13359
FOOl,
F002,
F003,
F004,
F005, FOb,
F020,
F021,
F023,
F024,
F026,
F027,
F028
1(001,
1(009,
1(010,
1(011,
1(013,
1(014,
1(015,
1(016,
1(017,
1(018,
1(019,
1(020,
1(021,
1(022,
1(023,
1(024,
1(025,
1(026,
1(027,
1(029,
K030,
1(031,
K032,
1(033,
1(034, K035L
1(036,
K037,
1(038,
1(039,
1(040,
1(041,
1(042,
1(043,
1(044,
1(045,
1(046,
1(047, K048L
K049,
1(050,
1(051,
1(052. K0S4,
1(060,
1(065,
1(073,
1(083,
K084,
K085.
1(086,
K087L
1(093,
1(094,
1(095,
1(096,
1(097,
1(098,
K099,
1(101,
1(102,
1(103,
K104, Kl05,
1(111.
1(112,
1(113,
1(114,
1(115,
1(116,
1(117,
1(118,
1(123,
1(124.
1(125,
K126.
1(136
D001, B012,
D013. D014,
BObS,
D016,
D017
BOARD NOTE:
35 Ill.
Adm. Code 729.301 and 729.312 include additional
limitations on the use of lab packs.
(Source:
Added at
15 Iii. Reg.
,
effective
117—570

251
Section 728.Appendix
F
Technologies to Achieve Deactivation of
Characteristics
The treatment standard for many subcategories of DOOl, D002 and D003 wastes as
well
as
for 1(044,
1(045 and
1(047 wastes
is listed in Section 728.142 simply as
“Deactivation to remove the characteristics
of ignitability,
corrosivity,
and
reactivity”.
USEPA has determined that many technologies,
when used alone or
in combination, can achieve this standard,
The following presents a partial
list of these technologies, utilizing the five letter technolocy codes
established
in Table
C.
Use of these specific technologies is not mandatory
and does not preclude direct reuse, recovery or the use of other pretreatment
technologies provided deactivation is achieved and these alternative methods
are not performed in units designated as land disposal.
Waste code/subcategory
Nonwastewaters
Wastewaters
DOOl Ignitable Liquids based on 35 Ill.
RORGS
n.a.
Adm. Code 721.121(a)(1)——Low TOC
WETOX
Noriwastewater Subcategory
(containing 1
INCIN
to 10
TOC)
CHOXD
BIODG
DOOl
Ignitable Liquids based on
35 Ill.
n.a.
WETOX
Adrn.
Code 72b.121(a)(1)——Ignitable
RORGS
Wastewater Subcategory
(containing 1
INCIN
TOC)
CHOXD
BIODG
DOO1 Compressed Gases based on
35
Ill.
RCGAS
n.a.
Adrn.
Code 721.b2b(a)(3)
FSUBS
INCIN
ADGAS
fb.
INCIN
ADGAS
fb.
(CHOXD; or
CHRED)
DOO1 Ignitable Reactives based on
35
Ill.
WTRRX
n.a.
Adm.
Code 721.121 (a) (2)
CHOXD
CHRED
STABL
INCIN
DOOl
Ignitable Oxidizers based on 35
Ill.
CHRED
CHRED
Adm.
Code 721.121(a)(4)
INCIN
INCIN
D002 Acid Subcategory based on
35
Ill.
RCORR
NEUTR
Adm.
Code 721.b22(a)(1j with PH loss than
NEUTR
INCIN
or equal to
2
INCIN
117—571

252
D002 Alkaline Subcategory based on
35
Ill.
NEUTR
NEUTR
Adm.
Code 721.122(a)(1)
with pH greater
INCIN
INCIN
than or equal to 12.5
DOO2 Other Corrosives based on
35 Ill.
CHOXD
CHOXD
Adm.
Code 721.122(a) (2)
CHRED
CHRED
INCIN
INCIN
STABL
D003 Water Reactives based on
35
Ill. Mm.
INCIN
n.a.
Code 721.123(a)(2),
(3)
and
(4)
WTRRX
CHOXD
CHRED
D003 Reactive Sulfides based on 35
Ill.
CHOXD
CHOXD
Adrn.
Code 721.123(a) (5)
CHRED
CHRED
INCIN
BIODG
STABL
INCIN
D003 Explosives based on 35
Ill. Mm.
Code
INCIN
INCIN
721.123(a)
(6),
(7)
and
CHOXD
CHOXD
CHRED
CHRED
BIODG
CARBN
D003 Other Reactives based on
35
Ill. Adm.
INCIN
INCIN
Code 721.123(a)(b)
CHOXD
CHOXD
CHRED
CHRED
BIODG
CAREN
K044 Wastewater treatment
sludges from the
CHOXD
CHOXD
manufacturing and processing of explosives
CHRED
CHRED
INCIN
BIODG
CARBN
INCIN
1(045
Spent carbon from the treatment of
CHOXD
CHOXD
wastewaters containing explosives
CHRED
CHRED
INCIN
BIODG
CARBN
INCIN
1(047 Pink/red water from
TNT
operations
CHOXD
CHOXD
CHRED
CHRED
INCIN
BIODG
CARBN
INCIN
Note:”n.a.”
stands
for
“not applicable”.
“fb.” stands for “followed by”.
117—572

253
(Source:
Added at
15
Ill.
Reg.
,
effective
117—573

254
Section ‘)28.Appendix G
Federal Effective Dates
The following are the effective dates
for the TJSEPA rules
in 40 CFR 268.
These generally became effective as Illinois rules at a later date.
Waste Code
Waste Category
Effective date
California list
California
list
California
list
California list
California list
California list
California list
Liquid hazardous wastes,
including free
liquids associated with
solid or sludge,
containing free cyanides at concentrations
greater than or equal to
1,000 m~/lor
certain metals or compounds of these
metals greater than or equal to the
prohibition levels
Liquid
(aqueous) hazardous wastes having
PH less than or equal to
2
Dilute HOC wastewaters, defined as
HOC-waste mixtures that are primarily
water and that contain greater than or
equal to
1,000 mg/b but less than 10,000
mg/b
Liquid hazardous waste containing PCB5
greater than or equal to 50 ppm
Other
liquid and non-liquid hazardous
wastes containing HOCs in total
concentration greater than or equal to
1,000 mg
Soil and debris
HOCs not
from CERCLA/RCRA
corrective actions
Soil and debris HOCs from CERCLA/RCRA
corrective actions
July
8,
1987
a July
8.
1987
July
8,
1987
July
8,
1987
Nov.
8, 1988
July 8, 1989
Nov.
8,
1990
DOO1
DOO2
DOO3
Aug.
8,
1990
Aug.
8, 1990
Aug.
8,
1990
DOO4
Inorganic solid debris
May
8,
1992
DOO4
DOO4
Nonwastewater
Wastewater
May
8,
199.2
Aug.
8,
1990
BOOS
Inorganic solid debris
May
8,
1992
117—574

255
D005
All others
Aug.
8,
1990
0006
Inorganic solid debris
May
8.
1992
0006
All others
Aua.
8,
1990
0007
Inorganic solid debris
May
8,
1992
0007
All
others
Aug.
8,
1990
0008
Inorganic solid debris
May
8,
1992
DOOB
Lead acid batteries
May
8,
1992
DOO8
All others
Aug.
8, 1990
D009
Inorganic solid debris
May
8,
1992
0009
High mercury nonwastewater
May
8,
1992
DOO9
Low mercury nonwastewpter
May
8,
1992
DOO9
All others
Aug.
8,
1990
DO1O
Inorganic solid debris
May
8,
1992
0010
All others
Aug.
8,
1990
DOll
Inorganic solid debris
May
8,
1992
BOll
All others
Aug.
8,
1990
DO12
All
Aug.
8,
1990
0013
All
Aug.
8,
1990
DO14
All
Aug.
8,
1990
D015
All
Aug.
8,
1990
D016
Al.
Aug.
8,
1990
0017
All
Aug.
8,
1990
FO01—F005
All, except in next listing
Nov.
8, 1986
117—575

256
FOO1—F005
FOO1—FOO5
FOO2
b
FOO5 c
FOO6
FOO6
FOO6
FOO7
F008
F009
FO10
FOb
FO11
FO12
FO19
FO2O
FO2O
FO21
F021
FO2 2
F02 2
F02 3
FO23
Small
quantity generators, CERCLA/RCRA
corrective action,
initial generator~s
solvent—water mixtures,
solvent—
containing sludges and solids,
and non
CERCLA/RCRA corrective action soils with
less than
1 percent total
solvent
constituents
Soil and debris
All
All
Wastewater
Nonwastewater
Nonwastewater
All
All
All
Soil and debris
All others
All
All
All
Soil and debris
All others
Soil and debris
All others
Soil and debris
All others
Soil and debris
All others
Nov.
8,
1988
Nov.
8,
1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
8,
1990
Aug.
8,
1988
July
8,
1989
July
8,
1989
July
8,
1989
July 8,
1989
June
8,
1991
June
8,
1989
July
8,
1989
July
8,
1989
Aug.
8,
1990
Nov.
8,
1990
Nov.
8,
1988
Nov.
8,
1990
Nov.
8,
1988
Nov.
8,
1990
Nov.
8,
1988
Nov.
8,
1990
Nov.
8,
1988
117—576

257
FO24
Soil and debris
June 8,
1991
FO24
(metals)
Nonwastewater
Aug.
8,
1990
FO24
Al.
Aug.
8,
1990
(dioxins/furans)
F024
All others
June
8,
1989
FO25
All
Aug.
8,
1990
F026
Soil
and debris
Nov.
8.
1990
F026
All others
Nov.
8.
1988
FO27
Soil and debris
Nov.
8,
1990
F027
1~.llothers
Nov.
8,
1988
FO28
Soil and debris
Nov.
8,
1990
FO28
All others
Nov.
8,
1988
FO39
Wastewater
Aug.
8,
1990
F039
Nonwastewater
May.
8,
1992
1(001
Soil and debris
Aug.
8,
1990
1(001
~
Aug.
8,
1990
(lead/organics)
1(001
All others
Aug.
8,
1988
1(002
Al.
Aug.
8,
1990
1(003
~ll
Aug.
8,
1990
1(004
~ll
Aug.
8,
1990
1(005
d
All
Aug.
8,
1990
1(006
Al.
Aug.
8,
1990
1(007
d
Al.
Aug.
8,
1990
KOO8
Al.
Aug.
8,
1990
KOO9
Soil and debris
June
8,
1991
KOO9
All others
June
8,
1989
117—577

258
1(010
Soil
and debris
June
8,
1991
1(010
All others
June
8,
1989
1(011
Wastewater
Aug.
8,
1990
1(011
Nonwastewater
June 8,
1989
1(011
Soil and debris
June 8,
1991
1(013
Wastewater
Aug.
8,
1990
1(013
Nonwastewater
June
8,
1989
1(013
Soil
and debris
June
8,
1991
1(014
Wastewater
Aug.
8,
1990
1(014
Nonwastewater
June
8,
1989
K014
Soil and debris
June
8,
1991
1(015
Wastewater
Aug.
8,
1988
K015
Nonwastewater
Aug.
8,
1990
K0l6
Soil and debris
Aug.
8,
1990
1(016
All others
Aug.
8,
1988
1(017
?~fl
Aug.
8,
1990
1(018
Soil and debris
Aug.
8,
1990
1(018
All others
Aug.
8,
1988
1(019
Soil and debris
Aug.
8,
1990
1(019
All others
Aug.
8,
1988
1(020
Soil and debris
Aug.
8,
1990
1(020
All others
Aug.
8,
1988
1(021 e
All
Aug.
8,
1990
1(022
Wastewater
Aug.
8,
1990
1(022
Nonwastewater
Aug.
8,
1988
K022
Soil and debris
Aug.
8,
1990
117—578

259
1(023
Soil and debris
June
8,
1991
1(023
All
others
June
8,
1989
1(024
Soil and debris
Aug.
8.
1990
1(024
All others
Aug.
8,
1988
1(025 e
Aug.
8,
1990
1(026
Aug.
8,
1990
1(027
Soil
and
debris
June
8,
1991
KO27
All
others
June
8,
1989
K028
Soil and debris
June
8,
1991
1(028 (metals)
Nonwastewater
Aug.
8,
1990
1(028
All others
June
8,
1989
1(029
Wastewater
Aug.
8,
1990
1(029
Nonwastewater
June
8,
1989
KO29
Soil and debris
June
8,
1991
KO3O
Soil and debris
Aug.
8,
1990
1(030
All others
Aug.
8,
1988
1(031
Wastewater
Aug.
8,
1990
K031
Nonwastewater
May
8,
1992
1(032
Aug.
8,
1990
1(033
~ll
Aug.
8,
1990
1(034
All
Aug.
8,
1990
1(035
All
Aug.
8,
1990
1(036 e
All
Aug.
8,
1990
1(037
Soil and debris
Aug.
8,
1990
1(037
Wastewater
Aug.
8.
1990
1(037
All others
Aug.
8,
1988
117—579

260
1(038
Soil and debris
June 8,
1991
1(038
All others
June
8,
1989
1(039
Soil and debris
June
8,
1991
KO39
All others
June
8,
1989
1(040
Soil and debris
June
8,
1991
1(040
All others
June
8,
1989
1(041
Al.
Aug.
8,
1990
1(042
Al.
Aug.
8,
1990
1(043
Soil and debris
June
8,
1991
KO43
All others
June
8,
1989
KO44
All
Aug.
8,
1990
1(045
Aug.
8,
1990
1(046
Nonreactive nonwastewater
Aug.
8,
1988
1(046
All others
Aug.
8,
1990
K047
Aug.
8,
1990
1(048
Wastewater
Aug.
8,
1990
1(048
Nonwastewater
Nov.
8,
1990
1(049
Wastewater
Aug.
8,
1990
1(049
Nonwastewater
Nov.
8, 1990
1(050
Wastewater
Aug.
8,
1990
1(050
Nonwastewater
Nov.
8,
1990
K051
Wastewater
Aug.
B,
1990
1(051
Nonwastewater
Nov.
8,
1990
1(052
Wastewater
Aug.
8, 1990
1(052
Nonwastewater
Nov.
8,
1990
KO6O
e
All
Aug.
8,
1990
117—580

261
1(061
Wastewater
Aug.
8,
1990
1(061
Nonwastewater
Aug.
8,
1988
1(062
~ll
Aug.
8,
1988
1(069
~ll
Aug.
8,
1990
1(073
~ll
Aug.
8,
1990
KO83
Aug.
8,
1990
1(084
Wastewater
Aug.
8,
1990
1(084
Nonwastewater
May
8,
1992
K085
~.ll
Aug.
8,
1990
1(086
Aug.
8,
1990
1(087
Soil and debris
Aug.
8,
1990
1(087
All others
Aug.
8,
1988
1(093
Soil and debris
June
8,
1991
1(093
All others
June
8,
1989
1(094
Soil
and debris
June
8,
1991
K094
All others
June
8,
1989
1(095
Wastewater
Aug.
8,
1990
1(095
Nonwastewater
June
8,
1989
1(095
Soil and debris
June
8,
1991
1(096
Wastewater
Aug.
8,
1990
KO96
Nonwastewater
June
8,
1989
1(096
Soil and debris
June
8,
1991
1(097
All
Aug.
8,
1990
1(098
All
Aug.
8,
1990
1(099
All
Aug.
8,
1988
1(100 e
All
Aug.
8,
1990
117—581

262
1(101
Wastewater
Aug.
8,
1988
1(101
Nonwastewater
May 8,
1992
1(102
Wastewater
Aug.
8,
1988
1(102
Nonwastewater
May 8,
1992
1(103
Soil and debris
Aug.
8,
1990
Kb03
All others
Aug.
8,
1988
1(104
Soil and debris
Aug.
8,
1990
1(104
All others
Aug.
8,
1988
1(105
Aug.
8,
1990
K106
High mercury nonwastewater
May 8,
1992
1(106
Low mercury nonwastewater
May.
8,
1992
K1O6
All others
Aug.
8,
1990
1(113
Soil
and debris
June
8,
1991
K1l3
All others
June
8,
1989
1(114
Soil and debris
June
8,
1991
K114
All others
June
8,
1989
K11S
Soil and debris
June
8,
1991
KI1S
All others
June
8, 1989
1(116
Soil and debris
June
8, 1991
1(116
All others
June 8, 1989
POOl
~ll
Aug.
8,
1990
P002
~ll
Aug.
8,
1990
P003
Al.
Aug.
8,
1990
P004
~JJ.
Aug.
8,
1990
P005
&U.
Aug.
8,
1990
P006
All
Aug.
8,
1990
117—582

263
P007
All
Aug.
8,
1990
P008
Al.
Aug.
8,
1990
P009
~ll
Aug.
8,
1990
POlO
Wastewater
Aug.
8,
1990
POlO
Nonwastewater
May
8,
1992
Poll
Wastewater
Aug.
8,
1990
POll
Nonwastewater
May 8,
1992
P012
Wastewater
Aug.
8,
1990
P012
Nonwastewater
May
8,
1992
P013
~jJ~
Aug.
8,
1990
P014
Aug.
8,
1990
P015
?~ll
Aug.
8,
1990
P016
~jJ.
Aug.
8,
1990
P017
~jJ..
Aug.
8,
1990
P018
~ll
Aug.
8,
1990
P020
~ll
Aug.
8,
1990
P021
All
June
8.
1989
P022
Al.
Aug.
8,
1990
P023
Al.
Aug.
8,
i990
P024
Al.
Aug.
8,
1990
P026
Al.
Aug.
8,
1990
P027
Al.
Aug.
8,
1990
P028
All
Aug.
8,
1990
P029
Al.
June
8,
1989
P030
~ll
June
8,
1989
P031
Al.
Aug.
8,
1990
117—583

264
P033
All
Aug.
8,
1990
P034
Aug.
8,
1990
P036
Wastewater
Aug.
8,
1990
P036
Nonwastewater
May
8,
1992
P037
~ll
Aug.
8,
1990
P038
Wastewater
Aug.
8,
1990
P038
Nonwastewater
May 8,
1992
P039
Soil and debris
June
8,
1991
P039
All others
June
8,
1989
P040
Soil and debris
June
8,
1991
P040
All others
June
8,
1989
P041
Soil and debris
June
8,
1991
P041
All others
June
8,
1989
P042
All
Aug.
8,
1990
P043
Soil and debris
June
8,
1991
P043
All others
June 8,
1989
P044
Soil and debris
June
8,
1991
P044
All others
June
8,
1989
PO4S
Aug.
8,
1990
P046
Al.
Aug.
8.
1990
P047
~ll
Aug.
8,
1990
P048
Al.
Aug.
8,
1990
P049
All
Aug.
8,
1990
P050
~ll
Aug.
8, 1990
P051
MI
Aug.
8,
1990
P054
MI
Aug.
8,
1990
117—584

265
P056
MI
Mig.
8,
1990
P057
Mi
Aug.
8,
1990
P058
MI
Aug.
8,
1990
P059
All
Aug.
8, 1990
P060
Mi
Aug.
8,
1990
P062
Soil and debris
June 8,
1991
P062
All others
June
8, 1989
P063
~ll
June
8,
1989
P064
Mi
Aug.
8,
1990
P065
High mercury nonwastewater
May
8,
1992
P065
Low mercury nonwastewater
May
8.
1992
P065
All others
Aug.
8,
1990
P066
Aug.
8,
1990
P067
Mi
Aug.
8,
1990
P068
MI
Aug.
8,
1990
P069
Mi
Aug.
8,
1990
P070
Ml
Aug.
8.
1990
P071
Soil and debris
June
8,
1991
P071
All others
June
8,
1989
P072
MI
Aug.
8,
1990
P073
~ll
Aug.
8,
1990
P074
MI
June
8.
1989
P075
MI
Aug.
8,
1990
P076
MI
Aug.
8,
1990
P077
MI
Aug.
8.
1990
P078
~ll
Aug.
8,
1990
117—585

266
(silver)
P099
(cyanides)
Soil and debris
All others
All
All
Soil
and debris
All others
High mercury nonwastewater
Low mercury nonwastewater
All others
Soil and debris
All others
Soil and debris
All others
Soil and debris
All others
All
Soil and debris
All others
All
Wastewater
Wastewater
Nonwastewater
All
Aug.
8,
1990
Aug.
8,
1990
Aug.
8,
1990
June
8,
1991
June 8,
1989
May 8,
1992
Aug.
8,
1990
June
8,
1991
June
8,
1989
May
8,
1992
May
8,
1992
Aug.
8,
1990
May
8,
1992
Aug.
8,
1990
June
8,
1991
June
8,
1989
May
8,
1992
Aug.
8,
1990
Aug.
8,
1990
June
8,
1991
June
8,
1989
June
8,
1989
Aug.
8,
1990
June
8,
1989
June
8,
1989
Aug.
8,
1990
All
All
All
P081
P082
P084
P085
P085
P087
P088
P089
P089
P092
P092
P092
P093
P093
P094
P094
P095
P095
P096
P097
P097
P098
peg g
P099
(cyanides/silver)
P101
117—586

267
P102
Ml
Aug.
8,
1990
P103
MI
Aug.
8,
1990
P104
(silver)
Wastewater
Aug.
8,
1990
P104
(cyanides)
Wastewater
June
8,
1989
P104
Nonwastewater
June
B.
1989
(cyanides/ailver)
P105
MI
Aug.
8,
1990
P106
MI
June
8,
1989
P108
Soil and debris
May
8,
1992
P108
All others
Aug.
8,
1990
P109
Soil and debris
June
8,
1991
P109
All others
June 8,
1989
P110
Mi
Aug.
8,
1990
P111
Soil and debris
June
8,
1991
P111
All others
June
8,
1989
P112
MI
Aug.
8,
1990
P113
MI
Aug.
8,
1990
P114
MI
Aug.
8,
1990
P115
Mi
Aug.
8,
1990
P116
Soil and debris
May 8, 1992
P116
All others
Aug.
8,
1990
P118
Soil
and
debris
May
8.
1992
P118
All others
Aug.
8,
1990
P119
MI
Aug.
8,
1990
P120
MI
Aug.
8,
1990
P121
MI
June
8,
1989
117—587

268
P122
MI
Aug.
8,
1990
P123
MI
Aug.
8,
1990
13001
All
Aug.
8,
1990
0002
Mi
Aug.
8,
1990
0003
Soil and debris
May
8,
1992
0003
All others
Aug.
8,
1990
0004
Mi
Aue.
8,
1990
0005
MI
Aug.
8,
1990
0006
Soil and debris
May
8,
1992
0006
All others
Aug.
8,
1990
13007
Soil and debris
May 8,
1992
13007
All others
Aug.
8, 1990
0008
MI
Aug.
8,
1990
0009
MI
Aug.
8,
1990
0010
Soil and debris
May
8,
1992
0010
All others
Aug.
8,
1990
0011
Soil and debris
May
8,
1992
13011
All others
Aug.
8, 1990
0012
MI
Aug.
8,
1990
0014
Soil and debris
May
8,
1992
0014
All others
Aug.
8,
1990
UO1S
Soil and debris
May
8,
1992
UO1S
All others
Aug.
8,
1990
0016
MI
Aug.
8,
1990
0017
Soil and debris
May 8,
1992
0017
All others
Aug.
8, 1990
117—588

269
13018
MI
Aug.
8,
1990
13019
Mi
Aug.
8,
1990
0020
Soil and
debris
May
8,
1992
UO2O
All others
Aug.
8,
1990
0021
Soil and debris
May
8,
1992
0021
All others
Aug.
B,
1990
0022
Mi
Aug.
8,
1990
0023
MI
Aug.
8,
1990
0024
MI
Aug.
8,
1990
13025
MI
Aug.
8,
1990
13026
Soil and debris
May 8,
1992
0026
All others
Aug.
8, 1990
1.3027
MI
Aug.
8,
1990
0028
Soil and debris
June
8,
1991
0028
All others
June
8,
1989
U029
MI
Aug.
8,
1990
0030
MI
Aug.
8,
1990
0031
Mi
Aug.
8,
1990
0032
Mi
Aug.
8,
1990
0033
Soil and debris
May
8,
1992
13033
All others
Aug.
8,
1990
0034
Soil
and
debris
May
8.
1992
0034
All others
Aug.
8,
1990
0035
Soil and debris
May 8.
1992
0035
All others
Aug.
8,
1990
0036
MI
Aug.
8,
1990
117—589

270
0037
MI
Aug.
8,
1990
0038
Soil and debris
May
8,
1992
0038
All others
Aug.
8,
1990
0039
Mi
Aug.
8,
1990
0041
Soil and debris
May
8,
1992
0041
All others
Aug.
8,
1990
U042
Soil and debris
May 8,
1992
1.3042
All others
Aug.
8, 1990
0043
MI
Aug.
8,
1990
0044
MI
Aug.
8.
1990
0045
MI
Aug.
8,
1990
0046
Soil and debris
May
8,
1992
0046
All others
Aug.
8,
1990
0047
MI
Aug.
8,
1990
0048
MI
Aug.
8,
1990
0049
Soil and debris
May
8,
1992
0049
All others
Aug.
8,
1990
0050
MI
Aug.
8,
1990
0051
Mi
Aug.
8,
1990
0052
MI
Aug.
8,
1990
00S3
Mi
Aug.
8,
1990
0055
MI
Aug.
8,
1990
0056
MI
Aug.
8,
1990
0057
MI
Aug.
8,
1990
0058
Soil and debris
June
8,
1992
0058
All others
June
8,
1989
117—590

271
13059
Soil and debris
May
8,
1992
0059
All others
Aug.
8,
1990
0060
Soil and debris
May 8.
1992
UO6O
All others
Aug.
8,
1990
0061
Soil and debris
May
8,
1992
0061
All others
Aug.
8,
1990
0062
Soil and debris
May
8,
1992
0062
All
others
Aug.
8,
1990
0063
Mi
Aug.
8,
1990
0064
Mi
Aug.
8,
1990
0066
Mi
Aug.
8.
1990
0067
MI
Aug.
8,
1990
13068
MI
Aug.
8,
1990
0069
Soil and debris
June
8,
1991
0069
All others
June
8,
1989
0070
MI
Aug.
8,
1990
0071
Mi
Aug.
8,
1990
0072
MI
Aug.
8,
1990
13073
Soil
and
debris
May
8,
1992
0073
All others
Aug.
8,
1990
0074
Soil and debris
May
8,
1992
13074
All others
Aug.
8,
1990
0075
MI
Mig.
8,
1990
13076
MI
Aug.
8,
1990
0077
MI
Aug.
8,
1990
0078
MI
Aug.
8,
1990
117—591

272
0079
MI
Aug.
8,
1990
0080
MI
Aug.
8.
1990
0081
MI
Aug.
8,
1990
0082
Mi
Aug.
8,
1990
0083
Mi
Aug.
B,
1990
0084
MI
Aug.
8,
1990
0085
MI
Aug.
8,
1990
0086
MI
Aug.
8,
1990
0087
Soil and debris
June 8,
1991
0087
All others
June
8,
1989
0088
Soil and debris
June
8,
1991
0088
All others
June
8,
1989
0089
MI
Aug.
8,
1990
0090
MI
Aue.
8,
1990
0091
Soil and Debris
May
8,
1992
0091
All others
Aug.
8,
1990
13092
Soil and debris
May
8.
1992
13092
All others
Aug.
8,
1990
0093
Soil
and debris
May
8,
1992
0093
All others
Aug.
8,
1990
0094
MI
Aug.
8,
1990
0095
Soil and debris
May
8,
1992
0095
All others
Aug.
8,
1990
0096
MI
Aug.
8,
1990
0097
Soil and debris
May
8,
1992
0097
All others
Aug.
8,
1990
117—592

273
0098
MI
Aug.
8,
1990
0099
Mi
Aug.
8,
1990
UlOl
Mi
Aug.
8,
1990
0102
Soil and debris
June
8,
1991
0102
All others
June
8,
1989
0103
MI
Aug.
8,
1990
0105
MI
Aug.
8,
1990
0106
MI
Aug.
8,
1990
0107
Soil and debris
June
8,
1991
0107
All others
June
8,
1989
0108
Mi
Aug.
8,
1990
0109
MI
Aug.
8,
1990
0110
Soil and debris
May
8,
1992
0110
All others
Aug.
8,
1990
0111
Mi
Aug.
8,
1990
0112
MI
Aug.
8,
1990
0113
MI
Aug.
8,
1990
0114
Soil and debris
May
8, 1992
0114
All others
Aug.
8,
1990
0115
MI
Aug.
8,
1990
0116
Soil
and debris
May
8,
1992
0116
All others
Aug.
8,
1990
0117
MI
Aug.
8,
1990
0118
Mi
Aug.
8,
1990
0119
Soil and debris
May
8,
1992
0119
All others
Aug.
8,
1990
117—593

274
0120
MI
Aug.
8,
1990
0121
Mi
Aug.
8,
1990
0122
MI
Aug.
8,
1990
0123
MI
Aug.
8,
1990
0124
MI
Aug.
8,
1990
0125
MI
Aug.
8,
1990
13126
Mi.
Aug.
8,
1990
0127
MI
Aug.
8,
1990
0128
MI
Aug.
8,
1990
0129
MI
Aug.
8,
1990
0130
Soil and debris
May 8,
1992
0130
All others
Aug.
8,
1990
0131
MI
Aug.
8,
1990
13132
Soil and debris
May
8,
1992
0132
All others
Aug.
8,
1990
0133
MI
Aug.
8,
1990
0134
MI
Aug.
8,
1990
0135
MI
Aug.
8,
1990
0136
Wastewater
Aug.
8,
1990
0136
Nonwastewater
May
8, 1992
0137
MI
Aug.
8,
1990
0138
MI
Aug.
8,
1990
U140
MI
Aug.
8,
1990
0141
MI
Aug.
8,
1990
0142
Mi
Aug.
8,
1990
0143
Soil and debris
May 8, 1992
117—594

275
0143
All others
Aug.
8,
1990
0144
MI
Aug.
8,
1990
0145
MI
Aug.
8,
1990
0146
MI
Aug.
8,
1990
0147
Mi
Aug.
8,
1990
0148
Soil and debris
MaY
8,
1992
13148
All others
Aug.
8,
1990
0149
Soil and debris
May
8,
1992
0149
All others
Aug.
8,
1990
0150
Soil and
debris
May
8,
1992
U150
All others
Aug.
8,
1990
0151
High mercury nonwastewater
May
8.
1992
0151
Low mercury nonwastewater
May
8,
1992
0151
Soil and debris
May
8,
1992
0151
All others
Aug.
8,
1990
13152
MI
Aug.
8,
1990
13153
Soil
and
debris
May
8,
1992
13153
All others
Aug.
8,
1990
0154
MI
Aug.
8,
1990
0155
MI
Aug.
8,
1990
0156
Soil
and
debris
May
8,
1992
0156
All others
Aug.
8,
1990
0157
MI
Aug.
8,
1990
0158
MI
Aug.
8,
1990
0159
Mi
Aue.
8,
1990
0160
MI
Aug.
8,
1990
117—595

276
0161
MI
Aug.
8,
1990
0162
MI
Aug.
8,
1990
0163
Soil and debris
May
8.
1992
0163
All others
Aug.
8,
1990
0164
Soil and debris
May
8,
1992
0164
All others
Aug.
8,
1990
0165
MI
Aug.
8.
1990
0166
MI
Aug.
8,
1990
0167
Soil and debris
May
8,
1992
13167
All others
Aug.
8,
1990
0168
Soil
and debris
May
8,
1992
0168
All others
Aug.
8, 1990
13169
MI
Aug.
8,
1990
13170
MI
Aug.
8,
1990
0171
Soil
and
debris
May
8,
1992
0171
All
others
Aug.
8,
1990
0172
Mi
Aug.
8,
1990
0173
Soil and debris
May 8,
1992
13173
All others
Aug.
8,
1990
13174
MI
Aug.
8,
1990
13176
Soil and debris
May
8,
1992
0176
All others
Aug.
8,
1990
0177
Soil and debris
May
8,
1992
0177
All others
Aug.
8.
1990
13178
Soil and debris
May 8,
1992
0178
All others
Aug.
8, 1990
117—596

277
0179
MI
Aug.
8,
1990
0180
MI
Aug.
8,
1990
0181
MI
Aug.
8,
1990
0182
MI
Aug.
8,
1990
0183
MI
hug.
8,
1990
13184
Soil and debris
May
8,
1992
0184
All others
Aug.
8,
1990
0185
MI
Aug.
8,
1990
13186
MI
Aug.
8,
1990
0187
MI
Aug.
8,
1990
0188
MI
Aug.
8,
1990
13189
MI
Aug.
8,
1990
0190
Soil and debris
June
8,
1991
0190
All others
June 8,
1989
0191
Soil and debris
May
8,
1992
0191
All others
Aug.
8,
1990
13192
MI
Aug.
8,
1990
0193
Soil and debris
May
8,
1992
0193
All others
Aug.
8,
1990
0194
Soil and debris
May
8,
1992
0194
All others
Aug.
8,
1990
0196
MI
Aug.
8,
1990
13197
MI
Aug.
8.
1990
0200
Soil
and
debris
May
8,
1992
0200
All others
Aug.
8,
1990
13201
MI
Aug.
8,
1990
117—597

278
13202
Soil and debris
May
8,
1992
13202
Al.
others
Aug.
8,
1990
0203
MI
Aug.
8,
1990
13204
Mi
Aug.
8,
1990
0205
MI
Aug.
8,
1990
0206
Soil and
debris
May
8,
1992
0206
All others
Aug.
8,
1990
13207
MI
Aug.
8.
1990
0208
MI
Aug.
8,
1990
1.3209
MI
Aug.
8,
1990
0210
MI
Aug.
8,
1990
0211
MI
Aug.
8,
1990
0213
MI
Aug.
8,
1990
0214
MI
Aug.
8,
1990
13215
Mi
Aug.
8.
1990
0216
MI
Aug.
8,
1990
13217
MI
Aug.
8,
1990
0218
Soil and debris
May
8,
1992
0218
All others
Aug.
8,
1990
0219
Soil and debris
May
8,
1992
0219
All others
Aug.
8,
1990
0220
MI
Aug.
8,
1990
0221
Soil
and debris
June
8,
1991
13221
All others
June
8,
1989
1.3222
Soil and debris
May 8, 1992
1.3222
All others
Aug.
8,
1990
117—598

279
0223
Soil and debris
June
8,
1991
0223
All others
June 8,
1989
0225
MI
Aug.
8,
1990
0226
Mi
Aug.
8,
1990
0227
MI
Aug.
8,
1990
0228
MI
Aua.
8,
1990
13234
Soil and
debris
May
8,
1992
0234
All others
Aug.
8,
1990
13235
Soil and debris
June
8,
1991
1323S
All others
June
8,
1989
0236
Soil and debris
May
8,
1992
0236
All others
Aug.
8,
1990
0237
Soil and debris
May
8,
1992
0237
All others
Aug.
8,
1990
0238
Soil
and
debris
May
8,
1992
0238
All
others
Aug.
8,
1990
0239
MI
Aug.
8,
1990
0240
Soil and debris
May
8, 1992
0240
All others
Aug.
8,
1990
0243
MI
Aug.
8,
1990
0244
Soil and debris
May
8.
1992
0244
All others
Aug.
8,
1990
0246
MI
Aug.
8,
1990
0247
MI
Aug.
8,
1990
0248
MI
Aug.
8,
1990
0249
MI
Aug.
8,
1990
117—599

280
a
This table does not include mixed radioactive wastes
(from the First,
Second,
and Third Third rules) which are receiving a national capacity
variance until May
8.
1992 for
all applicable treatment technologies.
b
Standards are being promulgated for 1,1,2—trichloroethane and 2—
nitropropane for wastewaters and nonwastewaters.
c
Standards are being promulgated for benzene and 2—ethoxyethanol for
wastewaters and nonwastewaters.
d
Treatment standards
for nonwastewaters disposed of after June
8,
1989,
were promulgated June
8,
1989.
e
Treatment standards for nonwastewaters disposed of after August
17,
1988, were promulgated May
2,
1989.
BOARD NOTE: This table
is provided for the convenience of the reader.
(Source:
Added at
1S
Ill.
Reg.
,
effective
117—600

D002 b
D003
(cyanides)
DOO3
(sulfides)
0003
(explosives,
reactives)
B007
D009
DOO9
FO11
F039
K009
1(011
1(011
KO13
1(013
All
All
High Mercury Nonwastewater
Low Mercury Nonwastewater
All
Wa
St
ewater
Wastewater
Nonwastewater
Wastewater
Nonwastewater
Wastewater
May
8,
1992
May
8,
1992
May
8,
1992
May
8,
1992
May
8,
1992
May
8,
1992
May
8,
1992
June
8,
1991
May
8,
1992
June
8,
1991
June
8,
1991
May
8,
1992
June 8,
1991
May
8,
1992
Wastes
Effective date
August
8,
1990.
281
Section 728,Appendix H
National Capacity LDR Variances for UIC
Waste Code
Waste Category
FOO1—FOO5
All scent F001—F005 solvent containing
less than
1 percent total FOO1—F005
solvent constituents
California list
Liquid hazardous wastes,
including free
liquids associated with any solid or
sludge, containing free cyanides
at
concentrations greater than or equal to
1,000 mg/i,
or containing certain metals
or compounds of these metals greater than
or equal to the prohibition
bevels
California list
Liquid hazardous waste having a pH less
than or equal to
2
California list
Hazardous wastes containing HOCs
in total
concentrations less than 10,000 mg/l but
greater than or equal to 1,000 mg/l
August
8.
1990
August
8, 1990
August
8,
1990
All
All
All
117—601

282
1(014
MI
May
8,
1992
1(016 (dilute)
MI
June 8,
19fl
1(048
MI
August
8.
1990
1(049
MI
August
8,
1990
1(050
MI
August
8,
1990
K051
MI
August
8,
1990
1(052
MI
August
8,
1990
1(062
MI
August
8,
1990
1(071
Mi
August
8,
1990
1(104
MI
August
8,
1990
a
Wastes that are deep well disposed on—site receive a six—month variance,
with restrictions effective in November 1990.
b
Deepwell iniected 0002
liquids with a pH less than
2 must meet the
California List treatment standards on August
8,
1990.
BOARD NOTE:
This table
is provided for the convenience of the reader.
(Source:
Added
at
15
Ill,
Reg.
,
effective
117—602

283
Section 728.Tab.e
A
Constituent Concentrations in Waste Extract (CCWE)
Concentration
(in mg/L)
roOi
I’OOS
Opent
Colvents
Waste~aters
All other
containing
spent
spent
colvent
solvents
wastes
Acctone
0.05
0.59
n
Dutyl
alcohol
5.0
5.0
Carbon dieulfjde
1.05
4.81
Carbon tetrachloride
0.05
0.06
Chlorobentene
0.15
0.05
Crcsols
(and crcsylic acid)
2.82
0.75
Oyclohexanone
0.125
0.75
1,2 Dichloroben~cne
0.65
0.125
Ethyl acetate
-
0.05
0.75
Ethylbenzenc
0.05
0.053
Ethyl ether
0.05
0.75
Isobutanol
E.g
5.0
Methanol
0.25
0.75
Methylene chloride
0.20
0.06
Methyl ethyl ketonc
0.05
0.75
Methyl
isobutyl ketone
0.05
0.33
NitrobenEenc
0.66
0.125
Pyridinc
1.12
0.33
Tetrachioroethylene
0.070
0.05
Toluene
1.12
0.33
1,1,1 Trichlorocthanc
1.05
0.41
1,1,2 Triehboro 1,2,2 trifluoroethane
1.05
0.96
Trichloroethylene
0.062
0.091
Trichiorofluoromethane
.
0.05
0.96
Xylene
0.05
0.15
P006
nonwastewaters
(see
also Tablc
B)
Cadmium
Concentration
(in mg/L)
0.066-
Chromium (Total)
5.2
1~eud
0.51
Nickel
0.32
Cilver
0.072
Oyunidcs
(Total)
fleserved
117—603

284
Dio~cinContaining Waste3
(Maximum)
UxCDD
All
IlexachlorodibenEo
p
dioxins
1
ppb
IixCDr
All Ilexachlorodibentofurans
1 ppb
PcCDD
All Pentachlorodibento p dioxins
1 ppb
FcCDF
All rentachlorodibenzofurans
1 ppb
TODD
All TetrachlorodibenEp p dioxins
1 ppb
TOOl”
All TetrachlorodibenLofurans
1 ppb
2,4,5
Trichlorophenol
0.05
ppm
2,4,6 Trichlorophcnol
0.05 ppm
2,3,4,6 Tetraehlorophenol
0.10 ppm
Pentachiorophenol
0.01 ppm
1(001 nonwastewatcr3
(see also Table
D)
Concentration
(in mg/L)
0.51
Lead
1(022
nonwastewatcrs
(sec also Table B)
Chromium
(Total)
Concentration
(in mg/L)
5.2
Nickel
0.32
1(046 nonwa3tcwaters
(Nonreactive Cubcatcgory)
Concentration
(in mg/L)
0.18
Lead
1(048,
1(040,
1(050,
1(051
and
1(052 nonwastewaters (see also Table B)
Concentration
(in mg/L)
0.004
Arsenic
Chromium
(Total)
-
1.7
Nickel
0.048
Selenium
0.025
1(061 nonwastcwaters
(Low Zinc Cubcatcgory
less than 15
total
Einc)
Concentration
Cadmium
(in mg/L)
0.14
Chromium
(Total)
5.2
Lead
0.24
Nickel
0.32
117—604

1(061 nonwastewatcrs
(nigh
Zi
effective until 8/8/00
(in mg/L)
285
I
tn
3
I
I.,~aJIu.um
~nrom~um (rotal)
Lead
0.24
Nickel
0.32
1(062 nonwastewaters
Concentration
-(in
mg/L)~
Chromium
(Total)
0.094
Lead
0-.37
1(071 nonwastewatcrs
Concentration
(in mg/L)
Mercury
0.025
1(086
nonwastewaters
(Solvent Washes Cubcatcgory)
see also Table
B
Concentration
-(-in mg/L)
Chromium
(Total)
0.004
Lead
0.37
1(087 nonwastewaters
(see also Table
13)
Concentration
(in nig/L)
Lead
0.51
1(101 and
1(102 nonwastewaters
(Low Arsenic Cubcategory lcss than
1
Total
Arsenie)~ (see also Table
0)
Concentration
(in mg/L)
Cadmium
0.066
Chromium (Total)
5.2
Lead
0.-S-i
Nickel
0.32
D,
F and
K Listed Wastes
Waste See
Regulated
CAS No.
for
Regulated
Hazardous
Concentration
(mg/li
Non—
Code
D004
Also
Table B
Hazardous Constituent
Constituent
7440—38—2
Wastewaters
~
wastewaters
~Q.j
Arsenic
DOO5
Table B
Barium
7440—39—3
100.
117—605

286
D006
Table
B
Cadmium
7440—43—9
NA
DOO7
Table B
Chromium (Total)
7440—47—32
DOO8
Table B
Lead
7439—92—1
0009
(Low Mercury Subcategory——bess than 260 mg/kg Mercury)
Tables
Mercury
7439—97—6
NA
0.20
B
&D
0010
Table B
Selenium
7782—49-2
DOll
Table B
Silver
7440—22—4
FOO1—FOO5
spent solvents
Tables
Acetone
67—64—1
0.25
0.59
B&D
n—Butyl alcohol
71—36—3
5.0
5.0
Carbon disulfide
75—15—0
1.05
4.81
Carbon tetrachloride
56—23—5
0.05
0.96
Chlorobenzene
108—90-7
0.15
0.05
Cresols
(and cresylic
2.82
0.75
acid)
Cyclohexanone
108—94-1
0.125
0.75
1,2—Dichlorobenzene
95—50—1
0.65
0.125
Ethyl acetate
141—78—6
0.05
0.75
Ethylbenzene
100-41—4
0.05
0.053
Ethyl ether
60—29—7
0.05
0.75
Isobutanol
78—83—1
5.0
5.0
Methanol
67—56—1
0.25
0.75
Methylene chloride
75-9-2
0.20
0.9
Methyl ethyl ketone
78—93—3
0.05
0.75
Methyl
isobutyl ketone
108—10-1
0.05
0.33
Nitrobenzene
98—95—3
0.66
0.125
Pyridine
110—86—1
1.12
0.33
Tetrachloroethylene
127—18—4
0.079
0.05
Toluene
108—88—3
1.12
0.33
b,1,1—Trichboroethane
71—55—6
1.05
0.41
1,l,2—Trichloro—b,2,2—
76—13—i
1.05
0.96
tetrafluorethane
Trichloroethylene
79—01—6
0.062
0.091
Trichborofluoromethane
75—69—4
0.05
0.96
Xvlene
0.05
0.15
FOO6
Table B
Cadmium
7440—43—9
NA
0.066
Chromium
(Total)
7440—47—32
Lead
7439—92—1
0.51
Nickel
7440—02—0
NA
0.32
Silver
7440—22—4
NA
0.072
F007
Table B
Cadmium
7440-43—9
NA
0.066
Chromium
(Total)
7440-47—32
117—606

287
F008
Table B
FO11
Table
B
F026—F028 dioxin—contain
HxCDD-All Hexachloro-
dibenzo-p-dioxins
HxCDF—All Hexachloro—
dibenzofurans
PeCDD-All Pentachloro-
dibenzo-p-dioxins
PeCDF-All Pentachloro-
dibenzofurans
TCDD-All Tetrachloro-
dibenzo-p-djoxins
TCDF—All Tetrachloro-
dibenzofurans
2
,
4
,
5—Trichlorophenol
2,4,6—Trichlorophenol
2 ,3,4,6—Tetrachlorophenoi
Pentachlorophenol
7440—47—32
7439—92—1
7440—02—0
NA
NA
NA
0.073
0.021
0.088
FOO9
Table B
Lead
Nickel
Silver
Cadmium
Chromium
(Total)
Lead
Nickel
Silver
Cadmium
Chromium (Total)
Lead
Nickel
Silver
Cadmium
Chromium
(Total)
Lead
Nickel
Silver
7439—92—i
7440—02—0
7440—22—4
7440—43—9
7440—47—32
7439—92—1
7440—02—0
7440—22—4
7440—43—9
7440—47—32
7439—92—1
7440—02—0
7440—22—4
7440—43—9
7440—47—32
7439—92—b
7440—02—0
7440—22—4
7440—43—9
7440—47—32
7439—92—b
7440—02—0
7440—22—4
7440—47—32
ins wastes
*
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
0.51
0.32
0.072
0.066
5.2
0.51
0.32
0.072
0.066
5.2
0.51
0.32
0.072
0.066
5.2
0.51
0.32
0.072
0.066
5.2
0.51
0.32
0.072
0.072
F012
Table B
F019
Table
B
F020—F023 and
Cadmium
Chromium (Total)
Lead
Nickel
Silver
Chromium
(Total)
1.
ppb
1.
ppb
1.
ppb
1.
ppb
1.
ppb
1.
ppb
1.
ppb
1.
ppb
1.
ppb
1.
ppb
95—95—4
0.05
ppm
0.05
ppm
88-06—2
0.05
ppm
0.05
ppm
58-90-2
0.05
ppm
0.05
ppm
87-86—5
0.05
ppm
0.05
ppm
F024
Table B
Chromium
(Total)
Lead
Nickel
117—607

288
1(005
Table B
Chror’4”
Lead
1(006 (anhydrous)
1(006
(hydrated)
Table B
Chromium (Total)
1(007
Table
B
Chromium
Lead
1(008
Table B
Chromium
Lead
1(015
Table B
Chromium
(Total)
Lead
1(021
Table B
Antimony
1(022
Table B
Chromium (Total)
Nickel
1(028
Table B
Chromium
(Total)
Lead
Nickel
1(031
Table B
Arsenic
(Total)
7440—47—32
7439—92—1
NA
Antimony
Arsenic
Barium
Cadmium
(~hrr~m~
urn
F039
Table B
1(001
Table B
KOO2
Table B
1(003
Table B
1(004
Table
B
(Total)
Lead
Mercury
Nickel
Selenium
Silver
Lead
Chromium (Total)
Lead
Chromium
(Total)
Lead
Chromium
(Total)
Lead
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
7440—36—0
7440—38—2
7440—39—3
7440—43—9
7440—47—32
7439—92—1
7439—97—6
7440-02—0
7782—49—2
7440—22—4
7439—92—1
7440—47—32
7439—92—b
7440—47—32
7439—92—1
7440—47—32
7439—92—1
7440—47—32
7439—92—1
7440—47—32
7439—92—1
7440—47—32
7440—47—32
7439—92—1
(Total)
Table B
Chromium
Lead
(Totals
0.23
5.0
52.
0.066
5.2
0.51
0.025
0.32
5.7
0.072
0.51
0.094
0.37
0.094
0.37
0.094
0.37
0.094
0.37
0.094
0.37
5.2
0.094
0.37
0.094
0.37
1.7
0.2
0.23 #
5.2
0.32
0.073
0.021
0.088
5.6 1
(Total)
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
7440—47—32
7439—92—1
7440—36—0
7440—47—32
7440—02—2
7440—47—32
7439—92—1
7440—02—2
7440—38—2
117—608

289
1(046
K048
Table B
Lead
Table B
Chromium (Total)
7439—92—1
7440-47-32
NA
7440—02—2
NA
0.18
Li
0.20
Nickel
1(049
Table B
Chromium (Total)
7440-47—32
7440-02—2
Nh
Li
0.20
Nickel
1(050
Table B
Chromium
(Total)
7440-47—32
7440—02—2
NA
Li
0.20
Nickel
1(051
Table
B
Chromium (Total)
7440-47—32
7440—02—2
NA
Li
0.20
Nickel
1(052
Table B
Chromium
(Total)
7440-47-32
7440-02—2
NA
Li
0.20
Nickel
1(061
(Low Zinc Subcategory——bess than 15
Total Zinc)
7440-43—9
NA
7440-47—32
NA
7439—92—1
NA
7440—02—2
NA
0.14
~
0.24
0.32
Table B
Cadmium
Chromium (Total)
Lead
Nickel
1(062
Table
B
Chromium
(Total)
7440—47—32
NA
7439—92—b
NA
0.094
0.37
Lead
1(069
(Calcium Sulfate Subcategory)
7440—43—9
NA
7439—92—1
NA
0.14
0.24
Tables
Cadmium
B
&
B
Lead
1(071
(Low Mercury Subcategory-—lesa than 16 mg/kg Mercury)
7439—97—6
NA
0.025
Table
B
Mercury
1(083
Table B
Nickel
7440—02—2
MA
0.088
1(084
Table B
Arsenic
7440—38-2
NA
5.6
#
1(086
Table
B
Chromium (Total)
7440—47—32
NA
7439—92—1
NA
0.094
0.37
Lead
1(087
Table
B
Lead
7439—92—1
NA
0.51
K100
Table B
Cadmium
Chromium (Total)
7440—43—9
MA
7440-47—32
7439—92—b
NA
0.066
~
0.51
Lead
1(101
Table B
Arsenic
7440-38—2
NA
5.6
1
1(102
Table
B
Arsenic
7440—38—2
NA
5.6 1
117—609

290
1(106
(Low Mercury Subcategory-—less
than 260 mg/kg Mercury——residues from
RMERC)
Tables
Mercury
7439—97—6
NA
0.20
B &D
1(106
(Low Mercury Subcategory—-less than 260 mg/kg Mercury——that are not
residues from RMERC)
Tables
Mercury
7439—97-6
NA
A
0.20
B&D
KllS
Table B
Nickel
7440—02—2
NA
0.32
1——These treatment standards have been based on EP Leachate analysis but
this
does not preclude the use of TCLP analysis.
*__These waste codes are not subcategorized into wastewaters and
nonwastewaters.
NA--Not Applicable.
Commercial
Regulated
_________
____________________
Waste See
Chemical
Hazardous
_________
________
Code
Also
Name
Constituent
___________
___________
___________
POlO
Table
B Arsenic acid Arsenic
_________
POll
Table
B
Arsenic
Arsenic
__________
pentox ide
P012
Table B
Arsenic tn—
_______
_________
oxide
P013
Table
B
Barium
______
_________
cyanide
P036
Table B
Dichloro—
_______
_________
phenylarsine
P038
Table
B Diethyl
-_______
_________
arsine
P065
(Low Mercury Subcategory-—less
RMERC)
Tables
Mercury ful— Mercury
__________
____
B & D
minate
P and U Listed Wastes
CAS No.
for
_________
Regulated
Concentration
(mg/I)
__________
Hazardous
Non—
____________
Constituent Wastewaters
wastewaters
_______
7440—38—2
_______
7440—38—2
Arsenic
7440—38—2
Barium
7440—39—3
Arsenic
7440—38—2
Arsenic
7440-38—2
than 260 mg/kg Mercury—-residues from
_______
7439—97—6
0.20
117—610

‘O-,--,
Mercury——incinerator
Tables
B
&
B
Mercury ful— Mercury
7439—97—6
NA
0.025
minate
Nickel
Nickel
P073
Table B
Nickel
______
7440—02—2
carbonyl
P074
Table
B
Nickel
______
7440—02—2
cyanide
P092
(Low
Merr~ury Sub-~-i~r~ory
—-
leac
t-h~n
260 mg/kr~
M~r~ii~~
RMERC)
Tables
Phenyl
Mercury
7439-97—6
B & B
mercury
acetate
P092
(Low Mercury Subcategory--less than 260 mg/kg Mercury-—i....~....
residues
(and are not residues
from RMERC’i)
Tables
Phenyl
Mercury
7439—97—6
B & B
mercury
acetate
P099
Table
B
Potassium
Silver
7440—22—4
silver
cyanide
P103
Table
B
Selenounea
Selenium
7782—49—2
P104
Table B
Silver
Silver
7440—22—4
cyanide
P110
Table B
Tetraethyl
Lead
7439—92—1
lead
P114
Table B
Thallium
Selenium
7782-49—2
selenite
U032
Table B
Calcium
Chromium
7440—47—32
chromate
(Total)
1J051
Table B
Creosote
Lead
7439—92—1
U136
Table
B
Cacodylic
Arsenic
7440—38—2
acid
U144
Table B
Lead acetate Lead
7439—92-1
U145
Table B
Lead phos—
Lead
7439-92—1
ii~
phate
!!~
0.32
0.32
residues
291
P065
(Low Mercury Subcategory--less than 260
mg/kg
r~dn~a
f~inri
ar~
nr~t-
r~~c4r1ii,~
from
~
from
0.20
nn~
0.025
0.072
5.7
0.072
0.51
5.7
0.094
0.51
5.6
0.51
0.5.
117—611

292
U146
Table
B
Lead sub-
Lead
7439-92—1
NA
0.51
acetate
U151
(Low Mercury Subcategory——less than 260 mg/kg Mercury——residues from
RMERC)
Tables
Mercury
Mercury
7439-97-6
0.20
B&D
Ub51
(Low Mercury Subcategory——less than 260 mg/kg Mercury——that are not
residues from RMERC)
Tables
Mercury
Mercury
7439—97-6
0.025
B&D
U2O4
Table B
Selenium
Selenium
7782—49-2
dioxide
v205
Table B
Selenium
Selenium
7782—49—2
sulfide
——These treatment standards have been based on EP Leachate analysis but this
does not preclude the use of TCLP analysis.
*__These waste codes are not subcategorized
into wastewaters and
nonwastewaters.
MA--Not Applicable.
(Source:
Amended at
15
Ill.
Reg.
,
effective
117—612

293
Section 728.Table B
Constituent Concentrations
in Waste
(CCW)
FOOl,
P002,
P003,
P004 and P005 wastewatera
(Pharmaceutical
Industry)
Concentrat
(in
mg/L)
P006 nonwastewaters
(see also Table A)
Concentration
(in
mg/kg)
eyanidcs
(Total)
fleserved
KOOl nonwastewaters
(Bee also Table A)
Naphthalenc
Concentration
(in mg/kg)
8.0
Pentachlorophenol
37.
Thcnanthrone
8.0
Pyrene
7.3
Toluene
0.14
Xybcneo
0.16
1(001 wastewaters
Concentration
(in mg/L)
Nephthalenc
0.15
Pentachlorophenol
0.88
Phenanthrene
0.15
Pyrene
0.14
Toluene
0.14
xylenes
0.16
Lead
0.037
1(015 wa~tewaters
Concentration
(in mg/L)
Anthracene
1.0
Benzal
chloride
0.20
Benio
(b or
k)
fluoranthene
0.29
Phenanthrene
0.27
Pe-luene
0.15
Chromium
(Total)
0.32
Niekel
0.44
117—613

(in mg/kg)
I1exachloroberu~ene
28.
Uexachlorobutpdjene
Uexachloroeyclopentadiene
Uexachloroethane
5. 6
5.6
28.
Tetrachioroethene
6.0
1(016 wastewatcrs
Concentration
(in mg/L)
Hexaehlorok~enzene
0.033
Uexachlorobutadiene
0.007
Uexechlorocyclopentadiene
0.007
Ilexachloroethpnp
0.033
Tetrachboroethene
0.007
1(018 nonwastcwaters
Concentration
(in mg/kg)
..
Ohloroethane
1,1 Dichloroethane
1,2 Dichboroethanc
6.0
6.0
6.0
Uexachlorobentene
Hexachlorobutpdlena
flexachioroethane
28~
28.
rentaehloroethane
1,1,1 Trichloroethane
5.6
6.0
1(018 wastewaters
Chlorccthane
.
Concentration
(in mg/L)
0.007
Chloromethane
0.007
1,1 Dichloroethane
0.007
1,2 Dichloroethane
0.007
flexachlorobcn~ene
0.033
Ilexachborobutadlane
0.007
Pentaehloroethanc
0.007
1,1,1 Trichloroethanc
0.007
117—614
294

295
1._ni
I
t~
(in mg/kg)
Bis(2 chlorocthyl)ether
Chiorobenrene
5.6
6.0
Chloroform
6.0
1,2 Dichloroethane
6.0
~exachloroethane
28.
ffaphthalenc
5.6
Phenanthrene
5.6
Tetrachioroethene
6
0
1,2,4 Trichlorobentene
19.
1,1,1 Trichloroethane
6.0
1(010 wastewatera
Bis(2 chloroethyl)ether
Concentration
(in mg/L)
0.007
Ch1oroben~ene
0.006
Chloroform
0.007
p
Dichlorobenrene
0.008
1,2 Dichboroethane
0.007
Pluorene
0.007
Hexachlorocthanc
0.033
Naphthalene
0.007
Phenanthrene
-
0.007
1,2,4,5 Tetrachlorobenzcne
0.017
Tetrachloroethene
0.007
1,2,4 Trichlorobcnzene
0.023
1,1,1 Trichioroethane
0.007
1(020 nonwastewaters
Concentrati-en
-(in
mg/kg)
1,2 Dichloroethano
1,1,2,2 Tetrachloroethane
6.0
5.6
Tetrachloroethene
6.0
1(020 waptcwaters
1,2 Diohioroethanc
Conccntration
(in mg/L)
0.00?
1,1,2,2 Totrachloroethane
0.007
Tetrachlorocthene
0.007
117—615

296
(in mg/kg)
Acetophenonc
10.
Sum of Diphenylamine and Diphenylnitrosamine
13.
Phenol
12.
Toluene
0.034
1(024 nonwastewatcrs
Concentration
(in mg/kg)
28.
Ththalic acid
1(024 wastcwaters
Phthalic acid
Concentration
(in mg/L)
0.54
1(030 nonwastewaters
Hexachlorobutpdiene
Concentration
(in mg/kg)
5. 6
Ilcxaehloroethane
28.
Hexachloropropene
19.
Pentachlorobentcnc
28.
Pentachioroethane
5.6
1,2,4,5 Tetrachlorobenrene
14.
Tctrachlorpethene
6.0
1,2,4 Trichlorobenzene
19.
1(030 wastewate-re
Concentration
(in
mg/L)
o
Dichlorobenzenc
0.008
p Dichiorobenrenc
0.008
flexachlorobutadienc
.
0.007
Hexaehloroethano
0.033
Pentachloroethane
0.007
1,2,4,5 Tetrachloroben~ene
0.017
Tetrachloroethenc
1,2,4 Trichborobenzene
0.023
1(037 nonwastewaters
Disulfoton
Concentration
(in mg/kg)
0.1
Toluenc
28.
117—616

(in
mg/L)
Disulfoton
0.003
Toluenc
0.028
1(048 nonwastcwaters
(see also Table
A)
Concentration
(in mg/kg)
Ben~cne
9.5
Bento(a)pyrene
0.84
Bis(2 ethylhcxyl)phthalate
37.
Chrysenc
2.2
Di n butyl phthalate
4.2
Bthylbenzene
67.
Naphthalcne
flcscrved
Phenanthrenc
7.7
Phenol
2.7
Pyrcne
2.0
Toluene
9.5
Xylcnes
fleserved
Cyanides
(Total)
1.8
1(048 wastewatera
Bensenc
Concentration
(in mg/L)
0.011
Benzo(a)pyrene
0.047
Dis(2 ethylhexyl)phthalate
0.043
Chrysenc
0.043
Di
n butyl phthalato
0.060
Ethy1ben~ene
0.011
Fluorcne
0.050
Naphthalene
0.033
Phenanthreno
0.039
Phenol
0~O47
Pyrenc
0.045
Toluenc
0.011
Xylenes
0.011
Chfomium
(Total)
0.20
La-ad
0.37
117—617
297

(see also Table
A)
Anthracene
DenLene
6.2
9.5
Bento(a)pyrenc
0.84
Dia(2 ethylhexyl)phthalate
37.
Chrysene
2.2
Dthylbeneene
67.
Naphthalene
(fleserved)
Phenanthrenc
7.7
Phenol
2.7
Pyrone
‘.‘°
Toluene
9.5
Xylencs
fleaerved
Cyanides
(Total)
1.8
1(040 wastewaters
Anthracenc
Concentration
(in mg/L)
0.039
Bentone
0.011
Ben~o(a)pyrene
0.047
Dio(2 ethylhexyl)phthalate
0.043
Carbon di9ulfide
0.011
Chrysene
0.043
2,4 Dimethylphenol
0.033
EthylbenEenc
0.011
Naphthalcne
0.033
Phcnanthrene
0.039
Phenol
0.047
Pyreno
0.045
Toluene
0.011
Xylenes
0.011
Chromium
(Total)
0.20
Lead
0.037
1(050 nonwastewaters
(Sec
also
Table
A)
Benzo(a)pyrene
Concentration
(in
mg/kg)
0.84
Phenol
2.7
Cyanides
(Total)
1.8
117—618
IF
fl
A
(i
298
(in mg/kg)

(in mg/L)
Bento(a)pyrcne
0.047
Phenol
0.047
Chromium (Total)
0.20
Lead
0.037
1(051 nonwa3tewatcrs
(Sec also Table A)
Concentration
(in
mg/kg)
Anthracene
6.2
Den~enc
9.5
DenLo(eanthracene
1.4
Dento(a)pyrene
0.84
Dis(2 ethylhexyl)phthalate
37.
Chrysene
Q~4
Di n butyl phthalatc
4.2
BthylbenEene
67.
Naphthalene
fleserved
Phenanthrene
7.7
Phenol
-
2.7
Pyrene
2.0
Toluene
9.5
Xylenes
Reserved
Cyanides
(Total)
1.8
1(051 wastcwaters
Acenaphthenc
Concentration
(in
rng/L)
0.050
Anthracenc
0.039
Bentene
0.011
Bento(a)anthracenc
0.043
Dento(a)pyrene
0.047
Bi~(2ethylhexyl) phthalate
0.043
Chrysene
0.043
Di n butyl phthalate
0.060
flthyiben~ene
0.011
Fluorcne
0.050
Naphthalene
0.033
Phenanthrenc
0.039
Phenol
0.047
Pyrene
0.045
Toluene
0.011
Xylenes
0.011
Chromium (Total)
0.20
Lead
0.037
117—619
299

300
-(-see also Table
A)
Ben~ene
9.5
Dento(a)pyrene
0.84
o Oresol
2.2
p Creed
0.90
lJthylbenzeno
67.
Naphthalene
Reserved
Phenanthrene
7.7
Phenol
2.7
Toluene
.
9.5
Kylenos
Reserved
Cyanides
(Total)
1.8
1(052 wastcwaters
Concentration
(in mg/L)
0.011
Denzene
Bento(a)pyrene
0.047
o Orecol
0.011
p Cresol
0.011
2,4 Dimethy~phenol
0.033
Ethylbenecne
0.011
Nephthalene
0.033
Phenanthrcnc
0.039
Phenol
0.047
Toluene
0.011
Xylenes
0.011
Chromium (Total)
0.20
Lead
0.037
1(062 waptewaters
Chromium (Total)
-
Concentration
(in mg/L)
0.32
Lead
0.04
Nickel
0.44
1(071 wastcwaters
Mercury
Concentration
(in mg/L)
0.030
117—620
IF
(in mg/kg)

(in mg/kg)
bis(2
ethylhcxyl)
phthalatc
0.49
n
Dutyl
alcohol
0.37
Cycbohexanone
0.49
1,2
DichiorobenEene
0.49
Ethyl acetate
0.37
Ethyl beneene
0.031
Methanol
0.37
Methylene chloride
0.037
Methyl ethyl ketone
0.37
Methyl isobutyl ketone
0.37
Naphthalene
0.49
Nitroben,ene
0.49
Toluene
0.031
1,1,1, Trichlorocthane
0.044
Trichioroethylene
0.031
Xylenes
0.015
1(086 wastewaters Solvent Washes
Cuboategory
Concentration
(in mg/L)
Acetone
0.015
bis(2 ethylhexyl)phthalate
0.044
n Dutyl alcohol
0.031
Cyclohexanonc
0.022
1,2 Dichboroben~ene
0.044
Ethyl acetatc
0.031
Ethyl bentene
0.015
Methanol
0.031
Methylene chloride
0.031
Methyl ethyl ketone
0.031
Methyl
isobutyl ketone
0.031
Naphthalene
0.044
Nitrobcn~cne
0.044
Toluenc
0.029
1,1,1, Trichborc~cthane
0.031
Triehioroethyleno
0.029
tylenes
0.015
Chromium
(Total)
0.32
Lead
0.037
117—621
301

(see
also Table A)
302
(in mg/kg)
Chrysene
34
Fluoranthenc
3.4
Indeno(1,2,3 cd)pyrene
3.4
Naphthalene
t’henenthrene
3.4
Tolucne
0.65
Xylenes
0.070
1(087 wastewaters
Acenaphthalene
Concentration
(in mg/L)
0.020
Bentenc
0.014
Chrysene
0.028
Fluoranthene
0.028
Indeno (1,2,3
od)
pyrene
0.028
Naphthalene
0.028
t’henanthrene
0.028
Toluene
0.008
Xylenes
0.014
Load
0.037
1(090 nonwastewaters
2,4 Dichlorophenoxyacetic acid
Concentration
(in mg/kg)
1.0
flexachlorodiben~op dioxins
0.001
I1exachlorodiben~ofurans
0.001
Pentachlorodibenzo p dioxins
0.001
Pentachlorodibenzofurans
0.001
Tetrachlorodibenro p dioxins
0.001
Tetrachlorodiben~ofurpns
0.001
1(099 wastewatcrs
Concentration
(in mg/L)
1.0
2,4 Dichlorophenoxyacetic acid
Uexachlorodiben~op dioxins
0.001
Uexach1orodiben~ofurans
0.001
Pentachlorodiben~op dioxins
0.001
Pentachlorodibentofurans
0.001
TetrachiorodibenEp
p dioxins
0.001
Tetrach1orodibon~ofurans
0.001
117—622
Acenachthai.~zit~

303
1(101 nonwastewaters
(Low Arsenic Cubeategory
less than 1
total
arsenic)
(see
aloe
Table
A)
Concentration
(in mg/kg)
ortho Nitroaniline
14.
1(101 waeteweter-a
ortho Nitroanilinc
Concentration
(in mg/L)
0.27
?rsenic
2.0
emium
0.24
bead
0.11
Mercury
0.027
1(102 nonwactewaters
(Low Arsenic Cubcategory less than
1
total arsenic)
(see also Table A)
ortho Uitrophenol
Concentration
(in mg/kg)
13.
1(102 wastewaters
ortho Nitrophenol
Concentration
(in mg/L)
0.028
Arsenic
2.0
Cadmium
0.24
Lead
0.11
!icrcury
0.027
1(103 nonwastewaters
Aniline
Concentration
(in mg/kg)
5.6
Dentene
6.0
2,4 Dinitrophenol
5.6
Nitrobcntcne
5.6
Phenol
-5.-6
1(103 wastewaters
Aniline
Concentration
(in mg/L)
4.5
DonEene
0.15
2,4 Dinitrophenol
0.61
Nitrobentene
0
073
Pheno-l
1.4
117—623

304
Concentrat
(in
mg/kg)
Aniline
5.6
Denzcne
6.0
2,4 Dinitrophenol
5.6
Nitrobentene
5.6
Phenol
5.6
Cyanides
(Total)
1.8
1(104 wastewaters
Concentration
(in
mg/L)
Aniline
4.5
Dcnrene
0.15
2,4 Dinitrophenol
0.61
Nitrobentene
0.073
Phenol
1.4
Cyanides
(Total)
2.7
No Land Disposal
for;
1(004 Nonwastewaters
(Based on
No
Generation)
1(008 Nonwastewaters
(Based on No Generation)
1(015 Nonwastewaters
(Based on No Ash)
1(021 Nonwastewaters
(Based on No Generation)
1(025 Nonwastewaters
(Based on
No
Generation)
1(036 Nonwastewaters
(Based on
No
Generation)
1(044
(Based on flcactivity)
1(045
(Based on Reactivity)
1(047
(Based on Reactivity)
1(060 Nonwastewaters
(Based on No Generation)
1(061 !lonwastewatcrs nigh Zinc &ubcategory
(Based on Recycling):
(greater than or equal to 15
total
tine)
effective 8/8/90
1(060 Nonwastewaters Non Calcium Sulfate
(Dased on Recycling)
Cubcategory
1(083 Nonwastewatcrs
No
Ash Cubcatcgory
(Based on
No
Ash)
(less than 0.01
total ash)
1(100 Nonwa3tewaters
(Baz~edon
No
Generation)
B,
F and K Listed Wastes
CAS No.
for
Regulated
Concentration (me/U
Waste See
Regulated
Hazardous
Non—
Code
Also
Hazardous Constituent
Constituent Wastewaters
wastewaters
D003
(Reactive cyanides subcategory—-based on Cyanides
(Arnenable~ 35
Ill. Adm.
Code 721.l23(a)(5))
Cyanides
(Total)
57—12-5
Res.
1
590.
117—624

305
Cyanides
(Total)
Cyanides
(Amenable)
Cadmium
Chromium
Lead
Nickel
Cyanides
(Total)
Cyanides
(Amenable)
Chromium (Total)
Lead
Nickel
Cyanides
(Total)
Cyanides
(Amenable)
Chromium
71—55—6
0.030
a 7.6
71—43—2
0.070
a
3.7
industry wastewater subcate~orv)
75—09—2
0.44
NA
57—12—5
L.2
_____
57—12—5
0.86
7440—43—9
7440—47—32
0.32
7439—92—1
0.040
7440—02—2
0.44
57—12—5
_____
57—12—5
7440—47—32
0.32
7439—92—1
0.04
7440—02—2
0.44
57—12—5
_____
57—12—5
0.13
7440—47—32
0.32
7440—38—2
7440—39—3
7440—43—9
7440—47—32
7439—92—1
7439—97—6
7782—49—2
7440—22—4
720—20—8
58—89—9
72—43—5
8001—35—1
94—75—7
93—76—5
D004
Table A
Arsenic
D005
Table A
Barium
D006
Table A
Cadmium
D007
Table A Chromium
(Total)
D008
Table
A
Lead
D009
Table
A
Mercury
DOlO
Table A
Selenium
DOll
Table A
Silver
D012
Table D
Endrin
D013
Table D
Lindane
D014
Table B
Methoxychlor
D0l5
Table B
Toxaphene
D016
Table B
2,4-D
B017
Table B
2,4,5—TP Silvex
FOOl—F005 spent solvents
Tables
1,1,2—Trichloroethane
A&D
Benzene
F001—F005 spent solvents
(Pharmaceutical
Methylene chloride
5.0
100.
5.0
0.20
1.0
5.0
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
0.13
0.066
0.18
1.3
10.0
7.9
F006
Table A
F007
Table A
F008
Table A
590.
30.
NA
NA
NA
NA
590.
30.
NA
NA
NA
590.
30.
NA
117—625

306
57—12—5
57—12—5
7440—47—32
67—63—3
107—06—2
75—35—4
75—9—2
56—23—5
79—00—5
79—01—6
75—01—4
1.2
0.86
0.32
~_
0.046
5
0.21
~_
0.025
~
0.089
L.
0.057
~_
0.054
~_
0.054
5
0.27
(R~90.
(R)30.
NA
a
6.2
a
6.2
a
6.2
a
31.
a
6.2
a
6.2
9
5.6
a
33.
Lead
Nickel
FOO9
Table
A
Cyanides
ev~nid~q
(Total)
(Arn~n~b1~~
Chromium
Lead
Nickel
Cyanides
(Total)
Cyanides
(Amenable)
Cyanides
(Total)
Cv~niri~q
1Am~n~b~~
7439—92—1
7440-02—2
57—12—5
57—12—5
7440—47—32
7439—92—1
7440—02—2
57—12—5
57—12—5
57—12—5
57—12—5
7440—47—32
7439—92—1
7440—02—2
57—12—5
57—12—5
7440—47—32
7439—92—1
7440—02—2
(Total)
0.04
0.44
1.95
0.1
0.32
0.04
0.44
1.9
0.1
1.9
0.1
0.32
0.04
0.44
1.9
0.1
0.32
0.04
0.44
NA
NA
90.
NA
NA
NA
110.
NA
NA
NA
110.
9.1
NA
NA
NA
FOlD
__________________
FOil
Table A
________________
Chromium
Lead
Nickel
F012
Table A
Cyanides
(Total)
Cyanides
(Amenablel
Chromium
(Total)
Lead
Nickel
F019
Table A
Cyanides
(Total)
Cyanides
(Amenable)
Chromium
(Total)
F024
(Note:
Tables
______________________
A&D
Hexachloroethane
Chromium
(Total)
Nickel
F025
(Light ends subcategory)
Chloroform
1, 2—Bichloroethane
1, 1—Dichloroethylene
Methylene chloride
Carbon tetrachloride
F024 organic standards must be treated via incineration (INCIN))
2—Chloro—l,3—butadiene
126—99—8
a
0.28
~
0.28
3—Ch 1oropropene
1~1—Dichloroethane
1
,
2—Dichloroethane
1, 2-Dichloropropane
cts-1
,
3-Dichloropropene
trans—i,3—Bichloropropene
Bi~(2—~thv1h~xv~1
~nhthaiat-~
107—05—1
75—34—3
107—06—2
78—87—5
10061—01—5
10061—02—6
117—81—7
67—72—1
7440—47—32
7440—02—2
a
a
a
a
a
a
a
a
a
a
a
a
a
a
a
a
0.28
0.014
0.014
0.014
0.014
0.014
0.036
0.036
0.35
0.47
0.28
0.014
0.014
0.014
0.014
0.014
1.8
1.8
NA
NA
1
,
1, 2—Trichloroethane
Trichloroethylene
Vinyl chloride
117—626

307
F025
(Spent filters/aids and desiccants subcategory)
Chloroform
67—66—3
s
0.046
~
Methylene chloride
75—9—2
a
0.089
~
Carbon tetrachloride
56—23—5
a
0.057
~
1,1,2—Trichloroethane
79—00—5
~
0.054
~
Trichloroethylene
79-01—6
S
0.054
~
5.6
Vinyl chloride
75—01—4
5
0.27
Hexachlorobenzene
118—74—1
~
0.055
a37.
Hexachlorobutadiene
87—68—3
~
0.055
~
Hexachloroethane
67—72—1
a
0.055
a30.
F039
Table A
Acetone
67—64—1
9
0.28
a 160.
Acenaphthalene
208—96—8
S
0.059
~
Acenaphthene
83—32—9
S
0.059
~
j~Q
Acetonitrile
75—05—8
a
0.17
NA
Acetophenone
96—86-2
~
0.010
~
2—Acetylaminofluorene
53-96—3
S
0.059
a 140.
Acrylonitrile
107—13-1
a
0.24
~.
Aldrin
309—00—2
a
0.021
~
0.068
4—Aminobiphenyl
92—67—1
~
0.13
NA
Aniline
62—53—3
a
0.81
a14.
Anthracene
120—12—7
a
0.059
~.
Aroclor 1016
12674—11—2
a
0.013
~
0.92
Aroclor 1221
11104—28—2
~
0.014
~
0.92
Aroclor 1232
11141—16—5
a
0.013
~
0.92
Aroclor 1242
53469—21—9
a
0.017
a
0.92
Aroclor 1248
12672—29—6
a
0.013
~
0.92
Aroclor 1254
11097—69—1
a
0.014
~.
Aroclor 1260
11096—82—5
~
0.014
~
Li
alpha—BHC
319—84—6
a
0.00014
a
0.066
beta—BHC
319—85—7
a
0.00014
~
0.066
delta—BHC
319—86—8
a
0.023
~
0.066
gamma—BHC
58—89—9
a
0.0017
~
0.066
Benzene
71—43-2
a
0.14
Benzo~a)anthracene
56—55—3
S
0.059
~
Benzo(b)fluoranthene
205—99—2
S
0.055
~
Benzo(k)fluoranthene
207—08—9
a
0.059
~
Benzo(g,h,i)perylene
191—24—2
~
0.0055
~
Berizo(a)pyrene
50—32—8
~
0.061
~
Bromodichloromethane
75—27—4
a
0.35
Bromoform
75—25—2
a
0.63
Bromomethane (methyl
74—63-9
~
0.11
bromide)
4—Bromophenyl phenyl ether 101—55—3
~
0.055
~
n—Butyl alcohol
71—36—3
~.
~
Butyl benzyl phthalate
85—68—7
~
0.017
~
2-sec—Butyl—4,6—dinitro—
88—85-7
~
0.066
~
phenol
Carbon tetrachloride
56—23—5
a
0.057
~
Carbon disulfide
75—15-0
~
0.014
Chlordane
57—74—9
a
0.0033
a
0.13
p-Chloroaniline
106—47—8
s
0.46
117—627

308
Chlorobenzene
108—90—7
a
0.057
~
Chlorobenzilate
510—15—6
a
0.10
Chlorodibromomethane
124-48-1
a
0.057
~
Chloroethane
75—00—3
a
0.27
~
bis(2-Chloroethoxy)methane 111—91-1
~
0.036
~.
Li.
bis(2-Chloroethyl)
ether
111—44—4
~
0.033
~
Li
2—Chloroethvl vinyl ether
a
0.057
Chloroform
67—66—3
~
0.046
~
bis(2—Chloroisopropyl)
39638—32—9
a
0.055
~
Li.
ether
p-Chloro-m-cresol
59—50—7
a
0.018
a
~
Chloromethane
(Methyl
74-87—3
S
0.19
chloride)
2-Chloronaphthalene
91—8-7
~
0.055
~
2-Chlorophenol
95-57—8
~
0.044
~
3—Chloropropene
107—05—1
a
0.036
a28.
Chrysene
218—01—9
a
0.059
~.
~2
o—Cresol
95—48—7
a
0.11
a
j~
Cresol
(m— and p—isomers)
a
0.77
~
Cyclohexanone
108—94—i
a
0.36
1,2—Bibromo—3—chloro—
96—12—8
a
0.11
propane
1,2—Dibromoethane
106—93—4
a
0.028
~
(Ethylene dibromide)
Dibromomethane
74-95-3
8
0.11
2,4-Dichlorophenoxyacetic
94—75—7
a
0.72
acid
(2,4—D)
o,p’—DDD
53—19-0
a
0.023
~
0.087
p,p’—DDD
72—54—8
a
0.023
~
0.087
o,p’—DDE
3424—82—6
a
0.031
~
0.087
p,p’—DDE
72—55—9
a
0.031
~
0.087
o,p’—DDT
789—02—6
a
0.0039
~
0.087
p,p’—DBT
50—29—3
a
0.0039
a
0.087
Dibenzo(a,h)anthracene
53—70—3
a
0.055
~
m-Dichlorobenzene
541—73—1
a
0.036
~.
o—Dichlorobenzene
95—50—1
~
0.088
~.
p-Dichlorobenzene
106—46-7
a
0.090
~
Dichlorodifluoromethane
75—71—8
~
0.23
~.
Li
l,1—Dichloroethane
75—34—3
~
0.059
~..
Li.
1,2—Dichioroethane
107—06—2
~
0.21
~.
Li
l,1—Dichloroethylene
75—35—4
a
0.025
~
trans—1,2—Dichloroethene
~
0.054
~
2,4—Dichlorophenol
120-83—2
a
0.044
~
2,6—Dichlorophenol
87—65—0
a
0.044
~
1,2—Dichloropropane
78—87—5
a
0.85
cis-1,3—Djchloropropene
10061—01—5
a
0.036
~.
~.
trans—1,3-Dichloropropene
10061—02-6
~
0.036
~
Dieldrin
60—57—1
a
0.017
a
0.13
Diethyl phthalate
84—66—2
~
0.20
~.
2L.
p—Dimethylaminoazobenzene
60—11—3
~
0.13
2,4-Dimethyl phenol
105—67-9
a
0.036
~
Bimethyl phthalate
i31—l1-3
~
0.047
~
117—628

309
Di—n—butyl phthalate
84—74—2
a
0.057
a
~
i,4—Binitrobenzene
100—25—4
a
0.32
a
2.3
4,6—Binitro-o—cresol
534—52—1
~..
0.28
a 160.
2,4—Binitrophenol
51—28—5
a
0.12
a 160.
2,4—Dinitrotoluene
121—14—2
a
0.32
a 140.
2,6—Dinitrotoluene
606—20—2
a
0.55
Di—n—octyl phthalate
117—84—0
a
0.017
~2L.
Di—n-propylnitrosoamine
621—64—7
a
0.40
~14.
1,2-Diphenyl hydrazine
a
0.087
NA
1,4—Dioxane
123—91—1
~
0.12
a 170.
Disulfoton
298—04—4
~
0.017
~
6.2
Endosulfan
I
939—98—8
a
0.023
a
0.066
Endosulfan II
33213—6—5
~
0.029
a
0.13
Endosulfan sulfate
1031—07—8
a
0.029
~
0.13
Endrin
7—20—8
a
0.0028
a
0.13
Endrin aldehyde
7421—93—4
a
0.025
a
0.13
Ethyl acetate
141—78—6
~
0.34
Ethyl cyanide
a
0.24
NA
Ethyl benzene
100—41—4
a
0.057
a
6.0
Ethyl ether
60—29-7
a
0.12
a 160.
bis(2—Ethylhexyl)
117—81—7
a
0.28
a28.
phthalate
Ethyl methacrylate
97—63-2
a
0.14
a 160.
Ethylene oxide
75—21—8
a
0.12
Famphur
52—85-7
a
0.017
a15.
Fluoranthene
206—44-0
a
0.068
~
Li.
Fluorene
86—73—7
a
0.059
a
j~.Q
Fluorotrichloromethane
75—69—4
a
0.020
a~
Heptachlor
76—44—8
a
0.0012
a
0.066
Heptachlor epoxide
1024—57—3
a
0.016
a
0.066
Hexachlorobenzene
118—74—1
a
0.055
~
Hexachlorobutadiene
87—68—3
a
0.055
a j~.
Hexachlorocyclopentadierie
77—47—4
a
0.057
~
3.6
Hexachlorodibenzofurans
a
0.000063 a
0.001
Hexachlorodibenzo—p-
a
0.000063 ~
0.001
dioxins
Hexachloroethane
67—72—i
a
0.055
~
2.~.
Hexachloropropene
1888-71—7
~
0.035
~
Indeno(1,2,3,—c,d)pyrene
193—39—5
~
0.0055
~
Li.
lodomethane
74—88-4
a
0.019
~
Isobutanol
78—83—1
a
5.6
a 170.
Isodrin
465—73—6
a
0.021
~
0.066
Isosafrole
120—58—1
a
0.081
a
~
Kepone
143—50—8
a
0.0011
~
0.13
Methacrylonitrile
126—98—7
a
0.24
a
~
Methapyrilene
91—80—5
a
0.081
a
1.5
Methoxychlor
72—43—5
a
0.25
~
0.18
3—Methylcholanthrene
56—49—5
~
0.0055
~
4,4—Methylene—bis—(2—
101—14—4
~
0.50
chloroaniline)
Methylene chloride
75—09—2
a
0.089
~
Methyl ethyl ketone
78—93—3
a
0.28
117—629

310
Methyl
isobutyl ketone
_________
Methyl methacrvlate
_______
Methyl methansulfonate
Methyl
parathion
________
Naphthalene
_______
2—Naphtylamine
_______
~-Nitroaniline
________
Nitrobenzene
________
5—Nitro—o—toluidine
_______
4-Nitrophenol
_________
N-Nitrosodiethylamine
_______
N—Nitrosodimethylamine
_______
N-Nitroso—di-n-butylamine
_________
N-Nitrosomethylethylamine
________
N-Nitrosomorpholme
_______
N—Nitrosopiperidme
________
N-N itrosopyrrolidine
_________
Parathion
________
Pentachlorobenzene
_________
Pentachlorodibenzo—furans
Pentachlorodibenzo-p—
dioxins
Pentachloronitrobenzene
________
Pentachlorophenol
________
Phenacetin
________
Phenanthrene
________
Phenol
_________
Phorate
_________
Propanenitrile
(ethyl
________
cyanide)
Pronamide
Pyrene
_________
Pyridine
________
Safrole
________
Silvex
(2,4,5-TP)
_______
2,4, 5—T
________
1,2,4, 5—Tetrachlorobenzene 95—94—3
Tetrachlorodibenzofurans
Tetrachlorodibenzo-p—
dioxins
2,3, 7,8—Tetrachloro—
dibenzo-p-dioxin
1, 1, 1, 2—Tetrachioroethane
________
1
1,2, 2—Tetrachloroethane
_______
Tetrachioroethene
_________
2, 3,4,6—Tetrachlorophenol
_______
Toluene
_________
Toxapherie
__________
1,2,4—Trichlorobenzene
________
1, 1, l—Trichloroethane
_______
1, 1,2-Trichloroethane
_______
Trichioroethylene
_______
0.14
a
33.
0.14
a 160.
0.018
0.014
a
4.6
0.059
a
3.1
0.52
0.028
~
0.068
~
0.32
a
28.
0.12
a
29.
0.40
a
28.
0.40
0.40
a
17.
0.40
a
2.3
0.40
a
2.3
0.013
a
35.
0.013
a
35.
0.017
a
4.6
0.055
a
37.
0.000035 ~
0.001
0.000063 ~
0.001
s
0.093
a
1.5
s
0.067
a
8.2
s
0.014
a
16.
s
0.081
a
22.
s
0.72
a
7.9
s
0.72
a
7.9
s
0.055
a
19.
a
0.000063 a
0.001
~
0.000063 ~
0.001
~
0.000063
S
S
S
S
S
B
B
S
S
S
S
S
S
S
S
S
S
B
5
S
S
108—10—1
80—62—6
298—00—1
91—20—3
91—59—8
100—01—6
98—95—3
99—55—8
100—02—7
55—18—5
62—75—9
924—16—3
105—95—6
59—89—2
100—75—4
930—55—2
56—38—2
608—93—5
82—68—8
87—86—5
62—44—2
85-01—8
108—95—2
298—02—2
107—12—0
23950—58—5
129—00—0
110—86—1
94—59—7
93—72—1
93—76—5
0.055
~_
0.089
~
0.081
~_
0.059
~
0.039
~
0.021
5
0.24
a
4.8
a
7.4
a
16.
a
3.1
a
6.2
a
4.6
a 360.
630—20—6
79—34—6
127—18—4
58—90—2
108—88—3
8001—35—1
120—82—1
71—55—6
79—00-5
79—01—6
~_
0.057
~
0.057
~_
0.056
~
0.030
~_
0.080
.L_
0.0095
.L~. 0.055
~
0.054
~_
0.054
~
0.054
a
42.
a
42.
a
5.6
a
37.
a
28.
a
1.3
a
19.
a
5.6
a
5.6
a
5.6
117—630

311
tn
fluoroethane
95—95—4
88—06—2
96—18—4
76—13—i
S
0.18
~_
0.035
s
0.85
.L_
0.057
~L.
a
37.
a
28.
a
28.
2,4, 5—Tnichlorophenol
2,4, 6—Trichlorophenol
1,2,3-Trichloropropane
1,1,2—Tnichloro—1,2,2—
Vinyl chloride
Xylene(s)
Cyanides
(Total~
Cyanides
(Amenable)
Fluoride
Sulfide
Antimony
Arsenic
Barium
Beryllium
Cadmium
Chromium
~Total)
Copper
Lead
Mercury
Nickel
Selenium
Silver
Vanadium
1(001
Table A Naphthalene
Pentachlorophenol
Phenanthrene
Pyrene
Toluene
Xylenes
(Total)
Lead
1(002
Table A Chromium
(Total)
Lead
1(003
Table A
Chromium
(Total)
Lead
75—01—4
57—12—5
57—12—5
16964—48—8
8496—25—8
7440—36—0
7440—38—2
7440—39—3
7440—41—7
7440—43—9
7440—47—32
7440—50—8
7439—92—1
7439—97—6
7440—02—2
7782—49—2
7440—22—4
1440—62—2
91—20—3
87—86—5
85—01—8
129—00—0
106—88—3
7439—92—1
7440—47—32
7439—92—i
7440—47—32
7439—92—1
7440—47—32
7439—92—1
7440—47—32
7439—92—1
57—12—5
7440—47—32
7439—92—1
7440—47—32
7439—92—1
57—12—5
L
0.27
~_
0.32
~
0.86
~_
0.82
L~ 0.20
~
0.37
~_
0.28
~_
0.15
~_
0.55
~_
0.82
~_
0.29
~_
0.042
0.031
~.
0.031
~_
0.031
~
0.028
~
0.028
~_
0.032
~
0.037
~
0.74
~_
0.74
a
33.
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
a
1.5
a
1.5
a
1.5
a
1.5
a
28.
a
33.
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
(R)
N~
1(004
Table
A
1(005
Table A
K006
Table A
1(007
Table
A
Chromium (Total)
Lead
Chromium (Total)
Lead
Cyanidee
(Total)
Chromium
(Total)
Lead
Chromium
(Total)
Lead
Cyanides
(Total)
117—631

312
1(008
Table A Chromium
(Total)
7440—47-32
~
Lead
7439—92—1
~
1(009
Chloroform
67—66—3
0..
a
j~.Q
1(010
Chloroform
67—66—3
0.1
1(011
Acetonitnile
75—05—8
38.
Acrylonitnile
107—13—1
0.06
LA.
Acrylamide
79—06—1
19.
23.
Benzene
71-43—2
0.02
0.03
Cyanide
(Total)
57—12-5
21.
~L.
1(013
Acetonitrile
75—05—8
38.
a
Li
Acrylonitrile
107—13—1
0.06
~
LA.
Acrylamide
79—06—1
19.
a
23.
Benzene
71—43—2
0.02
a
0.03
Cyanide
(Total)
57—12—5
21.
~L.
1(014
Acetonitnile
75—05—8
38.
~
Li
Acrylonitnile
107—13—1
0.06
~.
LA.
Acrylamide
79—06—1
~.
Benzene
71—43—2
0.02
~
0.03
Cyanide
(Total)
57—12—5
21.
1(015
Table
A
Anthracene
120—12—7
1.Oa
LA.
Benzal chloride
98—87—3
0.28
~
Sum of Benzo(b)fluor—
205—99—2
0.029
LA.
anthene and Benzo(k)fluor— 207—08—9
anthene
Phenanthrene
85—01—8
0.27
~
~.4.
Toluene
108—88—3
0.15
~
Chromium
(Total)
7440—47—32
0.32
Nickel
7440—02-2
0.44
1(016
Hexachlorobenzene
118—74-i
~.
0.033
~...2L..
Hexachiorobutadiene
87—68-3
a
0.007
~
Hexachlorocyclopentadiene
77—47-4
a
0.007
~.
Hexachloroethane
67—72—i
a
0.033
~2L.
Tetrachloroethene
127—18—4
a
0.007
~.
~Q
1(017
1,2—Dichloropropane
78—87—5
sa
0.85
~
1,2,3-Trichloropropane
96—18—4
sa0.85
Bis(2—chloroethyl)ether
111—44—4
sa
0.033
~
Li
1(018
Chioroethane
75—00—3
~..
0.007
~
1,1-Dichloroethane
75-34—3
a
0.007
~
1,2—Dichloroethane
107—06—2
a
0.007
a
~Q
Hexachlorobutadiene
87—68—3
~
0.033
~
Hexachloroethane
67—72—1
a
0.007
~
Pentachioroethane
76—01—7
a
0.007
~
117—632

313
1, 1, 1—Tnichloroethane
71—55—6
~_
0.007
a
6.0
K020
1(021
Table A
Phthalic anhydride
(measured as Phthalic
acid)
Phthalic anhydride
(measured
as Phthalic
acid)
1(019
Bis(2—chloroethyl)ether
Chlorobenzene
111—44—4
108—90—7
a
0.007
0.006
.~..Q
Chloroform
67—66—3
0.006
~Q
p-Dichlorobenzene
106—46—7
107—06—2
86—73—7
a
a
~
0.008
0.008
0.007
NA
~
1,2—Dichloroethane
Fluorene
Hexachloroethane
67—72-1
91—20-3
a
a
0.033
0.007
5.6
Naphthalene
Phenanthrene
85-01—8
0.007
1,2,4,5—Tetrachlorobenzene 95—94—3
a
~
a
a
a
a
0.017
0.007
0.023
0.007
0.007
0.007
0.007
0.046
~.
~.
~.
a
~
~
!!~
~Q
.
j~Q
~
5.6
L.Q
~
Tetrachloroethene
127—18—4
120-82—1
71—55—6
107—06—2
79—34—6
127—18—4
67—66-3
i,2,4-Tnichlorobenzene
1,1,1—Tnichloroethane
1,2—Dichloroethane
1,i,2,2—Tetrachloroethane
Tetrachloroethene
Chloroform
Carbon tetrachlonide
58—23—5
58—23—5
a
a
0.057
0.057
~.
a
6.2
Antimony
1(022
Table
A
Toluene
Acetophenone
Diphenylamine
Diphenylnitrosamine
Sum of Diphenylamine and
Diphenylnitrosamine
Phenol
Chromium (Total)
Nickel
108—88—3
96—86—2
22—39—4
86—30—6
108—95—2
7440—47—32
7440—02—0
a
a
a
0.060
0.010
0.52
0.40
~
0.039
0.35
0.47
~.
~
0.034
..~IL.
!j~
~
IL..
I2~.
~
~
1(023
1(024
1(028
Table
A
1,1—Dichloroethane
trans—i,2-Dichloroethene
Hexachlorobutadiene
Hexachloroethane
Pentachloroethane
1,1,1,2—Tetrachloroethane
1,1,2,2—Tetrachloroethane
1,1,1—Trichloroethane
i,1,2—Tnichloroethane
Tetrachioroethylene
85—44—9
85—44—9
75—34—3
87-68-3
67—72-i
76—01—7
630—20-6
79—34—6
71—55—6
79—00-5
127—18—4
a
~
~
~
~
a
a
a
a
a
a
a
0.54
0.54
0.007
0.033
0.007
0.033
0.033
0.007
0.007
0.007
0.007
0.007
~.
~
~
~..
a
a
a
~.Q
L..Q
~
~
~
~&
j~
~
j~Q
~Q
117—633

314
Cadmium
7440—43—9
Chromium (Total)
7440—47—32
0.35
NA
Lead
7439—92—1
0.037
Nickel
7440-02—2
0.47
1(029
Chloroform
67—66—3
0.46
~.
~.Q
i,2—Dichloroethane
107—06—2
0.21
~
1,l—Dichloroethylene
75—35—4
0.025
~
6.0
1,1,i—Trichloroethane
71—55—6
0.054
~
Vinyl
chloride
75—01—4
0.27
~..
j~.Q
1(030
o-Dichlorobenzene
95—50—1
~
0.008
p—Dichlorobenzene
106-46—7
~
0.006
Hexachlorobutadiene
87-68—3
a
0.007
~
5.6
Hexachloroethane
67—72—1
~
0.033
~
Hexachloropropene
1888—71—7
~.
Pentachlorobenzene
608—93—5
~
2L..
Pentachloroethane
76—01—7
~
0.007
~
5.6
i,2,4,5—Tetrachlorobenzene 95-94-3
~
0.017
~j4~
Tetrachloroethane
127—18—4
~
0.007
~
6.0
1,2,4-Tnichlorobenzene
120-82—i
~
0.023
~
1(031
Table A Arsenic
7440—38—2
0.79
1(032
Hexachlorocyclopentadiene
77—47—4
~
0.057
~j4~
Chlordane
57—74—9
~
0.0033
~
0.26
Heptachlor
76—44—8
a
0.012
a
0.066
Heptachlor epoxide
1024—57—3
a
0.016
~
0.066
K033
Hexachlorocyclopentadiene
77—47-4
~
0.057
~.
LA
K034
Hexachlorocyclopentadiene
77—47-4
~
0.057
~
LA.
1(035
Acenaphthene
83—32-9
NA
a
3.4
Anthracene
120—12—7
3.4
Benz(a)anthracene
56—55—3
~
0.59
Berizo(a)pyrene
50—32—8
IA
Chrysene
218—01—9
L_
0.059
~
3.4
Dibenz(a,h)anthracene
53—70—3
3.4
Fluoranthene
206-44—0
~
0.068
~
3.4
Fluorene
86-73—7
3.4
Indeno(1,2,3—cd)pyrene
193—39—5
~....
LA
CreaolS
(in- and p-isomers)
~
0.77
Naphthalene
91—20—3
a
0.059
a
3.4
o—Cresol
95—48—7
~
0.11
Phenanthrene
85—01—8
~
0.059
~
IA
Phenol
108—95—2
0.039
Pyrene
129—00—0
S
0.067
~
1(036
Disulfoton
298—04—4
~
0.025
~
0.1
1(037
Disulfoton
298—04—4
~
0.025
a
0.1
117—634

315
Toluene
108-88-3
a
0.080
a2L.
1(038
Phorate
298—02—2
0.025
~
K040
Phorate
298—02—2
0.025
~
Q.J.
1(041
Toxaphene
8001—35-1
a
0.0095
a
L..~
____
2, 4—Dichlorophenol
120—83—2
_____
____
2
,
6—Bichlorophenol
87-65—0
_____
2,4,5—Trichlorophenol
95—95—4
_____
2,4.6-Tnichlorophenol
88-06—2
_____
Tetrachlorophenols
(Total)
_____
____
Pentachlorophenol
87-86—5
____
Tetrachloroethene
79-01—6
_____
Hexachlorodibenzo—p—
______
______
dioxins
Hexachlorodibenzo—furans
______
______
Pentachlorodibenzo-p-dioxi
_____
_____
ns
Pentachlorodibenzo—furans
______
______
Tetrachlorodibenzo-p-dioxi
_____
_____
ns
Tetrachlorodibenzo—furans
_____
_____
K046
Table A
Lead
7439—92—1
0.037
____
_______
_______
71—43—2
0.011
~
____________
50—32—8
0.047
~
__________________________ 117—81—7
0.043
~
________
218—01—9
0.043
~
____________________
84—74—2
0.06
~
___________
100—41—4
0.011
~j4~
________
86—73—7
0.05
ri~
__________
91—20—3
0.033
~
__________
85-01—8
0.039
~
______
108—95—2
0.047
~
_____
129—00-0
0.045
~
______
108—88—3
0.011
~
________
0.011
a
22.
_________________
57—12—5
0.028
~
Li
_________________
7440—47—32
0.2
____
7439—92—i
0.037
1(049
Table
A
___________
_________
_____
1(042
1(043
1,2,4,5—Tetrachlorobenzene 95—94—3
o—Dichlorobenzene
95—50-1
p—Dichlorobenzene
106—46—7
Pentachlorobenzene
808-93—5
1,2,4—Trichlorobenzene
120—82—1
~_.
0.055
~
0.088
~_
0.090
~_
0.055
~_
0.055
a
a
a
a
a
a
a
a
a
a
a
a
a
4.4
4.4
4.4
4.4
4.4
0.38
0.3
8.2
7.8
0.68
1.9
1.7
0.001
a
a
a
a
a
a
a
a
0.049
0.013
0.016
0.039
0.018
0.22
0.006
0.001
L..
0.001
~_
0.001
~._
0.001
~_
0.001
K048
Table A
~_
0.001
~
0.001
~
0.001
~
0.001
~._
0.001
L_
0.001
Benzene
Benzo( a)pyrene
Bis
( 2-ethylhexyl)phthalate
Chrysene
Di—n—butyl phthalate
Ethylbenzene
Fluorene
Na~htha1ene
Phenanthrene
Phenol
Pyrene
Toluene
Xylene(s)
Cyanides
(Total)
Chromium
(Total)
Lead
Anthracene
Benzene
a
a
a
a
a
a
a
a
a
a
a
a
a
120—12—7
a
0.039
71—43—2
~
0.011
a
28.
a
14.
117—635

316
Benzo(a)pyrene
50—32—8
a
0.047
a
12.
BiS(2-ethylhexyl)phthalate 117—81—7
a
0.043
~
Carbon disulfide
75—15—0
a
0.011
NA
Chrysene
218—01—9
~
0.043
~.
j~.
2,4—Dirnethylphenol
105-67—9
~
0.033
Ethvlbenzene
100-41—4
~
0.011
~ j4~
Naphthalene
91—20—3
~
0.033
a42.
Phenanthrene
85—01—8
~
0.039
~
Phenol
108-95—2
~
0.047
~
Ii
Pvrene
129-00-0
~
0.045
~
Toluene
108—88—3
a
0,011
~
Xvlene(S)
~
0.011
~2L.
Cvanides
(Total)
57—12—5
L
0.028
~
Li
Chromium
(Total)
7440—47—32
Lead
7439—92—i
0.037
1(050
Table A
Benzo(a)pyrene
50—32—8
~
0.047
~..
Phenol
108—95-2
a
0.047
~
3.6
Cyanides
(Total)
57—12—5
~
0.028
~
Li
Chromium
(Total)
7440—47—32
Lead
7439—92—1
0.037
NA
K051
Table.A Acenaphthene
83-32—9
a
0.05
Anthracene
120—12-7
~
0.039
~2L
Benzene
71—43-2
a
0.011
~
Benzo(a)anthracene
50—32-8
a
0.043
aZ~.
Benzo(a)pyrene
50—32—8
~
0.047
~
Bis(2—ethylhexyl)phthalate 75—15—0
a
0.043
a
L1
ChrySene
218—01—9
~
0.043
~
Di—n-butyl phthalate
105-67—9
a
0.06
~.
IA
Ethylbenzene
100-41—4
a
0.011
~
Fluorene
86-73-7
a
0.O5a
Naphthalene
91—20—3
a
42.
0.033
Phenanthrene
85—01—8
~
0.039
~
Phenol
108-95-2
a
0.047
~
IA
Pyrene
129—00-0
~
0.045
k...
Toluene
108—88-3
~
0.011
~.
~
Xvlene(s)
a
0.011
&.2.L
Cyanides
(Total)
57—12—5
~
0.028
~.
Li
Chromium
(Total)
7440—47—32
Lead
7439—92—1
0.037
1(052
Table
A
Benzene
71—43—2
fl....
0.011
a
14.
Benzo(a)pyrene
50—32—8
a
0.047
~
o-Cresol
95—48—7
a
0.011
~
p—Cresol
106—44—5
a
0.011
~.
2,4—Dirnethyiphenol
105—67—9
a
0.033a
Ethvlbenzene
100—41—4
a
0.011
aj~.
Naphthalene
91—20—3
~
0.033
~
Phenanthrene
85—01—8
a
0.039
a 34
Phenol
108—95—2
~
0.047
~.
IA
117—636

317
1(061
Tables
A&D
Toluene
Xvlene(sl
Cyanides
(Total)
Chromium
(Total)
Lead
108—88—3
~
0.011
~_
0.011
57—12—5
a
0.028
7440—47—32
7439—92—1
0.037
71—43—2
50—32—8
91—20—3
108—95—2
57—12—5
7440—43—9
7440—47—32
7439—92—1
7440—02—2
0.17
0.035
0.028
0.042
1.9
1.61
0.32
0.51
0.44
a
14.
a
22.
a
1.8
NA
0.071
3.6
3.4
3.4
1.2
NA
NA
NA
NA
7440—47—32
7439—92—i
7440—02—2
0.32
0.04
0.44
NA
NA
NA
1(069
Tables
Cadmium
K071
Table A
Mercury
1(085
71—43—2
62—53—3
22—39—4
86—30—6
98—95—3
108—95—2
108—94—1
7440—02—2
B
5
S
B
S
1.6
NA
0.51
0.030
0.057
0.046
0.055
0.056
0.054
0.14
0.81
0.52
0.40
NA
L_
0.068
0.039
0.36
0.47
a
6.2
a
6.2
a
30.
a
6.2
a
6.2
a
6.6
a
14.
NA
NA
a
14.
a
5.6
a
30.
1(060
Benzene
Benzo (a) PVrerLe
Naphthalene
Phenol
Cvanides
(Total)
Cadmium
Chromium
(Total)
Lead
Nickel
a
B
a
a
a
a
1(062
Table A chromium
Lead
Nickel
~_—---
(Total)
Lead
7440—43—9
7439—92—1
7439—97—6
58—23—5
67—66—3
67—72—1
127—18—4
71—55—6
Carbon tetrachloride
Chloroform
Hexachloroetbane
Tetrach1oroetherie
1
1, 1—Tnichloroethane
1(073
1(083
Table A
1(084
S
S
S
a
Benzene
Aniline
Bi~henyl
amine
Diphenylnitrosamine
Sum of Diphenylainine and
Diphenylnttro~amine
Nitrobenzene
Phenol
Cvclohexanone
Nickel
Az~senic
Benzene
Chlorobenzene
0—Bichlorobenzerze
rn—Bichlorobenzene
P—Dichlorobenzene
7440—38—2
71—43—2
108—90—7
95—50—1
541—73—1
106—46—7
0.79
8
0,14
~.
0.057
L..
0.088
~_
0.036
~_
0.090
NA
a
4.4
a
4.4
a
4.4
a
4.4
a
4.4
117—637

318
1,2
,
4—Trichlorobenzene
1,2 .4,5—Tetrachlorobenzen~
Pentachlorobenzene
Hexachlorobenzene
Aroclor 1016
Aroclor 1221
Aroclor 1232
Aroclor 1242
Aroclor 1248
Aroclor 1254
Aroclor
1260
120—82—1
~
0.055
95—94—3
~
0.055
608—93—5
0.055
118—74—1
~
0.055
12674—11—2
~
0.013
11104—28—2
~.
0.014
11141—16—5
a
0.013
53469—21—9
~
0.017
3.2672—29—6
8
0.013
11097—69—1
~
~014
11096—82—5
~
0.014
K086
Table A
Acetone
Acetophenone
Bis
(
2—ethvlhexvl
‘~
ohthalate
n—Butyl alcohol
Butylbenzylphthaiate
cyclohexanone
1,2—Dichlorobenzene
Diethyl phthalate
Dimethyl phthalate
Di—n-butyl phthalate
Di—n-octyl phthalate
Ethyl acetate
Ethylbenzene
Methanol
Methyl
isobutyl ketone
Methyl ethyl ketone
Methylene chloride
Naphthalene
Nitrobenzene
Toluene
1, 1, 1—Trichloroethane
Tnichloroethylene
Xylepe
(5)
Cyanides
(Totall
Chromium
(Total)
Lead
K087
Table A Acenaphthalene
Benzene
Chrysene
Fluoranthene
Indeno(1,2,3-cd)pyrene
~—
4.4
~A.
~.
0.92
~_
0.92
~.
0.92
L.
0.92
~Li
~Li
a 160.
-~
NA
-z~
NA
1.5
NA
NA
3.4
~
0.071
L
0.65
•~_~0.07
NA
67—64—1
96—86—2
117—81—7
71—36—3
85—68—7
108—94—1
95—50—i
84—66—2
131—11—3
84—74—2
117—84—0
141—78—6
100—41—4
67—56—1
108—10—1
78—93—3
75—09—2
91—20—3
98—95—3
108—88—3
71—55—6
79—01—6
(Total)
57—12—5
7440—47—32
7439—92—1
208—96—8
71—43—2
218—01—9
206—44-0
193—39—5
91—20—3
85—01—8
108—88—3
7439—92—1
0.28
0.010
•~_
0.28
•~_• 0.017
0.36
0.088
~_
0.20
~_
0.047
~_
0.057
~
0.017
~_
0.34
~
0.057
0.14
0.28
~
0.089
~
0.059
~_
0.068
~_
0.080
~_
0.054
~_
0.054
~_.
0.32
1.9
0.32
~_._Q_3
7
.L..
0.028
•~_.
0.014
~
0.028
L
0.028
L_
0.028
.L.
0.028
•&~
0.028
•~_ 0.008
~_
0.014
0.037
Naphthalene
Phenanthrene
Toluene
Xylene(s)
Lead
117—638

319
1(093
Phthalic anhydnide
85—44-9
a
0.54
a28.
(measured
as Phthalic
acid)
1(094
phthalic
anhydnide
85—44—9
~
0.54
~2L.
(measured as
Phthalic
acid)
1(095
1,11,2—Tetrachloroethane
630—20—6
0.057
~
5.6
3.,l,2,2—Tetrachloroethane
79—34—6
0.057
a
5.6
Tetrachloroethene
3.27—18—4
0.056
~.
LQ
1,1,2—Trichloroethane
79—00—5
0.054
~
Trichloroethylene
79—01—6
0.054
~.
~
Hexachloroethane
67—72—1
0.055
~.
2L.
Pentachloroethane
76—01—7
0.055
~
1(096
i,1,1,2—Tetrachloroethane
630—20—6
0.057
~.
1,l,2,2—Tetrachloroethane
79—34—6
0.057
~.
Tetrachloroethene
127—18-4
0.056
~
1,1,2—Trichloroethane
79—00—5
0.054
~
Trichloroethene
79—01—6
0.054
~...
.~i
1,3—Bichlorobenzene
541—73—1
0.036
a
5.6
Pentachloroethane
76—01—7
0.055
~..
~
1,2,4—Tnichlorobenzene
120—82—1
0.055
~
K097
Hexachlorocyclopentadjene
77—47—4
~.
0.057
LA.
Chlordane
57—74—9
a
0.0033
a
0.26
He~tachlor
76—44—8
a
0.0012
a
0.066
Heptachlor epoxide
1024—57—3
a
0.016
~
0.066
K098
Toxaphene
8001—35—1
~.
0.0095
~
K099
2,4-Dichlorophenoxyacetic
94-75—7
~
L.
~_
L
acid
Hexachlorodibenzo-p—
~
0.001
~
0.001
dioxins
Hexachlorodibenzofurans
~
0.001
~
0.001
Pentachlorodibenzo—p—
~
0.001
~
0.001
dioxins
Pentachlorodibenzofurans
a
0.001
a
0.001
Tetrachlorodibenzo—p—dioxi
~
0.001
~
0.001
nS
Tetrachlorodibenzofurang
a
0.001
a
0.001
1(100
Table A
Cadmium
7440—43—9
L.~
Chromium (Total)
7440—47—32
0.32
Lead
7439—92—1
0.51
NA
1(101
o—Nitroaniline
~
0.27
Arsenic
7440—38—2
0.79
Cadmium
7440—43—9
0.24
Lead
7439—92—1
0.17
117—639

320
Mercury
7439—97—6
0.082
1(102
Table A
o-Nitrophenol
a
0.028
~fl..
Arsenic
7440—38—2
0.79
Cadmium
7440—43—9
0.24
Lead
7439—92—1
0.17
Mercury
7439—97—6
0.082
1(103
Aniline
62—53—3
Benzene
71—43—2
~
0.3.5
~.
L~
2,4—Dinitrophenol
51—28—5
~
0.61
Nitrobenzene
98—95—3
~
0.073
~
5.6
Phenol
108-95—2
~
1.4
1(104
Aniline
62—53—3
~
Benzene
71—43—2
a
0.15
2,4—Dinitrophenol
51—28-5
a
0.61
Nitrobenzene
98—95—3
a
0.073
~
Phenol
108-95-2
a
LA
Cyanides
(Total)
57-12-5
2.7
a
Li
1(105
Benzene
71—43—2
0.14
~
j~A
Chlorobenzene
108-90-7
0.057
~
o-Dichlorobenzene
95—50—i
0.088
~
j~A
~-Dich1orobenzene
106—46-7
0.090
~.
2,4,5—Trichiorophenol
95—95—4
0.18
a
j~
2,4,6—Trichlorophenol
88—06-2
0.035
~
2—Chiorophenol
95—57—8
0.044
a
4.4
Phenol
108—95—2
0.039
~.
1(106
Tables
Mercury
7439—97—6
0.030
A&D
1(115
Table A
Nickel
7440-02—2
0.47
a
Treatment standards
for this organic constituent were established based
upon incineration
in units operated in accordanpe with the technical
requirements of 35
Ill.
Adin. Code 724.Subpart 0 or 725.Subpart 0,
or
based upon combustion
in fuel substitution units operatino
in
accordance with applicable technical requirements. A facility may
certify compliance with these treatment standards according to
provisions
in Section 728.107.
Based on analysis of composite samples.
i.BJ~
As analyzed using SW—846 Method 9010; sample size: 0.5—iO~distillation
time:
one hour to one hour and fifteen minutes.
NA
Not Applicable.
117—640

321
TABLE
B
(CCW):
P AND U LISTED WASTES
CAS No.
for
Commercial
Regulated
Regulated
Concentration
(mg/l)
Waste Chemical
See
Hazardous
Hazardous
Non
Code
Name
Also
Constituent
Constituent Wastewaters
wastewaters
~0Q4
Aidrin
Aldrin
309-00—2
0.21
0.066
POlO
Arsenic acid Table A
Arsenic
7440—38-2
0.79
POll
Arsenic
Table A Arsenic
7440—38—2
0.79
pentoxide
P012
Arsenic
Table A
Arsenic
7440—38—2
0.79
NA
tnioxide
P013
Barium
Table A
Cyanides
57—12—5
1.9
110.
cyanide
(Total)
Cyanides
57—12—5
(Amenable)
P020
2—sec—Butyl—
2—sec—Butyl—
88—85—7
0.066
*
25
4~6-dinitro-
4, 6—dinitro-
phenol
phenol
(Dinoseb)
lDinoseb)
P021
Calcium
Cvanides
57—12—5
110.
cyanide
(Total)
Cyanides
57—12—5
0.1
(Amenable)
P022
Carbon di-
Table B
Carbon di—
75—15—0
0.014
sulfide
sulfide
P024
p-Chloro—
p—Chloro-
106—47—8
0.46
aniline
aniline
P029
Copper
Cyanides
57—12—5
110.
cyanide
(Total)
Cvanides
57—12—5
9.1
(Amenable)
P030
Cyanides
Cvanides
57—12—5
110.
Isoluble
(Total)
salts and
complexes)
Cyanides
57—12—5
Thnienable)
117—641

322
P036
Dichloro—
phenylarsine
P038
Diethyl—
arsine
P039
Disulfoton
Disulfoton
298—04—4
0.017
*
0.1
P047
4,6—Dinitro—
o—cresol
P048
2,4—Dinitro—
phenol
4, 6—Dinitro—
534—52—4
o—cresol
2,4—Dinitro—
51—28—5
phenol
P050
Endosulfan
Endosulfan
I
Endosulfan
II
Endosulfan
sulfate
939—98—8
33213—6—5
1031—07—8
!._
0.023
~__
0.029
~
0.029
!_
0.066
*
0.13
*
0.13
P051
Endrin
Endnin
Endrin
aldehyde
72—20—8
7421—93—4
~.
0.0028
*
0.13
~
0.025
*
0.13
P056
Fluoride
Table
B
Fluoride
35.
P059
Heptachlor
Heptach1or
Heptachlor
epoxide
76—44—8
1024—57—3
0.0012
~
0.016
~_
0.066
!_
0.066
P060
Isodrin
Isodrin
465—73—6
*
0.021
~.
0.066
P065
Mercury
fulminate
Tables
Mercury
A&D
P071
Methyl
parathion
Methyl
parathion
298—00—0
0.025
*
0.1
P073
Nickel
carbony 1
P074
Nickel
cyanide
Table A
Cyanides
(Table)
Cyanides
(Amenable)
Nickel
57—12—5
57—12—5
0.10
7440—02—2
0.44
9.1
NA
P037
Dieldrin
Table A Arsenic
Dieldrin
Table
A
Arsenic
7440—38—2
0.79
60—57—1
~_
0.017
NA
*
0.13
NA
7440—38—2
0.79
!_
0.28
*
160.
!_
0.12
*
160.
18694—48—8
NA
P063
Hydrogen
cyanide
Cyanides
(Total)
Cyanides
(Amenable)
57—12—5
57—12—5
7439—97—6
Li
110.
0.10
0.030
Table A
Nickel
7440-02-2
0.44
110.
117—642

323
p—Nitro—
aniline
Table D
N—Nitrosodi—
methylamine
Phorate
Famphur
Cvanides
(Total)
Cyanides
(Amenable)
Table A
Cyanides
(Total)
Cyanides
(Amenable)
Silver
Ethyl cyanide
(Propane—
nitrile)
_______
Selenium
_______
Cyanides
(Total)
Cyanides
(Amenable)
Silver
Cyanides
(Total)
Cyanides
(Amenable)
______
Lead
P077
p—Nitro—
aniline
P082
N—Nitroso—
dirnethyl—
amine
9089
Parathion
P092
Phenyl—
mercury
acetate
100—01—6
~
0.028
~
62—75—9
~
0.40
Parathion
Mercury
Tables
A&D
P094
P097
P098
Phorate
Famphur
Potassium
cyanide
0.025
0.030
0.025
0.025
1.9
0.10
*
0.1
NA
*
0.1
*
0.1
110.
9.1
56—38—2
7439—97—6
298—02—2
52—85—7
57—12—5
57—12—5
57—12—5
57—12—5
7440—22—4
107—12—0
P099
Potassium
silver
cyanide
P101
Ethyl
cyanide
(Propane—
nitnile)
P103
Selenourea
P104
Silver
cyanide
Li
110.
0.1
0.29
*
0.24
______
Table
A
Table
A
9.1
NA
*
360.
NA
110.
9.1
NA
110.
9.1
1.0
1.9
0.10
0.29
1.9
0.10
P106
Sodium
cyanide
P110
Tetraethyl
Tables
lead
A&D
7782—49—2
~.
57—12—5
57—12—5
7440—22—4
57—12—5
57—12—5
7439—92—1
0.040
117—643

324
U009
Acrylo—
nitrile
____
Aniline
____
Benz(a)-
anthracene
____
Benzene
____
Benzo (a)
-
pyrene
U024
Bis(2—
chloro—
ethoxy)-
methane
Cyanides
(Total)
Cyanides
(Amenable)
P113
Thallic
Table D
Thallium
7440—28—0
oxide
9114
Thallium
Table A
Selenium
7782—49-2
aelenite
P115
Thallium(I)
Table B
Thallium
7440—28—0
sulfate
P119
Ammonia
Table B
Vanadium
7440—62—2
vanadate
P120
Vanadium
Table
D Vanadium
7440-62—2
pentoxide
P121
Zinc cyanide
________
_______
i~ 0.14
1.0
NA
!.....
0.14
*
28.
NA
*
28.
NA
57—12—5
57—12—5
8001—35—1
67—64—1
75—05—8
98—86—2
53—96—3
P123
Toxaphene
Toxaphene
U002
Acetone
Acetone
U003
Acetonitnile Table
D
Acetonitrile
U004
Acetophenone
Acetophenone
UOO5
2—Acetyl—
amino—
fluorene
2—Acetyl—
aminofluorene
1.9
0.10
!_
0.0095
0.28
0.17
!.._
0.010
!....
0.059
110.
9.1
*
1.3
*
160.
NA
*
9.7
*
140.
U012
U018
Acrvlonitnile
107—13—1
*
0.24
*
84.
U019
U022
Aniline
62—53—3
Benz(a)—
56—55—3
anthracene
Benzene
71—43—2
Benzo(a)—
50-32—8
pyrene
Bis(2—chloro—
111—91—1
ethoxy)—
methane
0.81
!_
0.059
*
0.14
!._.
0.061
*
14.
*
8.2
*
36.
*
8.2
0.036
*
7.2
117—644

325
U025
Bis(2—
Bis(2—chloro—
111—44—4
0.033
~
Li.
chloroethyl)
ethyl) ether
ether
1J027
Bie(2—
Bis(2—chloro—
39638—32—9
*
0.055
*
Li
chloro-
isopropyl)
isopropyl)
ether
ether
tJ028
Bis(2—ethyl-
Bis(2—ethyl—
3.17—81-7
~
0.54
bexyl)
hexyl)
pthalpte
pthalate
U029
Bromomethane
Bromomethane
74-83-9
!.
0.11
lMethyl
(Methyl
bromide)
bromide)
U030
4—
4-Bromophenyl
101—55-3
*
0.055
*15.
Bromophenyl
phenyl ether
phenyl ether
U031
n-Butyl
n-Butyl
71-36—3
!....
L.~
alcohol
alcohol
UO32
Calcium
Table A
Chromium
7440—47—32
0.32
chromate
(Total)
U036
Chlordane
Chlordane
5774...9
*
0.00033
*
0.13
(alpha and
(alpha and
gamma)
gamma)
UO37
Chloro—
Chlorobenzene
108-90—7
~.
0.057
~
benzene
U038
Chloro—
Table D
Chloro-
510-15—6
~.
0.10
benzilate
benzilate
UO39
p—Chloro-m-
p-Chloro-m-
59-50-7
~
0.018
~j4~
cresol
cresol
U042
2—Chloro-
Table
D
2-Chloroethyl
110-75—8
0.057
ethyl vinyl
vinyl
U043
Vinyl
Vinyl
75-01-4
~
0.27
chloride
chloride
U044
Chloroform
Chloroform
67—66—3
~
0.046
*
5~
U045
Chloro-
Chloromethane
74—87—3
!...
0.19
methane
(Methyl
(Methyl
chloride)
chloride)
117—645

326
U047
2—Chioro—
naphthalene
2—Chloro-
naphthalene
91—58—7
!_
0.055
*
5.6
0048
2—Chloro-
phenol
2 -Chloro-
phenol
95—57—8
!_..
0.044
0050
Chrysene
Chrysene
U051
Creosote
Table A Naphthalene
Pentachloro—
phenol
Phenanthrene
Pvrene
Toluene
Xylenes
(Total)
Lead
0052
Cresols
(Cresylic
acid)
o—Cresol
Cresols
(in—
and p-
isomers)
218—01—9
!_
0.059
85—01—8
_____
129—00—0
______
108—88—3
______
7439—92—1
~
0.037
95—48—7
~.
0.11
*
8.2
UO57
Cyclo—
hexanone
0.023
~
0.087
0.023
~
0.087
UO63
Dibenzo-
(a,h)—
anthracene
Dibenzo(a,h)—
53—70—3
anthracene
*
0.055
*
8.2
UO66
1,2—Dibromo—
3-chloro-
propane
1, 2-Bibromo-
3—chloro-
propane
96—12—8
*
0.11
*
15.
U067
1,2—Bi—
bromoethane
(Ethylene
dibrornide)
1, 2-Bibromo—
ethane
(Ethylene di—
bromide)
106—93—4
~:_
0.028
*
15.
91—20—3
87—86—5
!..
0.031
!_...
0.18
!_
0.031
!_
0.028
!.._
0.028
!_
0.032
*
1.5
*
7.4
*
1.5
*
28.
*
33.
NA
*
5.6
*
3.2
*
0.77
Table
D
Cyclohexanone
U060
DDB
U061
DBT
108—94—1
0.36
o,p’-BDD
p,~’-BDD
o,p’-DDT
p,p’ -DDT
o,p’—DDD
p,p’-DDD
o,p’-DDE
p,p~-DDE
53—19—0
72—54—8
789—02—6
50—29—3
53—19—0
72—54—8
3424—82—6
72—55—9
!_.
0.0039
•~_ 0.0039
0.023
0.023
~
0.033.
!_
0.031
!_
0.087
!_
0.087
!...
0.087
!....
0.087
!_
0.087
!_
0.087
117—646

327
UO68
Dibromo-
ethane
0069
Di—n-butyl
phthalate
Di-n-butyl
84-74—2
phthalate
0070
o—Dichloro—
benzene
o-Dichloro-
benzene
95—50—1
*
0.088
*
6.2
0071
m—Dichloro-
benzene
m—Dichloro—
541—73-i
benzene
0072
p—Dichloro-
benzene
P-D ich loro-
benzene
104—46—7
~
0.090
*
6.2
0075
Dichiorodi—
fluoro—
methane
Dichlorodi—
f1uoromethane
75—71—8
*
0.23
*
7.2
0076
l,i—Di—
chloroethane
0077
1,2—Di—
chloroethane
1, 1—Dichloro—
75—34—3
ethane
1, 2—Bichloro—
107—06—2
ethane
!_.
0.059
*
0.21
7.2
*
7.2
1, 1—Dich1
ethylene
U079
1,2—Bi—
chloro—
ethylene
trans—i, 2—
Dichloro-
ethylene
3.56—60—5
!_
0.054
33.
x
UO8O
Methylene
chloride
Methylene
75—08—2
chloride
U081
2,4—Bi—
chlorophenol
2, 4—Dichloro—
120—83—2
phenol
0.044 Y
14.
X
0082
2,6—Di—
chlorophenol
2, 6—Dichloro—
87—65-0
phenol
0.044 Y
14.
X
0083
1,2—Di—
chloro—
propane
U084
i,3—Di—
chloro—
propene
cis—i,3—Di—
10061—01—5
chloro—
propylene
trans—i,3—
10061—02—6
Bichloro—
propylene
Dibromoethane
74-95—3
*
0.11
15.
*
0.54
*
28.
0.036
U078
1,1—Di—
chloro-
ethylene
....-~-.-
75—35—4
*
0.025
*
33.
0.089
Y
33.
X
1,2—Dichloro—
78—87—5
propane
0.85
Y
18.
X
0.036
Y
18.
X
0.036 Y
18.
X
117—647

328
0088
Diethyl
Diethvl
84—86—2
0.54 X
28.
X
phthalate
phthalate
UO93
p-Dimethyl-
Table B
p-Dimethyl-
60-11-7
0.13 Y
aminoazo—
aminoazo—
benzene
benzene
0101
2,4—Di—
2,4—Dimethyl—
105—67—9
0.036
Y
14.
X
methylphenol
Phenol
Ul02
Dimethyl
Dimethyl
131—11—3
0.54 X
28.
X
phthalate
~hthalate
0105
2,4—Dinitro—
2,4—Dinitro—
121—14—2
0.32
Y
140.
X
toluene
toluene
U106
2,6—Binitro—
2,6—Dinitro—
606—20—2
0.55 Y
28.
X
toluene
toluene
0107
Di—n—octyl
Di—n—octyl
117—84—0
0.54 X
28.
X
phthalate
phthalate
U108
1,4—Dioxane
1,4—Bioxane
123—91—1
0.12
Y
170.
X
0111
Di—n—propyl—
Bi—n-propyl—
621—64—7
0.40 Y
14.
X
nitrosoamine
nitrosoamine
U112
Ethyl
Ethyl acetate
141—78-6
0.34
Y
33.
X
acetate
0117
Ethyl ether
Ethyl ether
60—29—7
0.12
Y
160.
X
U118
Ethyl meth-
Ethyl rneth-
97-63-2
0.14 Y
160.
X
acrylate
acrylate
0120
Fluoranthene
Fluoranthene
206—44-0
0.068
Y
8.2
X
0121
Trichloro—
Trichloro—
75—69—4
0.020
Y
33.
X
inonofluoro-
monofluoro—
methane
methane
U127
Hexachloro-
Hexachloro—
118-74-1
0.055 Y
37.
X
benzene
benzene
U128
Hexachloro—
Hexachloro—
87—68—3
0.055
Y
28.
X
butadiene
butadiene
0129
Lindane
alpha—BHC
319—84—6
0.00014
0.066
X
Y
beta—BHC
319—85—7
0.00014
0.066
X
Delta—BHC
319—86—8
0.023
0.066 X
117—648

329
gamma—BHC
58—89—9
0.0017
0.066
X
(Lindane)
U130
Hexachioro—
Hexachloro-
77—47—7
0.057
Y
3.6
X
cyclopenta—
cvclopenta—
diene
diene
0131
Hexachloro—
Hexachloro—
67—72—1
0.055
y
28.
X
ethane
ethane
U134
Hydrogen
Table B
Fluoride
16964-48—8
1~.
fluoride
U136
Cacodylic
Table A
Arsenic
7440—38—2
0.79
acid
0137
Indeno—
Indeno(1,2,3—
193—39—5
0.0055
Y
8.2
X
(1,2,3—c,d)—
c,d)pvrene
pyrene
U138
lodomethane
lodomethane
74-88—4
0.19 Y
65.
X
0140
Isobutyl
Isobutyl
78—83—i
170.
X
alcohol
alcohol
U141
Isosafrole
Isosafrole
120—58—1
0.081
2.6 X
0142
Kepone
1(epone
143—50-8
0.0011
0.13
X
Ui44
Lead acetate Table A
Lead
7439—92—1
0.040
Ui45
Lead
Table A
Lead
7439—92—1
0.040
phosphate
U146
Lead
Table A Lead
7439—92—1
0.040
subacetate
U151
Mercury
Tables
Mercury
7439—97—6
0.030
A&D
U152
Methacrylo—
Z4ethacrylo—
126—98—7
0.24 Y
84.
X
nitrile
nitrile
0155
Methapyrilen
Methapyrilene
93.—80-5
0.081
1.5
X
e
Ui57
3—Methyl—
3-Methyl—
56—49-5
0.0055
‘1
15.
X
cholanthrene
cholanthrene
117—649

330
0158
4,4’—
Methylene—
101—14—4
0.50
Y
35.
X
Methvlene-
bis (2-chloro-
bis(2—
aniline)
chloro-4
aniline)
0159
Methyl ethyl
Methyl ethyl
78—93—3
0.28
36.
X
ketone
ketone
0161
Methyl
Methyl
108—10—1
0.14
33.
X
isobutyl
isobutvl
ketone
ketone
0162
Methyl
Methyl
80—62—6
0.14
160.
X
methacrylate
methacrylate
0165
Naphthalene
Naphthalerie
91-20—3
0.059
Y
3.1
X
Ul68
2—Naphthyl—
Table
B
2-Naphthyl—
91—59—8
0.52 Y
amine
amine
U169
Nitrobenzene
Nitrobenzene
98—95-3
0.068 Y
14.
X
U17O
4—Nitro—
4—Nitrophenol
100—02—7
0.12
Y
29.
X
phenol
U172
N—Nitroso—
N—Nitrosodi—
924—16—3
0.40
Y
17.
X
di—n-butyl-
n—butylamine
amine
Ul74
N—Nitroso-
N—Nitrosodi—
55—18—5
0.40 Y
28.
X
diethylamine
ethylamine
0179
N—Nitroso—
N—Nitroso—
100—75—4
0.013
Y
35.
X
pipenidine
piperidine
0180
N-Nitroso-
N—Nitroso—
930-55—2
0.013
Y
35.
X
pyrrolidine
pvrrolidine
U181
5—Nitro—o—
5—Nitro—o—
99—55—8
0.32
Y
28.
X
toluidine
toluidine
0183
Pentachloro—
Pentachloro-
608-93—5
0.055 Y
37.
X
benzene
benzene
U185
Pentachloro—
Pentachloro—
82—68—8
0.055
Y
4.8 X
nitrobenzene
nitrobenzene
0187
Phenacetin
Phenacetin
62—44-2
0.081
16.
X
0188
Phenol
Phenol
108—95—2
0.039
6.2
X
117—650

331
0190
Phthalic
Phthalic
85—44—9
0.54 X
28.
X
anhydride
anhvdride
(measured as
(measured as
phthalic
Phthalic
acid)
a~cid)
U192
Prpnamide
Pronainide
23950-58—5
0.093
1.5
X
U196
Pyrjdjne
Pvnidine
110—86—1
0.014
Y
16.
X
0203
Lafrole
Safrole
94—59—7
0.061
22.
X
U204
Selenium
Table A
Selenium
7782—49-2
L.Q
dioxide
0205
Selenium
Table A
Selenium
7782—49—2
1.0
NA
sulfide
U207
1,2,4,5—
1,2,4,5—
95—94—3
0.055
Y
19.
X
Tetrachloro—
Tetrachloro-
benzene
benzene
U208
1,1,i,2—
1,1,1,2—
630—20—6
0.057
42.
X
Tetrachloro—
Tetrachloro—
ethane
ethane
0209
1,1,2,2—
1,1,2,2—
79—34—5
0.057
Y
42.
X
Tetrachloro—
Tetrachloro—
ethane
ethane
U21O
Tetrachloro-
Tetrachloro—
i27—18-4
0.056 Y
5.6 X
ethylene
ethylene
0211
Carbon
Carbon tetra—
_______
0.057 Y
5.6 X
tetra—
chloride
chloride
0214
Tallium(I)
Table D
Thallium
7440—28—0
0.14 Y
acetate
0215
Thallium(I)
Table
B
Thallium
7440—28—0
0.14 Y
carbonate
0216
Thallium(I)
Table D
Thallium
7440—28—0
0.14 Y
chloride
U217
Thallium(I)
Table D
Thallium
7440—28—0
0.14 Y
nitrate
U22O
Toluene
Toluene
108-88—3
~8O
Y
28.
X
117—651

332
0225
Tribromo—
Tribromo—
75—25—2
0.63
Y
15.
X
methane
methane
(Bromoform)
(Bromoform)
U226
1,1,1—Tn—
1,1,1—Tn—
71—55—6
0.054 y
5.6 X
chloroethane
chioroethane
0227
1,1,2—Tn—
1,1.2—Tn—
79—00—5
0.054
Y
5.6 X
chioroethane
chioroethane
0228
Trichioro—
Tnichioro—
79—01—6
0.054 Y
5.6
X
ethylene
ethylene
0235
tnis—(2,3—
tris—(2,3—
126—72—7
0.025
0.10 X
Dibromo—
Dibromo—
propyl)-
propyl)—
phosphate
phosphate
0239
Xylenes
Xylene
a
0.32
Y
28.
X
U240
2,4—Di—
2,4—Bichioro—
94—75—7
0.72
10.
X
chloro—
phenoxyacetic
phenoxy-
acid
acetic acid
0243
Hexachioro—
Hexachloro-
1988—71—7
0.095 Y
propene
propene
0247
Methoxychlor
Methoxychlor
72—43-5
0.25 Y
0.18 X
Treatment standards for this organic constituent were established based
upon incineration
in units operated in accordance with the technical
requirements
of
35 Ill. Adm. Code 724.Subpart
0 or 725.Subpart
0,
or
based upon combustion
in fuel substitution units operating
in
accordance with applicable technical requirements.
A facility may
certify compliance with these treatment standards accordin~to
provisions
in Section 728.107.
I
Based on analysis of composite samples.
As analyzed using SW—846 Method 9010;
sample size:
0.5—10; distillation
time:
one hour to one hour fifteen minutes.
NA
Not Applicable.
(Source:
Amended at 15
Ill. Reg.
,
effective
117—652

333
Section 728.Table C
Technology Codes and Description of Technology—Based
Standards
Technology
code
Description of technology-based standard
ADGAS Venting of compressed gases into an absorbing or reacting media (i.e.,
solid or liquid)——ventinq can be accomplished throggh
physical release
utilizing values/piping;
physical penetration
of the container; and/or
penetration through detonation.
AMLOM
Amalgamation of liquid,
elemental mercury contaminated with
radioactive
materials utilizing inorganic reagents such as
copper,
zinc,
nickel,
gold, and sulfur that result in a
nonliguid, semi—solid amalgam and
thereby reducing potential
emissions of elemental mercury vapors to the
air.
BIQDG Biodegradation of organics or non—metallic inorganics
(i.e.,
degradable
inorganics that contain the elements of phosphorus,
nitrogen,
and
sulfur)
in units operated under either aerobic or
anaerobic conditions
such that a surrogate compound or indicator
parameter has been
substantially reduced
in concentration
in the
residuals
(e.g., Total
Organic Carbon can often be used as an
indicator parameter for the
biodegradation of many organic
constituents that cannot be directly
analyzed
in wastewater
residues).
CAREN Carbon adsorption
(granulated or powdered)
of non—metallic
inorcianics,
organo—metallics, and/or organic constituents,
operated such that a
surrogate compound or indicator parameter
has not undergone
breakthrough
(e.g., Total Organic Carbon can
often be used as
an
indicator parameter for the adsorption of
many organic constituents
that cannot be directly analyzed
in
wastewater residues). Breakthrough
occurs when the carbon has
become saturated with the constituent (or
indicator parameter)
and substantial change
in adsorption rate
associated with that
constituent occurs.
CHOXD Chemical or electrolytic oxidation utilizing the following
oxidation
reagents
(or waste reagents)
or combinations or
reagents:
fl
Hypochlonite
(e.g. bleach)
2J.
chlorine
~J.
chlorine dioxide
j~
ozone or UV (ultraviolet light)
assisted ozone
~J.
peroxides
~
persulfates
21
perchlorates
117—653

334
~
permangantes;
and/or
~
other oxidizing reagents of equivalent
efficiency,
performed in
units operated such that a surrogate compound on indicator
parameter has been substantially reduced
in concentration in the
residuals
(e.g., Total Organic Carbon
can often be used as an
indicator parameter for the oxidation of
many organic
constituents that cannot be directly analyzed in
wastewater
residues). Chemical oxidation specifically includes
what
is
commonly referred to as alkaline chlorination.
CHRED Chemical reduction utilizing the following reducinci reagents
(or
waste
neagents) or combinations of reagents:
fl
Sulfur dioxide
21
sodium,
potassium,
or alkali salts of sulfites, bisulfites,
metabisulfites,
and polyethylene glycols
(e.g.,
NaPEG and KPEG)
~j
sodium hydrosulfide
41
ferrous salts; and/or
~
other reducing reagents of equivalent efficiency, performed in
units
operated such that a surrogate compound or indicator
parameter
has been substantially reduced in concentration in the
residuals
(e.g., Total Organic Halogens can often be used as an
indicator
parameter for the reduction of many halocienated organic
constituents that cannot be directly analyzed
in wastewater
residues). Chemical reduction
is commonly used for the reduction
of hexavalent chromium to the trivalent state.
DEACT Deactivation to remove the hazardous characteristics of
a waste
due to
its
ignitability, corrosivity,
and/or reactivity.
FSUBS Fuel substitution in units operated in accordance with applicable
technical operating requirements.
HLVIT Vitrification of high level mixed radioactive wastes in units
in
compliance with all applicable radioactive protection
requirements
under control of the Nuclear Regulatory Commission.
IMERC Incineration of wastes containing organics and mercury
in units
operated
in accordance with the technical operating requirements
of
35
Ill. Adm. Code 724.Subpart 0 or 725.Subpart 0.
All wastewater and
nonwastewater residues derived from this
process must then comply with
the corresponding treatment
standards per waste code with consideration
of any applicable
subcategories
(e.g., High or Low Mercury
Subcategories).
117—654

335
INCIN Incineration
in units operated
in accordance with the technical
operating requirements of
35
Ill. Adm. Code 724.Subpart 0 or 725.Subpart
0.
LLEXT Liquid-liquid extraction
(often referred to as solvent
extraction)
of
organics from liquid wastes into an immiscible
solvent for which the
hazardous constituents have a greater
solvent affinity,
resultinci in an
extract high in organics that
must undergo either incineration,
reuse
as a fuel, or other
recovery/reuse and a raffinate (extracted liquid
waste)
proportionately low in organics that must undergo further
treatment as specified
in the standard.
MACRO Macroencapsulation with surface coating materials such as
polymeric
organics
(e.g.
resins and plastics)
or with a lacket
of inert inorganic
materials to substantially reduce surface
exposure to potential
leaching media. Macroencapsulation
specifically does not include any
material that would be
classified as
a tank or container according to
35
Ill.
Adm. Code 720.110.
NEUTR Neutralization with the following reagents
(or waste reagents)
or
combinations of reagents:
fl
Acids
21
bases;
or
~
water
(including wastewaters) resulting in
a PH greater than
2
but
less than 12.5 as measured
in the aqueous residuals.
NLBBR No land disposal based on recycling.
PRECP Chemical precipitation of metals and other inorganics as
insoluble
precipitates of oxides,
hydroxides, carbonates,
sulfides,
sulfates,
chlorides,
flourides,
or phosphates.
The
following reagents
(or waste
reagents)
are typically used alone
or
in combination:
fl.
Lime (i.e.,
containing oxides and/or
hydroxides of calcium and/or
magnesium
21
caustic
(i.e.,
sodium and/or potassium hydroxides
~
soda ash
(i.e.,
sodium
carbonate)
4j
sodium sulfide
jj
ferric sulfate or ferric
chloride
~j
alum;
or
21
sodium sulfate. Additional
floculating,
coagulation,
or similar
reagents/processes that
enhance sludge dewatering characteristics
are not precluded from
use.
117—655

336
RBERY Thermal recovery of Beryllium.
RCGAS Recovery/reuse of compressed gases including techniques auch as
reprocessing of the ciases for reuse/resale; filtering/adsorption
of
impurities; remixina for direct reuse of resale;
and use of
the gas as
a fuel source.
RCORR
Recovery of acids or bases utilizing one or more of the following
recovery technolociies:
fl
Distillation
(i.e., thermal
concentration)i
21
ion exchancie
~J
resin or solid adsorption
41
reverse osmosis:
and/or
~1
incineration for the recovery of
acid——Note: this does not
preclude the use of other physical
phase separation or
concentration techniques such as
decantation, filtration
(including ultrafiltration),
and
centrifugation,
when used in
conlunction with the above listed
recovery technologies,
RLEAD
Thermal
recovery of
lead in secondary lead smelters.
RMERC Retorting or roasting in a thermal processing unit capable of
volatilizing mercury and subsequently condensing the volatilized mercury
for recovery. The retorting or roasting unit
(or facility)
must be
subiect to one or more of the following:
~
A
National Emissions Standard for Hazardous Air Pollutants
(NESHAP)
for mercury
(40 CFR 61,
Subpart E):
A Best Available Control Technology (BACT) or
a Lowest Achievable
Emission Rate (LAER)
standard for mercury imposed Pursuant tpa
Prevention of Significant Deterioration
(980) permit
(including 35
Ill. Mm.
Code 201 through 203);
or
A state permit that establishes emission limitations
(within
meaning of Section 302 of the Clean Air Act) for mercury,
including a permit issued pursuant to
35
Ill. Adm.
Code 201.
All
wastewater and nonwastewater residues derived from this process
must then comply with the corresponding treatment standards
per
waste code with consideration of any applicable subcategories
(e.g., High or Low Mercury Subcategories).
RMETL
Recovery of metals or inorganics utilizing one or more of the
followiflg
direct physical/removal technolocies:
1).
Ion exchange
117—656

337
21
resin or solid
(i.e.,
zeolites) adsorption
1).
reverse osmosis
41
chelation/solvent extraction:
j).
freeze
crystalization
~j.
ultrafiltration; and/or
6 simple
precipitation
(i.e
crvstalization)
Note:
this does not
preclude the use of other physical phase separation
or
concentration techniques such as decantation, filtration
(including
ultrafiltration), and centrifugation, when used
in
conjunction with the
above listed recovery technologies.
RORGS Recovery of organics utilizing one or more of the following
technologies:
1).
Distillation
21
thin
film evaporation
~J.
steam stripping
41
carbon adsorption
~1
critical fluid extraction
j~.
liquid-liquid extraction
2.1
Precipitation! crystallization (including freeze crystallization)
or
~j.
chemical phase separation techniques
(i.e., addition of acids,
bases,
demulsifiers,
or similar chemicals);
Note: This does not
preclude the use of other physical phase separation
techniques
such as decantation,
filtration
(including ultrafiltration),
and centrifugation, when used in conlunction with the above listed
recovery technologies.
RTHRN Thermal recovery of metals or inorganics from nonwastewaters in
units
defined as cement kilns,
blast furnaces,
smelting, melting and refining
furnaces,_combustion devices used to recover sulfur values from spent
sulfuric acid and
“other devices” determined by the Agency pursuant to
35 Ill.
Adm.
Code 720.110,
the definition of “industrial furnaces”.
RZINC Resmelting in for the purpose
of recovery of zinc high
temperature
metal recovery units.
117—657

338
STABL Stabilization with the following reagents
(or waste reagents) or
combinations of reagents:
fl
Portland cement;
or
21
lime/
pozzolans
(e.g..
fly ash and cement kiln dust)——this does
not
preclude the addition of reagents
(e.g.,
iron salts,
silicates,
and clays) designed to enhance the set/cure time
and/or
compressive strength, or to overall reduce the
leachability of
the metal or inorganic.
SSTRP Steam stripping of organics from liquid wastes utilizing direct
application of steam to the wastes operated such that liquid and
vapor
flow rates,
as well
as,
temperature and pressure ranges
have been
optimized, monitored,
and maintained. These operating
parameters are
dependent upon the design parameters of the unit
such as, the number of
separation stages and the internal column
design. Thus,
resulting
in a
condensed extract high
in organics
that must undergo either
incineration,
reuse as
a fuel, or other
recovery/reuse and an extracted
wastewater that must undergo
further treatment
as specified
in the
standard.
WETOX -Wet air oxidation performed in units operated such that
a
surrogate
compound or indicator parameter has been substantially
reduced in
concentration
in the residuals
(e.g.,
Total Organic
Carbon can often be
used
as an indicator parameter for the
oxidation of many organic
constituents that cannot be directly
analyzed
in wastewater residues).
WTRRX Controlled reaction with water
for highly reactive inorganic or
organic
chemicals with precautionary controls for protection of
workers from
potential violent reactions as well
as
precautionary controls for
potential emissions of toxic!
ignitable levels of gases released during
the reaction.
Note
1:
When a combination
of these technologies
(i.e.,
a treatment traipi
is
specified
as
a single treatment standard, the order of
4pplication is
specified
in Table
D by indicating the five letter
technology
code that must be applied first, then the designation
“fb.”
(an abbreviation
for “followed by”),
then the five letter
technology code for the technology
that must be applied next,
and
SO
on.
Note
2:
When more than one technology (or treatment train)
are specified
as
alternative treatment standards,
the five letter technology
codes
(or the
treatment trains)
are separated by a semicolon
(;1
with the last technology
preceded by the word “OR”.
This
indicates that any one of these BDAT
technologies or treatment
trains can be used for compliance with the
standard.
(Source:
Added
at
15
Ill.
Reg.
,
effective
117—658

339
Section 728.Table D
Technology—Based Standards by RCRA Waste Code
WASTE DESCRIP-
TIONS AND/OR
WASTE
TECHNOLOGY CODE
TREATMENT
CODES
SEE ALSO
CAS NO.
WASTEWATERS
NONWASTEWATERS
SUBCATEGORY
D001
DEACT
NA
Ignitable
Liquids based
on
35
Ill.
Adm. Code
721.121(a) (1)—
—wastewaters
DOO1
NA
DEACT
Ignitable
Liquids based
on 35
Ill.
Mm. Code
721.121(a) (1)—
-Low TOC
Ignitable
Liquids
Subcategory--
Less than 10
total organic
carbon
DOO1
NA
FSUBS;
Ignitable
RORGS; or
Liquids based
INCIN
on
35
Ill.
Adm. Code
721.121(a) (1)—
-High TOC
Ignitable
Liquids
Subcategorv--
Greater than
or
equal
to
10
total
organic carbon
DOOl
DEACT**
Ignitable
compressed
gases based on
35
Ill. Mm.
Code
721.121(a) (3)
D001
NA
NA
DEACT
Ignitable
reactives
35
Ill.
Adm. Code
721.121(a) (2)
117—659

340
0001
NA
DEACT
DEACT
Oxidizers
based on 35
Ill. Adm.
Code
721.121 (a) (4)
D002
NA
DEACT
DEACT
Acid
eubcategory
based on 35
Ill. Adm. Code
721.122(a) (1)
0002
NA
DEACT
DEACT
Alkaline
subcategory
based on
35
Ill.
Adm.
Code
721.122(a) (1)
D002
NA
DEACT
DEACT
Other
corrosives
based on 35
Ill.
Adxn. Code
721.122(a) (2)
D003
DEACT
BEACT
Reactive
sulfides based
on
35
Ill.
Adm.
Code
721.123(a) (5)
0003
NA
DEACT
DEACT
Explosives
based on 35
Ill.
Adm.
Code
721.123 (a) (6),
(7)
and
(8)
0003
NA
NA
BEACT
Water
reactives
based on 35
Ill.
Adin.
Code
721.123(a) (2J,
(3)
and
(4)
DOO3
NA
BEACT
DEACT
Other
reactives
based on 35
Ill.
Adm. Code
721.123(a) (1)
D006
7440-43—9
RTHERM
Cadmium
containing
batteries
117—660

341
0008
7439—82-1
NA
RLEAD
Lead acid
batteries
(Note:
This
standard only
a~~liesto
lead acid
batteries
that
are identified
as
RCRA
hazardous
wastes and
that are not
excluded
elsewhere from
regulation
under the land
disposal
restrictions
of -this Part
or exempted
under other
regulations
(see
35 Ill.
Adm. Code
726.180).)
D009
Tables
A & B
7439-87-6
NA
IMERC;
or
Mercury:
RMERC
(High Mercury
Subcategory-—
greater than
or equaL to
260 m~/kci
total
Mercury——
contains
mercury and
organics
(and
are not
incinerator
residues))
117—661

342
0009
Tables
A &
B 7439—87—6
NA
RMERC
Mercury:
(High Mercury
Subcategory-—
areater
than
or equal to
260 ma/ka
total
Mercury—-
inorganics
(including
incinerator
residues
and
residues from
RMERC))
0012
Table B
72-20-8
BIODG;
or
NA
Endrin
INCIN
D0l3
Table B
58-89-9
CAREN; or
NA
Lindane
INCIN
DO14
Table
B
72-43—6
WETOX;
or
~
Methoxychlor
INCIN
D0i5
Table B
8001-35-i
BlOBS;
or
NA
Toxaphene
INCIN
0016
Table B
94—75-7
CHOXD
NA
2,4-B
BIODG; or
INCIN
0017
Table B
93-72—1
CHOXB; or
NA
2,4,5—TP
INCIN
F005
Tables A
& B 79—46-9
(WETOX or
INCIN
2-Nitropropane
CHOXB)
fb
CARBN; or
INCIN
FOO5
Tables A
& B
110-80-5
BIODG; or
INCIN
INCIN
Ethoxyethanol
F024
Tables A &
B NA
INCIN
INCIN
K025
NA
LLEXT fb
INCIN
Distillation
SSTRIP
fb
bottoms from
CAREN; or
the production
INCIN
of
nitrobenzene
by the
nitration of
benzene
117—662

343
KO26
NA
INCIN
INCIN
Stripping
still tails
from the
Production of
methyl ethyl
pyridines
K027
NA
CARBN; or
FSUBS; or
Centrifucie and
INCIN
INCIN
distillation
residues from
toluene
diisocvanate
production
K039
NA
CARBN;
or
FSUBS; or
Filter cake
INCIN
INCIN
from the
filtration of
diethylphospho
rodithioc acid
in the
production of
phorate
K044
NA
BEACT
DEACT
Wastewater
treatment
sludges from
the
manufacturing
and processing
of explosives
K045
NA
DEACT
DEACT
Spent carbon
from the
treatment of
wastewater
containing
explosives
K047
NA
DEACT
BEACT
Pink/red water
from TNT
operations
117—663

344
Tables A & B NA
FSUBS; or
INCIN
Emission
control
dust/sludge
from secondary
lead smelting:
Non—Calcium
Sulfate
Subcategory
Wastewater
treatment
sludge from
the mercury
cell process
in chlorine
production:
(High Mercury
Subcategory-
greater than
or equal to
260 mg/kg
total mercury)
Condensed
liquid light
ends from the
purification
of
toluenediamine
in the
production of
toluenediamine
via
hydrogenation
of
dinitrotoluene
Table B
NA
Emission
control
dust/sludge
from the
primary
oroduction
NA
NA
NLDBR
RLEAD
of
steel
in
electric
furnaces
(High
KO61
KO69
Kl06
K113
Zinc
Subcategory--
greater
than
or
equal
to
15
total
Zinc)
Tables A &
B NA
RMERC
NA
CARBN; or
INCIN
117—664

345
K114
NA
CARBN;
or
FSUBS; or
Vicinals from
INCIN
INCIN
the
purification
of
toluenediame
in the
production of
toluenediamine
via
hydrogenation
of
dinitrotoluene
K115
NA
CARBN;
or
FSUBS; or
Heavy ends
INCIN
INCIN
from the
purification
of
toluenediame
in the
production of
toluenediamine
via
hydrogenation
of
dinitrotoluene
1(116
CARBN; or
FSUBS; or
Organic
INCIN
INCIN
condensate
from the
solvent
recovery
column
in the
production of
toluene
diisocyanate
via
phosgenat ion
of
toluenediamine
POOl
81-81-2
(WETOX
or
FSUBS; or
Warfanin
CHOXD)
fb
INCIN
(0.3)
CARBN; or
INCIN
P002
591—08—2
(WETOX or
INCIN
1—Acetyl-2—
CHOXD)
fb
thiourea
CARBN; or
INCIN
117—665

346
9003
107-02—8
(WETOX or
FSUBS; or
Acrolein
CHOXB)
fb
INCIN
CARBN; or
INCIN
9005
107-18-6
(WETOX or
FSUBS; or
Allvl alcohol
CHOXD)
fb
INCIN
CARBN;
or
INCIN
P006
20859-73-8
CHOXD;
CHOXD;
Aluminum
CHRED; or
CHRED;
or
phosphide
INCIN
INCIN
9007
2763—96—4
(WETOX or
INCIN
5—Aminoethyl
CHOXB)
fb
3-isoxazolol
CARBN; or
INCIN
P008
504—24—5
(WETOX or
INCIN
CHOXD)
fb
Axninopyridine
CARBN;
or
INCIN
9009
131—74-8
CHOXB;
FSUBS;
Arnmonium
CHRED;
CHOXD;
picrate
CARBN;
CHRED;
or
BIODG;
or
INCIN
INCIN
P014
108-95—5
(WETOX or
INCIN
Thiophenol
CHOXD)
fb
(Benzene
CARBN; or
thiol)
INCIN
P015
7440—41-7
NA
RNETL; or
Beryllium dust
RTHRM
P016
542—88—1
(WETOX or
INCIN
Bis(chloro-
CHOXB)
fb
methyl)ether
CARBN;
or
INCIN
P017
598-31-2
(WETOX or
INCIN
Bromoacetone
CHOXD)
fb
CARBN;
or
INCIN
P018
357—57-3
(WETOX or
INCIN
Brucine
CHOXD)
fb
CARBN; or
INCIN
117—666

347
P022
Table B
75-15-0
NA
INCIN
Carbon
disulfide
9023
107-20—0
(WETOX or
INCIN
Chloroaceta.de
CHOXD)
fb
hyde
CARBN;
or
INCIN
9026
5344-82—1
(WETOX or
INCIN
1—(o—Chloro-
CHOXD)
fb
phenvl)thio-
CARBN; or
urea
INCIN
P027
542—76-7
(WETOX or
INCIN
3—Chloro—
CHOXD)
fb
propionitrile
CARBN; or
INCIN
P028
100-44—7
(WETOX or
INCIN
Benzvl
CHOXD) fb
chloride
CARBN; or
INCIN
P031
460-19—5
CHOXD;
CHOXB;
Cyanogen
WETOX;
or
WETOX;
or
INCIN
INCIN
P033
506-77—4
CHOXB;
CHOXD;
Cyanogen
WETOX;
or
WETOX; or
chloride
INCIN
INCIN
P034
131-89-5
(WETOX or
INCIN
2-Cvclohexvl-
CHOXB)
fb
4,6—dinitro-
CARBN; or
phenol
INCIN
P040
297—97—2
CARBN; or
FSUBS;
or
0,0-Diethyl 0—
INCIN
INCIN
pyrazinyl
phosphoro-
thioate
P041
311—45-5
CARBN;
or
FSUBS;
or
Diethyl-p—
INCIN
INCIN
nitrophenyl
phosphate
P042
51—43-4
(WETOX
or
INCIN
Epinephrine
CHOXD)
fb
CARBN; or
INCIN
117—667

348
P043
55—91—4
CARBN; or
FSUBS; or
Diisopropyl-
INCIN
INCIN
fluoro-
phosphate
(DFP)
P044
60-51—5
CARBN;
or
FSUBS;
or
Dimethoate
INCIN
INCIN
P045
39196—18—4
(WETOX or
INCIN
Thiofanox
CHOXD)
fb
CARBN:
or
INCIN
P046
122-09—8
(WETOX or
INCIN
alpha,alpha—
CHOXD)
fb
Dimethylphen-
CAREN;
or
ethylamine
INCIN
P047
534—52—1
(WETOX or
INCIN
4,6—Dinitro—
CHOXB)
fb
o-cresol salts
CARBN;
or
INCIN
9049
541—53—7
(WETOX or
INCIN
2,4—Dithio—
CHOXD)
fb
biuret
CARBN;
or
INCIN
P054
151—56—4
(WETOX or
INCIN
Aziridine
CHOXB)
fb
CARBN; or
INCIN
P056
Table B
7782-41-4
NA
ABGAS
fb
Fluorine
NEtJTR
P057
640-19-7
(WETOX or
INCIN
Fluoro-
CHOXB)
fb
acetan’iide
CARBN; or
INC IN
P058
62—74-8
(WETOX or
INCIN
Fluoroacetic
CHOXD)
fb
acid, sodium
CARBN;
or
salt
INCIN
9062
757-58-4
CARBN; or
FSUBS or
Hexaethyl—
INCIN
INCIN
tetraphosphate
117—668

349
P064
624-83—9
(WETOX or
INCIN
Isocvanic
CHOXDI
fb
acid,
ethyl
CARBN; or
ester
INCIN
P065
Tables
A & B
628—86-4
NA
RNERC
Mercury
fulminate:
(Hiah Mercury
Subcategory--
areater than
or
equal
to
260
mg/kg
total
Mercury——
either
incinerator
residues or
residues
from
RMERC)
P065
Tables A
& B
628-86-4
NA
IMERC
Mercury
fulminate:
(All non—
wastewater
B
that are not
incinerator
residues from
RMERC;
regardless of
Mercury
Content)
P066
16752—77-5
(WETOX or
INCIN
Methomyl
CHOXD)
fb
CARBN;
or
INCIN
P067
75—55—8
(WETOX or
INCIN
2—Methyl—
CHOXD)
fb
azinidine
CARBN;
or
INCIN
P068
60-34-4
CHOXD;
FSUBS;
Methyl
CHRED;
CHOXD;
hydrazine
CARBN;
CHRED; OR
BlOBS; or
INCIN
INCIN
P069
75-86—5
(WETQX or
INCIN
Methyllacto—
CHOXB)
fb
nitrile
CARBN;
or
INCIN
117—669

350
9070
116-06-3
(WETOX or
INCIN
Aldicarb
CHOXD)
fb
CARBN;
or
INCIN
P072
86-88-4
IWETOX or
INCIN
1—Naphthyl-2-
CHOXD)
fb
thiourea
CARBN; or
INCIN
P075
54_1l_5*
(WETOX or
INCIN
Nicotine and
CHOXD)
fb
salts
CARBN;
or
INCIN
P076
10102-43—9
ADGAS
ADGAS
Nitric oxide
P078
10102-44—0
ABGAS
ABGAS
Nitrogen
dioxide
9081
55-63—0
CHOXD;
FSUBS;
Nitroglycerin
CHREB;
CHOXD;
CARBN;
CHREB;
or
BIODG;
or
INCIN
INCIN
P082
Table B
65-75—9
NA
INCIN
N—Nitrosodi-
methylamine
P084
4549—40-0
(WETOX or
INCIN
N—Nitroso—
CHOXD)
fb
methylvinyl-
CARBN;
or
amine
INCIN
P085
152—16—9
CARBN;
or
FSUBS; or
Octamethyl—
INCIN
INCIN
pyrophosphor-
amide
P087
20816-12—0
NA
RMETL; or
Osmium
RTHRM
tetroxide
P088
145-73-3
(WETOX or
FSUBS; or
Endothall
CHOXD)
fb
INCIN
CARBN; or
INCIN
117—670

351
P092
Tables A
& B
62—38-4
NA
RMERC
Phenyl mercury
acetate:
(High
Mercury
Subcategory-—
greater than
or equal to
260 mg/kg
total
Mercury——
either
incinerator
residues
or
residues
from
RNERC
I
9092
Tables A
&
B 62—38—4
NA
IMERC; or
Phenvl mercury
RMERC
acetate:
(All
nonwastewaters
that are not
incinerator
residues and
are not
residues from
RMERC:
regardless of
Mercury
Content)
9093
103-85-5
(WETOX or
INCIN
Phenylthio-
CHOXD)
fb
urea
CARBN; or
INCIN
P095
75—44-5
(WETOX or
INCIN
Phosgene
CHOXDI
fb
CARBN;
or
INCIN
9096
7803-51-2
CHOXD;
CHOXD;
Phosphine
CHRED; or
CHRED; or
INCIN
INCIN
P102
107-19-7
(WETOX or
FSUBS;
or
Propargyl
CHOXD)
fb
INCIN
alcohol
CARBN:
or
INCIN
P105
26628—22—8
CHOXB;
FSUBS:
Sodium azide
CHRED;
CARBN CHOXD;
BlOBS;
or
CHRED; or
INCIN
INCIN
117—671

352
P108
57_24_9*
(WETOX or
INCIN
Strychnine and
CHOXD)
fb
salts
CARBN; or
INCIN
9109
3689—24-5
CARBN; or
FSUBS; or
Tetraethyldi—
INCIN
INCIN
thiopyro-
phosphate
9112
509—14-8
CHOXD;
FSUBS;
Tetranitro-
CHRED;
CHOXD;
methane
CARBN;
CHRED;
or
BIODG; or
INCIN
INCIN
P113
Table B
1314-32-5
NA
RTHRM; or
Thallic oxide
STABL
P115
Table B
7446—18—6
NA
RTHRM;
or
Thallium
(I)
STABL
sulfate
9116
79—19-6
(WETOX or
INCIN
Thiosemi—
CHOXD)
fb
carbazide
CARBN;
or
INCIN
P118
75-70-7
(WETOX or
INCIN
Trichloro—
CHOXD)
fb
methanethiol
CARBN; or
INCIN
P119
Table
B
7803—55—6
NA
STABL
Ainmonium
vanadate
9120
Table
B
1314—62-1
STABL
Vanadium
pentoxide
P122
1314—84-7
CHOXD;
CHOXD;
Zinc Phosphide
CHREB; or
CHRED;
or
(10)
INCIN
INCIN
0001
75-07-0
(WETOX
or
FSUBS; or
Acetaldehyde
CHOXB)
fb
INCIN
CARBN;
or
INCIN
0003
Table
B
75—05-8
NA
INCIN
Acetonitrile
0006
75-36-5
(WETOX or
INCIN
Acetyl
CHOXD)
fb
chloride
CARBN;
or
INCIN
117—672

353
0007
79—06—1
(WETOX or
INCIN
Acrvlainide
CHOXD)
fb
CARBN; or
INCIN
0008
79—10-7
(WETOX or
FSUBS; or
Acrylic acid
CHOXD)
fb
INCIN
CA.RBN; or
INCIN
0010
50-07—7
(WETOX or
INCIN
Mitomvcin C
CHOXD)
fb
CARBN;
or
INCIN
0011
61-82-5
(WETOX or
INCIN
Amitrole
CHOXD)
fb
CARBN;
or
INCIN
0014
492-80-8
(WETOX or
INCIN
Auramine
CHOXD)
fb
CARBN; or
INCIN
13015
115—02—6
(WETOX or
INCIN
Azaserine
CHOXD)
fb
CARBN;
or
INCIN
0016
225—51-4
(WETOX or
FSUBS;
or
Benz(c)—
CHOXD)
fb
INCIN
acnidine
CARBN; or
INCIN
0017
98-87-3
(WETOX or
INCIN
Benzal
CHOXD)
fb
chloride
CARBN;
or
INCIN
0020
98-09-9
(WETOX or
INCIN
Benzene—
CHOXD)
fb
sulfonvl
CARBN;
or
chloride
INCIN
0021
92-87—5
(WETOX or
INCIN
Benzidine
CHOXB)
fb
CARBN; or
INCIN
117—673

354
0023
98—07-7
CHOXD;
FSUBS;
Benzotri—
CHRED;
CHOXB;
chloride
CARBN;
CHRED;
or
BIODG; or
INCIN
INCIN
U026
494-03-1
(WETOX or
INCIN
Chiornaphazin
CHOXD)
fb
CARBN;
or
INCIN
0033
353-50-4
(WETOX or
INCIN
Carbonyl
CHOXD)
fb
fluoride
CARBN;
or
INCIN
13034
75-87—6
(WETOX or
INCIN
Trichloroacet—
CHOXD)
fb
aldehyde
CARBN; or
(Chloral)
INCIN
0035
305—03—3
(WETOX or
INCIN
Chlorambucil
CHOXD)
fb
CARBN;
or
INCIN
0038
Table
B
510-15-6
NA
INCIN
Chloro—
benzilate
0041
106—89—8
(WETOX or
INCIN
1—Chloro—2,3—
CHOXD)
fb
epoxypropane
CARBN;
or
(Epichloro-
INCIN
hydrin)
U042
Table B
110-75—8
NA
INCIN
2—Chloroethyl
vinyl ether
0046
107-30-2
(WETOX or
INCIN
Chloromethyl
CHOXD)
fb
methyl ether
CARBN; or
INCIN
0049
3165-93-3
(WETOX or
-
INCIN
4—Chloro-o—
CHOXD)
fb
toluidine
CARBN;
or
hydrochloride
INCIN
0053
4170-30—3
(WETOX or
FSUBS; or
Crotonaldehyde
CHOXD)
fb
INCIN
CARBN; or
INCIN
117—674

355
U055
98—82-8
(WETOX or
FSUBS;
or
Cumene
CHOXD)
fb
INCIN
CARBN;
or
INCIN
0056
110-82—7
(WETOX
or
FSUBS;
or
Cyclohexane
CHOXD)
fb
INCIN
CARBN;
or
INCIN
U057
Table
B
108-94—1
NA
F’SUBS; or
Cvclohexanone
INCIN
13058
50—18—0
CAREN;
or
FSTJBS; or
Cvclophosph-
INCIN
INCIN
amide
U059
20830—81-3
(WETOX or
INCIN
Daunomycin
CHOXD)
fb
CARBN; or
INCIN
0062
2303—16—4
(WETOX or
INCIN
Diallate
CHOXD)
fb
CARBN;
or
INCIN
13064
189—55—9
(WETOX or
FSUBS; or
1,2.7,8—Di—
CHOXD)
fb
INCIN
benzopyrene
CARBN; or
INCIN
0073
91—94—1
(WETOX or
INCIN
3,3~—Dichloro—
CHOXB)
fb
benzidine
CARBN; or
INCIN
0074
1476—11—5
(WETOX or
INCIN
cia—1,4—Di—
CHOXD)
fb
chloro—2-
CARBN;
or
butene; trans-
INCIN
3.,4-Dichloro—
2-butene
U085
1464—53-5
(WETOX or
FSUBS; or
1,2:3,4-Di—
CHOXD)
fb
INCIN
epoxybutane
CARBN; or
INCIN
0086
1615—80—1
CHOXD;
FSUBS;
N,N-Diethvl—
CHRED; CARBN CHOXD;
hydrazine
BIODG;
or
CHRED;
or
INCIN
INCIN
117—675

356
13087
3288-58—2
CARBN; or
FSUBS; or
O,O—Diethyl S—
INCIN
INCIN
methyldithio-
phosphate
U089
56—53—1
(WETOX or
FSUBS: or
Diethvl
CHOXD)
fb
INCIN
etilbestrol
CARBN;
or
INCIN
UO9O
94—58—6
(WETOX
or
FSUBS;
or
Dihydrosafrole
CHOXD)
fb
INCIN
CARBN;
or
INCIN
U09i
119—90—4
(WETOX or
INCIN
3,3’—Di—
CHOXD)
fb
methoxy-
CA.RBN;
or
benzidine
INCIN
U092
124-40-3
(WETOX or
INCIN
Dimethylamine
CHOXD)
fb
CARBN;
or
INCIN
13093
Table B
621-90-9
NA
INCIN
p—Dimethyl—
ammbaZO—
benzene
U094
57—97—6
(WETOX or
FSUBS;
or
7,12—Dimethyl—
CHOXD)
fb
INCIN
benz(a)-
CARBN;
or
anthracene
INCIN
0095
119-93-7
(WETOX or
INCIN
3,3’—Dimethyl-
CHOXB)
fb
benzidine
CARBN;
or
INCIN
U096
80—15—9
CHOXB;
FSUB5;
alpha,alpha-
CHRED; CARBN CHOXD
Dimethyl—
BIODG; or
CHRED;
or
benzvl hydro—
INCIN
INCIN
peroxide
U097
79—44—7
(WETOX or
INCIN
Dimethyl—
CHOXD)
fb
carbamoyl
CARBN;
or
chloride
INCIN
117—676

357
0098
57—14—7
CHOXD;
FSUBS;
1,1—
CHRED;
CHOXD;
Dimethylhydraz
CARBN;
CHRED; or
~
BIODG; or
INCIN
INCIN
0099
540—73—8
CHOXD;
FSUBS;
1,2-Dixnethyl—
CHRED;
CHOXD;
hydrazine
CARBN;
CHRED;
or
BIODG;
or
INCIN
INCIN
U1O3
77-78-1
CHOXD;
FSUBS;
Dimethvl
CHRED;
CHOXD;
sulfate
CARBN;
CHRED;
or
BIOBG; or
INCIN
INCIN
Ui09
122-66—7
CHOXD;
FSUBS;
1,2—Diphenyl—
CHRED;
CHOXD;
hydrazine
CARBN;
CHRED;
or
BIODG; or
INCIN
INCIN
0110
142-84—7
(WETOX or
INCIN
Dipropylamine
CHOXD)
fb
CAREN;
or
INCIN
0113
140-88-5
(WETOX or
FSUBS;
or
Ethyl acrylate
CHOXD)
fb
INCIN
CARBN;
or
INCIN
U114
111—54-6
(WETOX or
INCIN
Ethylenebis—
CHOXD)
fb
dithiocarbamic
CARBN; or
acid
INCIN
U115
75-21—8
(WETOX or
CHOXD;
or
Ethylene oxide
CHOXD)
fb
INCIN
CARBN;
or
INCIN
U116
96-45—7
(WETOX or
INCIN
Ethylene thio—
CHOXD)
fb
urea
CARBN; or
INCIN
117—677

358
13119
62-50-0
(WETOX or
INCIN
Ethyl methane-
CHOXD)
fb
sulfonate
CARBN; or
INCIN
0122
50-00-0
(WETOX or
FSUBS;
or
Formaldehyde
CHOXD)
fb
INCIN
CARBN;
or
INCIN
13123
64—18—6
(WETOX or
FSIJBS; or
Formic acid
CHOXDI
fb
INCIN
CARBN;
or
INCIN
U124
110-00—9
(WETOX or
FSUBS;
or
Furan
CHOXB)
fb
INCIN
CAREN;
or
INCIN
0125
98—01—1
(WETOX or
FSUBS; or
Furfural
CHOXB)
fb
INCIN
CARBN;
or
INCIN
13126
765—34—4
(WETOX or
FSUBS;
or
Glycidaldehyde
CHOXB)
fb
INCIN
CARBN;
or
INCIN
0132
70-30—4
(WETOX or
INCIN
Hexachloro—
CHOXD)
fb
phene
CARBN; or
INCIN
0133
302-01-2
CHOXD;
FSUBS;
Hydrazine
CHRED;
CARBN CHOXD;
BlOBS; or
CHRED;
or
INCIN
INCIN
13134
Table
B
7664-39—3
NA
ABGAS fb
Hydrogen
NEUTR;
or
Fluoride
NEUTR
0135
7783—06-4
CHOXD;
CHOXD;
Hydrogen
CHRED;
or
CHRED; or
Sulfide
INCIN
INCIN
13143
303-34-4
(WETOX or
INCIN
Lasiocarpine
CHOXD)
fb
CARBN;
or
INCIN
117—678

359
13147
108-31—6
(WETOX or
FSUBS;
or
Maleic
CHOXD)
fb
INCIN
anhvdride
CARBN; or
INCIN
0148
123—33—1
(WETOX or
INCIN
Maleic
CHOXO)
fb
hydrazide
CARBN; or
INCIN
0149
109-77-3
(WETOX or
INCIN
Malononitrile
CHOXD)
fb
CARBN;
or
INCIN
U15O
148—82-3
(WETOX or
INCIN
Melphalan
CHOXD)
fb
CARBN:
or
INCIN
U151
Tables A
& B
7439—97—6
NA
RNERC
Mercury:
(High Mercury
Subcategory——
greater than
or equal to
260 ma/kci
total Mercury)
13153
74-93—1
(WETOX or
INCIN
Methanethiol
CHOXD)
fb
CARBN;
or
INCIN
0154
67-56-1
(WETOX or
FSUBS; or
Methanol
CHOXD)
fb
INCIN
CARBN;
or
INCIN
0156
79-22-1
(WETOX or
INCIN
Methyl chioro-
CHOXD)
fb
carbonate
CARBN;
or
INCIN
U160
1338-23—4
CHOXB;
FSUBS;
Methyl ethyl
CHRED; CARBN CHOXD;
ketone
BIODG; or
CHRED; or
peroxide
INCIN
INCIN
117—679

360
0163
70-25-7
(WETOX
or
INCIN
N-Methyl—N’-
CHOXD)
fb
nitro-N-
CARBN; or
Nitroso-
INCIN
auanidine
13164
56-04-2
(WETOX or
INCIN
Methvlthio-
CHOXD)
fb
uracil
CARBN;
or
INCIN
U166
130—15—4
(WETOX or
FSUBS;
or
l,4-Naphtho—
CHOXD)
fb
INCIN
guinone
CARBN;
or
INCIN
U167
134-32—7
(WETOX or
INCIN
1—Naphthlv-
CHOXD)
fb
amine
CARBN;
or
INCIN
0168
Table B
91-59-B
NA
INCIN
2—Naphthyl-
amine
13171
79-46-9
(WETOX or
INCIN
2-Nitropropane
CHOXD)
fb
CARBN;
or
INCIN
U173
1116-54-7
(WETOX or
INCIN
N-Nitroso-di-
CHOXD)
fb
ethanolamine
CARBN;
or
INCIN
0176
759-73-9
(WETOX or
INCIN
N-Nitroso-N-
CHOXD)
fb
ethylurea
CARBN; or
INCIN
13177
684-93-5
(WETOX or
INCIN
N-Nitroso—N-
CHOXD)
fb
methylurea
CARBN;
or
INCIN
0178
615-53-2
(WETOX or
INCIN
N—Nitroso—N—
CHOXD)
fb
methylurethane
CARBN; or
INCIN
U182
123-63-7
(WETOX or
FSUBS;
or
Paraldehyde
CHOXD)
fb
INCIN
CA.RBN;
or
INCIN
117—680

361
U184
76-01-7
(WETOX or
INCIN
Pentachioro-
CHOXD)
fb
ethane
CARBN; or
INCIN
13186
504-60—9
(WETOX or
FSUBS; or
1,3—Pentadiene
CHOXBI
fb
INCIN
CARBN;
or
INCIN
U189
1314-80-3
CHOXO;
CHOXD;
Phosphorus
CHRED;
or
CHRED;
or
sulfide
INCIN
INCIN
Ul9i
109-06-8
(WETOX or
INCIN
2-Picoline
CHOXD)
fb
CARBN;
or
INCIN
Ul93
1120-71—4
(WETOX or
INCIN
1,3—Propane
CHOXD)
fb
sultone
CARBN; or
INCIN
0194
107-10—8
(WETOX or
INCIN
n-Propylamine
CHOXD)
fb
CARBN: or
INCIN
Ul97
106—51—4
(WETOX or
FSUBS; or
p—Benzoquinone
CHOXD)
fb
INCIN
CARBN; or
INCIN
0200
50-55—5
(WETOX or
INCIN
Reserpine
CHOXD)
fb
CARBN;
or
INCIN
U201
108-46-3
(WETOX or
FSUBS; or
Resorcinol
CHOXD)
fb
INCIN
CARBN;
or
INCIN
13202
8i_07_2*
(WETOX or
INCIN
Saccharin and
CHOXD)
fb
salts
CARBN; or
INCIN
117—681

362
0206
18883-66—4
(WETOX or
INCIN
Streptozatocin
CHOXD)
fb
CARBN;
or
INCIN
13213
109-99—9
(WETOX or
FSUBS; or
Tetrahydro-
CHOXDI
fb
INCIN
furan
CARBN; or
INCIN
0214
Table B
563—68-8
NA
RTHRN;
or
Thallium
(II
STABL
acetate
U215
Table B
6533—73—9
NA
RTHRM;
or
Thallium
(I)
STABL
carbonate
U216
Table
B
7791—12-0
NA
RTHRM;
or
Thallium
(I)
STABL
chloride
0217
Table B
10102-45—1
NA
RTHRM;
or
Thallium
(I)
STABL
nitrate
13218
62-55—5
(WETOX or
INCIN
Thioacetamide
CHOXD)
fb
CARBN;
or
INCIN
U2l9
62-56-6
(WETOX or
INCIN
Thiourea
CHOXB)
fb
CARBN; or
INCIN
U221
25376-45-8
CAREN;
or
FSUBS;
or
Toluenediamine
INCIN
INCIN
0222
636—21-5
(WETOX or
INCIN
o-Toluidirie
CHOXD)
fb
hydrochloride
CARBN;
or
INCIN
U223
26471—62—5
CARBN; or
FSUBS; or
Toluene diiso—
INCIN
INCIN
cyanate
13234
99-35—4
(WETOX or
INCIN
sym-Trinitro-
CHOXD)
fb
benzene
CARBN; or
INCIN
13236
72-57-1
(WETOX or
INCIN
Trypan Blue
CHOXD)
fb
CARBN; or
INCIN
117—682

363
U237
66-75—1
(WETOX or
INCIN
Uracil mustard
CHOXD)
fb
CARBN; or
INCIN
U238
51—79—6
(WETOX or
INCIN
Ethyl
CHOXD)
fb
carbamate
CARBN; or
INCIN
0240
94_75_7*
(WETOX or
INCIN
2,4—Dichloro—
CHOXD)
fb
phenoxyacetic
CARBN;
or
acid
(salts
INCIN
and esters)
U244
137—26—8
(WETOX or
INCIN
Thirani
CHOXD)
fb
CARBN;
or
INCIN
U246
506-68-3
CHOXB;
CHOXD;
Cyanogen
WETOX; or
WETOX; or
bromide
INCIN
INCIN
U248
81—81—2
(WETOX or
FSUBS;
or
Warfarin
CHOXB)
fb
INCIN
(greater than
CARBN;
or
or equal to
INCIN
13249
1314—84-7
CH0XD;
CHOXD;
Zinc Phosphide
CHRED; or
CHRED: or
(10)
INCIN
INCIN
*
CAS Number given for parent compound only.
**
This waste code exists
in gaseous form and
is not categorized as
wastewater or nonwastewater forms.
NA
Not Applicable.
BOARD NOTE:
When a combination of these technologies
(i.e.,
a treatment
train)
is specified as a single treatment standard,
the order of application
is specified in this Table by indicating the five letter technology code that
must be applied first, then the designation
“fb”
(an abbreviation for
“Followed by”),
then the five letter technology code for the technology that
must be applied next,
and so on.
When more than one technology
(or treatment
train)
are specified a alternative treatment standards, the five letter
technology codes
(or the treatment trains)
are separated by
a semicolon
(;)
with the last technology preceded by the word “or”.
This
indicates that any
one of these BDAT technologies or treatment trains can be used for compliance
with the standard.
See Section 728.Table C
for a listing of the technology
117—683

364
codes and technology-based treatment standards.
Derived from 40 CFR 268.42,
Table
2,
as adopted
at
54 Fed. Req.
22694, June
1,
1990.
(Source:
Added at
15
Ill.
Reg.
,
effective
)
117—684

365
Section 728.Table E
Standards for Radioactive Mixed Waste
TECHNOLOGY CODE
WASTE
NON-
WASTE DESCRIPTIONS AND/OR
CODES CAS NO.
WASTEWATERS WASTEWATERS TREATMENT SUBCATEGORY
D0O2
NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the Reprocessing of
Fuel Rods Subcateqory
0004
NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the Reprocessing of
Fuel Rods Subcategory
0005
NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the Reprocessing of
Fuel Rods Subcategory
0006
NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the Reprocessing of
Fuel Rods Subcategory
0007
NA
NA
HLVIT
Radioactive High Level Wastes
~Generated During the Reprocessing of
Fuel Rods Subcateqory
0008
7439-92—1
NA
MACRO
Radioactive Lead Solids Subcategory
(Note; these lead solids include,
but
are not limited to,
all forms of
lead shielding,
and other elemental
forms
of
lead.
These lead solids do
not include treatment residuals such
as hydroxide sludges,
other
wastewater treatment residuals,
or
incinerator ashes that
can undergo
conventional pozzolanic
stabilization, nor do they include
organo—lead materials that can be
incinerated and stabilized
as ash.)
DOO8
NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the Reprocessing of
Fuel Rods Subcategory
DOO9
7439-97-6
NA
AMLGM
Elemental mercury contaminated with
radioactive materials
0009
7439-97-6
NA
INCIN
Hydraulic oil contaminated with
MercurY Radioactive Materials
Subcategory
117—685

366
0009
NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the Reprocessing of
Fuel Rods Subcategory
0010
NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the Reprocessing of
Fuel Rods Subcategory
0011
NA
NA
HLVIT
Radioactive High Level Wastes
Generated During the Reprocessing of
Fuel Rods Subcategory
Ui51
7439-97-6
NA
AMLGM
Mercury: Elemental mercury
contaminated with radioactive
materials
NA-—Not Applicable.
(Source:
Added at
15
Ill.
Reg.
,
effective
117—686

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