ILLINOIS POLLUTION CONTROL BOARD
October
14,
1971
U.
S.
INDUSTRIAL
CHEMICALS
COMPANY
#71—44
v.
ENVIRONMENTAL PROTECTION
AGENCY
JAMES
F. LEMNA
(LEMNA & LEE),
AND
OWEN RALL
(PETERSON,
LOWRY,
RALL,
BARBER
&
ROSS),
ATTORNEYS
FOR
PETITIONER
FRED
PRILLAMAN,
JOHN
McCREERY
AND
THOMAS
SCHEUNENAN,
ATTORNEYS
FOR
ENVIRONMENTAL
PROTECTION
AGENCY
OPINION
OF
THE
BOARD
(BY
MR.
LAWTON):
Petition for variance was filed by
U.
S.
Industrial
Chemicals
Company,
a Division of National Distillers
and Chemical Corporation,
for variance
from the particulate emission limitations contained
in
the Rules
and Regulations Governing the Control of Air Pollution
relative
to the operation of
its five coal-fired boilers and
the
operation of
its sulphuric acid plant.
An electrostatic precipitator
has been installed
on one boiler which is presumably
being operated
in conctiance with
the Reculations,
The petitioner states that it is in the process of installing
electrostatic precipitators
to control the particulate emissions from
the
boiler operation pursuant to
a previous Air Contaminant Emission
Reduction Program
(Acerp)
approved by
the Illinois ~ir Pollution
Control Board and that the
new
hydration alcohol unit presently under
construction,
also pursuant to
a previously
approved Acerp,
will
suoplant the sulphuric
acid unit,
thereby eliminating
all emissions
from this source.
The Tuscola plant
of U,
S.
Industrial Chemicals Company manu-
factures
petrochemical
products
and
chemicals
for
use both
as
checical
feedstock
and
for
sale.
Among
the
petrochemical
products
manufactured
are two licuified petroleum gases,
propane and butane,
s~’ntheticethyl alcohol,
ethylene, diethyl ether
and polyethylene resins.
Inorganic chemicals manufactured
are sulfuric
and phosphoric
acid.
The foregoing products
are manufactured in several interrelated
units
all dependent upon
a 35,000 kilowatt power unit which is
a
prirciary source of air pollution.
The power plant provides
approx—
iraately
one-third
of
the
electricity
used
by
petitioner,
as
well
as the heating and motive steam used for refrigeration and gas compres-
sion in the petrochemical
complex.
The plant’s fiv,~boilers burn
400,000
to 500,000
tons of coal annually,
and generate
~an
amount
2
591
of
steam
equivalent
to that needed to supply
a city of 100,000
population with electricity.
The initial operation in the processing chain is the hydro-
carbon recovery
unit consisting of extraction and fractionation
elements.
Of
the one—half billion cubic feet of natural gas Pan-
handle Eastern Pipeline Co.
supplies the plant daily,
2
is removed
for
fuel,
and 8
is removed by
the extraction unit for processing
and retention in the form of liquified petroleum gases.
The re-
maining 90
is transmitted back
to Panhandle Eastern Pipeline Com-
pany for uses by its other customers.
This re—transmitted portion
consists primarily of methane,
which is suitable as fuel but un-
suitable as chemical feedstock.
Petitioner~spresent arrangement
with
its
gas supplier does not allow
use. of this residual
90
for
fuel burning.
Extraction occurs by contacting the natural gas with
a cold,
light oil which
absorbs
the heavy hydrocarbon components
of the gas.
The absorption oil is then sent to large absorption towers.
Heat
is applied to vaporize the desired hydrocarbons, which vapors
are
collected at the top of the towers and condensed
to recover mixed
hydrocarbons
at
a rate of
700 gallons per minute,
These hydrocarbons,
in
turn,
are pumped to the fractionation unit where through distil-
lation,
the hydrocarbon mixture
is divided into its components
—-
ethane
(15-20 Million Cubic Feet per day), propane
(400,000
-
500,000
gallons per day)
,
butane
(100,000
gallons
per day),
and gasoline
(25,000 to 30,000 gallons per day)
.
About
41
million gallons of the
propane and butane
are stored
at the plant,
largely
in
a limestone
strata 400 feet underground, for seaspnal sales.
The extracted ethane
is transferred
as
a chemical~feedstock
to
the ethylene unit,
A series of heatuinduced catalytic reactions,
gas com-
pression and separation converts
the ethane to ethylene,
the active
m~terialin the production of all of the petrochemicals produced
at the plant.
It becomes the feedstock
for the alcohol unit,
the
diethyl ether unit and
the polyethylene units.
The alcohol unit, which is
a mainstay of
U.
S. Industrial
Chemicals
Co., currently
relies on
the acid ester process for pro-
ducing synthetic ethyl alcohol from ethylene.
The ethylene is
dissolved in 98,5
concentrated sulfuric acid to produce ethyl sul-
fates which are then contacted with water in
a hydrolizer,
from
which reaction is produced ethyl alcohol, diethyl ether and dilute
sulfuric acid
(50
concentration)
.
The alcohol
(190 proof;
50-60
million gallons per year)
and
the ether
(5-10 million gallons per
year)
are purified
and sold,
The ether is used for pharmaceuticals
and for chemical solvents and reactants.
The sulfuric acid plant and the phosphoric acid plant
(now
shut down
are inextricably related to the production of alcohol and
diethyl ether,The primary purpose of the sulfuric
acid unit is to supply the
2
—
592
1,000 tons
of 98.5
concentrated sulfuric acid needed daily
in the
alcohol unit.
This is done by reconcentrating
a portion of the 2,000
tons
of
50
concentrated acid produced in the alcohol unit daily,
and recycling it through the
alcohol unit,
The primary purpose of
the phosphoric acid unit is to assist in the disposal of
40
of the
dilute
acid
generated
by
the
alcohol
unit.
This
dilute
acid
is
mixed
with
ground
phosphate
rock
to
produce
phosphoric
acid
which
is
marketed
Evaporation
of
the
water
under
closely
controlled
temperatures
permits
reconcentration
of
the
“black
acid”
to
85,
The
remainder
of the concentration,
up to 98.5,
is accomplished by adding sulphur
trioxide to the black acid.
Sulphur trioxide production
(SO3)
is initiated in the drying
unit by absorbing water vapor from air pumped through
a “drying tower”.
This dry air is then pumped to a sulphur burner where 10
of the com-
bustion gases
is sulphur trioxide,
The SO3
is sent to the absorption
towers, large brick—lined vessels containing packing designed to dis-
tribute evenly downflowing concentrated acid and upflowing SO3,
The
SO3 is absorbed and dilute acid is then injected into the towers to
stabilize the concentration at 98,5,
SO3 vapors leave these two
“black acid” towers and are vented with vapors from
a third absorption
tower through
a 200
foot stack
to the atmosphere, which emissions are
partially abated by
“demisters” composed of packing.
The third ab-
sorption tower produces virgin acid,
part of which
is sold and part
of which
is utilized both in the drying tower for absorbing water vapor
from incoming air and in the acid reconcentration process in the black
acid towers.
Four hundred tons per day of sulfuric acid are produced
by the reconcentration process and by
the virgin acid tower,
The
reconcentrated black acid and the unsold virgin acid are stored for
recycle back to the alcohol unit.
The remaining units, which do not appear to be sources
of
emission to the atmosphere,
are the polyethylene unit which relies for
its feedstock on the ethylene unit and the denaturing unit which
renders
the alcohol unpotable.
The foregoing description of the petitioner’s operation is
necessary, both to evaluate the propriety of the variance petition
and the contentions raised by the Environmental Protection ~gency
in opposition to its allowance.
As noted above,
the petition for variance requests permission
to continue
the operation of the
four coal—fired boilers and the re-
sulting
fly
ash emissions beyond
the limits prescribed by regulation,
end~
ing the installation of electrostatic precipitators,the
installation oE
2
—
593
which has been approved pursuant
to
a time schedule contained in an
Air Contaminant Emission Reduction Program
(Acerp)
granted by the
Illinois Pollution Control Board on August
5,
1969,
as will be more
fully described below.
The variance
also requests permission to
continue operation of the sulfuric acid unit, pending construction of
a direct hydration industrial alcohol
unit
presently under construc-
tion,
completion of which
is contemplated for March
30,
1972,
at which
time the sulphuric acid plant will shut down,
The variance petition alleges the employment of 1,042
employees
and an annual payroll of $10,800,000.00,
and that $152,000,000.00
have been invested in “buildings,
land improvements, pollution con-
trol devices and operating equipment”
during the last nineteen years,
14,000 tons
of natural gas
(520,000,000 cubic feet)
,
172
tons of
sulphur,
270 tons
of phosphate rock and 1,400
tons
of coal
are used
daily by petitioner in its manufacturing process.
The ethane,pro-
PanU,I butane and gasoline extracted from the natural gas total
2,040
tons per day.
Ethane is converted to ethylene for further
processing
to ethyl alcohol and polyethylene, propane, butane and
gas
are sold to commercial distributors
for heating,
industrial appli-
cation and motor fuel,
Sulphur is converted to sulphuric acid used
in the manufacture
of ethyl alcohol.
Sulphuric acid used in the
alcohol operation is reacted with phosphate rock to produce fertilizer.
Some high quality sulphuric acid is marketed.
Coal
is used to fire
the
five boilers which generate steam
for in—plant use,
as well
as
30
of the electric power used by the plant.
Petitioner represents that
three hydrocarbon double flares are employed for safety reasons,
equipped with smokeless
flare tips which do not constitute
a source
of pollution.
1,5 pounds of uncollected
fly ash are emitted per
million BTU’s fired from the coal boilers.
40 mil1igr~amsof parti-
culates
are emitted from the sulphuric acid unit per cubic foot of
stack gas.
Pursuant to Pollution Control Board Rule 310,
the Hearing
Officer allowed intervention of the following organizations:
Phillips Petroleum Company
Industrial Water Supply
Eastern Illinois Water Company
Morris Construction Company
Rottman—Hoke Construction Company
Tuscola Chamber
of Commerce
Ecoff Trucking Company
J.
L.
Allen Company
Quality Wood Products
The events leading up to the present variance petition
follow:
2
—
594
On July
14,
1969,
R.
H, Coleman, General Manager of Petition-
er, wrote
to
C.
W.
Klassen, Technical Secretary
of the
Air
Pollution
Control Board, proposing
as an Air Contaminant Emission Reduction
Program to control boiler emissions,
the purchase and installation
on Boiler
#1, of
a so-called Anderson Separator and Aerodyne Collec-
tor for completion by June,
1970, which,
if proven effective, would
be installed on two additional boilers by June,
1971 and on the
remaining two boilers by June,
1972.
The precise details of this
mechanism are of no current significance because the proposed Acerp
provided as follows:
“Should we
find
-
after our evaluation in the period
January
15 to June
1970
-
that the meChanical separabion
or collection equipment cannot be made to perform to meet
the emission standard,
an alternate plan will be followed
to bring the No.
1 Boiler into compliance by June 1971,
two additional boilers by June
1972,
and the remaining two
by
June
1973,
This
alternate
plan
takes
into
account
the
long
delivery
time
for
electrostatic
separation
and
collection
equipment
and
the
many
economic
factors
outlined
in
previous
correspon~nce and discussion.”
This proposed Acerp, including
the alternative proposal, was approved
by the Illinois Air Pollution Control Board on
August
6,
1969,
Tests
on the Anderson Aerodyne Collector demonstrated that this process
did not bring
the boiler emissions within the acceptable
limits,
(R. 349,
1756),
and,
accordingly,
the company embarked upon the
alternative program, providing
for the installation of electrostatic
precipitators
on all boilers,
in keeping with the
time
schedule
above outlined.
One precipitator has been installed on Boiler
#1
although continuing implementation of the program appears
to have
been suspended pending the present proceedings.
(R,l326-l327)
On August
20,
1968,
the petitioner wrote to
C. W. Klassen,
proposing
an
Acerp
for
its
sulphuric
acid
plant,
which
provided
for
modification and re-design of its acid distributor in the absorbers
and
for
the
use
of
i~proved
packing
which
would
provide
better
absorption of the SO
.
The
program
called
for
completion
by
October,
1970.
(Pet.
Ex.
19)
.
This program was approved by
the
Air Pollution Control Board on November
7,
1968
(Pet.
Ex,
20)
.
On
September
5,
1969,
R.
H. Coleman,
on behalf of petitioner,
advised
Mr. Kiassen that
a direct hydration alcohol plant had been authorized
which would supplant
the existing sulphuric acid plant used in the
alcohol manufacturing process.
This program was embodied in an
Acerp proposal dated September
15,
1969
and provided for shut-down
of the sulphuric
acid plant during the
last quarter of
1971, and
shut—down of the phosphoric
acid
unit
within
“six
months
to
one
year
later”.
(Variance
Pet.
Ex.
D)
.
As
an
alternate
to
the
pre-
viously
approved program, petitioner proposed installation in the
west black absorber of new acid distributor pans
and
a new York mesh
demister to replace the saddle-packed demister bed, which together
with improved liquid distribution was anticipated to improve re-
covery of the sulphur
trioxide,
This second Acerp was
approved
by
the Air Pollution
Control Board on September
29,
1969.
(Variance
Pet.
Ex.
E)
.
The record indicates
that this
program was
followed,
The variance petition alleges that while this construction
is
proceeding,
delays in delivery of major pieces of equipment require
suspending shut-down of the acid unit until the “first quarter of
1972”.
It
appears that the phosphoric acid plant
has
already been
shut down and that at least during the period of the hearing,
the
sulphuric acid plant has operated at levels complying with particulate
emission regulations,
although variance relative
to emissions from
this
plant
is
still
sought
pending
completion
of
the
direct
hydration
unit,
The petitioner asserts that denial of the variance will neces-
sitate complete shut-down of the entire industrial complex,
resulting
in
the
unemployment
of
1,042
employees,
the
loss
of
a $10,800,000
payroll,
the foreclosing
of
a major source of income to the suppliers
of coal, electric power
and water,
reduction in the open market of
one-fourth of the industrial alcohol produced in the United States,
and the elimination
of 500,000 gallons per day
of propane
as well
as large quantities
of diethyl ether from the open market,
The
Environmental
Protection
Agency
recommends
that
the variance
be denied,
The recommendation contains
a summary
of complaints
received
from
citizens
in the
area alleging excessive
odors,
smoke, fumes,
observed
damage
to
metal
surfaces
and extensive crop damage
as
a
consequence
of
particulate
and
fume
emissions.
The
position
of
the
Agency,
both
in
its
recommendation
and
as
developed
in~the
course
of
the proceeding,
is that
the variance should be denied for the follow-
ing
reasons:
1,
Petitioner constitutes
one
of the largest purchasers
of natural
gas, which the Agency asserts could be used
in its boiler operation and not only
as
a source of
supply
for
hydrocarbons
used
in
its
manufacturing
process;
2.
Petitioner could purchase low sulphur
coal
and
thereby
reduce
emissi~~nsof sulphur dioxide;
3,
Petitioner manufactures commercial fuel which could be
used
in
its
boilers
thereby
eliminating
the
need
for
coal burning;
4.
That
the
time
schedule
proposed
for
compliance
is
excessive
and
all
installations
could
be
made
within
a
one—year
period;
2
—
596
5.
Until such time as the new alcohol hydration plant is
in operation and the sulphuric acid plant shut down,
Petitioner could purchase the sulphuric acid used in
the alcohol process from commercial sources and thereby
eliminate the need for operation of the sulphuric acid
plant
and its resulting emissions.
Petitioner devoted the major part of its case to meeting the
contentions raised by the Agency as to the availability of alterna-
tive
fuels,
the acceleration
of the time schedule for installation
of the electrostatic precipitators and the desirability of sulphuric
acid
purchases
as
an
alternate
to
its
manufacture.
The unavailability of natural gas
for fuel purposes
and the
limitations
imposed
by
the
Federal
Power
Commission
were
adequately
set forth in the record
(R.l54—l59),
and support petitioner’s
position.
As previously noted, petitioner is required to re—transmit
the
methane
component
of the natural gas
after
the
hydrocarbon
stripping
has occurred.
The
record
demonstrates
a
shortage
of natural gas
-
which
is desperately
needed
elsewhere
as in metropolitan areas
where
there is a critical
need for alternatives to coal burning.
With re-
gard
to
the appropriateness
of burning low sulphur coal,
some
amount
of this
fuel
is available
in the western states.
However,
its use
would not solve the particulate problem
and
there has been
no
ade
-
quate proof
of
a sulphur problem calling for the use of this fuel.
The evidence supports petitioner’s contention that the use of
low
sulphur
coal
would
make
the
electrostatic
precipitators
less
effective for controlling fly ash emissions,
as presently designed.
Even
if low sulphur coal was available,
it would be far more appro-
priate to burn such
coal in highly populated areas
such
as
the Chicago
and
East
St.
Louis
regions,
where
intense
sulphur
dioxide
problems
are
known
to
exist,
rather
than
in
relatively
sparsely
populated
areas
where the sulphur dioxide problem is less
acute.
Nor does
the
substitution
of
fuels
manufactured
by
petitioner
for
coal
appear
to
be
a suitable alternative,
Propane manufactured by petitioner is sold
to Phillips Petroleum Company which,
in turn,
is
a major distribu-
tor of this product for home heating and agricultural operations
.708-—
723).
Perry E. Goth,
Jr.
testified
that
if
this
supply
of
propane
was cut off,
it would take Phillips
at least two years
to establish
a new source.
Approximately 15,000 homes
in the immediate area are
served by propane purchased from the Tuscola plant.
Conversion to oil
burning,
while
not
seriously
advocated
by
the
Agency,
would
not
appear
to be an appropriate alternative in consideration of the costs neces-
sary
for
such
conversion,
Nor
does
the
record
support
the
Agency’s
assertion
that
the
time
schedule
previously
approved
in
the
Acerps
could be accelerated.
Petitioner’s witness
in
this
respect
testified
to
a
programmed
schedule
of
installation
which
was
not refuted by
the
Agency’s witnesses.
He pointed
out
that
space
limitations
required
in-
stallation of the precipitators in
a sequential manner rather than simul-
taneously.
Likewise,
the proposal that sulphuric acid be purchased
2
—
597
to be used in the alcohol manufacturing process does
not have merit.
The approximate
1,000 tons per day
of sulphuric acid used in
the al-
cohol process must be 98.5
to permit its
use in that process,
After
the sulphuric acid is used in the alcohol process,
its strength is re-
duced 50
of which approximately 60
can be recycled and is reforti’-
fied for further use,
The remaining 40
is used in the phosphoric acid
plant.
Purchase of sulphuric acid from outside sources would create
substantial problems
of disposal in that the re—cycling process above
described would be eliminated,
and there is no market for the 50
acid
created and no suitable storage facilities are available.
In summary,
the Agency has
not established on the 1-ecord the avail-
ability of natural gas
or the appropriateness
of requiring low sulphur
coal
for use in the petitioner’s boilers nor does
use of
fuels manufac-
tured by petitioner appear to bea
suitable alternative to coal burning.
While purchase of sulphuric acid from
outside
sources
might be possible,
the
problems
it
creates
appear
to
be
far
worse
than
those
it
would
solve.
No solid evidence suggests acceleration of either Acerp program beyond
that
previously
approved,
nor
can
we
on
the
present
record
order
an
immediate
abatement
program
for
air~pollution
resulting
frofi
sulphur
dioxide as
directed
in
Environmental
Protection
Agency
v,
City
of
Spring-
field,
#70—9,
c.
f.
~
A enc
,
#71—193,
#7l—l95~
#71—196,
#71—197,
71—198,
p.
8.
It
is
clear
that
sulp
ur
dioxide
and
or
sulphurIc
acid
has
amaged
plants
in
the
area,
but
it
is
unclear
to
what
extent
this
is
attributable
to
the
boilers
and
to
what
extent
to
the
acid
plant.
We
will
therefore
order
that
a
study
of
the
problem
be
made
after
the
acid
plant
is
closed
and
that
appropriate
corrective
action
be
pursued
if
a
serious
problem
remains,
as
specified
below,
We believe petitioner has established its burden of proof for
the granting
of
a
variance.
Variance
is
granted
to
petitioner
in
substantial
conformity
with
its
petition,
but
subject
to
the
terms
and
conditions
hereinafter
set
forth.
While
we
allow
the
variance
on
the
time schedules
provided
in
the
petition,
we
will
insist
on
strict
adher-
ence to this program and countenance no~delay in its achievement.
We
do
not
look
favorably
upon
petitioner’s
cessation
of
activities
during
the
pendency
of
this
proceeding.
Petitioner
could
certainly
not
have
assumed
that
this
Board
would
sanction
a
program
for
the
installation
of
the
electrostatic
precipitators
that
would
be
slower
than
that
previously
sanctioned
by
our
predecessor
Board.
In
granting
this
petition,
we
are
not
unmindful
of
the
severe
problems
petitioner’s
operations
have
created
for
the
residents
in
the
area.
Fly
ash
and
particulate
emissions
attributable
to
the
boiler
and
sulphuric
acid
operations
have
significantly
interfered
with
the
enjoyment
of
life
and
property
in
the
community.
The
nuisance
is
severe
and
demonstrable.
Damage
to
metals
and
crops
unquestionably
have
re-
sulted
from
emissions
from
petitioner’s
plant.
However,
petitioner
is
pursuing
a program previously approved by the Illinois Air Pollution
Control Board and while petitioner unquestionably could have done more
2
—
598
and done
it
faster,
it was protected by the sanctions previously ob-
tained and is pursuing
a program previously approved.
On this state
of the record,
no penalty can
be
asserted.
However,
there is one facility that we
will
insist
be
improved
as
a condition of this variance,
The primary purpose for the sulphuric acid plant is the manufac-
ture
of acid used in the alcohol process,
However,
some virgin acid
is
manufactured
for
sale.
This facility appears to be operating
at
the
present time
in
compliance with emission
regulations.
As
a
condition
tc~
the
variance which we grant relative to
this
operation,
pending
comple-
tion
of
the new hydration plant,
we order
that
virgin
acid
production
for
external
sale
shall
cease
whenever
the
total
sulphuric
acid
plant
emissions
exceed
permissible
limits
as
set
forth
in
the
regulations.
This
production
limitation
will
permit
the
company to continue the
major
function
of
its
sulphuric
acid
unit
and
exceed
emission
limits
when
necessary
for
the
manufacture
of
alcohol,
but
at
the
same
time,
reduce
the
extent
to
which
emissions
from
this
unit
violate
the
law.
In
order
to
further
control
the
possible
plant
damage
from
sulphur
emissions
from
the
boilers
and
after
the
shut-down
of
the
sulphuric
acid plant,
U.
S.
Industrial Chemicals Co.,
through an independent re-
cognized consultant,
shall establish,
operate and maintain continuous
monitoring
stations
for
SO2
for
the
period
from
April
1,
1972
to
Septem-
ber
1,
1972
in
the
area
where
crop
damage
has
occurred
in
the
past.
Within
30
days
after
September
1,
1972,
the
company
shall
file
with
the
Board
and
Agency
a
program
for
the
alleviation
of
excess
SO2
levels
sufficient
to
cause
plant
damage.
The
Board
shall
issue
a
further
order
as
required.
Regrettably,
one
further
matter
must
be
mentioned
in
this
Opinion.
As
is
characteristic
in
many
cases
considered
by
this
Board,
great
emo-
tion
is often
generated
by
the proceedings and
the
issues
created.
Con-
cern is expressed on the one hand for the future of the business involved,
and
on
the
other
hand
whether
continuation
of
the
alleged
pollution
will
remain
a
lingering
burden
on
the
community.
Intense
feelings
are
aroused
on
all
sides
which
frequently
come
to
a
head
during
the course of
the
trial
and
are
often
expressed
through
the
media
and outside
of the hear-
ing
process.
In
cases
of
this
sort,
it
is
of
great
importance
that
the
Board
be
fully
apprised
of
all
aspects
of
the
issue
and
public
participa-
tion
is
both
sought
and
welcomed,
However,
the
place
where
these
views
should
be
expressed
is
in
the
hearing
itself,
for
this
Board’s
decision
can
only
be
made
on
the
basis
of
the
record
before
it,
Extra-judicial
accusations,
threats
and
innuendos
can
only
serve
to
exacerbate
an
al-
ready
difficult
situation
and
impede,
rather
than
assist,
the
Board’s
ability
to
render
an
equitable
decision.
It
is
unfortunate
that
such
circumstances characterized,
in part,
the present proceedings
and it is
hoped that they will not recur in the future.
599
This
opinion constitutes the findings
of fact and conclu-
sions of law
of the Board,
IT IS THE ORDER of the Pollution Control Board that petitioner
be granted
a variance
to exceed the particulate emission limitations
set forth in the Rules
and Regulations Governing the Control of Air
Pollution,
subject to the
terms,
conditions and time schedules here-
inafter set forth:
1,
Variance is granted to petitioner to operate its four
uncontrolled coal—fired boilers in
a manner causing
emission of particu.ates
in excess of
the regulation
limits pending the installation of five electrostatic
precipitators,
the
first
of
which
has
already
been
installed.
Two
additional
precipitators
shall
be
installed and in operation by
May
30,
1972.
Emissions
from all boilers on which precipitators have or will
be installed shall meet particulate emission limits
as
set forth
in
the regulations.
This variance shall
extend to Ogtober
13,
1972, prior to which date petitioner
shall have initiated installation of the two remaining
electrostatic precipitators on Boilers
#4 and
#5 for
operation by May
30,
1973,
and shall petition this
Board
90
days
in
advance
of
expiration
for
an
extension
of this variance demonstrating that it
has diligently
pursued
the time schedule for total installation
as set
forth in its variance petition.
2.
Variance is granted to March
30,
1972
to dperate the
sulphuric acid plant
in
a
manner
causing particulate
emissions
in excess of those allowed in the Rules and
Regulations Governing
the Control of Air Pollution
pending operation of the direct hydration alcohol plant.
On
March
30,
1972,
the
sulphuric
acid
plant
shall
be
shut
down.
No
virgin
acid
shall be manufactured for
sale
at
any
time
when
emissions
from
the
sulphuric
acid
plant exceed maximum emission limits presently in
force and effect in the Rules
and Regulations Governing
the Control of Air Pollution,
3.
U. S. Industrial Chemicals Co., through an independent
recognized
consultant,
shall establish,
operate and
maintain continuous monitoring stations
for SO2
for the
period from April
1,
1972
to September
1,
1972
in the
area where crop damage has occurred in the past.
Within
30 days after September
1,
1972,
the company shall file
with the Board and Agency
a program for the alleviation
of excess SO2 levels sufficient to cause plant damage.
The Board shall issue
a further order as required.
2
—
600
4.
The company shall, within thirty-five days after re-
ceipt of this order, post with the Agency
a bond or other
security
in the amount of $500,000.00,
in
a form satis-
factory to the Agency, which
sum
shall be forfeited
to the State of Illinois
in the event that the conditions
of this order are not complied with or the facilities
in question are operated after expiration of these variances
in violation of regulation limits.
I,
Regina E.
Ryan, Clerk of the Pollution Control Board, certify
that the Board adopted the above Opinion
this
14 day of October,
1971.
2
—
801