United Stales
Environmental Protection
Agency
Office of Air Quality
Planning And Standards
Research Triangle Park, NC 27711
EPA-450/2-90-011
October 1990
AIR
TOXIC AIR POLLUTANT EMISSION
FACTORS - A COMPILATION FOR
SELECTED AIR TOXIC COMPOUNDS
AND SOURCES, SECOND EDITION
X^X-«^"c:^<:7^'^'J^^^^>^"^">^V*'"^"y'"l-Xt-^"'^>"*"'^i"^'"^'I'^"*V'H'"^"^
.^.S^ag^^^^^J^^.y^.^.^
v^^'^^g^yyg^
I ...\.......1.-A v.-.X...^.^..
! • \ V \' \ \
STSc
•' ' -
-/ / .-./•• / i
\ \ \ \
\ \ \ \
'
' \
\
v. XN
••\"
"7"
\
\
\
7
\
\
-------
EPA-450/2-90-011
October 1990
TOXIC AIR POLLUTANT EMISSION FACTORS -
A COMPILATION FOR SELECTED AIR TOXIC
COMPOUNDS AND SOURCES, SECOND EDITION
By
Anne A. Pope
Air Quality Management Division
U. S. Environmental Protection Agency
Research Triangle Park, North Carolina 27711
Garry R. Brooks
Patrick F. Carfagna
Susan K. Lynch
Radian Corporation
Research Triangle Park, North Carolina 27709
U. S. EISlVIHUNMtN IAL HKUI tU IIUN AGENCY
Office Of Air and Radiation
Office Of Air Quality Planning And Standards
Research Triangle Park, North Carolina 27711
-------
This report has been reviewed by the Office of Air Quality Planning
and Standards, U. S. Environmental Protection Agency, and has been
approved for publication. Mention of trade names or commercial
products does not constitute endorsement or recommendation for use.
EPA 450/2-90-011
-------
TABLE OF CONTENTS
Section Page
1. Introduction 1
2. Use Of Emission Factors In Compilation 5
3. Emission Factors For Toxic Air Pollutants 11
4. Emission Factors For Sources Of Toxic Air Pollutants . . 327
References 643
Appendices
A. Compounds Having Emission Factors In Second
Edition Of Compilation A-l
B. Sources Having Emission Factors In Second
Edition Of Compilation B-l
C. Bibliography C-l
D. SIC Code Descriptions D-l
E. SCC Descriptions E-l
111
-------
LIST OF TABLES
Table Page
A-l. Alphabetical List Of Air Toxics In Second
Edition Of Compilation A-3
A-2. CAS Number List Of Air Toxics In Second
Edition Of Compilation A-15
IV
-------
SECTION 1. INTRODUCTION
The Environmental Protection Agency (EPA) and State and Local
air pollution control agencies are in the process of developing
programs to control air toxics. The development of an air toxics
program requires information about the types, sources, and
emissions of pollutants in a geographic area. One of the major
components of an air toxics program is an assessment of the
quantities of toxic compounds present in an area. Specific
emissions measurements are generally the best and most accurate way
to quantify emissions; however, measurement data are not always
available. An alternate method of estimating air toxics emissions
is by using emission factors. This report presents a compilation
of emission factors for selected toxic air pollutants and sources
of toxic air pollutants. The purpose of this report is to offer
a technical service to air pollution control agencies and others
in performing preliminary estimates of air toxics emissions. Users
are provided information so that they may review the referenced
literature where clarification or further details are needed.
An emission factor relates the quantity of a pollutant released
to the atmosphere with a source activity (e.g., combustion,
storage, handling, equipment leaks, processes, etc.). Emission
factors are usually expressed by units of mass of pollutant emitted
per unit of mass, volume, heat input, distance, or duration of a
process that emits the pollutant (e.g., Ib pollutant emitted per
ton of product). Sections 3 and 4 present listings of emission
factors for selected toxic air pollutants and sources and
associates the emission factors to levels of source activity for
pollutants. For example, in the smelting of copper, trace elements
such as arsenic or nickel may be emitted. An emission factor such
as "X" Ib nickel/ton blister copper produced, could be used to
estimate nickel emissions from the smelter.
In order to offer assistance to agencies and others in
estimating emissions of air toxics, EPA in October 1988 published
a report entitled Toxic Air Pollutant Emission Factors For Selected
Air Toxic Compounds And Sources (EPA-450/2-88-006a). The emission
factors in the 1988 edition were obtained from journal articles and
reports identified by a computerized literature search and from
published and unpublished EPA reports. The computerized literature
search accessed the following databases - Chem Abstracts, NTIS,
Enviroline, Pollution Abstracts, Compendex, Environmental
Bibliography, El Engineering Meetings, DOE and APTIC.
Since the publication of the 1988 compilation (first edition),
EPA has compiled additional emission factors into this Second
Edition. The Second Edition updates and expands the first edition
to include more than 6000 factors for approximately 270 compounds
and 470 source categories. To update and expand the first edition,
the data in the 1988 compilation were reviewed and some factors
-------
were revised based on comments received from users. New factors
were obtained primarily from EPA Background Information Documents
(BIDS) prepared in support of New Source Performance Standards
(NSPS) and National Emission Standards for Hazardous Air Pollutants
(NESHAP), EPA Control Technology Center (CTC) documents, Office of
Research and Development (ORD) reports, EPA's series of "Locating
and Estimating Air Toxic Emissions From (or of) (Source Category
or Substance)" reports, and other published and unpublished EPA
reports. In addition, other emissions reports have been obtained
from state, local and international agencies, trade associations,
and journals that have not yet been included in this second
edition. Plans call for this second edition to be further updated
with these reports and articles as well as other emission factors
that have been submitted by users. New references added to the
second edition are numbered from 166 to 214 in the List of
References. A bibliography of related reports obtained and
reviewed but which did not contain emission factors is included in
Appendix C.
Section 2 of this report describes the components of the
emission factor tables and explains the uses and shortcomings of
the information. Sections 3 and 4 contain the emission factor
tables. Section 3 presents the emission factor data sorted by
pollutant names. Section 4 presents the same factors sorted by
industrial process (e.g., smelting, petroleum refinery, oil
combustion, dry cleaning, etc.).
The EPA has also revised the Air Toxic Emission Factor (ATEF)
data base management system that accompanied the first edition
report. The ATEF data base has been revised and combined with the
Crosswalk (XWALK) data base to form the "XATEF11 data system. The
XATBF system containing both air toxics emission factor data and
air toxic pollutant/source crosswalk data has been developed to
allow for easy access to the data. The software is an IBMT
personal computer (PC) based application that combines the air
toxic emission factor data (formerly ATEF) and crosswalk data
(formerly XWALK) into one database. The XATEF presents emission
factors associated to pollutant names, Chemical Abstracts Service
(CAS) numbers, industrial process descriptions, Standard Industrial
Classification (SIC) codes and descriptions, specific emission
source descriptions, Source Classification Codes (SCCs) and
descriptions, notes on the process control or development of
factors, and references. The XATEF presents crosswalk data
consisting of air toxic compounds names, CAS numbers, SIC codes and
descriptions, SCCs and descriptions, and references. The data
management system allows one to search and download data to print
or data files. The system has been designed specifically for easy
data manipulation by fairly inexperienced users. No specific
programming knowledge is required to search or download data. Use
of the XATEF system is explained in a user's manual entitled
Crosswalk/Air Toxic Emission Factor Data Base Management System
User's Manual, EPA-450/2-89-018. The user's manual and data system
-------
are available to Stateand local agencies from EPA upon request.
Users will need an IBM AT PC or compatible machine that runs MS-
DOS™ or PC-DOS™ version 3.0 or later; at least 640 KB of free
random access memory (RAM); a fixed disk with at least 20 MB of
storage; and a 5 1/4 inch external disk drive. Requests for the
system and user's manual can be made by contacting the Noncriteria
Pollutant Programs Branch, U.S. EPA, OAQPS, MD-15, Research
Triangle Park, North Carolina 27711, or by calling (919) 541-5373
or (FTS) 629-5373.
This air toxic emission factor compilation will be updated and
expanded as new information is obtained on process descriptions,
operating practices, control measures, and emissions data.
Comments on the usefulness of this document are welcomed as is any
emissions information that would allow EPA to update and expand
this list of toxic air emission factors.
-------
-------
SECTION 2. USE OF EMISSION FACTORS IN COMPILATION
The emission factors compiled in this report are presented in
Sections 3 and 4. The data included in these sections for each
factor include:
- chemical name and CAS number,
- industrial process description,
- specific emission source description,
- SIC code,
- SCC,
- notes, and
- references.
CAS numbers, SIC codes, and SCC's are used in this compilation to
provide a means of identifying in standard terminology, pollutants,
industrial processes and specific emission processes/sources. For
some substances, CAS numbers are not available such as for
polycyclic organic matter. If CAS numbers are not available, no
CAS numbers are assigned in the tables. Similarly, when SIC codes
and SCC's are not available for some sources and processes, they
are not included in the tables. For some sources, the SIC codes
and SCC's are truncated in the tables based on available data. SIC
codes may be shown as two, three or four digit numbers based on
available information. SCC's may also be truncated to less than
the full eight digits.
Appendix A presents the air toxics that have factors in the
compilation. Table A-l lists alphabetically the air toxics and
their respective CAS numbers and chemical synonyms, if available,
contained in this edition. Table A-2 lists the air toxics for
which emission factors have been compiled by CAS number. Because
available information on air toxics emissions is limited, emission
factors are only provided for selected air toxic compounds and not
for all identified air toxics. The list of air toxics in Appendix
A represents air toxics for which emissions data are available.
The SIC codes associated to the factors are broad descriptors
of industry segments that are used throughout the Government to
define industries in accordance with the composition and structure
of the economy. For this reason, the SIC codes may not represent
specific emitting sources. In this compilation, SIC codes are
unavailable for some industrial processes such as wood combustion.
The SCC's represent processes or functions within a source
category associated with a point of air pollutant emissions. The
National Emission Data System (NEDS) uses SCC's to associate
criteria pollutants with emission factors for various sources.
SCC's are included in this document primarily for identification
purposes. The units for factors in Sections 3 and 4 do not
necessarily correspond to the units of factors listed in NEDS
having identical SCC's. For example, the toxics factor for carbon
-------
black manufacturing may show "X" Ib POM emitted/ton product from
the dryer, whereas the NEDS factor for the same SCO is "X" Ib
particulate matter/ton carbon black produced. Users should be
aware of this difference and consider it if applying these emission
factors to the SCC's in NEDS. In the XATEF data base management
system, the SCC's associated to toxics factors that do not
correspond to SCC's in NEDS or SCC's that have been truncated are
noted. As new SCC's are assigned for toxics in NEDS, it is
anticipated that future updates of this report will use SCC's
consistent with NEDS.
Brief descriptions of the industrial processes and specific
emission sources are included for each emission factor in Sections
3 and 4. Industrial process descriptions define source categories
and specific emission sources refer to operations within a source
category. An example of an industrial process is a petroleum
refinery, and specific emission sources within a petroleum refinery
include catalytic crackers, storage tanks, and equipment leaks.
Appendix B contains a list of the industrial processes that have
emission factors in the compilation. For most available SIC codes
and SCC codes associated with factors, the industrial process
descriptions are similar to SIC code descriptions and the specific
emission source descriptions are similar to SCC descriptions.
Appendix D presents SIC code descriptions and Appendix E lists see
descriptions.
The emission factors in Sections 3 and 4 are listed usually in
terms of mass of pollutant per mass of product produced (i.e., 0.8
Ib ammonia/ton urea product). When no other data are available,
some factors are presented in units of mass per time (Ib/sec,
Ib/day, Ib/hr, etc). Other factors are presented in typical units
specific to source categories. For example, factors for combustion
sources are shown with units of Ib/million BTU's. Most units are
presented in American engineering units (Ib, foot, ton, etc.) to
be. consistent with NEDS criteria factors. Some factors have not
been converted from metric units because they are conventionally
expressed in metric units such as ng/cubic meter or mg/amp hr.
Sections 3 and 4 also contain additional information in the
"Notes" part of each emission factor listing. Brief descriptions
concerning the derivation of emission factors (mass balance, test
data, engineering judgment) and any assumptions tat have been made
to derive the factors are shown in the "Notes". If an averaged
factor has been listed, the range is shown in this column. For
some toxic air pollutants, emission factors associated with
processes or operations are further characterized in the "Notes"
by the presence or absence of emission reduction techniques or
controls. For many of the controlled operations, the type of
emission reduction control is identified. However, the emission
reduction techniques in this report do not necessarily represent
the best available control technology (BACT) or reasonably
available control technology (RACT).
-------
References are included for each factor in this compilation.
The reader is encouraged to consult the references for more
detailed information on the factors.
The quality of emission factors presented in this compilation
varies considerably. Emission factors are derived in a variety of
ways including source tests, theoretical calculations, or a
combination of both tests and calculations. Extensive analyses of
source tests or a single source test may be used to derive some of
the factors in this compilation. Other factors are calculated by
using material balances or national emissions estimates divided by
national production capacities for chemicals. The "Notes" in
Sections 3 and 4 provide a brief description of the basis of each
factor, such as whether it is derived from source tests,
engineering judgment, or other methods. References are also given
so that the user can obtain more information about a specific
factor.
The data depth of the factors contained in this report is also
highly variable. For some processes, emission factors are
available for individual release points or unit operations within
processes. In other cases, factors are only available for an
entire process or emission source. This is illustrated in Section
3 for carbon tetrachloride. Carbon tetrachloride is emitted when
it is produced as a product, by-product, or intermediate during
various processes and when it is used to formulate other compounds.
Emission factors for carbon tetrachloride releases from
perchloroethylene production are listed for neutralization, drying,
distillation, and other operations; whereas only a single factor
for the emissions of carbon tetrachloride from pharmaceutical
production facilities is shown.
Emission factors are very useful tools for estimating emissions
of toxic air pollutants. In many cases, these factors are simply
averages of all available tools and do not generally consider the
influence of various process design parameters such as temperature,
age of equipment, reactant concentration, etc. If the emission
factors were correlated to process design variables, they would
provide more precise emission estimates than factors in this
report. Because insufficient data exist to determine the accuracy
or validity of the emission factors in this compilation, no
estimates can be made of the error that results from using these
factors to calculate toxic air emissions from any given facility.
The emission factors in this report are intended to be used for
making preliminary estimates of toxic air emissions from various
sources of air pollution. Emission factors are more appropriately
used to estimate the collective emissions of a number of sources,
such as in an emissions inventory for a selected geographic area.
The emission factors in this compilation will not likely provide
exact estimates of emissions from any particular facility. Because
these factors are obtained from data of wide range and varying
-------
degrees of accuracy, emissions calculated for a given facility
using these factors are likely to differ from the actual emissions
of the facility. In some cases, the differences in emissions
estimated from emission factors and actual emissions could vary
significantly. Only specific source measurement can determine the
actual emissions of a pollutant under conditions at the time of a
test. For the most accurate emissions estimates, source specific
data should be obtained whenever possible. When source specific
data are not available, emission factors can be used to estimate
emissions. More accurate air toxics emission estimates can be made
by using information contained in the primary references listed in
Sections 3 and 4 in addition to the emission factors.
Emission factors are one method used to estimate emission of
air toxics from sources. Inputs needed to calculate emissions
using emission factors include:
1. Activity information about sources (amount of product
produced, fuel used, etc.),
2. Emission factors to translate activity information into
"uncontrolled" emission estimates, and
3. Control device efficiency information to provide basis for
estimation of emissions to the atmosphere after passage
through a control device.
The basic emission estimation algorithm is:
E = R x EF x (1 - C/100)
where:
E = emission estimate for source
R = activity level
EF = emission factor
C = control device efficiency.
The accuracy of the emission estimate is equally dependent upon the
relative accuracy of each of the components. Errors introduced by
any one of these components affect the final emission estimate.
To illustrate the application of emission factors, an example
is provided for acrylonitrile. If an agency decides to estimate
air releases of acrylonitrile in an area, it could make preliminary
estimates of emissions by using emission factors in Section 3 and
data on material usage records, permit applications, or inspector
records of facilities producing or using acrylonitrile. However,
it must be emphasized that these estimates can vary greatly from
actual emissions because the factors are based on releases from
hypothetical plants with hypothetical emission controls. To
develop a more accurate emission estimate, the primary reference
listed in Section 3, Locating and Estimating Air Emissions From
8
-------
Sources Of Acrylonitrile, should be reviewed. A comparison of the
process parameters of the hypothetical plant contained in the
primary references and of those of the actual facility allows the
agency to determine the sources of error associated with using the
emission factors and to produce more realistic emission estimates.
If source specific data are not available, then the agency should
view the calculated emissions of acrylonitrile as only a
preliminary estimate.
-------
10
-------
SECTION 3. EMISSION FACTORS FOR TOXIC AIR POLLUTANTS
11
-------
Pie* HO.
Ot/21/tO
CM SIC
Munm COM iMOMTftiM. PMCCM
CIIIMIOM UUMCt
%CC COM flllMIQN FACTO*
Acanipnthen*
Aceniehthene
Aceniphthene
Aceniphthene
•IU*
fere* tin. MM burning Tlr«» I* oxperleentll
burn but
Scr*** ttr«, Q»*M burnlnv Tlr«» in •Mi*wiMnt*l
burn hut
Scrw tir«. o»iM burninfl T*r«» In •xp«rl.Mfit..l
burn hut
Scrip tiro, open burning Tire* III oxpertaantll
burn hut
J.44t Ib/ton
•.114 Ib/ton
0.42* Ib/ton
O.S1I Ib/ten
Sue •< PAH aaaly on IK «lr.t. H 1*0-2 t«.t i filter 212
coepont. gnrad) condition • 2- by 2' piece, burn
r>t«>I.I t«/br. uncontrellxl
tu* ft r*H ui.ly Ml IU Wltr.t. of 1*0-2 tmt « filter 212
cowont. «hr«d condition • 2* by 2* »lK>. burn
r*t<>l.l kt/hr. uncontrolUo
iu. al f*H M«ly on ll« ««tr«t. o( IAO-2 tut • «11 tor 212
cowont. «hr«t«*2.I kt/hr. uncontrolled
2S Uood canbuttlon.
InduitrUI
••Unceit drift nlck«»
•tok«r-flrod InouHrUI
boiler
I0200WM 2.2 x IOC-4 Ib/ton
Croon yood. one »Unt. »>rtlculet< control »/»ech«nlc«l
coll actor (t«lone>. xood lead rata 0.54 kf/». ball.
eff. tl.U
177
ncen«phth«na
25 Uood coabuitlM,
InduitrUI
ItUnceO drift »Ukei
etoker-flred Induetrlel
boiler
10200WM 2.2 II IOC-5 Ib/ton
Dry wod. one alent, aertlculetl control »/aech»nlc«l
collector (cyclone), wood faad reta 0.2* ta/a. ball.
eff. SS.II
Acanebhthana
25 Uood cnabuetlon.
InduitrUI
lilinced drift ulckee
•tuker-flred Induetrlil
tool Ur
I0200>0« I.I * IOC-4 Ib/ton
Croon uood. one (lint, aartlculeta control v/aachtnlcil
collector (cyclone), mod feed reta 0.54 ke/i, bell.
eff. 41.11
Aceniphthylene
Scrip tire, open burnlni Tlrei In experlaentil
burn hut
0.747 Ib/ton
IAO-2 extricta »/M inelyela. ehrad condition • 2* by
2" plocee. burn rite • I.S keVhr. uncontrolled
Aceniphthyleno
Scrip tire, open burnlnt Tlrn In axparlaintil
burn hut
0.604 Ib/ton
1AD-2 extntte u/ni inilyeli. thred condition • 2* by
2' plocee. burn rite • 1.1 kff/hr. uncontrolled
Aceniphthylone
Scrip tire, open burning Tlrei In expertaentil
burn hut
1.154 Ib/ton
HAD-2 extricta u/KS inilyile. Chunk condition • 1/4-1/4
of tire, burn rite • 1.7 k«/hr, uncontrolled
Aceniphthylene
Scrip tire, open burning Tlrei In experleintil
burn nut
0.4*1 Ib/ton
IAO-2 extrecta H/nS inilvile. Chunk condition • 1/4-1/4
of tire, burn rite • 2.3 ka/hr. uncontrolled
Aceniphthylone
Scrip tire, open burning Tlr«» In experlnentll
burn hut
Sue of PAH inily on lie extnt. of 1*0-2 teet a filter
coepont. thred condition • 2B by 2" piece, burn
rite't.I kg/hr. controlled
Aceniphthylene
Scrip tire, open burning Tint In experlnintll
burn hut
0.»72 Ib/ton
Sue of PAH inely on lie extnt. of IAO-2 te
-------
roe* No. 14
0*/21/*0
POLLUTANT
Ac en withy I one
Acenwhthylene
Acoteldehyde
Aceteldehyde
Acetoldehyde
Acetaldehydo
Acittldahvde
Acetildehyde
AcoUldehyde
Acatoldohyde
CM (1C
Munw* cool iMumiM. FKOMM
Acetlldohydo
Acot«ldehyd«
AciUldehyde
Ac«t«ld«hyd«
Acottldahydo
ncottldehydo
—
20I»M
7(070
7(070
7(070
7(070
7(070
7(070
7(070
75070
7(070
7(070
7(070
7(070
75070
75070
7507O
(crop tiro, aeon bureloa
» Head coebu»tlen,
InduetrUI
0*0* bureloe
Uood coebuotloe.
reddentUI
Uood conbuftlon.
reilaentUl
Uood coobultlon.
rotidontUI
raildmtUl
rxldontlil
Uood coobuttlMi.
roildontUI
Uood coobuttlan.
Uood caobuitlon.
r»ld«ntUI
Uood coobuttlon.
Uood coobuftlon.
Uood co.bu.tlon,
r«ld>ntl«l
Uood conbuttlon.
Tirol In oworlnoi
burn nut
Horlianttl rotum
Aro4 vourco
Flroploco
Flroploco
Flroplaco
Flroplac*
Flropltca
Flriplaco
Non-biXlod Itovo
S>«U •trtlflM
S..11 ilrtloht
yood»tov«f. birch
S»ll >lrtl«ht
woodttovt*. tpruct
(••11 >lrtl«ht
Uoodttovo
Ucotlftt ovc
lUI
tuba
wood
• wood
*cc cm HIIMIOK r*cio«
1.14* Ik/tM
I»200t0t 4.* « IOi-4 Ib/tM
MOTM
(un •« MM anoly on ll< oxtr.t. *t 1*0-2 tmt • «lltor
content, ohrod condition • 2' by 2- •loco, burn
r.to'2.1 ca/kr. contrallod
*a«ilto *t SC/M
212
(0300201 0.72 - 1.4* Ib/ton weed IitlMtod Iran • tot.l oldahyda voluo oi 10.4 Ib/ton
burnod
0.21 Ib/ten wood burnod lurnlno Jock Pino
0.4 Ib/ton wed buriod
O.U Ib/ton wood burnod (urnlni red e«t
0.172 Ib/ton wood burnod lurntna eroon olno
IJO
1.4 Ib/ton
1.4 Ib/ton burn«d
Uncontrolled, avoroeo onlatlon J.ctor buod on eeurco
totto
Uncan trail id
0.2 - 0.4 Ib/ton wood (urnlne ereon o*k or eroon olno
burnod
0.0228 Ib/ton dry lu«I NOTM! kl«n-tooeor
-------
Papa No. IS
09/21/90
POLLUTANT
Ace t aldehyde
Acetaldehyde
Acetaldehyde
Acetaldehyde
Acetaldehyde
Acetaldehyde
Acetaldehyde
Acetic acid
Acetic acid
Acetic acid
Acetic acid
Acetic acid
Acetone
Acetone
Acetone
Acetone
Acetone
CM (1C
NUMB COM INDUtniM. PMCItS fnlitlON COURCC
7*070 209* Coffee keen roeatlng Contlnuova keen reeeter
7*070 2*4* Acetone/phenol Cueane peroxtdatlon vent
•enuf actur* from cueena
7*070 2149 Acataldehyde production Oll-.lr vent
75070 2849 Acrylic acid production - Ouenck abeorber off-gae
Propylene oxidation
75070 49S1 nunlclpal uaeta rlaaa burn unit atack
coebuatlon
75070 49S1 Hunlclpal Mate nodular burn unit atack
coebuatlon
75070 49S1 nunlclpal veeta *e«uae derived fuel unit
coebuatlon atack
44197 2141 Charcoal nanulacture Batch kiln
44197 2841 Charcoal oanuf acture Overall proceaa
44197 2849 Acrylic acid production - Quench abaorber off-gaa
Propylene OKldatlon
44197 2B49 Terephthallc acid (crude! Reactor vent
production
47441 247 Paper coating Coating line
47441 284S Acetone/phenol Cu.«ne pero«ldetlon vent
47441 2B4S Acetone/phenol Storage tank ventf
eanulacture froe Cueane
Propylene oxidation
chlorlnatlon proceaa allvl alcohol atep
ICC COM
30200201
10120202
101 12011
Ml 11222
50100102
S0100IOI
50100121
10100401
10100404
10100401
10111222
10101102
40201101
1012021 1
10120202
407228
DIIMIOM FACTO*
0.0144 Ib/tan bean*
O.OO42 Ib/ten phenol
8.4 Ib/ton acetaldehyde
0.2 Ib/ton acrylic acid
produced
1.4 ii 10E-9 Ib/ton uaate
burned
4.4 « I0£- 10 Ib/ton naato
burned
1.0 1C IOE-9 Ib/ton naate
burned
12 Ib/ton charcoal
II Ib/ton charcoal
211 Ib/ton charcoal
2.1 Ib/ton acrylic acid
produced
1.2 Ib/ton crude TPA
produced
2. OS « 10-4 Ib/ft paper
coated
1.2 Ib/ton phenol
0.12 Ib/ton phenol
produced
produced
NOTES
Controlled nit* efterburner. average e4 » t*«te
Controlled (not specified), baaed on eaapllng. 1*77
date, average factora
Controlled, high proaaure acrubbar. data from on* plant
•aaod on data fron onn plant
Froe teat reaulta. no data on control*
Fron teat reaulta. no data on control*
Fron teat reaulta. no data on control*
Controlled, afterburner, engineering judgment
Controlled, efterburner. engineering Judgement
Uncontrolled, range of 204-212 Ib/ton, engineering
Judgement
Baaed on data free one plant
Uncontrolled
Baaed on one aaepllng progran, aaapled at dlacharge of
afterburner
Controlled (not epeclflodt. baaed on laapllng, 1977
Controlled lumped ( lad) , baaed on teat data, 1977
data, average factora
calculatlona
9XFEWNC
IM
12S
141
1*1
110
110
110
124
124
124
1*1
42
11
1
125
I2S
I2S
151
ISO
-------
Pate No. la
0*/21/M>
POLLUTANT
Acatona
Acatonltrlla
Acatonltrlla
Acatonltrlla
Acatopnonona
Acatopkanon*
Acatylana
Acrelaln
Acrolaln
Acrolaln
Acrolaln
Acrolatn
Acrolaln
Acroleln
Acrolaln
Acrolaln
CM «K
Hun*o COM iMDumiM. MOCIM tmtsiON MUM*
47441 MM Tank truck claeola* fntlra procaaa
7SOM *•*» Acrvlaaltrlla production Afcaorber vant
- fOHIO procaaa
7SOH 4M1 (axaa aluoaa Hultlpla ketrtk furnace
InctneraUaA
7SOM 4*51 SoMaaa ilud** Ikiltlpla kaartk furnaca
•M42 2*eS Acatana/pkaml CleeveM aactla* vanta
aanufactur* fraia cuaana Uoatlnad)
t**a2 2*4* Acetana/ekenol cuaana peroxidatlon vant
aanufactura from cuaana
74*42 2*t* Carbon black aanufecture luln procaaa purt* vant
- oil furnaca
10702* Uood coabuatlon. Flrwlaca/veodatava
10702* 2095 Coffaa baan roaotlne. Coatlmioua roaattne.
10702* 20*5 Caffaa baan roeatln* Contlnuoua roaatln*
10702* 2*4* Acralaln praductlan Acrolaln procaaa ecrubber
v owarhaada
10702* 2*«» Acrolaln production Proc... fugltlva
•allilons
a«l ttltmn
propylana oxidation
acid production ha«d«r
10702* 4951 nunlclaal waata HM* burn unit
coabustlon
10702* 495] nunlclptl w*«ta nodul«r burn unit
coabuttlon
coabuttion lncln«r«lor
*CC COM niMION FACTO*
«*00»< •.«•* Ik/truck claanod
MI2t40* «.« Ik/tea, acrylaaltrlla
aroducad
(OIOOSO* 0.02142 Ik/ton dry *lud«*
(OlOOMa O.OOIM Ib/ton dry aludia
UI202II *.* X IOt-« Ib/ton phenol
10120202 0.0172 Ik/tan pnanel
10100S04 M Ib/ton carkon klack
produced
0.01 Ik/tan nood burned
10200201 0.074 Ib/ton baana
raaatad
10200201 0.012 Ib/ton baan*
raaatad
1011201 0.04 Ib/ton acralaln
produced
10112017 l.t Ib/ton acrolaln
produced
produced
produced
produced
50100101 a. I » IOt-» Ib/ton >4>te
50IOOIOI I.I X IOE-10 Ib/ton
NOTM
falffllaii a«a*ur*jpMt
Uncontrolled, baaad on data fro* plant* and IP* atudla*
Ona teat, ecrubber
Ona teat, ecrubber ana! afterburner, better aparatln*
cendltlane
Controlled tunepoclf lad) . kaaed en teat data. 1*77
data, avora** factor*
Controlled (not apeclflod). eaaad on aavlln*. 1*77
data, avarao*. factor*
Ken** of 10-120 Ik/ton baled an aurvay of operatln*
plant*
Uncontrallad
Afterburner
Incinerator, kaaed an (.1* x 10f7 Ib/yr capacity plant
Leek detection and rooatr. kaaad on *.I* X IOC7 Ik/yr
capacity plant
Uncontralled. plant of I.S a IOCS Ik capacity, aaa
reference for oor* data
Control not oaacrlbad
Control not deccrlbed
KFIMM
n
14*
101
101
in
12*
t7
140
140
140
1
140
140
140
151
140
MO
140
140
-------
face No. 17
09/21 /9O
rOLLUTAMT
Acreloln
Acrylic acid
Acrylonltrlle
Acrylonltrllo
Acrylonltrlle
Acrylonltrtle
Acrylonltrlle
Acrylonltrlle
Acrylonltrlle
Acrylonltrlle
Acrylonl tr I le
Acrylonltrlle
Acrylonltrlle
Acrvlonl trl le
Acrylonltrlle
Acrylonl trl le
Acrylonltrllo
CAS (1C
HUIK* COW INMHTIIM. MOCM* OIIUION MUKf
107021 49SI UestoMater treatoent POTU
79107 2B49 Acrylic acid production - Ouenck abaorber off -tea
propylone oxidation
107131 2149 Acrylonltrlle production Abaorber vent
107131 2149 Acrylonltrlle production Abaorber vent
107131 2(49 Acrylonltrllo production Absorber vent (atari up)
107131 2149 Acrylonltrllo production Acrylonltrlle run tank
vont a
107111 2149 Acrylonltrlle production Acrylonltrllo run tank
venta
107111 2149 Acrylonltrlle production Acrylonltrllo etoraoe
venta
107111 2849 Acrylonltrlle production Acrylonltrlle storaoo
vents
107111 2849 Acrylenltrlle production largo loadlne
107111 2849 Acrylonltrlle production Column vents
107111 2849 Acrylonltrlle production Coluan vents
stor*9e venta
107111 2849 Acrylonltrlle production Cruda acrylonltrlle
stor*9* vanta
107111 2849 Acrylonltrlle production Fugitive eelsslons
•
«CC COM OIIUION rACTM NOTM
(0100701 110 Ik/tool •? ocrelele le lased en eel*, oodellno for kypotk. POTU. reerMeolU
Influent avereee MTU that treats l«duitrlal uaeteueter
10111222 14.0 Ib/ton acrylic acid laaod on date free. MM plant
produced
JOI2S404 0.20 Ik/ton acrylonltrlle Uncontrolled
produced
10125404 0.004 Ib/ton Thoreal Incinerator
acrylonltrlle produced
10125407 0.174 Ib/ton Mo control, eelsslone vented to avoid explosion, factor
acrylonltrlle produced la averaee for 1 year
407074 0.254 Ib/ton Uncontrolled, easuoed fixed roof
acrylonltrlle produced
407074 0.00254 Ib/ton Uator scrubber
acrylonltrlle produced
407074 1.042 Ib/ton Uncontrolled, assueed fixed roof
acrylonltrlle produced
407074 0.01042 Ib/ton Uater ocrubber
acrylonltrlle producod
10125409 0.1 Ib/ton ecrvlonltrlle Uncontrolled
produced
30125409 0.003 Ib/ton Uater acrubber
acrylonttrllo produced
10125408 10 Ib/ton acrylonltrlle Uncontrolled
producod
30125408 0.20 Ib/ton acrylonltrlle Flare
produced
407074 0.094 Ib/ton Uncontrolled, asaueed fixed roof
acrylonltrlle produced
407074 0.00094 Ib/ton Uater acrubber
acrylonltrllo produced
30125409 1.412 Ib/ton Uncontrolled
•crylonl trl le produced
sWniHCE
I*
1(1
1*2
142
142
142
142
142
1*2
142
142
142
142
142
142
142
142
Acrylonltrllv produced
-------
Pag* Mo. II
Ot/21/fO
CM SIC
Hume* COM iMDusraiM. MNCCM
IDIMIOH MUMC
«CC COM UtmiOaJ rftCTQ*
Mom
Acrylonltrll*
107111 2M* Acrylonltrll* woductlw T«k car loading v«t>M
1012*4 0.JJ4 Ik/to*
•crylgaltrll* pri
Uncontrolled
1*2
Acrylonltrll*
Acrylonltrll*
Acrylonttrll*
Acrvlonltrll*
Acrvlonltrtl*
Acrylonltrll*
I07IJI 2«4» Acrylonltrllo production Tan* car loading (ranting
I071JI
214* AcrylOfUtril* twoductio
- SOHIO g»r*c«a
107111 4VS1
107131
4*S1 S*IMM >lutf*<
lncln«rM< M *«t«
In InUuwit «u«r«»« POTU th«t tr««t« InduitrUI •«»t«u«t«r
101
101
Mlrlc «cld
Mlrlc acid
12404* 2M» MUlc Mid reduction
I2404t 214* Adlrlc tcld woductlwi
2*11 r«tral«u r««ln«ry
««houi«
Uncontrolled
Fluldlaid bid c«t«lytlc
cr«ck«r unit r«*«nw«tor
3040O201 0.0$4 kf/B*3 of lr«*h Uncentrollad ••.»•!on*
4u«l tl*rouahi*ut
»7
IIS
nldrln
Allyl chlorldo
Allyl chlorldo
10*002 4*51 tonfd (ludol
Inclnoratlon
10*002 4t» <««•••
Inclnorttlon
107051 2i4* (olchlorohydrln
production by
hydrochlorlnttlon
107051 284* Idchlorohydrln
production by
hydrochlorlnctlon
742»*05 Hood coobuitlon.
roildintltl
742>*05 224 Uouon iibrlc hln<
Fluldllod-bod «urn«co
h«*rtlv furntco
S«»«r«tlon unit
Uooditouo uithout b«lUnc* «nd t*otlng
Control unclair. b»««d on •«*• b«l«nc« >nd t*sttn«
Uncontrolled. b«»«d on on* itudy. nonb>
-------
Pat* Mo. It
Ot/21/M
CM IIC
NUnK* COM INDUSTIIAL PKICEII
inlMIOH tOUKI
ICC COM OIIMION r*CTM
Mom
Aluminum
Aluainua
Aluainua
Aluainua
742**0f 22* laww fabric flnlanlat Janttr fraaaa - rttl* JJOOOI O.O024 Ik/to* fabric Uncontrallad. avarat* af four taata
AaaonI•
Aaaonla
AaaonI a
Aaaonla
Aaaonla
22*
««brlc tA«
Tnarcaaal dyalnt
Plant ttack
Plant atack
Inclnarator atack
Fartllliar application Anhydrou* aaaonla
742t*OS 2»JI AMhaltlc concrata
productlwi
742t*05 2*SI AMhaltlc concrata
production
742t*BS 4MJ
Natural •«•
Ian Caaaarclal ballar
Natural tat coabuatlon Induatrlal bollara
Oil CMtUltllM
7««4417 0211 ••«« cattla faad lota
Full «ll
tntlr. IOUTC*
7««4417 12 Coal ra 100 tona NHJ/yaar
burnad
It Iba/ton fartllliar tourcaa aalttlnt > 100 tana NHJ/yaar
0.4t lb/10E« cubic faat tourcaa aalttlnt > 100 tona NHI/yaar
taa burnad
1.2 tba/IOC* cubic faat Sourcaa aalttlnt > 100 tana NHI/yaar
taa burnad
O.I lb/1000 tallona fual Sourcaa aalttlnt > 100 tana NHI/yaar
all burnad
0.011 lb/day/1000 haad Entlnaarln* Judtaaant
capacity
l.« x 10C-I Ib/hr/ton
11 Iba / anlaal Sourcaa aalttlnt > 100 tana NHI/yaar
I.I Iba / anlaal Sourcaa aalttlnt > 100 tana NHI/yaar
I. 1 Iba / anlaal Sourcaa aalttlnt > 100 tana NHI/yaar
2.0 Iba / anlaal Sourcaa aalttlnl > 100 tona NHI/yaar
2* Iba / anlaal Sourcaa aalttlnt > 100 tona NHI/yaar
0.024 Ib / anlaal Sourcaa aalttlnt > 100 tona NHI/yaar
0.1* Ib / anlaal Sourcaa aalttlnl > 100 tona NHJ/yaar
0.1» Ib / anlaal Sourcaa aalttlnl > 100 tona NHJ/yaar
I7t
I7t
I7t
17*
17*
»7
II*
I7P
I7t
I7t
17*
17*
17,
17*
17*
IUd>IX>l
5
-------
Pat* No. 20
0»/2l/tO
CM tIC
POLLUTANT kUUU COM INDMTRIM. NOCCM
Aoowtle 7444417 217 Aooonla ayntkaala
Aooonta 7444417 217 A—on I a ayntkaala
Aooonla 7444417 217 Uraa production
Aooonla 7444417 217 Uraa production
Aooonta 7444417 217 Uraa production
Aooonla 7444417 217 Uraa production
Aooonla 7444417 217 Ur«a production
Aooonla 7444417 217 Uroa production
Aooonla 7444417 2171 Aooonluo nltrato
production
Aooonla 7444417 2171 Aooonluo nltrata
production
UllttlON (OUKI
Condanaato ataaal atrlopor
Carbwi dloxlda
roaanarator
Rotary druo oranulator
coolara
Bruo granulation
Fluldlzod bad drllllM
load arada
PluUlaad bad drllllM
aarlc. arada
Honlluldlied bad drllllM
agrlc. orado
tolutlon loroatlon /
concentration
Cvtporatlon/condanaatlon
oearttlona
HI an danalty prill
coottra
SCC COM
MI0010*
IOIOOKW
10104012
10104004
1010401 1
10104010
10104001
10104002
10102717
10102714
UlItStON FACTO*
2.2 Ika/tan product
S.O Iba/ten product
0.00*1 Iba/ton coal
charaad
2.2 Iba/ton product
4.1 Iba/ton product
2.* Iba/ton product
0.17 Iba/ton product
11.2 Iba/ton product
O.S4 - 11.4 Ib/ton MH4
N01 produced
0.04 Ib/ton HH4 NOI
producad
mm
tourcaa oolttlo* > IOO tana NHI/yoar. uncontrolled
fourcM oolttlno > IOO tana HHI/yaar. uncontrollod
tourcaa oolttlni > 100 tons MHI/yoar
tourca* oolttlo* > IOO ton* NHI/yoar
tourcaa aolttlnn > IOO tana NHI/yoar
tourcaa aolttlnd > IOO tana NHl/yaar
fourcaa oolttln* > IOO tana NHI/vaar
tourcaa aolttln* > IOO tana NHl/yaar
uncontrollod. preaontad aa ranaa bacauaa of data
uarlatlana
uncontrollad, ropraaanta coolva and pre-coolora
UfiMCNCK
»7. 17*
»7. 17*
»7»
17*
17*
17*
17*
17*
»7
»7
74*4417 2873 A**»ontue nltratti
7444417 Z873
7444417 2873 Aaaonlyo nitrate
production
Low dan«ity pr.U cooler*
Low danilty prill dry«r»
30102724 0.10 Ib/ton NH4 N03
produced
3010272S 0 - 3.11 Ib/ton NH4 M03
produced
30102704 0.84 * 3i.O Ib/tMl HH4
M03 producad
Uncontrolled. r«pre»«nt» cooler* and pre-coolert.
•ourcM e«lttin» >100 ton* NH3/ye«r
Uncontrolled, presented *» rent* duo to d«t«
wwlctlon*. repreaente dryer and pre-dryer
Uncontr0U«d. presented A* r«n«e bec4U*« of d*t«
7444417 2873 A»*>onlu*) nitrate
production
7444417 2873 *Monlu« nitrate
production
7444417 2873 AMonlua nitrate
production
7444417 2873 rtasonlua nitrate
production
«r*nuUtor cooler* 30102730 0 Ib/ton NH4 N03 produced Represent* cooler and pro-cooler
7444417 2873 AuonlUM nitrate
production
ftot*ry drue ara
Solid* formation - low
d*n(4ty prill towers
Solids 4orM*tlon - p*n
ar*nul«tor>
Solids fore*tlon - rot*ry
dru« 0r«nulktors
30(0272* I.1C Ib/ton MH4 M03
produced
30102722 0.24 Ib/ton NH4 N03
produced
30102708 0.14 Ib/ton NH4 N03
produced
30102707 59.4 Ib/ton NH4 N03
produced
Uncontrolled, represent* cooler and pre-cooler
UncontrolUd. source* eelttlne >100 tons HHJ/yew
Uncontrolled
Uncontrolled
97. 179
97. 179
-------
rood Me. 21
0*/2I/>0
POLLUTANT
nrnnnl-
Aeeonla
Aeeonle
Aeeonla
Aneonla
Annonla
Aeeonta
Aeeonla
Annonla
Aneonla
Aeeonla
Aeeonla
Aeeonla
Aeeonla
Aaeonla
Aeeonla
CM
Munm
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
7444417
*IC
COM
2*71
2171
2171
2171
2171
2171
2171
2171
217!
2174
2*11
2*11
2*11
1112
1112
3312
INOUSTKIAL PWOCfo*
Aurnlue nitrate
production
Aaaonlue nitrate
production
Aeoentun nltrete
production
Annonlud nltrete
production
Aenonlun nltrete
production
Aeeonlun nitrate
production
Urea production
Urea production
Uree production
Aenonlue phoaphete
production
Petroleue refinery
Petreleue refinery with
cracklng/reforelng
Petroleue refinery with
cracktng/reforeln*
Coke production.
by-product recovery
proceta
Coke production.
by-product racovary
firocat*
Coke production.
IMIfflON SOUMf
felloe 'ereetlooe - Me*
denalty prill te-ere
Cr adulator coaler
Lou denelty prill drvero
fir emulation
Evaperetlen/condoneetloo
operatlone
Neutral Izor
Evaporeter
tiranulatlon
Prill toner
Total plant eeloelone
Fluldlied catalytic
cracklne. unit
Fluldlxed catalytic
cricking unit
engine*
Tec unite Ithereal
catalytic cracker!
Fee unite (fluid
catalytic cracker)
Coka puahlng
Door leaka
ICC COM UUfflON PACTO*
JOIM7U f7.2 Ib/ten MM NM
produced
10102704 1 Ib/ton product
10102723 1.4 Ibe/ton product
30I0270S W Ibe/ton product
UI027I7 17 Ibe/ton product
30102704 II Ibe/ton product
UI040 1.44 Ib/ton urea produced
30104004 O.f Ib/ton urea produced
1010400! O.M Ib/ton urea produced
301030 0.14 Ib/ton phoephate
produced
10400201 1.2* Ib/IOEl gal freah
feed
10400201 Negligible
20200202 0.2 Ibe/IOOO cubic feet
gae burned
4 Ibe/IOOO bbl feed
10400201 54 lbe/1000 bbl feed
3030010J O.I Ib/ton coal charged
10300308 0.04 Ib/ton coal chareed
30300302 0.02 Ib/ton coal charged
Mom
Uncontrelloel. eourcee ealttln* >IOO tew NKI/yeer
fourcee eel tt Ing > 100 tone NHl/year
tourcee eel tt Ing > 100 tone NHl/year
Seurcee eelttlng > 100 tone NHl/year
fourcee eelttlng > 100 tone NHl/year
tourcee eelttlng > 100 tone NHl/year
Controlled by wet ecrubber. teat date for on* plant
Controlled by ecrubber. teat data
Uncontrolled, dete fro. three plant*
Controlled (not epeclflodl. eourcee eelttlng >IOO tone
NHl/year
Uncontrolled
Controlled by eloctroetatlc preclpltator and CO boiler
fourcee eelttlne > 100 tone NHl/yoar
Sourcee eetttlno > 100 tone NHl/year* enleelon fector
rating 1
Sourcee eelttlng > 100 tone NHl/year. eoleetofl fector
rating 1
Uncontrolled, eourcee eelttlng MOO long NHJ/year
Uncontrolled, eourcee eelttlng MOO tone HHl/year
Uncontrolled, eourcee eelttlng MOO tone HHl/year
WMfNC*
n. m
17*
17*
17*
17*
17*
117
117
117
*7, 17*
*7. IIS
I
*7
*7, 17*
17*
17*
»7. 17*
»7. 17*
»7. 17*
by-product recovery
proc*««
-------
Pate NO. at
OC/21/tt
CM
SIC
COM IMUtmlM.
(MUIDH
«cc COM IHIMMN MOOR
7444417 IU Coke; production
7*44417 41 Internal coebuetlon
enoinet - eoblle
7M44I7 41 Internal contention
eneloot - eoblle
7444417 41 Interne! coobuetlon
wntlnet
7M44I7 4* Haturtl M« c«rtx»tlaii Utility kallv
(cooteeletted JMOM «.M Ike/ten coal ceoroed
Aononlue tulfato (2il) 7711202 21 Aeoonlue eulfato
Aeeonlue eulfate Hill
Aeeonluo tulfate (Zil)
7711202 2«*» MMOlui «ul(«t«
productlflA
by-product
7711202 214* MMOlua >ulf«t<
production • cw
tutor)
tletol fuel
Loaded eatllee
'luldliod-bod dryor
•otwy dryor
O.tf Ib/IOOO o*l. «uol
burnod
2WSMOI 0.42 Ib/IOOO o>l. «uol
burnod
UBBMOI 0.4S Ib/IOOO oal. iuol
barnod
10100*01 1.2 Ib>/I0f4 cubic loot
•at burnod
101 0.12 Ib/tm »«m I--
oulfato oroducod
MI2100t 220 Ib/ton oooooliio
tulf*to produced
1012100? 12 Ib/ton aoonolud
tulfato produced
toured* eeUtle* > 100 toot NHl/yeer. Colette* foctor 17*
ratine •
eourcee ootttleo > 100 tone nW/yoar. eel.tlon factor »7»
ratlnt I
fourcee eelttlne > 100 tout tea/year, eolation factor 17*
ratine, I
fourcoe oolttlno > 100 tone NH2/year. ooltelon lector I7f>
ratlnt »
Sourceo eelttin* > 100 tone ml/year, eoltilee foctor 17*
ratlnt C -
Met ecrubbor. booed en tett date free ell typo* of M 12*
dryere
Uncontrollod. booed on eource tett 12*
Uncontrollod. ranee of O.I-IS4 Ib/ton. bated on toot
data
noeonluo tuKate I2ill
7711202 217] Aeeonlue tulfate notary dryer
production • eynthotlc
10111004 §2 Ib/ton aooonluo
tulfoto produced
Uncontrollod. ranee of O.I-IS4 Ib/ton. bated on tett
data
Aeoonlue tulfato tjitl
Anthracene
Anthracene
7711202 JJI2 nooonlui «ui««t«
production • coko ovon
by-product
4291] 4*SJ
out
Kot*ry dryor
tcrw tiro, open burnlnt Tlr«> In ouporloontol
burn hut
120127 Scrip tiro, opon burnlnt Ilr» In o«porlMnt
-------
Paw No. 21
Ot/21/M
CM (1C
NUnm COM INOUtnUM. PROCIM
inlMION MUKt
KC COM OI1MI01I r*CTM
Anthracene
Anthracene
Anthracene
Anthracene
Anthraoulnone
Anthraeutnone
Anthraoulnone
Antleony
Antleony
120127 24*1 Mood areaervtne
120127 24*1 Mood ereaorvU*
120127 24*1 Mood ere.ervlne
120127 24*1 Mood eraeervln*
120127 24*1 Mood eraaervlnf
120127 2S Hood ceebtiBtloii.
Industrial
•4411 224 Uoven fabric flnlehlne
§4*51 224 Uoven fabric flnlenln*
•4411 224 Woven fabric flnlahln*
7440140 Uood coebuatlon.
realdantlal
7440340 224 Uoven fabric flnlehlm
Creoeot* coadltlMlee 1O70OWI 0.000* Ibs/hr
10700* 0.0012 Iba/br
107001*7 0.001I lee/hr
J0700S»7 O.OOO* Iba/hr
107001*7 0.012 Iba/hr
P«nl4Chloro«li«ltol
PentackloroahMMl
treating - futltlw
lalancod draft xtctai 10200*04 4.4 ii 101-4 Ike/to* fuel
atoker-flred Induatrlal
boiler
Curing even - r«*ln
flnUk
Thareoaol dvelito
Uaodltov* olthout
Curl At av«n - r«lln
llnltk
7440340 224 Uoven fabric flnlahlni H.«t ael
74403*0 224 Uoven fabric flnlahlne Tenter fraaaa - real
910001 0.011 Ib/ton fabric
Tenter fraaea - reel* 130001 O.OO*2 Ib/ton fabric
flnlah
130001 0.01*2 Ib/ton fabric
4.4 x 101-5 Ib/ton uood
130001 1.7* x IOC-4 Ib/ton
fabric
130001 1.14 K IOC-4 Ib/ton
fabric
330001 0.00124 Ib/ton fabric
r*a> »t MM (
•aHd MI MM aaeallne proeraa at one facility
laaed Ml MM eaeellm >roerae at MM facility
laaed on MM eaeollne eroeraa) at Ml* facility
I Ml MM »aeel!n* »ro*rae at MM facility
W-WM iMod, MM »l«it. MTtlcuUI* control M/MKhMtul
cotloctor IcyclMM). wad <«ut r«t. 0.>4 kt/«. boll.
Uncontrolled, awaw of too t««t«
Uncontrolled, averaae of tw tiata
Uncontrollad. auwat*. of tw taata
Uncontrollod, baud on on* (turfy, m«ba«l*d «t«w
burnln* troon oln«
Uncantrallod, on* t«t
Uncontrolled, baaod on teat data
ncontrolled, avoraoo of tuo taata
10
10
10
177
7440140 224 Uov.n Ubrlc
-------
Pee* Mo. 14
W/2I/M
POLLUTANT
CM «IC
Nunm CMC iMuiniM.
MISSION
sec COM mitsioM MCTO*
744O3I2 CMl COekUeklea
744O312 CMl COobUStlOn
coekuatlM
7440312 CM! coabufklen
7440U2 CM!
7440U2 CMl coebuetlon
7440112 CMl coeoustlon
7440112 Co«l combustion
7440)12 CMl coebusklon
HUtkreclto) CMlHIrod I
cyclone boilers.
utll/ceee*rc/ledutti>
tatkreclte coal-lire*1 I
cyclone botlora.
fuikhractta coal-d
ovmrlumd Itokflf tollers.
utll/cuuvc/lnduitr
iid dry bottwi
4J-1M Ik/IOCU Itu IM»»kr*ll«d. calciiUkad MMd M *»tl»**rtmf Judmmt M
Mthrtclka co«l*flr«d
»ulwarli«d dry botke*
ball. utll/co*Mrc/lnd
Anthr«clt< ca>l-flr«d
»ulw«rlxad dry boktea
2*« lk/IOC12 Iku
130 Ik/10112 Iku
IS.4 IWIOEI2 Iku
dtf Hltk •ultlclMn. c«lcul*k«d
21-S* Ik/IOCIt Iku
*.» IWIOfta Mv Cwtrdlwl ultk IV. cUcuUtvl b«»d w
2IO-4OI Ik/10112 Iku UncMtr*ll*d. calculated k*Md «* dmliMcrliKI Judimnt M
101-t** Ib/IOCU Iku Cantr»lt»d >Uh •ultlclMM. c«Uul«k«d k«Md Ml
2«-» Ik/10112 Itu Co«kr>ll«d olkk ttf. c«lcul«k*d ku*d on •ntlMlrlm
JudMMnk
Unconkroll«d. calcuUk«d baud on afiilnwln*; Judimnt M
C«nkrall«d ulkk •ultlclwM. calculakad kaMd on
antlnoorln* Judtaoonk
Conkrollad xlkk ISP. calculated ka»ad on ontlnoorlm M
7440312 Coll coebuaklon
7440112 Coal coabustlon
7440312 Coil coabusklon
7440312 Coal coebustlon
Knthrtclke caal-ulv«rliad uak botkoa
bollart. ukl1/coaaarc/lnd
t.1 lb/IOCI2 Iku
25* U/IOEI2 Iku
lb/IOCI2 Iku
Cenkrollad wlkh acrukbar. calculakod baaod on
enolnaarlnv Judaaoank
521 U/IOCI2 Itu Uncontrolled, calculated baaad on englneortn* judeeoent I*
Control I ad ulth •ultlclona. calculated baaed on
engineering Judoaeent
Control I id Kith ESC. caUulaked baaad on engineering
Judgeeenk
-------
Pate Ma. 2*
ot/2t/*a
fOLLUTMT
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
AT cant c
Arsenic
Arsenic
Arsenic
CM (1C
NUMO COM INOUtnlM. HMCCM
74401*2 Cool ceofcutle*
74403*2 Coal ceekuotton
74401*2 CMl co-bust Ion
74403*2 CM! coetoustlon
7440312 Ceel contention
7440U2 Cool ceebustlon
7440U2 Co«l coebuetlon
7440112 Co«l coebustlon
7440112 Coil coobustlen
7440312 Coil cognition
7440312 Coil coebustlan
7440312 Co«l co^nlitlon
74403B2 Co«l co«buctlon
inifSION «OUKf
*>ttirtcltt caal>HrW
•ulwlnd Mt kattM
ballori. utll/cooMTC/IM
Antnrtcllo CMl-flr«d
••rudor stakv bollori.
utll/co«Hrc/lridu>tr
fcttlu-utt* cMl-flrW
wrudv itokor bollors.
uttl /cOMWc/Indultr
Anthrtclt* calnou> bet lor
•ltu«lnoui cool-llrod
cvclono tool tor.
utll/coooorc/lntfuotr
klkuolnoua cool-lirod
cvclano Bailor.
utll/cooaorc/lnduotr
lltuolncMio caol-ilrod
cvclono botlor.
utl 1 /couorc/lnduttr
lltuolnixit co«l-l-od on ooolooorlix Judn.ont 14
10-101 Ik/10112 Itu Controlled ultk eultlclene. colculoted kooed en
enolneerlM ,
11-2* Ik/10112 Itu Control lod ultk Iff. colculotod kuod on onolnoorln*
2.31 Ik/ton flyuk
lli-110 Ik/10112 Itu
14.4 Ik/10112 Itu
«I4 Ib/IOCli Itu
33S Ib/IOCU Itu
40.1 U/IQCI2 Itu
l.3o - 1.4 Ik/ton *f lly.o*
Uncontrolled, kooed w eeoeured end calculated eelssloe
iactero
I
M
M-K2 lk/IOCI2 Itu nultlclono. colculotod koood en ontlnoorlnt Judn.ont
ESf. koood on oourcd toots
142-1030 Ik/IOCU Itu Uncontrollod. b«»od on source toot*
24S-SOS Ik/10112 Itu Controlled ultk eultlclene. colculatod kaoed en
entflneerlAe Judeeeent
47-12* lb/IOCI2 Itu Controlled ulth ESP. calculated kaoad en engineering
Judoeoent
Uncentrollod. kMod en oolnlon toot d«to
Controlled ulth oultlclone, cilculotod booed on
engineering Judeeeent
Controlled ulth ESP. b<«ed on source tests
s
5
-------
Paaa *o. 2*
0»/2I/*0
POLLUTANT
CM SIC
MMO COM IMUtmiM. PMCIU
HIItalON «OUKf
COM IMIMNN WC1W
74403U c«ai caaauatiaa
7440112 Coal caabuatlan
rulwlnd dry IrattM
kallw*.
»ulu«rll«d ixt MttM
I 17.1 Ik/10112 ttu ControllW xltli KnlMv. k«M< M Mure* tat*
1140 Ib/IOCll itu Unc«ttrall«d. calculated ba*«4 an •ntlMVln* Jud«««ant M
7440JI2 Caal caabuatla*
7440112 Coal caatouatla*
7440112 Coal caabuatlan
7440H2 Caal caatuatlan
7440U2 Caal caabuattan
lltuiUaua caal->lra4
•uluarlxd «at »«tta«
boll.ri. utl
lltualnoua caal-u« to...~t.r«d .
•?r«*dar ticker tMllw*,
uiii/co*»«rc/in4amir
ftttuk.nout co«i-fir«tf 1
•pn«d«r itokw t»ollars»
«M Ik/IOfU IU
IM Ik/IOtIZ Itu
Cwitr«ll*d HUk MiUUIww. c«lcuUt«d **•*< M
lb/10CI2 ttu
Controllad Hltk IIP. kaaad an aaurca taata
74.7 >b/10C12 >tu Controll«d Httli «crubb«r, c«lcul«t«d b«m«d i
•ng.n*«rlnt Jud««Mflt
2*4-142 Ik/10112 Itu Uncontrallad. baaad an aaurca taata
Controllad ultk aultlclona. calculatad kaaad ea
analnaarln* Judaaaaflt
7440112 Caal to.tou.Uon
7440112 Coal coabuitlan
7440112 Coal
tUu»inou« co»\-*lr«4 1
•pratdar .ttokw ball«r«.
ukil/cea««rc/tndu«tr
Ll«nU« co«l-*lr«d t
cyclon* botl«rs,
util/coM«rc/lndu*tr
LlvnUfl co*l-ftr«d 1
cyclon* boiler*,
util/coB*.«rc/induBtr
11-47 IB;lotU Itu
U4-J10 Ib/I0€12 Itu
Controllad «lth ISP, ulculatad kaaad an analnaarloa
Judaaaant
2H-41Z U/10C12 Itu Uncentrollad. calculatad baaad an anilnaarlna Judaaaant M
Controlled utth aultlclwia. calculatad baaad an
analnaarlnv Judaaaant
7440112 Coal cc^twitlo
7440182 Co«l
Llanlta co«l-flrad
cyclona bollara,
uil 1 /coaaarc/1 ndustr
Llanlta ceal-flrad
ov>rf««d stokar bollar,
utt 1 /£o«aarc/lndu«tr
It lb/IOCI2 Itu
ControUad ulth CSP, calculatad baaad an an«lnaarln«
Judaaaant
1100-2100 lb/IOE12 Itu Uncantrallad. calculatad baaad an analnaarlm Judaaaant
7440312 Coil ccmbutllo
Llenita co*l-fflrad
ov«rf««d itokar bollar.
utt 1 /coaaarc/lnduttr
540-1010 lb/IOEI2 Itu Controll«d ulth aultlclona. calculatad baaad an
anglnaarlnfl Jud«aaant
-------
Page No. 27
o*/2i/*o
CM tic
Nunwi COM INDUSTRIAL moan
(MISSION
MX COM IMMION FACtM
mnt
7440112 Coal coetouetlon
7440U2 Co*l ceebuetlon
Lignite coal-flroo)
ovorlaod atokar boiler.
utll/c
Limit* cMl-«lr«4l
^ulv«rl««d dry botto*
117-2*1 U/IOCI2 Mil
11*0 Ib/IOIU Itu
C«itr*ll«« «ltk HP. c*lcul*t«4 teMtf w ««*ntt* u*l-«tr*4
^ulv«rla«4 dry bottM
ball«r.
Lltnlt* co«l-«lr«l
pulvwlxad dry b«tto«
ballw.
Utl I /COMM-C/lAdU»tr
Llwilt* »d
rulvwlxvd dry tottM
MI Ib/IOOl It*
•2 ID/IOEU Itu
M lb/10C12 Itu
Can trailed «lth 1ST. calcul>t*d bttad an •nclnnrlnt
ContralKd xlth scrubbv. c«Uul«t*d b*Md en
•n*ln«rl*«
7440312 CM! ceobuetlM
7440312 Coil coebuatlen
7440312 Co.l coebuetlon
utl 1 /
Limit* C04l-«d i«t battaa
boll.
util/co»M«rc/lnduitr
Llsnlt* co«l-)lrid
pulvarlaad w«t botto*
bollar*.
ut U /co««arc/lndu«tr
2710 tb/IOCU Itu
1)40 Ib/IOCI] Itu
341 lb/IOEI2 Itu
Uncoatr«ll*d. c«lcul«t«d b»«d an an«tn*arin« Judtaaant
Controlled xlth eultlclona. calculated b»*d en
enelneerlnv JudMeent
Controlled «lth fST. calculated baaed en anflnaarlne
Judgaeent
7440112 Coal coebuatlon
Lltnlta caal-
-------
Pat* Me. 21
0»/2I/M
POLLUTANT
Areenlc
Araenlc
Araanlc
Areanlc
Areanlc
Arsenic
Araenlc
Araenlc
Araenlc
Araenlc
Areenlc
Araonlc
Araenlc
Araonlc
Araanlc
Art ante
CM
NUIOn
74401*2
7440112
7440 JU
74401*1
74401*2
7440U2
74401*2
74401*2
7440312
74401*2
7440112
74401*2
74401*2
74401*2
74401*2
74401*2
(1C
COM INDUtniM. MOCMf
Coal coebuatlae
Coal coebuatlen.
Industrial
Coal ceebuetlee.
Industrial
Coal coebuetlee.
Industrial
Coal co^uatlM.
InduitrUI
Oal co^uatlM.
r«ld«itll-
-------
•eee (to. It
0*/2ISto
MU.UTMIT
CM SIC
NUMfl COM INHMraUL MOCU*
UIIHIOM lOUftCf
ICC COM HUSSION MCTM
7440X02
744OI02
7440M2
Oil coatouetlee
Oil coeouatlen
Oil CMkuettm
Oil coekuatloe
Oil ceetouetlon
Oil coebuetlen
Oil coobuetlen
tlstllleta ell~llred I
boiler.
lncln
d«ntUl
utl I /ca*««rc/lndumtryrtt«l
ll.ilduil >ll-«lr«d
bollv,
utl 1 /co«««rc/ltlcl«w. e«lcul*t«4 k«»W ••
CootrolUd tilth ESP. olcyUtid b»»«d on •nflnurlm
ContralUd ultft Mnibkir. c«Uul«t*d k««d) M
•ntlnmrln* Judi«««nt
. cilculatid k»«d an «ntti>««rl»l Judmwit
Control I'd ulth lultlcloM. c*lcul>t«d b»«d on
•nilMorlnf judfMMnt
Controllod ulth CSV. calculated b«»«d on ontlnoorlnt
JudwMnt
Controllod Hltk Krubbw. c«lcuUt«d b>Md on
•nalnowlnfl Jud»«««nt
0.000 - 0.021 lb»/ton dry Controlled by u
0.0041 lb>/ton
0.0007 Iba/ton dry aludae Uncontrolled eelaelona. etnvle teat
0.0004 - O.e4 Iba/ton dry Uncontrolled eelaalona. averaee oi 5 teate Kaa O.II
0.10 lb/1000
burnod
Uncontrolled. b««d on «l
-------
Pat* He. SO
M/2I/M
POLLUTANT
Araenlc
Araenlc
Araenlc
Araenlc
Araenlc
Araenlc
Araenlc
Ara*nlc
Araenlc
Araenlc
Araenlc
Araanlc
Araanlc
Araanlc
Artanlc
Ara*nlc
Araanlc
Araanic
CM
Hume*
74403*2
74401*2
74401*2
74401*2
74401*2
74401*2
74401*2
74401*2
74403*2
74401*2
74401*2
74401*2
74401(2
74401*2
7440312
7440102
7440182
7440382
(1C
COM
0724
0724
0724
0724
0724
1011
12
12
1112
11,1
nil
111!
1311
nit
1111
mi
nil
mi
IMPJeTOIM. •MClal
Otto* llealM
Cotton tlnaln*
Cotton ilnnln*
Cotton *lMla«
Cotton oliMUe
Iron ere production
«...*»u.«tu,,n.
61*»c •Muff.cturln*
C**t Iron production
Ffirro*.loy production
F4N-ro.il toy production
Fevro*l toy production
•r conic or*
Copper •Mltlfl.rh.ol.
*r««nlc or*
*ri«ntc or«
Copper Moltiiifl'Mah
•rvontc or*
*r tonic ore
Co*>P*r ••«ltiA9-M«h
etrcunle orti
INIMION MMKI *CC COM HMMION FACTO*
btlre preceaa . J02OO4I* *.OOO*-*.014 Ik/ten
cettae el Mod
Fugitive eeleelem 102O04IO 0.00141 Ik total el**.
••/kale lint
man oreaaure a*ctl*n 102004 0.00141 Ik tetal elee.
•a/kale lint
Lou preaaure aoctlon 102004O4 ».? « IOI-* Ik total
ala*. fka/kal* lint
Unloadln* fan cyclone 10200401 0.000* Ik/ten cotton
•tuned
101 0.2 Ik/tee of crude ere
tntlre proceaa 305014 0.3* Ik tiwrcanlc Aa/to*
plaaa mlled
Entire proceaa 30S014 O.M Ik total el*..
Aa/tMi aUaa pulled
303008 0.014 Ik/ton of eetal
charted
flectr!c arc furnace. 30300701 0.02*4 Ik/w-hr anerw
opan. f*rr**an*an*a* conaueed ky furnace
Ilactrlc arc furnace. I03O0702 0.001* lk/*u-kr eneroy
aaal'aaaled. farrealllcon conaueed ky furnace
flawtrlc arc furnace, 30300702 0.00013 Ik/ax-kr eneriy
aa*lad, alllcoaantanaaa conaueed ky furnac*
Fualtlva aataalona fro* 303009 0.001 H araonlc contant
flua duat handling of flue duat
Futltlva eelaalona fro* 30300914 0.20 » araenlc content of
anod* furnace kllater capper
Fugitive oelaalona froe 30100911 0.0001 « araenlc contant
cilcln* tranafar of calcine
•>U« twpln* of aatte
Fusltlwa aalaalona fro* 30300SI7 0.0012 M araanlc contant
tin tapping of furnace elag
Fu«ttlw* aalaalona
-------
row N>. at
0*/2I/M
PtXLUTAin
ATOMIC
ATOMIC
ATOMIC
ATOMIC
ATOMIC
ATOMIC
ATOMIC
ATOMIC
ATOMIC
ATOMIC
ATOMIC
ATOMIC
Aroonlc
ATOMIC
Arocnic
Aroonlc
Aroonlc
CM
MUnMH
7440IU
7440M2
7440112
74401*2
7440182
7440 Jff.2
7440 JI2
7440U2
7440M2
7440JI2
7440111
7440JI2
7440312
7440JI2
7440112
7440182
7440182
(1C
COM
mi
in,
mi
mi
mi
mi
jut
nil
mi
nil
Jin
jut
3331
mi
mi
mi
1111
INMMniML MOCK*
Coe*or ee*lUae-hl*h
Cooper oeeltloo-hllh
oroonlc *r*
COOPOT OOOltlAf-IOM
OTOMlC OT*
Copper oooltlno-loii
oroonlc or*
£.«•;.•.;.""•"'"
arsenic are
arsenic are
:r:.~:"rrl~
Capper e-olUng-10M
areenic are
•runic ore
Copper SMltlng-lOM
arsenic ore
Capper seel ting- low
arsenic are
Copper saeltlne-lOM
arsenic ore
Capper fecit. ne-low
arsenic ore
Copper seeltlng-lou
arsenic ere
Copper seeltlng-Iow
arsenic ore
fni-SION SOUKf
converter operation*
Fugitive e-Uslone fra*
ar**nlc building
Fugitive) ael**lan* Iran
flu* duet handling
Fugitive Ml ••lone Iroei
enode furnace
Fugitive eel •• Ian* fra*>
converter operation*
Fugitive eel as Ion* fro*
•lag tapping
Fugitive e*l**lon* fro*
•atte tapping
Fugitive emissions froa
calcine transfer
Fluid-bed
roaster/converter tacld
plant outlett
Fluid-bed roaster
Fluid-bed roaster
Converter secondary hood
outlet
Acid plant outlet
Converter (acid plant
Inlet)
Converter
KC COM OUtiiai FACTO*
JOJOOJI* «.ll X OTOMlC CMt.
J0100* 0.00* X OTOMlC content
Of CnoTOO to OTOMlC Pit
10IOOS 0.001 x «o CMt. In tho
troniferrod duot
JOJOOSU 0.11 x or*Mlc CMt. In
onod* furnoc*
JOJOOSIS O.lf X OTOMlC CMt. I*
proc. *ff*oo
of furnoc* olot
JOJ009I4 O.OIS X oroMlc contont
of ootto
30300511 O.O05 x oroonlc contont
of cilclno
J01O09 0.0071 - 0.02J Ibo/ton
3030050» J x IOE-4 - 4 x IOC-4
Ibo/tM food
3030050* O.OI» - O.OJI Ibo/ton
30300515 O.OJS - 0.174 Ibo/ton
10100514 0 0072 * 0.012 Ibo/ton
food
103005 1 « IOE-4 - 2 « IOC-4
Ibo/ton food
30300504 2 > IOE-4 - 7 x IOE-4
Ibo/ton food
10100504 2 * IOC-4 - 1.4 » IOE-1
lb>/ton food
MOTfl
Uncontrolled Ml»IMO. booed M t«ot« *4 M* plMt
Uncont rolled Mloolom. b.ied M toot* of M* plant
RepruMt* uncontrolled fuoltlv* oolttlono
RoprMMt* uncontrolled futltlve o*l»lono
koprooMt* Uncontrollod fuoltlvo ooUolono
RoprooMt* uncontrolled futltlv* ooloolono
Roprooonto uncontTOllod fu*lttw« oaloolono
Acid plont functions oo control oyotoo
Eoloolono control lad by vontTl ocrubbeT
Uncontrolled oaloolono. Inlet to ocrubbeT
UncontTOllod ealoolono
Uncontrollod oolflolono
EoUolono controlled by ESP
Eoloilona control lod by ESP
Uncontrollod ooloolono. Inlot to ESP
E.I. .Ion, olio y P y <
MPfloDCC
204
204
204
2O4
204
204
204
204
204
204
204
204
204
204
204
204
204
-------
»••* no. n
O*/2I/*0
MUUTANI
MMMM. MOCIM
ArMnlc
lit
74443*2 1331
74403*2 3331
74403*2 lilt
7440312 3111 COOMT MOltlM-lM
•reonlc era
74403*2 3331 Copper
AreenlC
74403*2 3331 CB..V Mel
74403*2 II1I
74403*2 3331 Copper «
.TMAlc <
74401*2 3131
tnlMIOM lOUKf
fCC COM fMMION »AC10*
Mon*
I bod] 30300*24 4.4* - e.20 Ibe/tea «Md UncoMr*!!** eojulone
r.otor/electrlc
10100*14 0.0074 - *.00*7 IM/ton E.I.lion, control 1*4 by . boohOMM
J0100SI. 0.0044 • 0.014 lt»/ton Contr*ll*« k» . »w«» cfc.*v/c»ld f*f
30300504 7 « IOC-4 - O.OU lb«/tM C.l••!•«• contrail** ky * k.«houM
rl..ri> l..d •••Itl/it Entlr. .roc.ii
74401*2 1341 t«cond.ry lo.d ».ltlni ATM ..I..Ion - o.t.rl
7440312 1141 S.cond.ri> lo>d o.ltlni lint >nd r.v.rB.r.tory
7440112 3141 («cond.ry l..d «««ltlns (Kit .nd r«v«rb«r«torx
furn«c.«
7440302 3141 S.cond«ry l..d ...Itlne •!«.! *nd r.v.rb.r.torv
furn.c.*
tor <»rl*«-y) 10100* 12.S Ib/hr
•«nt« 25-150 Ib/hr. ••!••! on factor «lvwi •• old-ran**
•oconoftry hood
I010OS 0.10 Ib/ton Cu oroducod «««•». v.luo. controlled by >lr ci
•yttM. b»ad on ono >l>nt cnly
101005 0.02S Ib/ton •!.( >kl...d Controll.d by >lr curt.In ..condvy hood .yiton. b.Md
on on« »lMit only
303010 0.1*4 Ib Inort.nlc A./ton Noueh ostlo.t* only* r.nto 0.020-0.9* Ib Ac/ton lo.d.
load .roduc.d f.brtc flltor control
104004 0.12 Ib/ton I.>d .roduc.d For •••11 ...lt«-
304004 0.00*4 Ib/ton lead
produced
304004 0.002* Ib/ton l.id
produced
104004 0.072 Ib/ton l.
-------
Pane No. H
tt/21/SO
POUJUTAHT
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
Arsenic
CAS IIC
MjnKR MM INDUSTRIAL PROCESS
744O1U 1141 Secondary lead soellln«
7440112 1141 Secondary lead seel tint
74401S1 4*51 Municipal Mote
cnokustlen
74401(2 4*sl nunlclpal Mete
coobustlon
7440311 4fS3 Municipal uaate
coobustlon
7440112 4*51 Runt cl Ml Mete
coobustlon
744OIK a»e
coebustlon
(
7440112 4*51 Municipal Mate
coobustlon
7440111 4*51 Hunlclpsl neste
coebuatlon
7440111 4*51 nunlclpal nasto
coebustlon
74403S1 4*51 Municipal uaste
c«*uetlon
74401S1 4*51 Municipal uaato
conation
7440311 4*51 nunlclpal Haato
conation
74403S1 4*53 Municipal waste
coobustlon
7440382 4*53 nunlclpal uaste
coobuatlon
74403B1 4*33 nunlclpal Heate
coabuatton
mission SOURCI
Futltlvoe - lureace
Special battery seeltlne
furnace and futltlves
Naaa burn, refractory
facility
Maee burn, uater nail
incinerator
nodular Incinerator
Refuse derlwed fuel
- Incinerator
Refuse derived fuel
Incinerator
Reluae derived fuel
Incinerator
Reluae derived fuel
Incinerator
Refuse derived fuel
Incinerator
nodular starved-alr
coabuator
nodular starvad-atr
coabuator
nodular excaaa-alr
coabuttor
coabuttor
naaa burn. Hater uall
Incinerator
ta«taru»ll coabuttor built
altar 19BO
ICC CMC INiMMM FACTO*:
104004 I.Ofe Ik/ton lead
10400S 4.1 x IOC-4 Ik/ton lead
•reduced
SOIOOI 0.013S Ib/ton controlled
•articulate eeleslons
SOIOOI 0.47 Ib/ton controlled
•articulate eelsslons
SOIOOI 0.704 Ib/ton controlled
partlculate eetsslona
301001 0.11 Ib/ton controlled
partlculate eeleslons
SOIOOI 0.004 Ik/ton ROF
coobusted
SOIOOI 0.007 Ib/ton RDF
coobustod
SOIOOI 0.003 > 0.011 Ib/ton RDF
coobusted
SOIOOI 4.4 x IOE-S Ib/ton RDF
coebuated
SOIOOI 0.0002 Ib/ton feed
301001 0.0034 Ib/ton leed
SOIOOI • x IOE-4 Ib/ton lead
301001 1 x 10C-10 Ib/ton laad
301001 0.0032 Ib/ton lead
301001 4.4 x IOE-5 Ib/ton laad
NOTES MFCRCNCC
For snail seel tor, central ultk labrlc filter 11
Avorete proc. end lusltlve factor, controlled by labrlc 10
Illter
Controlled by ESP. baaed on source test HI
Controlled by ESP. based on eource tests HI
Controlled by ESP. kasod on source tests 111
Controlled by ESP. baaed on eource tests 111
IOOS RDF fuel only. ESP control only, overall overate 110
of several source avereeee. rente If 0.002 - 0,OO>
Ib/ton
IOOS RDF fuel only, uncontrolled, overall rente of 110
several source evoraeee
IOOS RDF only, uncontrolled, overall ranee of several IW
source everates
Spray ov-ylnt after acid tae end Pit control, detection 110
Holt reported. IOOS ROF fuel only, averaee value.
ranse Is 2.0 x 10-S - 0.0001 Ib/ton
ESP control only, overall avoraoe of aeveral source 110
averaeea. ranee Is 4.4 x 10-4 - 0.00012 Ib/ton
Uncontrolled, overall avoraoe of several source 1>0
averaeea. ranee Is 5.2 x IOE-5 - 0.001 Ib/ton
ESP control only, overall averaee of aevoral source ISO
averasas. ranee la 1.4 x lOE-e - *.2 x IOC-4 Ib/ton
Dry sorbant Injection alter acid tae and Pit control. ISO
one data point only
uncontrolled, one data point only 1*0
Capacity > 400 toni/day. ESP control only, overall 110
IOE-S - 4 x IOE-5 Ib/ton
s
$
3
-------
POM "o. 34
0*/2t/tO
POLUITANT
CM IIC
NUM* COM iNMtniM. Mocm
UIIMIOM
(CC C00( IMIMION FACTOR
NOTU
Aroonlc
Araenlc
74401*2 4*SS NwlclMl «eote
atlaej
744«IU 4t»3 IhMlcloal WetO
COObuetlOO
74401*2 4>I1 IhMicloal Mete
COObvetleO
74401*2 4W1 Huolcloal Mete
ceebuatlon
74401(2 4»S1 Itunlcleel naeta
coebuetlen
74401*2 4tSJ nunlcltd oeete
coobuatlon
74401*2 4tSl Ikinlcleal Matte
coobuatlon
7440112 4*11 nunlcl»«l »««t«
dxtxittlon
7440H2 4fSl KullUlMl M«tl
coabustlan
7440112 4»SJ SIIUM lludw
Inctnwttlon
7440312 4«J f«»M
tncln«r«tlwi
74403*2 104 Hoaeltal Mate
Incineration
1312214 Atbtttoi building <•••<•
dl lootil
1132214 Aftbvito* bullttlns u«it«
Leree oeeo buro rotary
Meteryall coobvator built
after IMO
(.tree oaaa buro rotary
MtterMatl coobuator built
•fter l»00
lUia buro MaterMall
coobuator. eoall alia oex
oodel to any aoo oodluo
tlaae burn Maternal1
coabuator. aoall elxo MM
•odel to any aea oedluo
n«»> burn iMt
slor. •••!! •!•• n«
in «ny ••* n«dlun
Itaat burn Maternal I
coabuator. built before
IMO
Hast burn Maternal1
cotbuator. built before
IMO
tlatt burn, refractory
facility
tlait burn, refractory
facility
fOIOOl t.002l Ik/tM IM4
M1001 1.1 II IOC-S Ib/ton <««d
SOIOOI 4.2 « lOt-1 Ib/tM i«d
SOIOOI 1.4 x IOC-4 Ib/ton (««d
> 400 t«M/*W. UKMtrdlW. «w ««t« Ml**
only
Capacity > 4OO tont/dav. eeray dry I of aftor acid eaa
and Ml control.averaee of eourco averaoea. ranoo !• 3.4
x IOf-1 - 4.2 x I0f-f Ib/to
Caaacltv < 400 tent/day. ISP control only, overall
overate: e« aevoral aource averaoea. ranoe li 1.0 x
10I-S - 7 x I0€-s Ib/ton
Capacity < 4OO tent/day, aoray drylno after acid oae
and PR control, ono data oolnt only
SOIOOI 4.0 x 101 - • Ib/ton <•«« Cwaclty < 400 tono/4ay. dry aorbont Injection aftor
•eld «»• and Pfl control , ono data »otnt only
(01001 0.0012 Ib/ton faad
SOIOOI 0.00* Ib/ton feed
CS> control only, ovorall avoraoo of tovoral aourco
avoraoaa. ranoo la O.OO024 - 0.002 Ib/ton
Uncontrolled, overall averaoo of eevoral aourco
averaeea. ranee le 0.000*4 - O.OIS Ib/ton
SOIOOI 1.4 x IOC-4 Ib/ton faad Stray dryln* ««t«r acid oao and Ml control, ono data
•olnt only
SOIOOI 0.0004 Ib/ton food
Uncontrolled, ono data »olnt only
Fluldlied-bod furnace 5010050* 0.00012 Ib/ton dry aludee nvoraoe of too toata. venturl and laalnoeoent acrubbor
nultlala hearth furnace 5010050* 0.001 Ib/ton dry aludia Averaoo of ten teata. acrubber
L*v«llnv and conpacilon
•t duap ttt«
S020050S I.I x IOC-4 Ib/ton ftad Uncontrolled, teat data
1.74 x IOC-4 Ib/cublc last oatloato of uncontrolled aelialon. r«noe 1.12 x
foot v»ta IOE-1 U 0.00131
1.4 x 10-4 Ib/cublc foot B»t aitloate of uncontrolled aolatlon. ranee 1.241 x
•••to 10E-S to 1.04 x lOt-4
Aabaatoa butldlna u«ata
dtapotal
Ulnd aroclon after flrtt
2.» x IOE-4 Ib/cublc foot Ba»t aitlaita of unco
uaate IOE-S 10 4.4 « IOE-4
-------
Pete Mo. IS
OV/2I/00
POLLUTANT
Aebaeto*
Aebeetoe
AobootM
AebMtoe
Aeboetoe
Aeboetoe
Aeboetoe
Aeboetoe
Aeboetoe
Aeboetoe
Aeboetoe
Aebeetoe
Aobeetoe
Aeboetoe
Aeboetoe
Aebeetoe
Aeboetoe
CAS SIC
MMC* COM INHimiM. PMOCCH WIM ION HUM*
1312214 Aebeetoe bulldlnf «eeta HIM or eel on durlae llret
dleeooel veer et due» lit*
1112214 Aeboetoe product u.eee Irate llnlnoe
1112214 Aeboetoe product ueew Construction Indue try
1112214 AeboetM product ueeee Ineuletlnf cooont
1112214 Aeboetoe product ueeta (tool llreproollm
1112214 Doootitlon end renovetlon Ueeto ooveoont to toaa.
el bulldlnie etorete end trenefor to
trucke
1332214 I4»» Aebeetoe eilllnt Entire proceee
1112214 I4»» Aeboetoe atlllnt Entire proceee
1332214 I4»» Aebeetoe otlltnt Entire proceee
1332214 14»t Aebeetoe ollllni Entire proceee
I1I22I4 14»» Aebeetoe at Hint Entire proceee
1332214 14»» Aebeetoe alnlnf Entire proceee
1132214 M»» Aebeetoe •mini M.ullne
1112214 M»» Aibeetoe elnlne Lotdlne
1112214 11»» Aebeetoe alnlnt nlnlni
1112214 M»f Aibeetoe alnlng Unle
-------
Pet* N>. M
0*/1I/M
POLLUTANT
ftehtltoi
Aebeetoe
Aebeetoe
Aebeetoe
Aebeetoe
Aebeeto*
Aeboetoe
Aebeetoe
Aebeetoe
Aebeetoe
Aefreetoi
Aebeetoe
Aeboetoe
Aebeetoe
Aebeetoe
Aeboetoe
Aebeetoe
CM
Numn
,«2M
1132214
1112214
II122I4
1112214
1112214
1112214
1112214
1112214
1332214
1112214
1112214
1112214
1112214
1112214
1112214
1112214
tie
COM IMMTMM. PMCtt* tnltllON tOtMCt
12*2 Aebeetoe - c*o*»t fin entire procope
•emileckurliw
12*2 Aebeetot - coo**t elieet Intlre procoeo
12*2 Aebeitee - coMnt eheet Intlre eroceee
12*2 AekMttt coetlM* end Entire troctet
eoelentt •enulecturlnt
12*2 Aebeetoe coetlnte end tntlre oroceee
eeel entt *emilecturlAt
12*2 ABbestot friction Entlr* eroceee
12*2 AebietM Irlcllon entire eroceet
12*2 Aebeetoe teekete end Entire eroceee
12*2 Aebeetoe teeiete and Entire erocoee
12*2 Aeboetoe Ineuletlon Entire ereceee
12*2 Aebeetot Ineulotlo* Entire erecoet
••terlele oenulacturlnt
12*2 Aebeetoe peper Entire oroceee
•enulecturlnt
12*2 Aeboitoe etper Entire eroceee
lebrlcetlon
librlcetlon
32*2 Atboetoe eroduct Atbeetoe eeper
12*2 Atbeetoe product Drill tnt esoesto
<he«t
tCC COM BHMION >«CTM
MWII2* t.in Ik/tM eeboetoe
10MII20 2M.S U/tM eebeetoe
contu«*d
WSOII20 0.712 Ik/ton eebeitoi
•.11 Ik/tM eebeetve
0.114 Ib/ton eeboetoe
M4.4 Ik/too eebeetoe
f.74 Ik/Ion eebeetoe
2.41 Ib/ton eebeetoe
0.00012 Ib/ton eebeetoe
20.* Ib/ton eeboetoe
O.ol Ib/ton eebeetoe
coneuoed
0.071 Ib/ton eeboetoe
0.0007* Ib/ton eebeetoe
coneuood
producte 30SOII20 t>0 Ib/ton eebeetoe
4 Ib/ton eeboetoe
produced
1.0 Ib/ton oebestoe
produced
B cement 2B3 llbere/cc elr/fl
eebeetoe oechlncd
NOTIt
0-1.04
Celculeted evweto
rent* »».4-45S.2
CtUuletod ouvet*
0-SS.I2
Celculetttf «wojret*!
rent* 1.27 « loc-t
Celculet*d everet*
0-1000
Celculeted evtret*
rente 4.M-2000
Celculottd ev*ret*
0.004-20
Celculetod eweret*
rente 0.20-17.2
Celcutetod evtreto
0-0. II
Celculeted evoret*
rente 4.74-17
Celculetod evoret*
0.041-1.7
Celculetod everete
rente 0.0002-1.44
Celcutetod ewerete
10.2 > lOE-l to O.I
Controlled
Uncontroll ed
Controlled
cefltr«!l*d lector, catculeteiol rente)
mw«itr«ll*d lectov« celcyletaol
controlled lector, Celculeted rent*
uncontrolled lector, olculeted
- 2000
contrtllod lector. Celculetod rent*
uncontrolled lector, ctlcuUted
controlled lector. Celculeted rent*
uncontrolled lector, calculated
controlled lector. Celculetod rent*
uncontrolled lector. Celculetod
controlled lector. Celculetod rent*
uncontrolled lector, celcuteted
controlled lector. Celculeted rent*
)I
MFIMM
too
too
too
too
100
100
100
100
100
too
100
100
100
3]
11
11
22
-------
Pew No. 17
M/2I/M
POLLUTANT
AobootM
Aebeetoe
Aobeetoe
Aebeetoe
Aabeetoe
Aebeetoo
Aaboetoe
Aabeetoa
Aabeetoa
Aebeetoe
Aebeetoe
Aebeetoe
Aebeatoe
Aebeetoe
Aebeetoe
Aabeetoe
•arlue
CM
Nunm
1312214
1112214
1112214
1112214
1112214
1112214
1112214
ISI22I4
1112214
1112214
1112214
1112214
1112214
1112214
IJJ22H
1112214
M401M
IIC
COM
32*2
32*2
1202
32*2
12»2
12f2
1212
12*2
12*2
12»2
12*2
12»2
12*2
12*2
12»2
IMUmiAL MOCfN
Aebeetoe product
Aabeatoe product
fabrication
Aabeatoe product
Aobeeto* product
fabrication
fabrication
fabrication
Aabeatoe product
fabrication
Aabeetoe product
fabrication
Aabeatoe product
fabrication
Aabeetoe product
fabrication
Aabeetoe text 1 lee
Aabeetoe tenttlee
oanufacturlne
Plaatlca oanuf acturlno
olaftlca eanuf acturlno
eanufacturlne
Vinyl /aebeetoe tile
•anufacturlne
Uaate oil coebuatlon
Ollof ION «OMCt KC COM fHIMION FACTM
•rllllM elllbeare) 10* flfcore/cc alr/»
rioor tllo « |b/tepj aabeatee
produced
rioor tllo 1.0 Ib/to* aeboeto*
produced
Frlctloe oaterlel 4 Ib/ton aabeetee
production produced
•Vlndlx brake ohooe 4*1 flbere/cc elr/i
eebeetoe oachlned
$auln< eebeetoo ceoent IIU flbera/cc alr/f
eheet eebeetoe oachlned
laulne aeboetoe ceoont 30S flbore/cc alr/e
eheet eebeetoe oachlned
lot no aaboetot oil [board 447 flbera/cc alr/e
aetaeatoe oachlned
Textlleo 40 Ib/ton aebeetoe
produced
Text 1 lee 2 tb/tofl eabeatoe
produced
Cntlre proceee 41.' Ib/ton aeboetoe
coneuoed
tntlre proceee 1.S4 Ib/ton eebeetoa
coneuoed
(ntlre proceae flO.I Ib/ton aebeetoe
conauoed
conaueed
coneuoed
coneuoed
U*ate oll-flred bollera 1 1.01 lb/1000 «al oil
KI50 million Btu/h) or burned
•pace haatara
Mm
•WCTaMoi •! tM% f oitultl
Uncontrolled
Control loo)
Controlled
Avoreoo of toet rooulto
Averaeo of toet roeulto. cut-off aAool ea«
Avoraoe of toet reeulte. toothed blade a ax
Averaoe of toet reaulta. toothed blade aa«
Uncontrolled
Controlled
Calculated ovorepo uncontrolled factor, calculated
ranee 2e. 7-Oi. •
Calculated everate controlled fector. calculated ranM
0. 024-15. »
Calculated averete uncontrolled factor, calculated
ranee 0.44-2000
Calculated averaee controlled factor, calculated ranee
».4» x 10-5 - 200
rente 0.24-271
2.4 x 10-5 to 0.21
Judeeoent, variable
~~«
22
33
33
33
22
22
22
22
11
11
100
100
100
100
100
100
5$
s
-------
POM Me. M
0*/2I/M
POLLUTANT
••rlu*
••rlue
•erftu*
••rlu*
••rlu*
••rlu*
CM IIC
KUnK* COM IMUtTIIM. PHOCIS* UIIUION HUM* KC COM UIIMION FACTO* MOTM
74401*1 MoW CMkuetlM. llood.lov* ultheut ktffl* 4 « IM-4 Ik/tM «oo« UncMtr*ll**1. kued M *n* *tu*V. nonb«ffl*d *t*v«
re.lde.tl.1 kur*l«* VOT plM
74401*1 224 «*VM t*krl* f I.I thin. Curl.. *VM - re.1. 1JOOOI S.I m IM-I Ik/tM «»brU UncMtr*ll«l. .MT«M .« thr«* te.1.
rl.lrt
74401*1 224 M«VM frt»-le fl*l*kl»« H*.t eettln* 110001 7.t x IM-4 Ik/tM «.krU Uncontrolled. k.»d M te.t tfet.
74401*1 224 Woven lokrlc flnllhln. Tenter lr.ee> - reel* 110001 1 x IM-» Ik/tM f«brlc Uncontrolled. .ver«M of four te«t.
74401*1 224 UOVM ftkrlc fl.lthl.e Tl>er*oe*l dvelne 110001 7.1 x IOC-S Ik/tM f.brlc Uncontrolled. ev*r«e* of three t«.U
74401*1 2S Wood CMtautlM. Morl.ont.l return tub* 10200*04 2M.O* Ik/10112 Itu h..t l.eplo reiultl. 1 Pl«nt. «ood flo«r.le . .(14 >•/«.
InduetrUI Input boiler «•• I-p»« de«l*n >/fly»D relnjectlon.
uncontrolled
nraxtt
M
(2
12
<2
52
174
177
74401*1 » Uood cookMtlM.
liufcutrl.l
74401tS 4*93 Huni«i»«I w*«t«
«tdk>r-llr«il Induitrl*!
boll or
Itluicotf or.lt >Uk«
>totor-t« 0.2* »•/«. boll.
til. 15. K
I020O»04 0.0074 Ik/ton «uol
0.00* Ik/tM xinlc. solid
•••to-dry Mt.
firoon nood» on* Blant. o*rtlcul«t* control
col Kc tor IcyclM*). Mod lood r«t« O.S4 tt/«. boll.
oil. 41.11
Controlled by •»r«y-bftlfl* scrubber. b««dd on ••terlal
b«l«nc« for Bodol tnclneretor
••rlua Iron OH|<
••rliM Iron 0nld«
•MIS <•> •nthracan*.
IIIIIII7 112 Iron loundc-Ui
III1III7 112 Iron loundrUi
Elackrlc trc furn«c« •
Electric arc furntco
chArgo «nd tM cvclo.
Scr*i» tlr«, o»*n burntnt Tir«« In •M»«rt*i«n
burn hut
0.14-0.ft lkn«ly on tl« txtret. ol I Ml-1 t««t t ftltor
coepont. vhrod condition • 2* by 2" tlmcm, burn
r*t«*l.l ki/hr. controlled
It4
ens let enthrecene
0.172 Ib/ton tire
Sue ol PAH «n«ly on lie extr«t. ol InO-2 test t filter
coeeont. ihrod condition • 2* by 2* piece, burn
r «nthrecene
Scrw tire, open burnln* tlrei In enperleentil
burn hut
0.232 Ib/ton tire
Sue of r»H «n«ly on ll< «»tr«t. of >AO-2 te«t t filter
coopont. tihred condition • 2" by 2" piece, burn
r«te'l.7 k9/hr. controlled
212
•ensenthr*ceno
Scr«p tire, open burning Tire* In experiment*!
burn hut
O.OM4 Ib/ton tire
Sue of PAH «n«ly on lie extr«t. of IAD-2 test t filter
coepont. ihred condition • 2" by 2" piece, burn
r«te>2.1 kfl/hr. controlled
lenseldehyde
Scr*p tire, op«n burning Tir«s In exp«rlM«ntftl
burn hut
1.2704 Ib/ton tire
1*0-2 extrict* u/nS «n4lf«l«. condition > 2' by
I- sl.c... burn r»te • I.I H/hr. uncontrolled
-------
•*M ate. 1*
0*/21/tO
POLLUTANT
tanz.ldohyde
•anialdehyd*
tanialtfahyd*
tanialdahyda
lenilldehvda
MnzaldOiyda
lanuldehyd*
Mnxaldahyd*
tani.ldahyda
lanz.ldahyda
lenzcn*
tanzan.
•anzan.
CM tIC
Munm coot iNMtraiM. macctt
100*27 fcraa tlra. an* aural.*
10OJ27 Scrap tlr*. op** kurnln*
100127 Scraa tlr*. *pan hurnln*
100*27 Scrap tlra. open burning
100*27 Scraa tlra. open kurnln*
100*27 Sera* tlra, a*an kurnln*
100*27 Scrap tlra, oaan kurnln*
100927 Scrap tlra. often kurnln*
100*27 Icri. tlr*. open kurnln*
100)27 Scrap tlra, *»earla*nt*l
kurn hut
burn hut
kurn hut
Tlr.. In axearlaent.t
burn hut
Tlr.a In axperlaant.l
kurn hut
burn hut
kurn hut
Tlr.. In *nf>arl*ent.l
burn hut
Tlra. In ax.arlaent.1
burn hut
burn hut
burn hut
burn hut
exhaust ..lesion.
MIMIC* MCTM
0.7*4 Ik/to, tlr*
O.I»J2 Ik/ton tlr*
0.1704 Ik/tan tlra
0.4*4 Ik/tan tlr*
0.44* Ik/tan tlra
0.42* Ik/ton tlr*
0.144 Ik/tan tlr*
0.17* Ik/tan tlr*
1.734 Ik/ton tlra
0.34* Ik/ton tlr.
O.S7» Ik/ton tlra
0.414 Ik/ton tlra
HCs
HOTtt mrunu
««0-2 extract* H/M *n.ly*ll, Chunk condition a l/«-l/4 212
of tlr*, bum r*t« • 1.7 kg/hr, uncontrolled
IMI-2 mtract* •/"» analyal*. Chunk condition • 1/4-1/4 212
of tlr*. kurn rat* • 2.1 k«/br. uncontroUad
voiT .saales. burn rat* - I.S kg/hr. *hr*d condition * 212
2- by 2* *l*c*. uncontrolled
UOST auala*. bur* rat* - 2.1 kg/hr. *hr*d condition • 212
2- by 2* .lace, uncontrol 1 «d
UOST aaavla*. burn rata - 0.» kg/hr, shr.d condition • 212
2* by 2* alaca. uncontrallad
UOST *aa»la*. burn rata - 1.1 ki/hr. ahrad condition * 212
2* by 2* alaca. uncontroUad
VOST s>ap)es. burn r.ta - 1.4 kg/hr. shr.d condition • 212
2* by 2* alaca. uncontrallad
2* by 2* aleca. uncontrolled
VOST a.a»lea. burn rata - O.I kg/hr, chunk condition. • 212
1/4 ta 1/4 of a tlra, uncontrolled
VOST *u.la*, burn r.t* - 1.7 k«/hr, chunk condition* • 212
1/4 ta 1/4 of a tlra, uncontrolled
VOST a«*le*. kurn r.ta - l.t kg/hr. chunk condition. • 212
1/4 t* 1/4 of a tlr*, uncontrolled
VOST KMles. burn r.ta - 1.27 kg/hr. chunk condition* 212
• 1/4 ta 1/4 of . tlr*. uncontrolled
VOST ••*»lo«, burn ret* - 2.27 fct/hr, chunk condition. 212
• 1/4 to 1/4 a< a tire, uncontrallad
VOST ••a.l... kurn r.t. - 4.43 kg/hr. chunk conditions 212
• 1/4 to 1/4 of . tlr.. uncontrolled
s
-------
Pega Ha. 40
09/21/90
POLLUTANT
Banzana
— -
§*MS«t«
••AlMltl
•mime)
••nitutoi
•etizonti
Mnt«n«
••AXtWItl
•enx«n«
Benzene
•enzen«
lenient
Benzene
Benzene
*""""•
CM SIC
MUntfft COM IMKItniM. PKOCCM DIlMION MURCf
71431 Internet CMoMiatioM Ut*t **ltt« dl«*«l WfcUlf
etlfjUe* * Mollc «Kh»utt «• I ••!•«•
71431 Ifit«riiet C4Mbu.it I M Ufht duty f>*MliM truck
•flfjlne* - Mbltd •HhlUi.t Ml •»lOO*
71431 Interne! coe.tH.st I on LI Kit duty e*solln« truck
en tines - •eblU *Kli«u>i Mi«»l«n«
71431 lAtwiul CtMbuttlon Ll«ht duty •••oll*i«
•n«tn«« - oMbild w«htel«, tmhauftt
71431 Intarnal cottbuctlon Ll*hk duty •••ollna
•ntlncft * Bobtltt v«hlcl*«. 3-w*>y c*t*ly«fc.
•Kh«u»t ••is.iiont
71431 Intcrnkl c«*>uitlon Llttht duty t»»ol.n«
•n«ln«t - Bobllti vehicles, 3-w*y c*t«ly«t.
•Ahtuct ••Itslon*
71431 lnt«rn*l cooibustlen Lloht duty fA*olln«
•ntin«* * oMitollii vehicles.
flonc»tftly*t/aKtd*ilen
c«t*lytt, «xh*ust
71432 N«tur*l «*s CMbustlon teller*. *xheu«t systea
71432 Sera* tlr«, «»en Ixjrn.n* Tire* In experleental
burn hut
burn hut
71432 *cr«p tire, open burnlnf Tires In e-.perleent.il
turn hut
burn hut
burn hut
burn hut
71432 Scrip tire, open burntne Tires In experimental
burn hut
burn hut
•cc coot minioN ricn*
t. 41 peme.!* •« «if*»u«t
HC«
1.141 l*u**nm •* «Kh*utt
HCl
I.II tMllttM* •«
•w«t*«r«tlvii HCo.
0.3S-l.m beoiM* •*
aveparetlwa HC*
1. 121 banxana of anheust
HC*
2.701 banxana of athsust
HC*
1.951 benxena o( exhiuit
HCs
102004 1.11! by vol (or 41 by
ntl •< total VOC
4.102 Ib/ton tlra
1.117 Ib/ton tire
4.705 Ib/ton tire
1.9B5 Ib/ton tire
4.704 Ib/ton tire
5.495 Ib/ton tire
1.0S2 Ib/ton tlra
1.051 Ib/ton tire
NOTCS '
•n.,.~,.. Jud««»t
KnglnaarlHf Judgaaant
0.15-O.441 fuel-lnjactad uahlcles, I.II-I.(II
carbureted light duty gu uahlcles. an*. Judaaaant
Cnilneerln* Judgaaant
Engineering Judgaaant
Engineering Judaaaant
South Caaet study. California, engineering judgaa»nt
VOST aaaplas. burn rste - 1.5 kg/hr. shred condition •
2* by 2* place, uncontrolled
VOST steples. burn rate - 2.1 kg/hr. shred condition •
2" by 2" piece, uncontrolled
VOST saaple*. burn rete - 0.9 kg/hr. shred condition •
2* by 2* piece, uncontrolled
VOST staples, burn rate - 1.1 kg/hr. shred condition •
2" by 2' place, uncontrolled
VOST saaples. burn rste * 1.4 kg/hr. *hr*d condition •
2" by 2B piece, uncontrolled
VOST saaples* burn rate - 0,8 kg/hr, shred condition •
2" by 2" place, uncontrolled
VOST saaples. burn rate - 0.5 kg/hr. chunk conditions •
1/4 to 1/4 of s tire, uncontrolled
Kraut*
IK
112
112
112
112
112
112
112
212
212
212
212
212
212
212
212
-------
**•• N». 41
Ot/21/tO
MLUJTMff
•MMM
•MMM
•MifiM
••n««fi*
Mnx«n«i
•*nxwi«
•«nx«n«
Mnz«fi«
§«mft«
••nz*na
•*ni«n*
••nacna
•*nz«nt
•«n2«n*
••nxanft
CM IIC
MUnKII COM IMDWnilM. mOCCM
M4J2 Scrap tin. MM bur*l*t
71412 «cr«* tlr«. opan bur*l*o;
71432 (era* tlr*. opan Inn-Hint
71412 Sera* tlr«. «o*n burnlnc
71412 Ua.to .11 coobu.tlon
71412 Uood combustion.
rasldantlal
71412 Uood coobu.tlo*.
r.aldantlal
71412 Uood coobu.tlen.
raaldantlal
71412 1>1 Aarlcultural
lndu>trv-fl«ld kurnlnt o<
plAsttc cro» cov*r*
71412 Ifl Awlculturtl
Induitry-IUld burnlni ol
plastic croa cowar*
71412 l»l «w-Uultur«l
Induetrvf l«ld burning ol
•l««tlc crop cftv«r»
71412 HI Avlcultur*!
lndu«try*4l*ld burning of
plastic crop covar*
71412 2491 Uootf prdiarvlnp
71412 24tl Uood pr««rvlni
71412 2fl* n«latc anhvdrlda
niMION UUDCf
TlrM In «xp«rl»«l
bur* but
Tlr*p 1* (iinrlMntPl
burn but
U»t« •ll-llrad b*ll«r>
«1SO •Illlen Itu/bl tr
•pac* h«atw«
fiall alrtltht
woodatovaa. blrcb wood
•••II atrtlpht
Hoodatovaa, birch Mood
(•all alrtlvht
Moodstowap. pprucd Mood
U»d black Plaatlc
Unuxd black plaptlc
Uaad black plastic
Unui«d black plaatlc
Tharaal (pan) •vaporatlon
of pantachlorophpnol
M«ttawatar
Product racovary abiorbar
KC COM INIM10N FACTO*
S.4M Ik/tM tlr«
4.22* Ib/tM tlr.
2.012 U/tM tlr.
2.111 Ib/tM tlr«
1 0.0417 Ib/IOOO Ml all
burnad
0.1IM Ib/ton dry
-------
P.** M*. 42
0*/2I/*O
POLLUTANT
•*ni*ne.
•onzen*
•onxen*
•enxone
Mnzon*
•onion*
•*nx*n*
•enxone
•*nx*n*
•enxan*
•*nx*n*
•enx*n*
•enxen*
••nzen*
••nzen*
•enzen*
•enzeno
•enzene
•enxene
•enxene
•enzene
CM tie
Mian COM iHutniM. PMCIM
71412 2*4 Petr*che»lcel production
71432 2M Petrecheelc.l production
71412 2M Petrocheolc.l production
71411 2M Petrechonlc.l production
71412 2M Petrocheolc.l production
71 432 2M Petr*ck*olcel production
71412 2M Potrecke*Uel production
71412 2M Petrocheelc.l production
71412 2*** Chlorobenion* production
71412 2141 Chlorobenxen* production
71412 2MS Chlorobenjene production
71412 2I4S Chlorobonzone production
71432 2145 Chlorobenzene production
71412 2(45 Chlorobenzon* production
71412 2I4S Chlorobenxene production
71412 2045 Cuoene production
71412 2B4S Cuoeno production
71412 2B45 Cuoene production
71412 2045 Cuoene production
71432 20*5 Cu..ne production
BIIMIIM MUM (CC COM
Plpelln* v«lv*e-«ee Ml
Pipeline v.lvee-lleuld Ml
t.fetK/r.U.1 v.lM. 101
OMn-^d.1 v.,v«. ... Ml
Open-ended v.lve.-lleuld 101
«.eel* connection* 101
Flen.ee Ml
Dr. In 101
ntooeenwlc dUtlll.tlon 3013010
went.
Atoo.pherlc dletlll.tlon 3013010
vente
•enzene etor.ee 407034
•enzene etoreee 407
Fudtlv* •oleelone 10110100
Fueltlve eoleelone 30130110
T.ll •>• tre.toont 10110101
co.u.n
coluan
l.nz.ne recovery coluon 30115.05
.crubber
OIIMION MCTM
4.21 Ik/kr
1.7* Ik/kr
1.17 Ik/kr
0.4M Ik/kr
2.7* Ik/kr
0.05 Ik/kr
0.15 Ik/kr
I.Of Ib/kr
0.44 Ib/ton cktorobenxen*
produced
0.0014 Ik/ton
Chlorobenzene produced
0.»2 Ib/ton chlorob.nx.no
0.12 Ib/ton chlorobenzen*
1.14 Ib/ton Chlorobenzene
0.12 Ib/ton chlorobenz.ne
1.04 Ib/ton Chlorobenzene
produced
0.0134 Ik/ton
Chlorobenzene produced
0.04 Ib/ton cueene
produced
produced
0.014 Ib/ton cueene
produced
0.0017 Ib/ton cueen.
produc.d
produc.d
HOTf* 1
Uncontr*ll*d, *etl*.tod o*leelone Ira* en ever.** pi wit
Uncontrolled, e.tlo.ted eol.ilone froo en «w*r«»e plent
Uncontrelled. e.tle.t.d eele.lon. Iran en .ver.ee plent
Uncontrelled, *etl*«t*d *nleelane 4ran en ever.** plent
Uncontrolled, cetlneted eel.iloni Ira* en .ver.t* plent
Uncontrelled. e.tla.ted oelxlon. Iron en .ver.ee plent
uncontrolled, e.tle.ted eelxlont froe en ov*ret* plent
Uncontrsllad, *etl*eted *oleelone fron en overete ptent
Uncontrolled
Controlled, cerkan tdeorptlan.
-------
Pete Mi' 41
Ot/Il/M
POLLUTANT
CM (1C
NU1KII COM INOUmlM. PMCCM
MISSION MUKI
«CC COM BIISSION FACTM
MOTH
TI4I2 2M* Cue em production
Cetelylt e(x tent
ecrubkor
714J2 21*» CUMM production Ueek-decenter eyltM
214J Cueene production Uaen-decMter eyetM
71411 2149 CyClohMMM production toy Fuottlv* «•.•»!en*
3OIIUO3 O.OU Ik/tM CUMM Contr«ll«4. «l«r«. t(S
•reduced
10115*04 0.01 Ik/tM CUMM Uncontrollod. 71.4 utl b«»M«
produod
U1IS«04 0.0001 Ik/tM CUMM Controlled, five. nS o«UI*ncy
produced
10II97M O.JO* Ik/tM cyclehexMo l»ed M Mdel pl«nt ultk cepoclty el 1.1 * 101* Ib/yr.
preduced uncontrolled
112
71412 2*4S
•rMuctlon by Fuittlv* «l>ilon<
10111700 0.1021 Ib/tM cyclohe»ne l»ed M eoMI Plent ultk Mpoclty ef 3.11 » IOEI
produced Ib/yr, unceAtrelled
71412 2149 Cpcloh.MMi.1 production bv Fuiltlvo ••..••ton*
10115780 0.014 Ik/ton cycloho»uio l»ed M Mdel Plent Kith cepeclty o( S.SI « 10EI
produced Ib/yr. controlled by Jl»eectlan/o*lntenence
71412 2I4S
i production by fuvltlwo Missions
IOIIS7IO 0.0*14 Ik/ten cyclohe»ne lind on eedel pUnt ulth cweclty e< S.SI « I utl
produced Ib/yr. uncontrolled
2S4S CyclohtxM.4 production bv Fue.tl
b*nz«n« tivdroonction
vo ••Isalon*
10115710 0.07 Ik/ten cyclohoKine l»ed an Mdel plent Kith 1.1 x IOCS Ib/yr cweclty.
preduced controlled ky Inepectton/eetntenence
71432 M45 Cvclohaxan* production bv Fugttlvo Mlccloni
30I157BO 0.0214 Ik/ton cyclohoxne lieed en eadel plent ultk I.It « IOCS Ib/yr cepectly.
produced controlled by Ineeectton/ealntenenco
2i*5 Cycloh«x«n« production bv Stor*«
b«nx*n« hvdro*«n*tlon
»rocfi«*
214$ Cvcloh«»«n« production bv 4tor49
b«nB«n« hydro«an*tIon
40701* O.SS Ib/ton cyclohexite l«.«d en eodel PUnt ultn cweclty of l.t x IOC* Ib/yr.
produced uncontrolled
407014 0.142 Ib/ton cyclohe«4ne »»»«d en eodel pUnt ulth cwulty ol 1.11 x IOEI
produced Ib/yr. uncontrolled
71432 28*5 Cvclon«Man* production bv Stor*p*
b*nzcn« hydro«in«tion
procaci
71432 2B*5 CvclohM»n« production bv Stor*t*
40701* 0.14 Ib/ton cyclohoxtni l»ed on eodel plent Kith cepeclty e< S.SI x 10EB
produced Ib/vr. uncontrolled
0.1272 Ib/ton cycloheKine lited on eodel plant ulth 1.1 x IOEI Ib/yr cepeclty,
produced controlled by Internet Heetlne-roof ttnke
2643 CyclohoKana production by &tora««j
t«nz«n« nydro««ri*tlon
procci*
0.12*2 Ib/ton e^cloh.-.n. l<«ed on «od.l plint xlth 1.31 « IOC1 Ib/yr cweclty
produced controlled by Internal floating-roof tanke
-------
Pew He. 44
0*/21/*0
CM tIC
KtUJTANT NUMCR COM HeXHTHIM. MOCIM inlltlOM «OMCt
•Mixene 71432 2B*C CyclebexafW >r eductlee by Iterate
rrecei*
lenione 71412 2MC Itfcyl benzene/a tyr one nlkylatlee reactor ere*
production vent*
lemene 71412 2MI Etkylkeniene/etyrene Alkylatloe reactor ore*
•reductlee vent*
leniene 71412 21*1 Itkylkeniene/«tyrene Ateottharlc/praaeure
•reduction coluen vent*
teniene 71412 2M> ftkylkeniene/ityrene Ateoaeherlc/rre**ur*
production coluen vent*
lensene 71412 214* Itkylkeniene/etyrene lenzene/toluene vacuue
production vont
lenlono 71412 2I4S ftkylbenzene/otyrene lanzena/toluon* vacuue
•reduction vent
lenxene 71412 214* ftkylben
•roductlon
lenzene 71412 284S Etkylbenzene/atyrene Other vacuue vent*
•roductlon
leniene 71412 284* Ethylbenzene/ityrene Secondary ealtilont
production
ICC COM DIIMION MCTO*
407 1.124 Ik/ton cyclehexane
10114*02 0.4 Ik/ten
etkyl ken«/*tyrene
produced
10114*02 0.000* Ik/tee
ethyl benz/ltyren*
•reduced
JOI14* 2.4 Ik/ten ethylkenzene
•reduced
10114* 0.024-0.** Ik/ten
etkylbeni/*tyrene erod
101 l«* « Ik/ton
ethylboni/atyrone
•reduced
10IU* 0.04-2.4 Ib/ton
ethylbenz/atyrene eroduc
10114*10 0.22 Ib/ton
ethylbent/atyren*
•reduced
10114*10 0.051 Ik/ton
ethylbonz/atyrene
•reduced
30114* O.OO4 Ib/ton
•tkylbeni/atyrene
•roducod
10114* O.OOOO4-0.0024 Ib/ton
ethylbenz/atyrene
10114* 0.1 Ib/ton
ethyl bonz/atyrene
•reduced
10114* 0.001-0.004 Ib/ton
ethylbenz/atyr prod
10114* 0.114 Ib/ton
ethyl benz/ttyrene
produced
Mom
laaed ee eedel plant ultk I. II x IOEI Ik/yr ceeeclty.
controlled by Internal fleatlne-reef tank*
Uncontrollod. for ethylkeniene production, bated on
eedel elent capacity ef 4.41 x IOEI lb/yr
Controlled, erece** heater *»•! efficiency, kaaocfon
eedel el*nt cwaclty ef 4.41 x IOEI Ik/yr
Uncontrollod. ba.ed en eedel elant «lth cwaclty ef
4.41 x IOCI Ik/yr
Controlled, flare «0-**X efficiency, bated ee eedel
•Unt elth capacity ef 4.41 x IOEI Ib/yr
Uncontrolled, eedel plant «lth capacity ef 4.41 x IOEI
lb/yr
Controlled, flare *0-**I efficiency, eodel plant Kith
capacity et 4.41 x 10EI Ib/yr
Uncontrolled, eodel plant elth 'capacity ef 4.41 x IOEI
Ib/yr
Controlled, detection and correction. 74X efficiency.
eodel plant vlth capacity ef 4.41 x IOEI lb/yr
Uncontrolled, eodel plant Kith capacity of 4.41 x IOEI
lb/yr
Controlled. *0-**> efficiency, flare, eodel plant "Ith
capacity of 4.41 x IOEI Ib/yr
Uncontrollod, eodel riant Kith opacity of 4.41 x IOEI
lb/yr
Controlled, flare 40-**S efficiency, eodel plant Kith
capacity ef 4.41 x IOEI Ib/yr
Uncontrolled, bated on oodel plant with capacity of
4.41 x IOE8 Ib/yr
MFIMMCf
14*
112
112
112
132
112
112
112
112
112
112
112
112
112
-------
»a«a kto.
09/21/9O
POLLUTANT
CM SIC
NUMC* COM IMUfTMM. PHOCIM
DllltlON MMCC
UC COM mlttlOtt PACTOR
7HJI 2MI ItkvlkMMIM/ai
production
2MS ithvloaniana/atv
productlM
Itarata a«4l ka*4»l*«
•alaalwta
ftorao* and kandliM
aalaalona
71412 2MS EtKytbaoiona/ttvrana ftorat* •»* ka»dlln«
production aalaalona
71411 2I4S ItkylkoniaM/atyron*. ttwao* and handling
production aataalona
407014 1.14 Ik/tM
407 0.172 Ib/tM
407014 0.00114 Ik/to*
407014 0.121 Ik/tM
plwt Mltk cwKltv *f «.«! K ion in
Ik/yr
CwitrollMl. flMtlm root. 151 iffUlMKy. »odl*nt ul «>u. ol 4.41 I IOCS Ik/yr
132
71412 2ttf Nltrobaniana production ianiana atoraaa
407 O.OW Ik/ton »Urc*«ni«n«
Contrcllod. Intarnal lloatlno rool. •»! oil.. k«M4 on
l.tt x IOCI Ik/yr cwaclty maOml riant
71412 2lif NttroktnsaM >roductlon lantwia atorava
71412 2I4S Nltrebaniana production laniana ateraca
71412 2l4t Nltrakaniana rroductlon laniana atoraoa
7I4I2 2I»I Hltraoanian* production Fualtlva aalaalena
407014 0.142 Ik/ton nltrobanian*
407014 O.S44 Ik/tan nltrobaniaita
•roducod
0.0142 Ik/ton
nltrobanaana produced
lOlltSIO 1.24 Ik/ton nltrobaniana
Uncontrollad. kaaad an 1.11 x IOCI Ik/yr capacity nodal
Plant
Uncontrallad. kaaad on !.»• x IOEI Ik/yr capacity aadal
Plant
Controlled, llaatlni rael. MS all., kaaad on 1.11 x
IOCI Ik/yr capacity aodal plant
Uncontrollad. kaaad on I.M x IOEI Ik/yr capacity nodal
plant
71412 2I4S Nltrokaniana production Futltlvo oolaalona
0.1! Ik/ton nltrobaniana
Contr.. 47.71 all. datact/carroct alnor laaki/Mch.
aaala. kaaad on !.*• x IOC* Ik/yr cap. oodal pla
71412 2149 Hltrokaniana production Fuiltlva anlaalona
71412 2I4S Nltrobaniana praductlon fuittlv* aalaalana
1011*580 0.74 Ik/ton nttrob«nz«na
producad
3011>580 0.1»• ID/Ion nltrobaniana
producad
Uncontrollad. aach plant. 42 punpa. SOO procaaa valvas.
20 prascura-rallat vatvaa
Contr.. 47.71 all., datact/corract laaka/aach. aaala.
42 puapa, 500 procaaa valvaa, 20 praa-ral val.
71412 2B«5 Nltraoanxana production Hltrobaniana
lOlltSOI 0.02H Ib/ton
nltrobaniana
Controllad. tharaal eKldlsar, 991 all., kaaad on 1.91 x
IOEI Ib/yr capacity oodal plant
71412 2145 Nltrobaniana production Nltrobaniana atrlppar 10II9S05 0.14 Ik/ton nltrob«n»na
Uncontrollad. kaiad on 1.91 x IOEI and 1.11 x IOEI
Ib/yr capacity nodal planta
71412 2145 Nltrobaniana production Nltrobaniana atrlppar
1011950S 0.0214 Ib/ton
nltrobaniana
Controllad. tnaraal ooldliar. 99.01 all., kaaad on I.11
x IOC a Ib/vr opiclty oodal plant
71432 2B45 Nltrobaniana production Urn
tor 30II9S02 1.92 Ib/ton nltrob.nj«n«
Uncontrollad, b
-------
Pea* Ma. 44
O*/21/*O
CM *S04 0. If ft Ik/tan
Kltretoentana,
!«„,„,« 71432 ZMI Nitrobenzene production u«l> end neutralization 3011*904 0. If 41 Ib/ton
Ml trabaniana produced
Imzono 71432 IMS Nltrobeniene production Uaeh and neutralization 1011*904 0.01*2 Ib/tan
tmnlfn, 71432 2I4S Nitrobenzene production U.a to-acid atarata 3011*504 0.102 Ib/ton nitrobenzene
,.„,«„. 71411 lie! Nitrobenzene production Uaeta-acld atarata 3011*504 0.0*4 Ik/ton nitrobenzene
|mln|( 7,432 M,5 Nitrobenzene production Uaeta-edd etrlppar 3011*501 0.34 Ib/ton nitrobenzene
produced
!„!„, 71432 2t*S fhanal production u.ln, -Spent air' fro. tne 10120202 0.004 Ik/ton ahanol
cuoena pracaaa oxldlzer
(anzana 71432 214* Aniline production rrocae* vent a 301034 0.0114 Ib/ton aniline
•enzana 71432 294* •enzana atoraae tanka CNternal floating roof 407 2.944 ton/yr
tank - total oaltlont
tank - total aalalont
tank - total ealatona
tank - total eeliloni
ttant '
Uncoatrollad, keaad a* I.M n IOU anal l.II • ion
Ik/yr capacity aodel plant!
Uncontrolled, fcaeed on I.M « 10ft Ik/yr capacity aodel
Plant
Uncontrolled, fcaeed an 1.11 11 IOCI Ik/yr capacity nodal
Plant
Controlled, vent abaarfcar. »4.4I elf., baaed an I.M *
IOCI Ib/yr capacity nodal plant
Uncontrolled, baaed an I.M x tOCf and 1.11 « IOEI
Ib/yr capacity nodal pi ant a
Controlled, vent abaarbar, t4.«l off., baaad on l.II «
10CI Ib/yr capacity nodal plant
Uncontrolled, baead an I.M « IOCS Ib/yr capacity nodal
plant
Uncontrolled, baaad an l.II K IOC* Ifc/yr capacity nodal
alent
Uncontrolled, ba.ed en I.M « IOCI and l.II « lOCf
Ib/yr capacity nodal pi ant a
At one aourca. eeaaured at poat oxldtior condanaar vent
Uncontrolled, froa data provided by producer
EF dataralnad far a nodal benzene tank UO.OOO «al vol.
CF deterelnad for a nodal benzene tank 140.000 eel vol.
30ft dla. SOturnovar/yr. llauld ant prl aaal
CF deteralned for a aodel benzene tank UO.OOO aal vol.
30ft die. 50turnover/yr. vapor ant prl eael
EF detaralnetf for a nodal benzene tank UO.OOO fal vol,
30ft dla. SOturnover/yr. vapor antd prl aaal
EF daterelned for e aodel benzene tank 1*0.000 aal vol.
10ft dla. SOturnover/yr. aach ahae >eal/rla
EF deteralned for a aodel benzene tank UO.OOO eat vol.
loft dla. SOturnover/yr. eech ahoe aeal
CF deterelned for a Model benzene tank 140.000 flal vol.
KFEHOI
III
III
111
112
111
111
112
112
112
112
112
202
202
202
202
202
202
202
-------
rot* He. 47
04/21 / tO
CM (1C
Muwn cow iMutnuM. men*
inlMION MUMCf
ICC COW niMION FMTM
7I4S2 2tt» tonzene etereeo ttnki
7I4J2 2M» lenzene etoreoe ttnke
71431 2M* lenzeno etoriee link*
71412 2Mt Beniono otareoo tMke
7 MM 2M* CeerelKtu production
71412 2ttt Cwrol*ct» »ro4uctlo«
71412 2Mt CwolMtu troductlon
I prod.
IOC-* Ib/ton LAI Controlled. u«ed ee luel. »t.«l ell.
vent produced
•en»ne atrlpplnt celuen JOI2II25 0.0074 Ib/ton LAI Uncontrolled
vent produced
••none (tripping coluen 10I2II2S 1.41 « 10C-* Ib/ton LAI Controlled, ueed ee iual. •*.*« ell.
v«nt produced
202
202
71412 284 » Lln.tr >ltyl6
-------
MUUTMIT
MMC* cox IMUSIMM. raocns
HUSSION
(CC COM HIIMIQM F*CTM
MOTM
71412
71412
71412
71412
71412
71412
7I4I2
71412
7 1412
71412
71412
71412
71112
71432
71432
71432
2*4*
2fMt
2*4*
2*4*
2*11
2*11
2*11
2*11
2*11
2*11
2*11
2*11
2*11
2*1 1
2*11
2*1 1
Linear alkylkoniono
olofln procoao
Llnoar alkylkonioM
•lolln erocopp
Llooar alkylboniono
•leflp, procooo
Llnoar alkylboniono
oloflii procooo
(thyloM production froo
nwhtka/oee oil
Ethyl ana production froo
naphtha/tarn oil
Etkylono production froo
naphtka/oae oil
Ethyl ana production froo
naphtha/oaa oil
Cthylono production froo
naphtha/«aa oil
Ethyl ana production fro.
naphtha/pao oil
Cthylono production Iroo
naphtha/paa oil
Ethyl ana production troa
naphtha/pee oil
Caaollno atoraoo at bulk
tor.lnala
torolnals
Gaiollne atorapo at bulk
torolnala
terelnala
Peaiene eieetroplc col UK
vont
Mydroooji 7 0.2022 Ib/ton othylono
producod
3011*7 0.0202 - 0.004 Ib/ton
othylono producod
1011*7 1.S14 Ib/ton othylono
producod
J0tl>7 O.IU4-0.01U Ib/ton
othvlono producod
407014 0.2*4 Ib/ton othvlano
produced
407 0.0442 Ib/ton othylono
producod
404001 <0. 44 « 10E-7 Oln«/vr, 0
la throughput
404001 4.41 x 10E-7 lb/yaar tank
of flaaollna
of 9110! Ina
Controllod. VHd •• luol. *t.*OS •<«.
Uncontrollod
Controllod. uaod aa fuol, M.*n off.
Control lod. llor*. MS oH.
Uncontr.. hxpothatlcal plant uatnp SOX naphtha/SOX oaa
oil ao food •/ othylono cap. 1.2 x IOC* Ik/yr
Uncontr., hypothotlcal plant ualno SOX naphtha/SOX *ao
oil al load •/ othylono cap. 1.2 x IOE* Ib/yr
Uncontr., hypothotlcal plant uilno SOI naphtha/SOI taa
oil aa <*od •/ othvlono cap. 1.2 x IOC* Ib/vr
Controlled. «larei (»0-»i» efficiency)
Unconlr., hypothotlcal plant Ullnp SOX naphtha/SOX •••
oil 11 feed •/ othvlono cap. 1.2 x IOC* Ib/yr
Controlled, flar.i (M-MX ofllcloncyt
Uncontrollod
Controllod. (loatlni roof tank, MX efficiency
laaod on a capacity of 14.000 boll
tinka for oaiollno
Inod on torolnal ulth 251. OOO pal /day and four atoraoo
tinka lor 9aaollna
112
112
112
112
112
112
112
112
112
112
112
112
112
112
112
132
-------
Pata Me. 4»
Ot/21/*0
NLUITMIT
BdAdUIW
•emzanej
BenMM
•anzaiM
•onzenej
•anzanej
fcanzana
•enzena
toflzena
ianzena
•ansene
•enzane
Ben zone
Benzene
CM SIC
NimtCft COM INBUtTMlM. MOCCSS
71432 2911 tAMllM •tar«a« at bulk
tar*J*al»
71432 2*11 Patreleue) refinery Mlth
er Mkl ntj/ref oral 119
71432 2*1! fetroleua refinery
without
cr*cklne/reforBifif
71432 3312 Coka avail ••• coabuetlon
71432 3312 Coke production.
by-product recovery
•rocau
71432 3312 Coko •roductton.
by-product rocowy
procosB
71432 3313 Coka production.
by-product racovvry
procasi
71432 3312 Coka production.
by-product racov«ry
procac*
71432 3312 Coka production,
by-product recovery
procau
71432 3312 Coka production.
by-product recovery
f roc 999
71412 3312 Coka production.
by-product recovery
process
71432 3312 Coka production.
by-product recovery
proceet
7M32 3312 Coka production.
by-product recovery
process
71432 3312 Coke production,
by-product recovery
proce««
BIIMION MMH KC COM OI1U10H FMTM MOTtt
ItWtM I*M. HCM4W-V 40KMI 4.41 II I0»-i Ik/VMT/tMt I.M4 M • (WKltV •< M.OOO MU
Mlilllc tlmm n«l. •* MMliM
•«t«rn IOt-4 Ik/ten caka Con trail ad. nltrawn er natural aaa klankatlnt avataa.
araducad fix alflclancy
lanaana atarxa 407 l.l* x IOE-I Ik/ton coka U»fh-ell acrubbar. *OX af
-------
Paee He. M
0*/2I/»0
CM IIC
NUHM*. COM
PMCW HUSSION SOUK*
sec COM tnissiON PACTM
N01M
71412 Hit eeke eraductlee.
bv-preduct recovery
preceee
71412 1112 toko production.
by-product recovery
procaaa
71412 1312 Coke production.
[ recovery
Coollna toner, tar bettoe 1O1O01 Metllalble
Oio Hoik Ml dual cool or. 10OX o44lcloncy
f>co>l-oooa*U II«MT
t.nk
f«co»l-«oo«nU llouor
toik
IOI001 0.011 Ib/ten coke Uncontrollad
103001 1.4 « IOC-4 Ib/ton eeke
produced
Coko ovon oaa blankatln* Iroo) colloctlra Mil.
of II Clancy
1112 Coke i
by-product recovery
erocoae
1112 Coke production,
. recovery
71412 1112 Coke production.
by-product recovery
proceaa
71412 1112 Coke production.
by-product recovery
proceaa
71412 1112 Coke production,
by-product recovery
proceaa
71412 1112 Coke production.
by-product recovery
FluiMncllouor
circulation tank
•luihlnt-llouor
circulation tank
301003 O.OK Ib/ton coke
produced
101001 1.4 K IOt-4 Ib/ton coke
produced
Llfht-oll condanaer vent 303003 0.171 Ib/ton coke
produced
Lllht-011 condenaer vent 101001 0.0014 Ib/ton coke
produced
Union troll ad
Coka ovon oaa blankatlnt Iroo] colloctln* aaln.
af II Clancy
Uncon troll ad
112
Llaht-oll atoraM
Llaht-otl atoraao
O.OIU Ib/ton coka
producad
Caka ovon ••• blankatlna I
alflclancy
Uncontrollad
roo ua hoi dor. MX
2.4 x IOE-4 Ib/ton coko Coo troll ad. coka ovon aaa blankatlno Iroo ••• nald
producad til aHlclancy
71432 1112 Coke production,
by-product recovery
proceaa
71412 1112 Coke production.
by-product recovery
procaaa
71412 1312 Coke production,
by-product recovary
procaaa
7M12 1312 Coka production.
by-product recovery
Llat>t-oll atoraoo
Lllht-oll auap
Llont-oll «uap
407 1.14 « 10E-1 Ib/ton coke Utah-ell acrubbar, »OI efficiency
producad
303003 0.03 Ib/ton coke producad Uncontrolled
303003 4 » IOE-4 Ib/ton coka Controlled, aourca encloaure. »BI efficiency
producad
>ln« 303003 0.04 Ib/ton producad Uncontrolled
-------
fate No. SI
NLLUTMT
CM tIC
MUnm COM INMMTRIM. MOCIM HIIMION MMCf
tec COM OIIMIOM MCTOH
teMxene)
•enxone
Benxene
lenxene
Benxene
•enxeA*
Benxene.
Benxene
tenxene
Benxena
Benxene
Benxene
Benxene
71412 Hit Coke production. Naphthalene eaearatlM 101001
byproduct recovery
procaia
71412 1112 Coke production. Tar decanter WlOOl
by-product recovery
procaia
71412 1112 Coke production. Tar decanter 103OO1
by-product recovery
procoaa
71412 H12 Coke production. Tar danaterlni JOlOOl
by-product recovery
proceaa
71412 1112 Coke production. Tor danaterlnt 101001
by-product recovery
procaap
71412 1112 Coke production. Tar dn.it.rlna UlOOl
by-product recovery
proceae
71412 1112 Coke production. Tar etoraee 1OJO01
by-product recovary
procoaa
71412 1112 Cake production. Tar •toraea 303O03
by-product recovary
procoaa
71412 1112 Cake production. Tar atoraee 101001
by-product recovary
proceaa
71412 1112 Coke production. Tar-lnterceetlno auep 303003
by-product racovary
procaaa
71412 III] Cake production. tar-lntarceptlne auep 301001
by-product recovary
proceic
71412 3312 Coke production, Wain-oil circulation tint 301003
by-product racovarv
procaaa
by-product racovary
•.174 Ib/tee coke Uncontrolled
produced
O.lt4 Ib/ton coke Uncontrolled
produced
7.1 x IOf-1 Ib/ton coke Controlled, coke even tee blenkatlne troe Collecting
produced a»i«, m efficiency
0.042 Ib/ton cote Uncontrolled
produced
0.0042 Ib/ton coke Controlled, "aah oil (crabber. MX efficiency
produced
B.4 * IOC-4 Ib/ton coke Controlled, coke even tee blank. tine free collectlne
produced a.m. tflt efficiency
0.024 Ib/ton coke Uncontrolled
produced
4.1 x IOt-4 Ib/ton coke Controlled, coke oven eaa blankatino free collectlne
produced oven. 9tfc efficiency
2.4 x tOC-1 Ib/ton coke Controlled. ..ih-ell acrubbar. tOS efficiency
produced
0.1*0 Ib/ton coke Uncontrolled
produced
0.0011 Ib/ton coke Controlled, coke oven eae blanket Ine free collectlne
produced aaln. *ii efficiency
7.4 « IOE-3 Ib/ton coke Uncontrolled
produced
producad froa «aa holder
132
l»
112
112
112
112
112
112
112
112
112
112
5
112
-------
rat* Mo. *2
Ot/ll/M
NUUTMIt
lemojio.
•enxone
•enxeno
•eflxone
•enxeno
•enxene
•enxene
•enxane
ftonxene
•onxone
CM IIC
NUMo* COM UMmiM. MOCCtt
71412 HI* Co*« •reduction.
erocoM
71412 H12 Cake production.
by-product recovery
oroceff
71412 44*1 CaaollM laadlne at kulk
71412 44*1 Caeellm leadlnf at kulk
71412 44*1 Ceaollno loadlnt at kulk
71412 44*1 Caoollne leadln* In
ear I no veaaala
71412 44*1 Caeollno leadlAf In
71412 44*1 Caeollne loadlm U
71412 44*1 Caeollno loadlnt In
oarlne veaael*
71412 44*1 Caaollno leadln* In
•arlne veiaola
71412 44*1 Caaellna loadln* In
71412 44*1 Caaellno loadint In
71412 44*1 Oaaollno loadlni In
tmttiON MMCt KC COM outturn r*«Q»
Uaad-ell decanter 10JO01 7.* • IOC-I Ib/tM coke
Uaen-oll decanter MUOl 1.12 • IOt-4 Ik/to* coke
Caagllne loadlet rack*. 404002 0.0711 Ib/IOCl oil
Caaollne loadlno rack*. 404002 0.02*2 Ib/IOCl «al
tub.ar*ad leadlne 404002 0.04*2 Ik/1011 eal
laraa. •••-freed, any 40*002 0.012* Ik/1011 oal •••
••rg«. tx.lc.l altuatlon. 40*002 0.020* Ib/IOCl eal *aa
•area, uncleanod, 40*00210 0.0214 Ib/IOCl «l •••
Shir/ocean barte any 40*0021 0.00417 Ib/IOCl «al •••
condition, nonvolatile tr*nafarr*d
•rovkoua carlo
Shl»/ocoM barte 40«002H 0.01 Ib/IOCI eal •••
b*ll««tad. volatile tranaferred
arovlou* c«rto
ShU/ocoan b.r*. cleaned. 40*0021 0.00*11 Ib/IOCI ••! •••
pravlout c«r«o
Shlp/oc«»fi b>r» ty»lc«l 4ut002J 0.0108 Ib/IOEl ••! •••
• 1 tuition, my careo trantf erred
Snlp/ac»n biroa 40*00237 0.01* Ib/IOCl ••! e»>
unclacnad. volatile tranaferrad
\
\
NQTtt
Unc on trolled
Controlled. »il efficiency, coke oven eaa blanletlni
free «aa koldor
Terelnal ailtk 2*1.000 eal /day. four atoraee tank a for
Torelnal liltk 2*1.000 eal/day. four (toraoe tanke for
Tarelnal vltk 2*1.000 eal/day. four 'toraoo tank* for
Uncantrollad, aaauolnt a kenxene/VOC ratio of 0.004. no
baall tlrth
Uncontrolled, aaauelni a benion./VOC ratio of 0.004. no
b.ale .Ivan
Uncontrolled, aa.u.lne a konxene/VOC ratio of 0.004. no
baale flrtli
Uncontrolled, aeeualn* a bonxone/VOC ratio of 0.004. M
baale elrth
Uncontrolled, aeaueln* a benxone/VOC ratio of O.OO4, no
baalt llrth
Uncontrolled, a«uelnf a penxene/VOC ratio of O.OOt, no
Uncontrolled, aaauelno a bonxene/VOC ratio of 0.00*. no
Uncontrolled, aaauolnt a banxana/VOC ratio of 0.00*. no
bill! firth
Uncontrolled, aaauelnf a benxene/VOC ratio of 0.004. no
btala ttrth
wmo
^ «.-----
112
112
112
112
112
112
112
112
112
112
112
1132
112
112
44M C*tollti« lo*d.n« In
•trln* vessels
T«nk«r b*lItstlnfl
404.00241 0.00501 lb/10C] 9*! «•*
transferred
Uncontrolled, assueln* • benzene/VOC rstlo ol 0.004. no
b*sls elrth
-------
row MO. ti
OttH/tO
POLLUTANT
eensene
~-
§•«•«!•
Mnswia
B«ntm«i
-.en.
.en,™
eeniene
.„,.„.
— ~
•«flZ«n*
•«nt«n«
••nt«n«
l.n,.n.
~" ~
••nxcnt
CM
hum*
71412
71412
71412
71412
71412
71412
71412
71412
71412
71412
71 412
71412
71412
71412
7I4I2
71432
71412
71432
71412
tic
COW
««.
4401
44»l
44»l
4UI
4»2S
4»2S
4»2S
025
4»2S
4>25
4*25
4*25
4*25
4*25
4»2S
4*25
4*25
INDUSTRIAL MOCIM HUSSION SOUkCf
taaolloe leadlet 1* Transit
oarlM veaaala
Caaollno atoraoo at bulk Iterate tanks. fixe* roof
plants breathln* loss
Caaollne storate at bulk Iterate tanks, fixed, roof
plants drain!** loos
(atollno iterate at bulk Iterate tanks, fixed roof
Internal coebuotlon Jet entlne okhaust
entlnos - ooblle
Coko by-product plants Open-ended lines
Coke by-product plant* Saepllnt connections
Coko by-product planta Praaaure relief devlcea
Coke by-product plaffta ffMnauatar*
Coke by-product ple/ita Puep*
Coke by-product planta valvae
Coko by-product planta FlufMno-llouor
circulation tank
Coko by-product planta laniano storage
Coke by-product planta ITX atorase
Coka by-product planta Ll»ht-otl auap
«CC COM IHItf ION FACTO*
40400242 *.OI4 Ik tear u*)/!OH
tol ••• tronsfor
404002 0.0] Ik/IOEI tal (000110*
404002 0.022S Ik/IOC] tal
•asolln*
404002 0.0174 Ib/IOEl tal
taaolloe
2 11.4 Ib/ton totol
hydrocarbons eolttod
101001 0.00* Ib/day
103003 0.40 Ib/day
10300) 4.S Ib/day
303003 0.51 Ib/day
101001 4.4 Ib/day
I01O01 0.42 Ib/day
101001 4.4 Ib/day
101001 0.004 Ib/ton coko
101001 0.011 Ib/ton coke
101001 0.004 Ib/ton coko
10100! 0.004 Ib/ton coke
103001 0.004 Ib/ton coke
103001 0.014 Ib/ton coke
MTf*
UnCMtrollod. M«M!M * Ixmm/VOC ratio of 0.004. m
baals ilrth
lased on keniene/vapor ratio of 0.004. typical bulk
plant u/ taa throuohput of SOI* tal /day
Tarelnal ulth 251. OOO tal /day. four atoraoo tanks for
•asollno
Torolnal ulth 2SI.OOO eal/da». four atorate tanks for
tasollno
lenxone ossuoed to bo 0.0471 of HC ooloolons
Uncontrolled fueltlvo Missions, avt. valuo. ronoo 1*
0.014 - 0.0*1 Ib/day
Uncontrolled fueltlvo delations, avf. valuo, rente 1*
0.57 - 0.42 Ib/day
Uncontrolled futltlvo eolation*, ave. value, rente It
4.17 - 4.11 Ib/day
Uncontrolled futltlvo eolaalene.
-------
O*/2I/M
•1C
roujUTMn
fMWIOH MUM
tCC CON HIIMIOM ««CTM
•anno*)
_«M.
to-iMA*
•*mi«A«
— -
•M.M.
MA-MAC
•«nx*f>as
•«ni4M«
**,.«.
— -
••flZtUt*
Wnxttn*
•«nz«fi«
••nZotfieTj
71422
714X2
71412
714)2
71412
71412
71412
71412
71412
71412
71412
71412
71412
71412
71412
71412
71412
71412
71412
4»2S
4»2J
4*2*
4»2I
4*2*
4*21
4f2f
4f2S
4»2S
4»2S
4*2S
4*51
4»SI
4*51
4*53
5012
5171
5171
5171
Can* ay product plant a Tar ateraa*
Cokd kyorooluc* atlanta Tar docantav
Cokd kyoroduct alanta Tar dawatorliiaj
Caka ky-product planta Tar-Utorca*tlm euoo
Caka ky-product planta lltht-all cendonaer vant
Cot* ky-product planta Maphtkalon* aaparatlea
and procaaalnt
Cokd ky-product planta Cool In* towor. tar kotta*
Cok* kyoroduct plant* Coellno touor. dlroct
Cthylon* production froa Futltiua aolaalona
napKtha/«a* oil
EthylMo production froo Fuiltlv* MlaalMa
naplitha/taa oil
Cthylono production froo 5acondarv aaurcaa
naphtha/taa oil luattauatar* atc.l
taua** aludoo fluldliod-bad furnac*
InclnoratlM
aoMao* aludo* Hultlpl* haartk ffurnaco
Sana** aludoo Stack taaaa
InclnoratlM
Caaolln* loadlnt at bulk lalinca larvlca
tarolnala and bulk planta
Caaollno loadln* at bulk Sulaih
tarolnala and bulk planta
jOyMH
mooi
101001
303001
303001
301001
101001
301001
3011*74*
3011*74*
101 1*7
50100504
50100504
50200504
50100701
4040014
40400134
40600111
•••II Ik/tM «**•
0.072 Ik/tM coka
0.01* Ik/tM coka
•.0* Ik/tM coka
0.0*4 Ik/tM coda
0.15* Ik/tM coka
0.102 Ik/tM coka
0.3*4 Ik/tM coka
0.0*10 Ik/tM otkvlan*
0.0174 Ik/tM ethyl ana
0.0414 Ifc/tM ethyl ana
1 » 101-4 Ib/tM dry
aludee
0.0204 Ib/ton dry aludio
(-31 ua/dace
Influent
0.077 Ib/ton aephalt
0.04*2 Ib beni vap/IOEl
*al taa tranafor
0.02*2 Ib ban> vap/IOEl
9al oaa tranafer
0.0711 Ib banl vap/lOE]
UncMtrolloO
UncMtrallod
Uncontrolled
Uncontrollod
Uncontrollod
Uncontrollod
Uncontrollod
Uncontrolled
Uncontrolled
Oet*ctlM/c*rr*ctlM of laaka
Uncontrolled
On* toot, ecrubber
nvoraoa of tlwo toota. acrufcoor
Colaalon teat* ualn« volatile ordanlc eeeollno. train
avaraa* fOTy that treat* Induatrlal oaatoMatar
•enxone aaauoad to be *.4I of THC
Uncontrollod, aaauotno a banxane/VOC ratio of 0.004. no
baal* el von
Uncontrolled, aaauoln* a banzane/VOC ratio of 0.004. no
baal* *lvan
Uncontrolled, eaaualne a benxane/VOC ratio of 0.004. no
171
171
171
171
171
171
171
171
132
132
132
101
101
132
50
*2
112
112
112
t«r»ln«lB and bulk el*nts bottaa
B*.l «•» tr»nif«r
-------
raw Mo. t*
0*/2I/*0
CM
POLLUTANT MUTODI
•onzene 71412
•anaano 71412
aenzene 71412
aenzene 71412
Sanzana 71412
aenzene 71412
Benzene 71412
aenzene 71412
•enzene 71412
1.2-lejnzleotMtzol-l-o«a. IIOT2
l.l-dla«lda
Senzo(a)pyrene 50121
•enzo1a)pyrene 50121
•enzofalpyrane 50121
lenzolalpyrene 50121
•enzofa)pyrene 50121
•enzola)pyrene 5012S
tie
COM ItfSUSTRIM. PMCfl*
5541 •aeollno Marketing
actlvltlaa
1*41 taaallM Marketing
actlvltlaa
5541 CatoIlM aarkatlat
actlvltlaa
S54I (atoll na aarketlng
actlvltlaa
5541 fatal |M etorate at
aervlca atatlona
5541 Eatollna etorate at
aervlca atatlona
S54I Cetollna itor.ee at
aervlca etattone
5541 Caaollna atorate at
aervlca atattona
•0* Hoaaltal Katte
Incineration
Internal coobuetlon
englnea - Mobile
Internal coaibuetlon
englnee - poblle
Internal coobuttlon
englnea - Mobile
Internal coebuttlon
englnea - Mobile
Internal coebuetlon
englnee - Mobile
Internal coMbuetlon
englnea - Mobile
mission SOUK* sec COM mission MCTM
Automobile ref Italia* 40*00401 0.0*5» lb/IOfl Ml
AutOMObllo refuel !«• 40*004 0.00*7 Ib/lOtl Ml
Stage II
Splllaao 40*00402 0.00417 Ib/IOfI M!
aaeollne throughput
VetiUla refueling, vapor 40*00101 0.0*4 Ib/gal of Ma
loaa pueped
Underground ttorage 40*00107 0.00514 Ib/IOCl Ml
tanka. breathing loaaaa Maollna
Underground atorate 40*0010* 0.001*7 Ib/IOC] Ml
tank*, tank filling gaaollne
loaaee ttaalanced
Underground atorate 40*00101 0.0*«1 Ib/IOCl Ml
tanka. tank filling gaaollne
loaaee (aplath fill)
Underground atoreae 40*00102 0.0442 Ib/lOE] gal
loaaea (aubeerged fill)
50200505 0.1-0.4 Ib/hr benzene
burn hut
4 cylinder car engine 1.54 K IOE'10 lb/elle
I cylinder car engine ». l» « lOt-f Ib/.lla
• cylinder engine * H IOC-9 Ib/elte
Dleael car engine 0.0071 Ib/ton partlculate
Turbochargad dletel truck 5 x lOC-S Ib/ton fuel
engine
engl ne
MOTH
Uncontrolled, baaed on bani./yepor ratio pf 0.00*
typical bulk alt •/ Ma thruput of Ml* gal /day
Controlled, bated on benz. /vapor ratio of 0.00* typical
bulk pit •/ Mt thruput of SOI* Ml/day
Controlled, bated on benz. /vapor ratio of 0.00* typical
bulk tit •/ Ma thruput of SOI* Ml/day
Terelnal ulth 251.000 eal/day. four ttoraae tanka,
Maollna
Terelnal vlth 251.000 gal /day, four atorate tanka
gatollna
lerelnal HltK 2SI.OOO Ml/day, four tterate tanka
aatol Ina
Terelnal ulth 251.000 gal /day, four atorate tanka
aaaolina
Teat report by California Air Metourcaa loard.
englnearln* Judgeoant
lnD-2 entractt u/M analytlt. ahrad condition • 2
4 cylinder catalytt, l»»l car
Range 0.002* - 0.014* Ib/ton
12«0 rpe. no load
1260 rpe, half load
far
for
for
for
• by
112
112
-------
l>a*o Ho. to
O*/2I/*0
POLLUTMrr
SenseCeloyreno
BenseCaleyron*
Sense (el eyr one
Sense <»)pyren*
BensoUlpyrene
BensoUlpyrene
Sense (e>eyr en*
Sense (elpyr one
Sense (elpyr one
BoAsoUlpyrone
Senso(e>pyrene
Sense (a) pyr one
Bense(elpyrene
Sense (etpyr one
Sense (a)pyr one
CM SIC
MUnSO COM IWUSTtlM. MOCtSS
S012S Intoroel (eebuetloe
onslno* - eoblle
S012I Uteroel ceebu*tle*
en*ine* - oeblle
S032S Internel coebuetlon
en*lnee - eoblle
50128 Internel coebuetlen
enolnee • eoblle
S012S Screp tire, open bureln*
S012S Scrao tire, open bur nine
S012S Scree tire, open burnln*
SOUS Screp tire, open burnln*
S032S Hood ceebuetlen.
reeldentlal
U12I Uood coobultlon.
reeldentUI
5012S Uood ceebuetlon.
residential
5012B Uood coebustlon.
residential
5012S 2*11 Petroleue refinery
5032B 2*11 ntroleuo refinery
50128 1112 Coke production.
mission soutcf
lereockereod dleeel truck
oe*lno
V-S *eeellM en*lee
V-B oaeollno on«lno
Tlree 1* experimental
burn hut
Tires In eKperleentel
burn hut
flree In OKporloentel
burn hut
fires le ONeerleentel
burn hut
(••II slrtltht
woodstovos blrck uood
full elrtloht
•oodstoves. klrch Mood
(••II elrtltht
uoodstovas. spruce need
(••11 •Irtleht
woodstoves. spruce uood
crtcker unit reeonorator
Fluldlsed bed catalytic
crscker unit roffenerstor
Slot oven cokln* - coke
quanchin*
SCC COM HUSSION rKTOX
I.t « 1M-* Ik/ton fuel
S.SI « IM-I Ib/elle
X.S2 it IOS*S Ib/elle
S.2* II lOt-S Ib/elle
0.2SS Ib/ton tiro
0.1*7 Ib/ton tire
0.221 Ib/ton tire
0.117 Ib/tan tiro
0.0012 Ib/ton dry fuel
burned
4.S » IOC-4 Ib/tan dry
fuel burned
1 « IOC-4 Ib/tan dry fuel
burned
0.00124 Ib/ton dry full
burned
10400201 Oi4B lb/1000 barrels of
10400201 1. II > IOE-S lb/1000
barrel* of feed
10100104 1 » IOC-4 Ib/ton coal
MOTM
1(00 ree. lull load
Uncontrolled, eountod on dyneeoeetor. o*t. SOOO-I2.0OO
•lloaoe. Incl. Sef> fr. condeneor collect, tor
Uncontrolled, eountod on dynaooeotor. eetloeted
1».OOO-2S.OOO olloeoo
Uncontrolled, eounted on dyneeoeoter. estleated
2S.SOO-2*.OOO ellea**
SUB of PM enely on II* ontrat. of InB-2 teet k filter
coepont. shred condition • 2* by 2* piece, burn
rete*I.I «*/hr. controlled
Sue of PnH anely en II* ex t rat. of InB-2 teet S filter
coeeont. ehred condition • 2* by 2* place, burn
rataM.I k*/hr. controlled
coepont. ehred condition • 2* by 2* piece, burn
rato>1.7 k*/hr. controlled
Sue of 'AH analy on 114 extrat. of IAO-2 test S filter
coeeont. ehred condition • 2* by 2* piece, burn
rata-2.1 k*/hr. controlled
Noreal kleh-teeeeraturo burnln* condltlone. based on
oel»ten teste
Sterved tir condition*, based on eelsslon tests
Noreal hlen-teeeerature burnln* condltlone. based on
eelsslon teste
Starved elr condltlone. based on eeleslon test*
Uncontrel 1 ed
Controlled by CO boiler .
ReTDOO
114
114
114
114
212
212
212
212
57
17
S7
57
148
I4S
114
3312 Cok« production.
by-product rtcovmrv
Slot ow«n coklnff - door 30300308 Ml nfl/N.3
Uncontrolled
-------
P*M No. 9V
09/JI/9O
fOLUITMir
S**i**U>»yraw«
SaAntatalayraA*
t*nxo U> eyrM*
•*AXoU>avraM«
•anxoUtayratta
ftanxa(a>ayr«na
ftaoxo»yrana
•artiaavrana
Banxa»vrana
la*ioU>ayr«nt
•aflxoayr«na
••fizotalpyrana
••niota>pyrana
CA$ SIC
MUMS* COM INBU9TRIM. MOCf IS
90321 3312 Cvk« aroductloA.
by-ar«duct racavary
N-ocaaa
S032* S3U r«rro4Uov »rQtfucttaA
S032S 4992 Smaaa; atudta
Inc.Aaratlo*
S032I 4953 nunUU.iI -Mta
coasbuatlon
90121 4953 fluitUlaal w*«t«
ctMfauctten
90321 4f53 HunUlit*! «**t«
COAbUVtlOA
K032S 4t53 nunUI»«l iMtta
C4MD4l«tIOA
50121 4tSI rtuntclvU M*«t«
CO«bU*ttOfl
S032I 4f93 HunlClpal «*«t«
S032B 4*53 IVinlcl**! M*tt«
coabuitlon
90321 4993 nunUlMt HMt«
co«bu«tlan
50321 4993 Huntc.**! uattfl
coabuftion
90321 4993 rXinUI»*l w»t«
coabuctlon
50321 4953 Ituniclp*! w«»t«
coBbustlen
9032B 4953 llunU.PAi »»*tk«
coaibuttlofl
90321 49S3 ttunl cl |*»I K**t«
coiibuttion
mission sowcc
l«*k>
tl«clrtc arc furftkct
4«rra«Ulco«* ffoductlwi.
lncin*w«tor
InclnwAter
n««« burn. h««t r«covwv
ficll.ty
Has* burn. h«4it r«cov«rv
lUcllJty
t1*«» bum. iionhfl«t
racowary facility
fU» burn. wat«r Mall
tncln*r*itor
nodular Inclnarator
nodular Inclnarator
ttultfpla chaaMr.
raclprocatlnt »tok«r
•rata
nultl*la chaabar,
raciprocttlntl vtokar
Hultl*l« chaabafi
trawallnv arata
Incinarator
ftafusa darlvad lual
Inclnarator
ftaluaa darlvad lual
incinerator
SCC COM
^
10100702
5
50100101
501001
501001
501001
501001
901001
901001
901001
50100101
90100101
50100101
501001
501001
miMION FACTO*
l.lnt/Nel
t.O •/Iki-hr enerey
coneuMd by furnace
1 x IOC-4 Ib/ton dry
aludee feed
5.1 n./el
f.4 x IOC-5 Ib/ton of
•aete coebuated
4 x IOC-4 Ib/ton of yaate
».4 x IOC-5 Ib/ton of
•aete coebuated
4 x IOC-4 Ita/ton ol »aate
coebuated
f.4 x 10E-5 Ib/ton uaate
burned
7.4 x IOC-4 Ib/ton el
uaate coebuated
4 x IOC-7 Ib/ton ol Hallo
coebuated
2.7 x IOC-5 Ib/ton uaate
burned
4 « IOC-7 Ib/ton uaate
burned
burned
2.42 x IOE-4 Ib/ton vaate
burned
2.4 K 10E-4 Ib/ton of
•aate coebuated
NOTt*
Uet Iff
Lou eneroy net acrubber. repreaenta (aaeoua end
partlculate KM
nveraee ol 2 x IOC-4. 1.4 x IOC-5. 2 Inclneratore each
.Ith net ecrubber. 1 cooeon atack
ESP. repreaenta both taeeoua and Partlculate POH
Controlled by K5P. baaed on aource teet dete
Controlled by dry alkaline acrubber t labrlc filter.
aeeueee »SI control efficiency
Controlled by ESP. beled on tource teet date
Controlled by dry alkaline Krubber 4 labrlc Illter.
aaaueee tSl control efficiency
ESP
Controlled by ESP. beeed on tource teet date
Controlled by dry alkaline acrubber * fabric filter.
aaaueea ess control elllclency
Uncontrolled, repreeente partlculate POfl
Hat acrubber. repreaenta partlculate POn
ESP
MPSHfN
114
114
114
114
111
111
111
til
114
III
111
114
114
114
-------
POM Mo. M
ot/tl/ro
POLLUTANT
•molalpVTOM
•oniofalpyrefMB
•onxo(a>pyrono
kanioUlpyrofio
•onsopyrono
oanao(a>pyrona
•enieU) pyrono
§onto pyrono
(on>a(b>lluoranthona
Banxa (b> 4 1 uor anthana
•enielbllluorantheno
lento (b) II uor anthana
•anxodlaalna
lensodlazlna
Benzodlazlna
CM SIC
NUH» COM INOUtTfllM. MOdM
(OUI 4M3 Municipal naoto
coabuatlan
(0121 4«1 Municipal uatta
coobuatlon
(0121 4«5I Municipal tuato
coobuatlon
(0121 4»5I Municipal luato
caabuatlao
(0121 4»5J Municipal uatta
caobuatlon
(0121 4fSJ Municipal twato
caobuatlon
(0121 4«5J (olid uaeto Inclaoratlan.
coaaarclal
(0121 4»5J (olid uatto Inclnaratlon,
(crap tiro, open burnln*
(crap tiro, open burnlna
(crap tire, open burnlna
million touKi .
•aluaa dorlyod luol
Incinerator
nodular atarvod-alr
nodular oxceeo-alr
coabuator
Laroa oaaa burn rotary
•atoruall coabuator built
attar l*«0
Larta oaaa burn rotary
uateruall coobuator built
alter 1*10
Heaa burn aiatarifall
caabuator. built baloro
Nultlplo cheeber ulth
auxllllery oea burner
II nil a chaeber
Incinerator
Tlrat In axpartaontal
burn hut
burn hut
Tlrat In exparlaantal
burn hut
burn hut
Tlrat In axparlaantal
burn hut
burn hut
burn hut
(CC COM tKIMION MCTM
fOIOQI 1.4 M !«€-( Ik/too, at
vaete coabutlod
M100I ».• x 10f-« Ik/ton teed
(01001 4.* x lOf-f Ik/ton lead
501001 0.00012 Ib/ton load
501001 0.00012 Ib/ton food
501001 *.« X IOt-4 Ik/ton lead
SOIOOI01 1.144 x IOI-J Ib/ton
waata burnad
(0100102 2.14 x IOC-4 Ib/ton Mate
burnad
O.IM Ib/ton tiro
O.Kf Ib/ton tiro
0.1*1 Ib/ton tire
0.00.4 Ib/ton tire
0.04( Ib/ton tire
0.0a2 Ita/ton tlra
0.04* Ib/ton tlra
NOTM
Central lad by dry alkaline acrubbar t labrlc Illtor.
eeaueeo *«S control atllcloney
uncontrollod. one data point only
UP control only, ona data point only
Capacity > 400 tone/day, up control only, ona dot*
point only, detection Holt reported
Capacity > 400 tana/day, uncontrollod. one data paint
only, detection Holt reported
UP control only, overall auereea at oovoral tourca
averaeee. ranee la 1.0 x 10E-4 - 1.1 x 10E-S
Uncontrolled, rapraaenta prloarllv partlculato POft
Uncontrolled, rapraaanta partlculato POM
(uo ol PAH onaly an lie axtrat. ol IAO-2 teat » Illtor
coapont. ahrad condition • 2* by 2* place, burn
rata-I.I ki/hr. controlled
(ue ol PAH onaly on tie oxtrat. ol IAO-2 teat A lilter
coapont. ahrad condition • 2* by 2* place, burn
rata«l.l ko/hr. controlled
(uo el PAH analv on lie axtrat. ol lnD-2 teat t Illtor
coepont. ahred condition • 2" by 2* piece, burn
rata*1.7 te/hr. controlled
(ue ol PAH analv on He extret. ol XAD-2 teet t lilter
coapont. ahred condition • 2" by 2" piece, burn
VOST aaaplaa burn rite - 1.5 k«/hr. ahrad condition •
2* by 2" piece, uncontrolled
UQST laaelet burn rate - 2.1 kv/hr. ahred condition •
2" by 2B piece, uncontrolled
VOST tiMplai burn rite - 1.1 ko/hr. ahrad condition •
2" bv 2" place, uncontrolled
III
1*0
1*0
114
114
212
212
212
212
212
-------
»•*» No. *»
Ot/21/tO
POLLUTANT
— .—
— "—
lensodlailn.
— —
•— "•—
••nzodUzl nm
•*nzo*ur*n
•—•*»-««
l«nio<«hl)p*ryl*n*
•«.•<""—'«'•
•anzolc *cld
••nzolc «ctd
CM SIC
NurtMR cone INDUSTRIAL mocc*$ snmio* MURCK
Scr** tire. .MOT kurwlit* Tir«> in .wwi.Miik.tl
burn hut
(crop ttra, «*an burnt n« Tirtta In *x»«rI.Mnfc*l
burn hut
•era* tlra, o»an burntnf Ttraa In *K**artaOTtal
burn hut
Scr*# tlra. «t>*n burnlnt T(ra» in ax»aria«(it..l
burn hut
Scr*w tlr«. o»an burnlnt Tlra« in aM.ftarI.Mnt*!
burn hut
•era* tlr«, o»«n burntni Tlr*n in «K»«rln«f.t*t
burn hut
burn hut
2711*4 Scr«» tlra. e*.H. burnlnt Tlr«» In *MB«rln«nt«l
burn hut
burn hut
1*1242 Scrap tlra. o**n burnlnt Tlr«» in .ixp«rl.»»nt*l
burn hut
IH242 icrM tlr«. oi*an burnlnt Tir.« |n axptrlaant..!
burn hut
191242 Scrt* tlra, opan burnlnt fir** In •Mp«rl««nt«l
burn hut
burn hut
45850 224 Uov*n fabric flnlthtnt Curtn« ow«n - rctln
f.ntih
•CC COW CflleUlON FACTCM
0.0ft Ib/tM tlra
0.04* Ib/ton tlra
0.02} Ib/ton tlra
0.042 Ib/tan tiro
0.029 Ib/ton tlr«
0.020 Ib/ton tlr*
0.044 Ik/ton tlr.
O.J5J Ik/ton tlr.
0.214 Ik/ton tlr.
0.207 Ik/ton tlr.
330001 0.24 Ib/ton fibrlc
worn
VOST 110*1 o. bur* r*t* • 1.4 li/kr. *hr*d condition o
2- ky 2* oloc.. uncontrolled
VOST «o*»le* bur. rat* - 1.7 k*/hr. chunk condition* o
1/4 to 1/4 of • tlr*. uncontrolled
VOST lieplo* bur. r*t. - I.I kf/kr. chunk condition* o
1/4 to 1/4 of • tiro, uncontrolled
VOST oioplo* bur. rite - 1.27 k*/hr. chunk condition* •
1/4 to 1/4 of e tire, uncontrolled
VOST >OBpl** bur* ret* - 2.27 t«/hr. chunk condition! •
1/4 to 1/4 of « tlr.. uncontrolled
VOST >iBpli> bur* ret* - 4.41 k«/hr. chunk condition* •
1/4 to 1/4 of o tire, uncontrolled
1/4 to 1/4 of e tire, uncontrolled
VOST *oB*le* burn rat* - 1.27 k*/hr. chunk condition* •
1/4 to 1/4 of a tire, uncontrolled
1/4 to 1/4 of a tlra, uncontrolled
Su. of PAH enaly on II. .utrat. of IAO-2 teat » filter
coapont. anred condition • 2* by 2' place, burn
riti'1.3 k*/hr. controlled
Sue ef PAH onily on II. ontrit. of IAB-2 teat * filter
coepont. ahrod condition • 2" by 2" piece, burn
rito-l.l k*/hr. controlled
Sue of PAH onily on 11* ontrit. of IAD-2 teit t filter
coapont. ihr.d condition • 2* by 2* piece, burn
coopont. *hrod condition • 2* by 2* piece, burn
ritO'2.3 kl/hr. controlled
Uncontrolled, on* teat
MFIMN
212
212
212
212
212
212
212
212
212
212
212
212
52
120
production - n«phth*lona
-------
Pace He. *o
Ot/2l/*0
CM »IC
HUtMn COJkt taOUITMM. PMCfU PIIMION SOU**
*CC CON
r«CTM
lanielC acid
*MM 2Mf Pktkallc anhydride Hale procaas Inclnerater MlOlt O.I Ik/ten M produced Centreline), tee* data and onelneerlno Judoeaeat
production - naphthalene
erMeae
«S*M 20*5 Phth.llc anhydride nala process Incinerator JOIOI* 0.211 Ik/ton PA produced Controlled, kaaed en teat data
production • xylene
120
«MM 20*5 Phth.llc
ilnerater 1OIOI* «.24 Ik/ten PA produced Unconlrellod. based en test data end i
120
Beniolc acid
*S*SO 2MS PkthaKc
production •
f«inidr«ducod Controlled, toot data and onolnoorlno Juaonont
••niolc acl<
45*50 20«S Phth.llc
production • xylano
process
fon kumlnt Tirol In o»oorloont*l
burn hut
30101* 2.1 Ib/ton P* oroducad Uncontrolled. kaHd an tolt data and engineer I no
Judtoaant
130001 1.2 Ik/tan ««brlc
0.21* Ib/ton tlr*
Uncontrolled, avaraea o« three teate
lue o( F*H onaly on It, extrot. ef InD-2 teat i filter
caepent. ahred condition • 2" by 2* Piece, burn
rate*!.! ke/lir. controlled
»enielk>«lueranthene 20700*
tcraa tire, ooan kuratne Tlraft la. OKaerleantal
burn hut
0.17* Ik/ton tire
hie ef PAH analy en lit axtr.t. of IM-2 teat a filter
coaoont. ahred condition • 2* kv 2* •loco, burn
rttoM.I ke/hr. controlled
lenie<«>flueranthene 20700*
Sere* tire, oeen burnlnf tiro* In oxterleental
burn hut
0.210 Ib/ton tiro
Sue of PAH analy en lie entrat. of >nO-2 teat t filter
coeoont. ohrod condition • 2* by 2* elece. burn
r«t«-1.7 to/hr. controlled
lenxofluoranthene 20700*
Scraa tire, aeon burnlnt Tiro* In axvarlaantal
burn hut
0.004 Ib/ton tire
aua af PAH analy en lie entret. of IAO-2 teat 1 filter
ceapont. ahrad condition • 2* by 2* etoca, burn
r
-------
Pee* Ma. ol
ot/2l/*o
POLLUTANT
•wxathloohon*
lon»thlo»hono
•onMthloehane
Mniethioehen*
lonlothloehene
•orvllluo
•oryl 1 1 uo
•oryl 1 1 uo
•oryl Hue
l.rvllUo
Beryl 1 1 U*B
lorvllluo
•oryllluo
Borvllluo
CM IIC
NUttM*. COM INDUSTMM. PMCES* UIIMION SOUHCf ICC COD
•SIM Icroo tiro, won burnln* Tlraa 1* o«*orloo*tol
bur* kut
»SUI fcro* tiro, **on kurnln* Tirol 1* oworloonUl
burn kut
»5U» Scrw tiro, won burnln* Tirol 1* oxoorloontal
burn hut
•SIM Cera* tiro, won burnln* Tiro* 1* oworloonUl
burn hut
•SIM (era* tlra. won burnln* Tiro* 1* oworloonUl
burn hut
7440417 Cool coobuotlon Anthracite co«l-«lrod 1
cyclono bollere*
7440417 Cool coebuotlon Anthracite co*l*flrod 1
cyclona bailor*.
utll/coooerc/lnduotr
7440417 Cool coobuitlon Anthnclte cool-llrod 1
cyclone bollor*.
utll /coooerc/lnduatr
7440417 Cool coobuotlon Anthracite coal-tired 1
•ulverlied (not/dry bot.)
bolloro. utll/cooo/lnd
7440417 Cool coebuotion Anthracite cool-ltrod 1
•ulvarltod (wet/dry bot.)
Dollar*, utll/cooo/lnd
»ulv«rliod
bollar*. uttl/cooo/lnd
7440417 Cool coobuitlon *ntnr>clto cool-flrod 1
•tok«r bolloro.
7440417 Co«l coobuctlon nnthr»c!to co*l-flrod 1
»tok«r boll«r»,
utll /cooMorc/lnduitr
C INIWIOM r«CTO«
O.OSS Ib/ton tiro
0.1*4 Ib/ton tlr*
0.071 Ik/ton tlr*
0.017 Ib/ton tlr*
0.011 Ik/ton tlr*
bur* rot* - O.I k*/hr. chunk condition* •
1/4 to I/* *f • tiro, uncontrollod
VOST ***olM burn r.t* - I.T k*/kr. chunk condltlono •
1/4 ta t/i *4 * tiro, uncontrollod
VOST ***»lo* bur* rot* - 1.27 k*/hr, chunk condition! •
1/4 ta l/o a* a tlra. uncontrollod
VOST **a»lo* bur* rat* - 2.27 k*/kr. chunk condltlono •
1/4 to I/* •< • tlr*. uncontrollod
Uncontrolled, colculotW b»od on an*ln**rla* Judoooont
onilnoorln* Judoooont
Contrallad ulth ISP. colcuUtod boood on *n*ln**rln*
Judooojont
Uncontrollod. calculated baood on *n*ln**rtn* Jutf*ooont
Controllod ulth wiltlclan*. calculated baled M
onfllnoorln* Judoooont
Controllod ulth ISP. colcuUtod baood on on*lnoerln*
Judtount
Controllod ulth ocrubber. calculatod b»od on
onvlnoorln* Judoooont
Uncontrallod. calculated baood on on*ln**rln* Judoooont
Controllod ulth oultlclono. caUuUtod baiod on
onalnoorlna Judoooont
mmtai
212
212
212
212
212
M
34
M
M
M
M
M
M
-------
Pata- Mo. 42
Ot/21/tv
MLUITMT
•eryllluo
lerylUuo.
lerylllue
lerylllue
tervllluo
lerylllue
•erylltue
leryllluo
leryllluo
terylltuo
lorylllue
lorvlllue
Beryl Hue
CM *IC
NUnKD COM IMWmlM. PMCCM WIMION MMKf
744O417 CMl ceebultlon Anthracite- coal-*lrod
atelier bailor*.
uUI/coaeerc/loduatr
7440417 Cut ceebu*tle« lUuelnou* coal-tlrod
cyclone boiler.
ut 1 1 /ceee*rc/l nduitr
7440417 CM! cw*u>tl«« (UU>IMMI(
bolleri. utll/cou/lnil
7440417 Co>l coabuetlon lltuolnoul ce«l-lnoue ce>l-
-------
Poo* Mo. el
0*/2t/M>
POLLUTANT
lor yl Hue
loryllluo)
Soryl 1 luo
loryllluo
•oryllluo
loryllluo
loryllluo
loryllluo
lory! Hue
loryllluo
loryllluo
lory luo
CAS SIC
IMISa COM INOUfTRIAL PMCtM (MISSION SOMCf
744O4I7 Coal coobuetlo* Llonlto coal-fired
cyclone boll or a.
7440417 Coal coobuotlon Llonlto ceal-Hrod
botto.) bo! lore.
utll/cooo/lod
7440417 Coal co-buetlon Llmlto coal -fired
eulverlied Idry/uet
botto.) bollera.
7440417 Coal coobuatlon Llonlto coal-llrod
bottool toller*.
utll/cooo/lnd
7440417 Coal coobuatlon Llonlto coat-fired
bottoo) bollera.
utll/coo./lnd
7440417 Coal coobuatlon Llonlto coal-llrod
utll/coee.rc/lnduetr
7440417 Coal coobuatlon 11 unite coal-
-------
p.aa No. 04
Ot/2l/»0
POLLUTANT
•orylllue
•orylllua
•orylllua
•orylllua
•erylllua
CM IIC
NUMM COM INDUtTRIM. rMKUf
7440417 Coal coakuatlee.
residential
7440417 Caal coekuatlon.
reildantlal
7440417 Coal coakuatlon.
ret! outlet
7440417 Internal coekuatlon
enolnea - otetlonery
7440417 Internal cookuatlan
enelflea - atatlonery
flUMION MUM* *CC COM HIIMIOM MCTO* NOTM
lallora llrad kv cool ».S Ik/IMIt MM Itatontrollod. calculated koaad on on tl near In. Judooeont
(roe rocky eountole
Lltnlta caal-llred 27.1 Ik/IOflt It* Uncontrolled, klokly variable, calculated kaaed en
aalUrt en»tnearlni Judeeeont
Sukbltuelnoua coal-fired II.« Ik/IMIX Itu Uncontrolled, klokly varlaklo. calculated kaaed on
ballera en.lneorlno Judooeoat
Raclarecatln* antlna - *.0*» Ik/IOfIX Itu Uncan trailed oolaalona
dUtlllate all lual
C» turklne - dletllleta O.S24 Ib/I0€l2 Itu Uncontrolled oelealone
ell fual
MFDhlMCK
M
M
M
XII
XIJ
•«rvlltm
Oil CMku>tl«l
Oil »«buitlo«
Oik co«bu«kken
Oil co«bu»tlo«
DlitllUt. all-llr«tf
bailor.
utl1/co««orc/lndu>tr/ro«l
OofltKI
OKtIIUto oll-«(r«4
bailor,
util/coul
donkl*!
X.I Ik/IOCU Ity
I.U lb/IOCI2 Itu
O.I* Ib/IOCIl Itu
0. If U/IOC12 Itu
Uncontrollod. calculated kaua) an antlnoorlm Judiooint
Controllod vltk aoUUlooa. calculatad kaoad an
analnaarlNV Judaooant
Control tod »lth It*, catculatad b«««d an axtlMartn*
Control lad ylth acrukbar. calculatad kaaad an
antlnaarlat Judtaaant
larylllua
•orylllua
Oil caaDutttan
Oil coobuitlon
«o>ldu
-------
Ot/21/to
CAS *IC
Nunm COM iNnumiM. MOCKS
tnlUION MMCI
«CC COM IHUIIOM MCTM
MTU
teryllluB
taryllliw
perylllu.
ierylllue
lerylllue
lerylllue
•orylllu*
oery I Hum
0.2S 1B/10C12 Mu
7440417
Mood cooouetlan.
rooldontlel
7440417 10»» beryl or« olnlno
7440417 224 UOVM febrlc
744O4I7 22* Woven febrU llnl«hlnt
7440417 22* Moxon lebrle «lnlthin«
7440417 22* woven iobrlc «lnl»Mn»
744O417 2»51 *»h«ltlc CMCr«t«
7440417 2»5I *»h>ltle eoncr«l«
production
Controlled vltk xrubbv. ulcuUtcd »«»W M
ontlMorUf
utll/conMrc/lnauitr/rofl
dontlal
Uooditov* .Ithout ko«IU
fntlr* procoss
Curln« avwi • rooln
«lnlM
Thoraoiol dyolnf
'Unt tt«ck
•lint itock
7440417 1241 Ceeent mnufocture - dry fnllre procoM
7440417 1241 Count nuiulicturi - y«t
»reco»s
Cllotor coolor
2.1 « IOS-7 Ib/tan Mood Uncontrollod. b»od Ml an* .tudv. nonbtKlod ttovo
bumliit froon Bin*
10* 0.2 Ib/ton oro alnod tntlnoorlnf JudMMnt
110001 l.« ii IO€-« Ib/tM l«nt. ov«. of 2 v
concroto rontw lo 2.1 - 2.t II 10C-II Ib/ton
305002 I. of, x IOf-12 Ib/ton Controlled lOt-t lb/Mi-hr
open, ferroeenfteneoo onerpy coneuoed by
4urn«co
Clectrlc «rc rc (urn.ce. 30300702 2.1 x 10E-« Ib/oy-hr
•e*l-»e«led. ferrotlllcan eneroy convuoed by
lurneco
J0» O.I Ib/ton te i
Uncontrollod
Controllad. wonturi icrubbor
Uncontrollod
let
-------
raea NO.
o*m/*o
POLLUTANT
CM (1C
MUrtKX COM IMUtniM. MOCIM
IHIIUON MUM*
tec COM mftioN FACTO*.
HOrif
leryllluei
lerylllue
lerylllue
•erylllue
lerylllue
•erylllue
•erylllue
aarvUlua
•ervlllue
•erylllue
•erylllue
7440417 M eerylllue alley - Koldlni MI
production
7440417 le lerylllue alloy - Holdlne 101
production
7440417 U >erylllue alley - Entire proceee 101
ataeplno/draulne
7440417 14 Ceraelce Entire aroceae
7440417 4MJ Municipal uaate Itaae bure. refractory SOIOOI
coebuatlon facility
7440417 4»SJ ItunUlpal Mete naaa burn, uater vail 101001
coebuatlon Incinerator
7440417 4*91 Municipal Maate Modular Incinerator SOIOOI
7440417 4993 Municipal waate ftefuaa derived fuel SOIOOI
coebuatlon Incinerator
7440417 40SI Municipal uaata flaluaa oarlvetf fuel SOIOOI
7440417 4tSl Municipal uaato Nodular atarved-alr SOIOOI
7440417 4PSI Hunlclpal uaate nodular atarvad-elr SOIOOI
coebuatlon coabuator
•••1 Ib/ton alley
0.0004 Ib/ton alley
produced
0. 1 Ib/ton M oreceaaed
I ,./,«, I. oro.....d
0.021* Ik/tan controlled
1.12 x IOt-4 Ib/ton
controlled parttculate
7.2 x IOC-S Ib/ton
controlled parttculate
0.11 Ib/ton controlled
eertlculata eelealona
0.0001 Ib/ton Uf
4.4 x IOC-7 Ib/ton feed
2.« x IOC-4 Ib/ton feed
Uncontrolled
••*«"•
*••'-"•• *-- "*
loelneerlne Judeeeent. controlled
Controlled by 1ST, baaed en aource teat
Controlled by IIP. baaed on eource teata
Controlled by IS*, baaed on eource teat
Controlled by IS*, booed on aource teat
1001 mr fuel only. (SP control only, overall averaoe
of aeveral aource averaeoa. ranee la t.t x IO€-7 -
O.OO02 Ib/ton
ESP control only, overall averaee of aeveral eource
averaee*. ranee le 4.4 x IOf-7 - 1.2 1OS-7 Ib/ton
Uncontrolled, overall averaee of aeveral eource
averaeea. rente le 1.4 x IOC-7 - 1.4 x IOE-4 Ib/ton
II*
III
II*
II*
U*
11*
II*
II*
IM
1*0
IW
••rylllut.
744O4I7 4951 ttuniel,»»l w.>ft«
1.9 M IOC-5 Ib/ton l**d tSP control only, dotoctlon li*lt roportod. ov«r«lt
*vg., r*n»« i* 4.1 x IOC-4 - 1.4 x IOC-5 Ib/ton
»«ry\\.u*
n**« burn. «*t«r H*U SOIOOI
InclnarAtOT
4.1 N IOC-5 Ib/ton *««d Uncontr«ll«d. onti d*t* point only
••rylllun
•orylllu
7440417 4*51
7440417 4953 rtuniclp*! w.»t>
co* 400 tont/iUv. CSP CBnlr&l only, on* d«t»
point only
4 > IO£-« Ib/ton d
Capacity > 4OO toni/day. apray drytno after acid eae
and fn control, dot. Holt, overall avi. . ranee le 3.1 x
IOE-4 - 4 X IOC-4 Ib/ton
••rylllu
7440417 4953
n**t burn Mit«ry«ll 501001
co«but,tor. •••!! ilxcnflw
nod*i. to »ny tgt Biidlu.i
2.4 » IOE-1 Ib/ton l«.a
C*p«clty < 400 tonrt/d«y, ESP control only, on* d«t«
point only
-------
••pa Ma. 4
09/21/90
POLLUTANT
•arvlllua
•grylllun
tarylllua
tarylllua
tarylllua
larylllua
laryltlua
larylllua
llbaniyl
llbanzyl
llghanvl
llghanvl
llghanyl
llghanyl
llghanyl
7
CAS lie
NUttM COK INCUtTP-IAL MOCfll
7440417 4951 Municipal Haata
caatauatlon.
7440417 4951 Iknlclpgl Mata
ca«bugtl«l
7440417 4951 Iknlclpal Mgta
caabuatian
7440417 4951 Itunlclpgl uaata
caabugtten
7440417 4951 nunlclpal nagta
caabugtlon
7440417 4951 Municipal Mata
coabugtlon
7440417 4951 5au«gg aludaa
inclnarttion
7440417 4951 Sgu>ga gludga
inclngrgtion
101297 224 Uovan fabric flnlahlng
101297 224 Uovan f.brlc flnl.hlng
92524 Scrtg tlra, oggn burning
92524 Scrgg tlrg. opan burning
92524 Scr4g ttrg. oggn burning
92524 224 Uovgn <4brlc flnl.hlng
92524 224 Uouan f.brlc hlng
inlSIION MMM
Hagg burn watarwall
n«gg burn uataruall
co.bu.tor. built bafora
I9M
lt*ga burn uatgrwall
coabugtar. built bafora
1910
lUgg burn, rafractary
l4Clllty
n»g burn. rafractary
facility
n«gg burn, rafractary
ficlllty
Fluldl lad-bad 1.1 Ig/hr. Uncantrallad
0.4,47 Ib/tan tlra lnD-2 axtracta v/KS analyglg. ghrad condition •
0.4.95 Ib/tan tlra IAO-2 axtr.ctg u/KS gn«lyg|g. Chunk condition >
0.147 Ib/ton tlra InO-2 axtrutg «/nS analyalg. Chunk condition •
af tlra. burn r*ta • 2.1 kg/hr. uncontrallad
110001 0.0044 Ib/ton ftbrlc Uncantrallad. a»ar
-------
rate NO. a*
04/21/»0
POLLUTMn
CAS IIC
Munm cone iiwitniM. men*
IMUION IWMCt
tec COM mistral roctfln
MOTIt
llphenvl
IIphonyI
•or on
»2»24 22* Ueve* fabric flalahlat
»2»24 2*11 Petrelou* refinery
7440421 Uood coobuttle*.
residential
Tkeraoaol eVelM
Fluldliod catalytic
crackln* unit, futltlvee
Uaadatovo Klthaut baffle
• JJOOOI «.eo*4 Ik/tw tikrlc UMMtralM. avvaw •! tM ta.t«
tat «.OO« Ik/nr laMd an Mlafctatl wlnlM itraan content
R
*2
0.0014* Ik/to* i
Uncontrollotf. oat** on on* atuoy. «onba«l«« itow*
ournlM* oroon oln«
7440420 22* Move* fabric flnlahlnt Cur lot eve* - rial* JJOOOI ?.« • IOf-1 Ik/to* fabric Uncontrolled, avarat* of three teat*
tor on
7440421 22* Woven fabric flnlehlnt
744042* 22* UOV4M fabric flnleklnf
4-kroeochlorobonzona IMltl
Iroeodlchlorooothane 71274
4»5J Senate tludta
Incineration
2-lroeo-4.«-dlnltrouillln 1II77JI 22« Uovan fabric flnlahlnt
Ha«t MttUt
7440421 22i Itovan fabric tlnlahln* TharMaol oValn*
22a Uouan fabric IInlthlnf • Tharooaol 4voln(
JJOOOI I « IOf-« Ik/to* lakrtc Uncontrollo4. kaao« on toat tfala
Tantar Iraoaa - roaU JJOOOI I.I » IOE-4 Ik/ton fabric Uncontrolled, avoraw ol four ta«ta
flnUhlni
JJOOOI I.14 x IOt-4 Ik/ton
fabric
Uncontrollod. avoraoo of throo taata
1)0001 2.» x IOC-4 Ik/to* fabric Uncentrollod. auoraw of tuo taata
haartk furnaca 50IOO5O* O.OOJ Ib/ton OVy aludaa Ono toat. acrubkor
dyalnf
JJOOOI 0.0024 Ib/ton fabric
Uncontrolled, ono toat
ft
12
12
101
12
|-orooo-2.4-rflnltroban>an SI44IS 22* Movan fabric flnlaMna
Curlna owan • raaln
flolth
t-lroeo-2,4-dtnltrobenien M44H 22* Uovan fabric flnlahlnt lonti
JJOOOI 0.0114 IB/too fabric Uncontrolled, overate of tee taata
rtat* JJOOOI 0.042 Ib/ton fabric
Uncontrolled
l-lrooo-2.4-dlnltrDboi
-------
Pet* Mo. 4*
09/21/90
CM
POLLUTANT NUnOM
1.3-lutdl*ne 104990
1.1-lutedlene 104990
I.I-*utBdl*ne 104990
l.J-Sutedlene 104990
1.3-tutedleno 10*990
l,3-*ut>dlene 104»>0
l.J-SutJdl.n. 10*990
l.3-»ut«dlene I0«990
SIC
CODE IHOUSniM. NOCtSt INISSION SOUK*
Scrw tlr*. MM burnln* Ilree 1* *x*erlBMt*|
bur* hut
Scrtp tlr*. M*n burnln* Tlree In e«»erloent«l
burn hut
Sere* tlr*. open burnln* Tlree 1* experleenUI
burn hut
Scr«* tlr*. MM burftlnt Tlr*« In ***«rl»Mt*l
burn hut
Scree tlr*. Men burnln* Tlr*e 1* *x»arl**ntel
burn hut
Sere* tlr*. oeen burnin* Tlree In exeortoentel
burn hut
2J»» Febrlc production- Eeulpoent le»ter CUrliler
28 Indu*trl«l u«ft€w*ter 0|i«n trench
off CODE KNIWION 'ACTOR
2.SSS Ib/tM tiro
0.3(2 Ib/tM tlr*
0.1(7 Ib/tM tlr*
•.170 Ib/tM tlr*
O.lll Ib/tM tlr*
0.0i3 Ib/tM tlr*
(.73 tMB/vr
307007 0.47 lb/»ef *l woferboerd
produced
301 0.2* x oeee o( *ollut«nt
In ueeto etree*
301 0.01 > •*»• a< *atlut«it
In u«eta etreeo
301 0.021 « ••!• of pollutant
.
301 0.43 * *••• 0< pollutant
301 0.059 M •«•• of pollutant
- '•
NOTM
VOST **vlm bur* ret* - O.f k*/hr. chunk condltlMO •
1/4 to 1/4 M • tlr*. uncontrolled
VOST *M*|*( bur* ret* - 1.7 kt/hr. chunk condition! •
1/4 to 1/4 «f * tlr*. uncontrolled
VOST •*e»lot bur* rite - 3.S kt/hr, chunk condl tl Ml •
1/4 to 1/4 *f * tlr*. uncontrolled
VOST eeool** bur* ret* - 1.27 k*/hr. chunk condition* •
1/4 to 1/4 *)i • tlr*, uncontrolled
VOST **Ml*« bur* ret* - 2.27 k(/hr, chunk condition* •
1/4 t* 1/4 of • tlr*. uncontrolled
VOST ••eoloe bur* ret* - 4.41 kt/hr. chunk condition* •
1/4 t* 1/4 of * tlr*, uncontrolled
Controlled lun*p*clf l*dl . end uncontrolled. Iw.ed M
on* plent'* dete
•vereo* **il**lM ftctor for thro* different reeln
eyetee*
Uncontrolled MleelMe
Uncontrolled Mleelon*
Uncontrolled e*leelone
Uncontrolled eel ••lone
Uncontrolled enlsvlone
•VIMM
212
212
212
212
212
212
144
207
20S
20S
20S
20S
205
JOS
JOS
JOS
105
-------
•a*. Me. 70
0»/2l/tO
POLLUTANT
CM (1C
m*m* cent INDMTMM. raonw
{MISSION SOtMCI
»CC COM KHIStlON FACTO*
I.I-tutadle
1.3-tutedtano
l.l-lutadlan*
I.J-tutadlane
I.S-ftitadlene
I.I-lutadlana
I.I-lutadlene
1 . 1- tut Adi one
I.I-lutadleno
I.I-lutadlene
l.}-(ut>dlen*
I.I-lutadleno
I.I-tutadlene
1.J-eutadlane
1.3"Sut«di«n«
I04*M 21 Induatrlel
I0*?»0
lOettO 21 Industrial naatanatar Junction kex
1049*0 21 Induatrlel uaeteuatar
104990 21
104990 21 Tetranydrophtnallc Iaul»Mnt laak
anhydrl4a/ac!d areductlMi
10»»»0 2121
l«k«K production
tyrana coaelyftar
•roductlen
I04>M 2(21 Acrylenltrlla-eutadlana-a rracaia vanta
tyrana ca»alvaar
pro4uctla«
!0«*tO 2B2I Acrylanltrlla'but«dlana-i *re<.»« vant*
aroductlen
I0«>»0 2821 nathyUat(ucrylata-but«dl CauU.ant laak
•reduction
I0*»«0 2821 nathylaath>cryl b»*d on one pUnt'a
-------
Pew Me. 71
Ot/2l/*o
POLLUTANT
I.J-eutedleno
l.l-lutedlana
l.l-lut>dlene
I.I-lutedlana
1.1-euttdlene
l.l-lutedlene
l.l-lutedlene
l.l-lutedlene
I.I-8utedtene
l.l-8utedlene
l.I-8utedlone
l.l-8utedtene
l.3-8utedlene
l.^lutedLn.
1.1-lutedlone
l.l-lutedlene
CM IIC
Nunm COM imuiTitiM. PMCIM
I0«f*0 2121 Polyvlnyl cklerlde
production
I0e**0 2121 Ityrene-butedlene
copal yoor production
10e*tO 2121 ttyrene-butedlene
copolyner production
I0e**0 2121 Ityrene-butedlene
copolyner production
IOe»tO 2121 ttyrene-butedlene
copal year production
IOe»M 2121 Styrene-butedlene
copolyner production
lOetM 2121 Styrene-butedlene
copolyner production
lOeMO 2122 Neoprene nenulecture
lOetPO 2122 Neoprene eenuiecture
lOetfO 2822 Neoprene eenuiecture
lOefM 2822 Neoprene eenuiecture
I0e»»0 2822 Neoprene nenuiecture
IO«ttO 2822 Neoprene eenuiecture
I0e»»0 2822 ralybutedlone production
I0e<»0 2822 Polybutedlene production
10e»»0 2822 rolybutedlene production
(HltllOH SOUnCI
fueeeneion eracaM*
entire plent
lecondery eourco-ethor
lleuld Meete
lecondery eource-atber
lleuld iteete
•ecendery eource-ether
lUuld veete
Ceul patent leek
Process vente
Procoss vente
Dlchlorobutene rollnlne
Dlchlorebutono eynthesls
Ceulpeent leek
Ceulpeent leek
process vente
""' "
Eaulpeent leek
Process vents
Proc««s vents
KC COM
IOIOIMI
JOIOII
101018
MIOII
JOIOII
101018
301018
101
101
101
101018
101018
101011
101
101
101
unman MCTOR
«.2 « IOf-4 Ib/ten PVC
0.02 Ib/ton
0.02 Ib/ten
O.MO Ib/ton
7.271 tone/yr
7.10 Ib/ton
14.2 Ib/ton
I. 12 Ib/ton neaprana
produced
0.« Ib/ton neeprene
produced
2.2 Ib/ton neoprene
produced
produced
2.TS4 tane/yr
2.22« tons/yr
12.210 Ib/ton
2.» Ib/tan Pld produced
O.OS2 Ib/ton Pld produced
1.0 Ib/ten Pld produced
MOTH
leene) an • oweM plent. l»« dete. I.I n lOU Ik
cepeclty. control etetue n»t corteln
Contrallad (unepeclllod) . evoreee enleelon lector beted
on I 1 eel 11 ties
Controlled lunepecllled) . evareee enleelon lector besed
en II lecllltles
Controlled (unspecllled) . evoreee enlsslen lector besod
an II lecllltles
Uncontrolled, ever sea oelselon lector beped an 1*
lecllltlee
Contrallad (unspecllled). evereee enlsslon lector besed
on II iecllltles
Uncontrolled, evoreee eelsslon lector beped an II
iecllltlee
Celculeted Iron netlenel enlsslons end netlenel
cepeclty. aeetly controlled
Celculeted Iran netlonel eelselons end netlonel
cepeclty. noatly Contrallad
Uncontrolled. Celculeted Iroa netlonel eeleslons end
netlenel cepeclty
Uncontrollad, evereee eelealan lector beeed an 2
(ecllttlee
Controlled lunspecllled) . evereae enlsslon lector besed
on 2 lecllltles
Uncontrolled, evereao eelsslon lector besed on 2
lecllltles
Uncontrolled, beted on evereia pi elK plent'e
cepecltlee end enlealons
Controlled (Here). Celculeted Iron evorsae ol lour
plente eelsslons end cepecttleo
Uncontrolled, besed on one plent 's eetsslone end
It*
121
-------
r0 2(22 rolykutedlone production Procoaa vonto
I04»*0 2(22 relrkutadtene production Eoulpoont leak
I04**0 2(22 Polykutadlene production H-ocunn vonto
JOI •.» Ik/toe *M ereduced Uncontrolled, kaaed on ono »l*nfi «aU
101 •.140 Ik/ton rM oroducod Uncontrolled, ovoroo oolMloo <«tor b*»od o> I
iMllltln
lot t.»*O Ik/ton rM oroaucod Uncontrollvd. OVOTMO oolnlon factor buod on i
lullltloo
Ml 10.4 to**/w
Ml 0.14 Ik/to*
Uncontrollod, ovoroto oolxlon loctor k»»d M *
iMllltlo*
Controlled (unooocKlodt, ovortw ooltilon foclor koood
on « locllltloo
1*0
loo
lo*
l.l-lutno
t.S->ut>dlono
I.I-lut«dlon<
IMttO 2122 Stvrofio-kutidlono rutbv tuttdlono idiarotlo
•raduc. ky owitalon
pokv«orli«tton
101024 ».2 Ik/ton (M producod Uncontrollod. koood on Induotry ootioitoo
I04*M 2122 ttyrom-butadlMio ruWwr
production
l«t
10*»M 2122 ftvrono-BUtadlona rubtxr Frocou uinto
production
10*MO 2122 ftyrono-butadlono rubbor MMtnutor o«l> 214* 1.1-lutadlono production rrocua vonta
104»M 214* t.l-(utadlono proouctlon i«ul»«nl Utk
101151 0.44S Ik/ton
JOI 15501 «.2 ItaMon producod
0.11 to«o/yr
Uncontrollod. avoraoo onl«
lacllltloa
Uncentroltad kaiod on ono plant'* data 14*
Controlled (unopocKUdl. and uncontrolled, kaoed en 144
ono plant'a data
l.l-Putadtano
I04«>0 284* ndlponltrlla produc
10125420 0.2 Ik/ton AON producad
Uncontrollod. kaaad on oolaalonp and capacltla* ol two
Planta
l.l-lut»dlona
I04»*0 2<4* ndlponltrllo production rroc<» v.ntt
3012S«I5 0.10 Ib/ton nON producad
Controlled, baaad on ooloalona and capacltlao of tuo
•linto
l.]-lut>dlana
1049*0 204* Adlponltrlla production y**t«w«t«r and handllnfl 3012S4 O.Olfl Ib/ton nON
Uncontrollad. baaad on anlaalon* and capacltioo of two
pUnta
-------
Pat* No. 71
0*/2I/*0
POLLUTANT
I.J-IUtadlan*
I.I-lutadlene
1.1-ouUdlone
I.J-lutadlene
I.I-Outadlene
l.I-tutadlene
l.l-lutadlene
1.1-Outtdlane
l.]-lutadlene
l.I-OuUdleno
l,]-*uUdlene
I.I-lutadlana
1.1-lutldlene
l.I-Outadlene
l,]-0utadlene
l.l-luttdlena
l.}-lut
1041*0 2»*»
lOatfO 214*
I04»eo 2S«»
104*aa »a<
lOitM 20a*
104»ao 214*
I04»»0 2I4»
104**0 30
104t*0 10
I0«»»0 10
10»»»0 10
10«»«0 10
I0*»>0 30
INDMTIIIM. PMCIH
MlMiiltrll* mductlM
«dUoaitril< ^reduction
MUvnltrlU >r>ductlwi
MlMaltrlU »r«ductl«i
fciUdlm cotrlMr
»ro4uctlo«
Iut4dl«<« production -
r«cov*ry »roc«««
lut>dl«M production -
r«cov*ry procast
lutldlana production -
racovary procasa
Tatrahydrobanialdahvda
production
Tatrahydrobanialdahyda
production
Tatr>hydrabwi»ldaliyda
production
Nltrlla aUitoiar
production
Nltrlla alaatoaar
production
Nltrlla alMtooar
production
Nllrllt altitoaar
production
Synthatlc rubbar
production
Synthatlc rufabar
production
iniHlw SOUKI
(•condary MUTCM
(yaatwatar. itc.l
Ca.ulp««nt Idak
Procaaa vonta
Procaaa wwita
Procaaa vonta
EaulpMnt loak
Procaaa vonta
Uaatawator aolaalona
Eaulpaant latk
Procata vanta
Procaaa vanta
Sacondary aourcaa
fMAitawatar. atc.l
Cqulpaant la«k
Procata vanta
Procaia vanta
Eauipaant lakk
Eaulpaant la*k
KC COM RIIMION PftCTM
1012*420 0.020 Ik/tM MM n-oducad
WI2S420 >.t» tona/yr
IOI2S4IS l.JJ tona/vr
I«l2S4lf 0.0t4 tOK/vr MH aroducatf
440 Ik/ton IPC producad
U1ISUO 2.4 Ib/tM produced
JOIIJ1 0.2 Ib/ton producad
101ISI O.o Ib/too troducad
4.1 tona/yr
I.S4 Is/ton TH» producad
0.0 JO Ib/ton THI producad
106004 0.010 Ib/ton altrlla
al aatooor produced
lOiOOa 0.741 tona/yr
J08004 la Ib/ton nltrlla
alaatoaar producad
30800* 4 Ib/too nltrlla
alaatoaar producad
St. 30 tona/yr
«7.7 tona/yr
NOTE*
Uncoajtrajlld*. (varow aa4aaloo « actor baaad M S
tacllltlaa
Uncontrollod, awat* aalaalon factor baaad M 2
laciUtldt
Uncontrollad. avaraaa aalailon factor baaad M 2
facllltUa
Contrallad tunapocl , avarato Mlaalon factor kaaad
on 2 facllltUa
Control lad (unapaclf lad) . and uncontrolled, kaaad M
on* plant 'a data
Calculated Iroe national ealaalona and capacltlaa.
averat* o( uncontrolled end controlled pi ant a
Calculated Iroe national eelaalon* and capacltlaa.
average df uncontrolled and controlled plant*
Calculated fro* national eelaalona and capacities.
averete *f uncontrolled and controlled ptanta
Controlled
-------
>«ee No. 74
0*/2I/M
POLLUTANT
CM (1C
Nunm coot IMXMTRIM. nociH
(MIMIM MUKI
«cc COM niiuioN r«CTM
I.I-eutidlene
1.1-lutldlene
lOettO «*$J Ueetweter treiteent
IO**tt SS41 CeeellM Mrkotlne
ectlvltle*
MTU
Vehicle refuel!*** veeor
loee
I0*t7l 28fS Cerban blect e«nuf.cturo Iteln ereceee euree vent
- ell furnace
•0100701 1700 Ib/ten I.J-butedleno Meed en o*4e. eedellee fer kwetb. POTH. rovroeonte IM
In Influent ivoriee POTH tint treite InduetrUl M.teiuter
40*00101 I.M Ib/eel of Me eoeeed LI.ted e* N-buteno/l.l-eutidlone Mleilon ret* 4
10100504 0.14 Ib/ten cerben buck I.eed en teet dete *7
produced
l-tutuel
l-lut.nol
l-Ktenol
1-fut.no!
I-lutinol
711*1
711*1
71J*1
711*1
7IM1
711*1
711*1
7IMI
711*1
711*1
711*1
711*1
711*1
713*3
2!
2*
21
21
21
20
20
28
28
28
28
28
28
28
InduotrUI Metewiter Uetr
InduetrUl Meteu'ter Oil -niter ewereter
Induitrl.l MMteMter Treiteent tmd
treiteent
InduetrUl «iete»ter Hon-ior.ted blob.. In
Induetrlel uiit«Kit«r nor. ted blob.eln
tre.teent
Indu.trl.l ui.teu.ter CUrlller
Induitrlil M.touiter nerited eeu.llMtlen
Indu.trl.l wi.t.Miter Non-iirited e^uilllltlon
tro.toent b.iln
Indu.trl.l u.«t.«.ter 0»on trench
Indu.trl.l u..te«.ter Sue*
Indu.trl.l ui.toiter LKt ititlon
Indu.trl.l wi.t.witer Junction box
Indu.trlil uiit.uitor ninliole
treito.nt
Indu.trlil ui.t.witer Driln
101
101
Ml
101
101
101
101
101
101
101
101
101
101
101
0.2* it MM e< eelluttnt
In met* etree*
«.» X IOE-4 X MM *f
2.* » IOC-1 X MM ol
0.10 x e.ee ef eellutwit
In MMt* etree*
0.041 x ee.e o« »ellut.nt
In w..te etreee
7.8 x IOC-1 x e.M e<
0.41 x BMO ef eollutint
In uiete etreie
0.11 it MM *f eollutint
4.1 x IOC-4 K eiee of
•ollut.nt In wiete .iro.o
2.1 x IOC-1 x e.M ef
eollut.nt In w..te .treie
I.« x IOf-1 x MM of
eollutint In H..te .true
l.f x IOC-1 x e.M of
I.I x lOC-S x MM o<
8.7 x IOC-S x MM of
wtcontrelle* eeAeeien*
Uncontrolled eele.lene
Uncentrclled eel Ml one
Uncontrolled eeleelene
Uncontrolled eeleelene
Uncontrolled eeleelene
Uncontrolled eeleelene
Uncontrolled eeleelen*
Uncontrolled eeleelene
Uncontrolled eeleelene
Uncontrolled eeleelene
Uncontrolled eeleelone
uncontrolled eel Ml on.
Uncontrolled eel Ml on.
20*
20*
20*
tat
s
-------
»••• HO. n
M/2UVO
POLLUTAHT
CM SIC
***** cow INDUSTRIAL nocctt
tniMidN MUetf
KC COM IMHIOH FACTO"
NOTH
2-K,tyl alcohol
•utyraloenvJe
•utyreldehyde
lutyraldahyde
7i»2* 2**» Clycorle production -
chlorleatloii eroceie
I04fll 2Ie* Acetone/phenol
Manufacture froe cuoon*
I2J72I Hood coobugtlM.
reeldeitUel
12172* Wood coebuatlon.
roeldentlal
UJ7J1 J»5l Awhllttc concr.t.
744041*
74404It Co«l CMbuitlon
744041* CatlM>
744041* Coll coobuitlon
744041* Coil coobultlo
744041* Coal coebuatlon
Coal coebuatlon
Coal coebuatton
MIIMIt Ut.« Ik/tM flvcvl*
•llyl ftlCOtMl •!•.»
CuMit* »ar«Kfd*tlM <
Plant »ttck
Anthrftctt* CMl-flrvd
UUI/CQUWC/.ndue.tr
Anthrulti co«l-Mr«d
cyclen* ball«r*»
ut 1 1 /couvc/ 1 nduitr
Anthriclt* co«l-(lr«d
ou.ro.d itokw b«ll«r,
ut 1 1 /co««rc/lnduitr
ov«rf««d stokw bollar.
utll/co«a«rc/lnduttr
MI20202 0.0044 Ik/tM »k«Ml
0.4 Ib/to* wad kurn«d
UKO«trall«d. MMMdJ m VQC I* butyl *1«M1. t*tt
d*t* M4 ulcuUtlm
Contrail** (Mi w«cl«l«U . b»*« on uwltM. Itn
d«t«, •»••••• tutor*
Uncontrolled. *vor«M wlulon <ourc«
t«»t»
IfO
O.t4 Ib/ton M«otf burneid Uncontrolled, avw*** MlHioA <*M:tor b«Mrf •* wurc*
AnthrAClt* co*l-ltr«d
ovtrfmtd »tok*r boiler,
utU/co.i.i«rc/lodu«tr
ArttftrJcU* co*l-*lr«d
pulv«rtz*d dry bottom
beilur*. utll/couirc/lnd
Anthr«c.t« eo*l-flr«d
pulverized dry botto*
boiler*. uUl/co»«rc/.nd
Anthrtctt* co»l-ftr«d
pulv«rlz«d dry bottoa
boil«r«. utU/co*..i«rc/tnd
AnthfAclt* co*l-ftr«d
pulv«rtz«d dry bottoti
boiler*, ulll/co-««rt/l,,d
IOS002 0.0024 Ib/tM cM«r
7.0 Ib/I0fl2 Itu
f.O Ib/IOCll Itu
11-20 Ib/IOCU Itu
7.f-14 Ib/IOCI2 Itu
2.7-S.2 U/IOCI2 Itu
II I6/IOCI2 Itu
7.* lb/IOCI2 Itu
2.1 lb/IOCI2 Itu
0.0»-0.40 lb/10CI2 itu
•»od on lloltod to«t d«t«. cycloM/xot Krubbv
control
Uncontrollod. c«Uul«tod b««od on ontlnoorlnt Jud*ooont
Controlled Hltb oultlclono. olcuUtod b<««d i
ontlnoorlnv Judvooont
Uncontrollod. calculator b»od on ondnoorlm Jud»»ont
Con trot lod Kith oultUlono. ctlcuUtod b>Md o*
onglnoorlnt Judoooont
Controlled ultK IV. celculeted beeod on ontlneorlne
Judeeoont
Uncontrolled1 with CSP, calculated baeed on enelnoerl*
judgement
Controlled with oultlclene,
en9lneerln9 Judgeoent
Controlled with ESP. ealcuUted b*»«d on «nfln«erin«
jud9*««nt
Controlled with ecrubber. calculated baeed on
engineering judgement
-------
•et» Ho. 7*
00/21/M
POLLUTANT
CM (1C
NUMi* COM IWXMTIIM. PMCIM UllfilON fOUWf
KC COM MINION FACTOI
NOTI*
744O4I*
744041* CMl
74404)* Ce«l
»ulv«rlt«d Mt kottM
744O4I* Coel coebu.tlM
744041* tool
744041* Coel coebu.tlon
744O4I* Coel coetouetlon
744041* Coel coebuetlon
744041* Coel coebuetlon
744041* Coel coebuetlon
7440419 Coel COebuitlon
744041* Coel
Antbractt* <»4l-«lr«*J
»ulv*rl»d Mt bokto*
botlwt. uit
bollere. utlUcoomrc/Ind
•pratdur stoker botlvr.
uttl/c«iM«rc/Indu*tr
Ito coel-flred I
eoreAder etokor boiler.
utll/coeeerc/lnduetr
Anthreclto co*l-flrod 1
esre«der etoker boiler,
utll/coeeerc/lnduetr
lltuelnoue coel-ilrod I
cyclone boiler.
utll/caeeerc/lnduetr
lltuelnoue cod-fired I
cyclone boiler.
utll/coeeerc/lnduetr
lltuelnoui coel-fired I
cyclone boiler.
utll/coeeerc/lnduetr
•Ituilnoue coel-fired I
overfeed ttoker boiler.
utll/coeeerc/lnduetr
•ltuelnou> coc«itr«ll«*.
I.O-lt lk/IMI2 Itu Control 1*4 ylth Miltlclen*. «lcuUt«tf b«nd M
t.4-7.( 1B/IOCU Itu
30-51 lb/IOCI2 Itu
It-It tbftOCtl
•.If Ib/IOfll Itu Controlled iiltk If. c«Uul«t«i» b»>«d on ontlnovlnt
0.12 Ib/IOCIZ Itu
1.2-11 Ik/IOCIl Itu Uncontrollod. c«lcuUto< b«««d on wiflnovliHr Judiooont M
Control lod ulth (IP. oUulltod k»«d on on.liloorlii.
Ju<
Controlled ulth Milttclon*. c«Uul«*«d bu*tf on
•n.lnoorln*
I.1-2.7 Ib/IOCII Itu Controlled Kith CM*, celculeted beeed on onolneorln* M
» Ib/IOCII Itu
20 ID/10CI2 Itu
l.J Ib/IOCII Itu
Uncontrolled. ko»od on MUTC. toot
Controlled ulth oultlclon*. celculetod beeed on
en.lnoortnv judveoent
Controlled ulth (ST. bued on ogurco t»t>
41-12 Ib/IMIJ Itu Uncontrolled, beted on (ourco to>t<
ov«rf««d stoker boiler,
Controlled ulth •ultlclone, cilcuUted b»od on
engineering Judeeeent
Controtied »Uh (S». c«tcul«ted b»ed on englneortni
judfleeent
-------
•••o M«. 77
0*/2t/*0
CM SIC
NUflKR COM INQMTRIM. MtOCfSS
EHIMION MIMCf
KC COM OIIMIM FMTM
NOTI»
744041* CNl coobuoUon
744041* Coil cortu.tlon
744041* Co.l
74404I* Co.i CMbuition
744041* Ca>l co.6u.tlon
744041* Co.l co.ou.Uon
7440«I* Coil cariMiitlan
744041* Ca«l caabuitlan
744041* Cail caabuitlan
744041* Ca«t caaauitlan
744041* Co»l coebuvtion
744041* CaI"*lr«d 1
0ulv«rlz*d uat bottoa
beiUra, utll/cotMarc/.nd
•Uualnout co«l-flr«d I
»uiv*rlx*d w«t b«tto»i
boiUrs. utlt/cOM«rc/lnd
•ltu«lnou* ce«l-ftr«d I
»ulv«rli«d vat botto.1
boiler*. util/CM.-«rc/.nd
•ltu«|nou« eo«l-«lr«d I
*pr«Ad«r itokar boll*r«,
utll/co-t«d«r »toh«r boiler*.
ut 1. /ce«*«frc/lndu«tr
•ituainout ca*l-lir«d I
•pra*d«r ttak*r boiler*.
utll/coeiaerc/lnduttr
L.ef.U*j co.vl-flr«d 1
cytlonc bolttr*,
ut11/co*««rc/lndu*tr
Lisnlt* co*l-Ur«d I
cyclone boiler*.
utM/co««erc/indu*tr
Litinlta co»l-fired 1
cyclone boiler*,
utlI/coMMcrc/lnductr
44.4 IWIOCI2 It*
11.* U/IOC12 Itu
1.4 lb/IOCI2 Itu
f.l-ll lb/IOEI2 Itu
31 Ib/lOCU Btu
22 Ib/IOEIJ Itu
1.4 lb/10EI2 Itu
Control lod. km*- M MWM t..t.
Controlled with wltUlon*. celeuUted b«*ed i
«n«ln««rln« Judgment
f.0-20 U/IOCI2 Itu C«itr«llur« «••«»
41-70 U/ICC12 Itu UncMtroll.d. c*IcuUt«d kmd an antlnaarlnt Jud.««ant
92-90 lb/10C12 itu Controlled with .wltlcloi.*. c*lcul*ted b**ed on
•ntlneerint Judowumt
M
Cantrallad Kith ($P. baaad a« aaurca taata
21-4] lb/IOCI2 Itu Uncontrolled. b.««d en aaurca taatl
4.4-30 Ib/IOCU Itu Controlled with •ultlcloao. o«ud on «e**ured and
Cetcul*t«d ••i**lon lectori
Controlled with CSP. calculetod b**ed on eneineerlne
judfleeent
Uncontrolled. c*lcuUted b«»ed on engineer I n« Jud9««ont
Controlled with •ultlclone, c*lcul*t«d besod on
engineering Judgement
Controlled with ESP, celcuUtod b««ed on enaineerina
Judgeaent
-------
•aee He. 71
oe/lt/M
CM IIC
POLLUTANT MUMn COOf IHOUITIIM. MOCEI*
Cadalue 744O4J» Coal coebuatloe
Cadelue 744041* Coal coebuatlon
Cadelue 744O41* Coal coebuatlee
Cedelue 744041* Coal coebueUe*
Cadelue 744043* Coal coebuatloe
Cadelue 744041* Coal coebuatlon
Cadelue 744041* Coal coebuatlan
Cadelue 744041* Caal coebuatlon
Cadelue 744043* Coal coebuatlon
Cadelue 744041* Coal coebuatlon
Cadelue 744041* Coil coabuitlon
million MUM* KC COM MINION r«CTO« MOW '
Llenlte coal-Hred 1 47-*O Ih/IOflt Itu Uncontrolled, calculated baaed ee eetleeorloe Judiaeoet
overfeed (tokor boiler,
utl 1 /coaaart/leduatr
Llanlta coal-Hred 1 31-44 Ik/lOCU Itu Controlled eiltk eultlclone. calculated baaed on
overfeed atoker boiler. enejeeerlet Judeeeent
Llenlte coal-fired 1 12-11 Ib/IOEU »t» Controlled eltb tf. calculated baaed ee enelneerlee
•verfeed cteker boiler. Judiaeeet
utl 1 /coeeerc/liiduatr
Llenlte coat-fired 1 41.1 Ik/lOEIJ Ito Uncontrolled, calculated baaed ee entleeerlao. Judiaeant
tulvertxed dry bottoe
boiler.
utl 1 /coeeerc/tnduetr
Llenlte coal-fired 1 14.1 Ib/!0fl2 Itu Controlled Kith eultlclene. calculated baaed en
•ulvarliad dry bottoe enelnoerleo; Judteeent
utlt /to»«»rc/ln*»*».r
Llanlta coal-fired 1 10 Ib/lOCU Itu Controlled eltli Hf, calculated baaed ee onalnaarlne
•ulvarliad dry bottoe Judeeeeet
utll/co^arc/lnduatr
Lltnlta coal-fired 1 O.ll-l.l Ib/IOEU Itu Controlled »tth acrubber. calculated baaed an
tulvarlied dry bottoe en«lneerl«« ludeeeent
boiler.
utt 1 /coeeerc/lnduatr
Llanlta coal-fired 1 4*-77 lb/IOEI2 Itu Uncontrolled, calculated baaed on en«leeerln« judeaeent
aulu.ru. d net bottoe
ballara,
utl 1 /coaaarc/lnduatr
Llanlte coal-fired 1 3S-55 lb/IOCI2 Itu Controlled ultn eultlclone. calculated baaed on
aulu.rliad uet battoe an«lneerlne judeeeent
bollara.
utl 1 /coaaarc/lnduatr
Llanlta coal-flrad 1 l.S lb/IOCI2 Itu Controlled ulth ES>, calculated baaed on enflneerlnf
oulvarlzed wet bottoe Jud*eeent
bollara.
utl 1 /coaaarc/lnduatr
Llanlta coal-fired 1 23-47 Ib/IOEU Itu Uncontrolled, calculated baaed on entlneerlno judveeent
utll/co».rc/lnduitr
laTERO
14
M
M
M
M
M
M
M
M
M
34
-------
•at* No. 7*
0»/2I/*0
POLLUTANT
Cadetue
Cadelue
Cadelue
Cadelue
Cadelue
Cadelue
Cadelue
Cadet ue
Cadeiue
Cadelue
Cadetue
Cadelue
Cadelue
Cadetue
Cadetue
CM IIC
NUHMI CODE IMUfTRIM. PMCISt
744O4I* Coal coebustlon
744041* Coal coebustlon
744041* Coal coebustlon.
Industrial
744041* Coal coebustlon.
Industrial
744041* Coal coebustlon.
Industrial
744041* Coal ceebuatlon.
Industrial
744041* Coal coebustlon,
residential
744041* Coal coebustlon,
residential
744041* Coal coabustten,
residential
744041* Coal coebustlen.
744041* Coal coebustlon.
residential
744041* Coal coebustlon.
residential
744041* Coal coebustlon.
744041* Oil coebustlon
744041* Oil coebustlon
CMIMIOH lOMCf
Llenlte coal-fired
utl 1 /coeeerc/leduttr
Pulverlied stoker
Underfeed stoker
•etertube boiler
Chelnersto stoker
uatartube boiler
Spreader stoker Hatertube
boiler
Anthracite coal -fired
boilers
lltuelnous coal-fired
boilers
•oilers fired by coal
free appal acht an ration
•oilers fired by coal
froa Interior rotten
•oilers llrad by coal
Iree northern plains
ration
Llsnlte coal-fired
boilers
Cubbltuelnous coal-llrad
boll are
Distillate oll-flred
bol 1 or ,
utl 1 /coeearc/lndustr/rasl
dantlal
Olitlllate oll-flred
boiler.
KC COM MINION FACTO* NOTft
| 7.J-JJ U/IOCI2 It* CoetroUed trttk "Ultlclene, calculated eased **
entleeerlee Judeeeent
1 f.l-IZ Ib/IOEIl Itu Controlled Kith IIP, calculated bated on online*
Judteeent
10200202 O.OOO4* Iba/lOCe ITU heat Uncontrolled eelsslbne
Input
10200204 0.00040 lbs/10C4 ITU heat Uncontrolled eelsslons
lout
102002 0.0004* Ibt/IOCo ITU heat Uncontrolled eelsslons
Input
10200204 O.OOO40 Ibs/lOCe ITU heat Uncontrolled eelaalont
Input
II. 0 lb/IOCI2 Itu Uncontrolled, hlehly variable, calculated bated
entlneorlee, Judteeent
(2.2 lb/IOE!2 Itu Uncontrolled, hlehly variable, calculated bated
entlneertnfl Judteeent
1.4 Ib/IOCIJ Itu uncontrolled, calculated baaed on entlneerlnt Jl
171 lb/10CI2 Itu Uncontrolled, calculated bated on entlneerlnt Jl
24.* lb/10EI2 Itu uncontrolled, calculated bated on entlneerlnt Ji
97.1 lb/IOEI2 Itu Uncontrolled, hlehly variable, calculated based
enttneerlnt Judeeeent
2*.l lb/10EI2 Itu Uncontrolled, hlehly variable, calculated bated
entlneerlnt Judteeent
1 10. S U/10EI2 Itu Uncontrolled, calculated bated on entlneerlnt Ji
1 7. 45 lb/IOE12 Itu Controlled Kith eultlclone. calculated based on
entlneerlnt Judteeent
rln*
on
OH
ideeeent
idteeent
Idtteent
en
on
4dae*ent
M
-------
Pet* Ho.
0»m/*0
CM *IC
NunMD COM IHOUtnlM.
MISSION SOUICC
KC COM tMMIOH r«C1M
Horn
74404)*
74404)*
74404)*
Oil ceotalotle*
Oil coefeuetlM
Oil coebultlen
Oil Coebuetlafl
IlltllUU •ll-flr«4l
boiler.
vtl I /co«Mrc/l**i*tr/r«>l
OUtllUt* lll-tlr** I
ballv.
ut 1 1 /cawc/liidu«tr/r*ll
dmtUI
ballw.
utl I /CM
d«ntl>l
I.M Ik/IMIS It*
•.«) Ib/lOEIl Itu
r. c*lcuUt*d k*Md M
Contr*U*dl ultk Krubbv. c*lcul*t«4 b«««d M
M
If.7 Ib/IOfia Itv UncMtrcllX. c«lcul«t«d b««.d M •nll««vUt JudtMoit
44.M Ik/IOClI Itu Controlled1 ailtk eultlclono. calculated baaed on
74404)*
Oil CO.bU.tlOn
bolUr,
utl I /cea«wc/lndu«tr/r««l
».»0 lb/IOCI2 Itu Controlled with ISP. calculated baaed on enelneerlnf M
744O4)*
74404)*
74404)*
74404)*
Oil coebultlon
iouAffO
Inclnerttlon
Seuae.e eludee
Incineration
Soutio eludee
Incineration
Sewage eludee
tnclniratlon
Vehicle tin wear
Uitto all ceebuttton
).»« Ib/IOCIl Itu
Contrell«4 vlth xrubbw,
•n*lnnrln* Judvnvit
utl I /CMMrc/tiidufttr/r«al
d«ntUI
Fluldlied-bed iureace SOI
0.000 - 0.0001 Ibl/ton Control I «d by iMt xrubbw
dry >lud9«
fluldl»d-bid (urn4C« 901 0.0014 lb>/t«l dry «lud«« Uncontrolled M|»|M». »ln«l« tot
ftultlpl* httcrth furn«ca SOI
nultl»l« hatrth lurn«c« SOI
Uaata oll-W/ton
1.07 xlOC-l - 1.07 muC-S Ixetf on three eeUelen fectere In the llteretur*
Ib/elle driven
0.025 Ib/IOOO ••! ell Uncontrolled, beeed on eeleelone data end envlneerlnt
burned Judfleeent. v«rl«ble
201
Uood eo»fau»tlon,
r««iJintl«l
7.2 x IOE-S Ib/ton Mood Uncontrolled. b»ed on one etudy. nonbiHled ttove
burning «reen pine
-------
reeoi Mo.
0«/2I/*0
POLLUTANT
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedoluo
Cedolue
Cedoluo
Cedolue
Cedoi ue
•1
CM
NunK*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
744041*
SIC
COM
0711
0711
0711
22*
22*
22*
22*
211*
2I*»
2*51
2*51
1241
1241
1241
1241
1241
324 1
INDUSTRIN. PMCIM MISSION MUflCt
For til liar application Application proem
Fartlllzar application. Application proc«a>
Funfltclda application Application procw*
Uovon fabric flnlahln* Curing ovon - main
t.nial.
Uovnn fabric flnlahln* Hnat »attlng
Woven fabric ftnlahlnt Tan tar franoa - main
4Ini thing
Uovan fabric fln.ahlna, Therooaol dyoino;
Cadniun pltwnta Total plant nnlaaiona
oanutacturo
Plaatlc atabiliiar* Total plant *nl«atona
•anuf actur*
Atphaltlc concrete Plant a tack
production
Atphaltlc concrete Plant stack
production
Caaant nanufactura - dry Flnlth •!!!
procett
Ca«ant nanufactura - dry Flnitt, al 1 1 air »aparator
procata
Canant nanufactura - dry Flniah alll fend
procati
Caaant nanufactura - dry Kiln
procaca
procaat
procett
sec cooc MISSION FACTO* NOTI*
Ma * * IOE-1 U/ton EntlnawrlM MtlMU. MM balancn
fartllUnr appllnal
302 a M IOC-4) Ib/ton
lortlliMr applied
302 1 * IOC*S Ib/Ml CnffinaMrftnff oat IMA to* MM balance
102 I.*** x IOC-4 lb/«.l
fuootcldo eopllod
110001 (.1 x lOf-S Ik/too fekrlc Uncontrolled, evoreco of two te.te
110001 ».2 x IOt-« Ik/ton febrlc Uncontrolled, keeed oo tott dete
IIOOOI I.I x lOf-S Ik/ton febrlc Uncontrolled, evoreeo of four toete
130001 1.4 x IOt-4 Ik/ton febrlc Uncontrolled, evereoo of three totte
101035 II Ik/too Cd cherted Inelnoorlno oetloete. oeee kelence. controlled with
* Ik/ton Cd cherood Cnilnoorloi eetloete. controlled with keohouM
concrete veluoo. rente U 1.24 x 10f-ll - 4.4 x IOC-10 Ik/ton
105002 1.12 x IOC-10 Ik/tan Uncontrolled «roo e ilnilo >Unt, ev|, of 2 vtluet,
concrete renge U l.ll x IOC-10 - I. II x IOC-10 Ib/ton
105004 1 > IOC-7 Ib/ton feed Controlled with beehouu
10500* 2.* x IOC-* Ib/ton feed Controlled with beohouee. eteck eeoellne
10500* 1 « 10E-* Ik/ton feed Controlled with ke«houee
10500*0* 1 x IOC-4 Ik/ton feed Controlled with e beohouee or ESP. eteck eeoolln«
ItfUCNCI
M
11.41
II
41
S2
12
52
(2
n
M
170
170
U
II
U
n
u
11
s
3
-------
pee* NO. 12
0*/2I/»0
CM *IC
NUHU COM IMKNTIIIM. moan
IHIMION
KC COM HIIHIM FACTO*
NOW
Cedetue
Cedelue
T44O4I* 1241 Ceeant eeoufectura - *v «*• «'H *oo*
eroceee
744041* 1241 Ceeant eenufecturo - net Clinker cooler
procoa*
744041* 1241 Ceeent •enufecturo • wet Kiln
proceaa
744041* 1241
procoag
744041* III Iteol protection
744041* III Steel production Open hear
744041* 3311 Ferroalloy production Ilectrlc
744041* 1111 Ferroalloy production flectrlc arc furnace.
744041* 112 Iron and eteel foundry Sreen aand ahakeout
744041* 112
744041* 112
744O41* 112
744041* 112
744041* 112
744041* 112
744041* 112
S«cond*ry Iron «nd •!••!
•reduction
Secondary Iron and ateel fasic eKyeen furnace
production
Secondary Iron and ateel electric arc furnace
production
Secondary Iron and ateel Oean hearth furnace
production
Secondary Iron and ateel Open hearth furnace
production
Secondary Iron and ateal Sintering oaerat
production ulndboK exhauat
744041*
744041*
111
133
Secondary Iron and ateel Sinterine operation*.
production uindboM exhauet
Prleary >!nc aeeltlng Caking
Prieary line eeeltlng Elcctrotheralc procea*
1OMO4 1.4 * IOC-7 Ik/tM <«d CMltrcllW Mttk k*«k«IM
I II »Ot-» Ik/tM »««d CantnllMl Hltk IV w klfhouu
J05004 2 il IOC-S Ib/tM <««d Cwitr«ll«4 «ltk
J050O* 1 x 10C-» Ik/tM t*d «rM d«*« pr«Mt«4 In
tk« r«l«TMC«
UncMtrall«d
Uncantral I «d
UncontrallM. Cd duit !••• th*n I ui llio only
Uncontrolled, keaed M Cd content IP. feed. fuel, or
eelaalone
2.7* » IOt-5 Ik/ton ateel Contrail led «lth venturl acrubber or ISP
3.4 K IOE-3 Ib/ton ateel
Cnmlneerln* eetieete). etack teat, concentration of Cd
in fuel. feed, or eelealona
104 S.7I « 10C-] Ik/tan ateet Uncontrolled, etack eaeplln*
1,1 » IOE-4 Ib/ton atael Controlled Kith ISP. atack caopllnf
2 > IOC-I Ik/ton feed Uncontrolled
t.S * IOE-4 Ib/ton feed Controlled Kith rotoclone and ISP
303030 2.24 Ib/ton Zn thru Engineering eatleate
303030 1.2 M IOE-2 Ib/ton Zn Engineering eetlaate
produced
-------
Page Ho. II
0»/2I/M
CM SIC
NUHKI COM IHOUfTRIM. HOO.lt
HIIM10N
(CC COM MISSION *«CTO«
NOTIS
744041* at Prlavary slue aeaUIn Horizontal retort
MMW « « JWt-I !»/t«t I*
744O41* II) Prleary sine eaaltlngj
744O4I* II) Prleary xlnc geeltlng
tlntarlng with cyclone
Slnterlne Hltk cyclone
•nd CSI*
744O41* II) Prleary xlnc eaaltlng Vertical retort
74404]* III Prleary xlnc aeeltlnt line alnter plant
101010 a.M Ik/tan In thru
1010)0 2.1* Ik/tan In thru
I010I4 «.I K IOE-2 Ib/ton In
tfcrv
1010JO 1. 11 Ib/tan produced
Stack aaeellfie;
Stack aanpllag
Stack aaepllnt
Controlled xltk cyclone, calculated free data preaented
In the reference
74404)* ID Prleary xlnc eeeltlng line alnter plant
101010 !.**• Ik/tM >r«duc«
Controlled «ltk cyclone and ESP. c«lcul«ted Ira* data
praiantad In tKe reference
744041* III Prlaary line aaaltlng line aaelter coker
10)010 0.144 Ik/tan
No controle. calculatad Iraa data preiented In the
reference
744O41* III Prleary xlnc aneltlng line vertical retort 10)0)0 0.002*1 Ik/ton produced
Ho controle. calculatad Irani data praeantad In tka
rafaranca
74404)* )}) Prlaary zinc/zinc o»!da Calcine handling
analtlng
744041* 11) Prloary alnc/Hn
i coaler
101010 *.l x IOC-S Ik/tan In
produced
Controlled tilth kaghauae. derived free aelaalen factora
101010 <2 Ik/ton In produced Controlled »lth deeleter. derived froe eelcelen factor
744041* 111 Prleary z:
aeeltlng
oxide Fune kiln
744041* 111 Prleary zinc/zinc oxide
•netting
744041* II) Prleary line/line oxide
•••I ting
744041* II] Prleary zinc/zinc oxide
•eelttng
Leach residue dryer
Nutt«nc« du«t collactor
101010 O.OOal Ik/ten InO
produced
101010 <] Ik/ton In produced
101010 4.al > IOC-4 Ib/ton In
produced
101010 <2 Ik/ton In equivalent
produced
Controlled Kith kaghouae, derived free eelaalen factor
ncontrolled, derived free, eeleelen factor
Controlled Kith baehouM. derived fraa eelaalon factora 4)
Controlled ulth kaghouie. derived free aelialen factor
744041* 111 Prlearv zinc/zinc oxide N*w Material «tora0e -
1010)0 2.4 « 10C-5 Ib/ton In
produced
Derived froe eelaalon factora
744041* 111 Prleary zinc/zinc oxide Ran eaterlal itorage -
•eeltlng dry icrubber
101010 O.OOOU Ib/ton In
equivalent produced
Derived froe enlaalon factora
744041* 11] Prleary ztnc/zlnc oxide R«w Material ttorage
••eltlng uncontrolled
Prleary zinc/zinc oxide Refining coluen
• ••1 ting
101010 0.001418 Ib/ton In
produced
101010 <2 Ib/ton In equivalent
produced
Derived froe eelealon factora
Controlled with kaghouao. derived froe enlaelon factor*
-------
Pat. No. 14
0»/2I/*0
CM fIC
Hunt** COW INMfTtlM. •MCCM
IMUIION MUMX
«CC CON WIMIOH MCTOI
NOW
744041* HI Prleery line/line oxide •oedvey*
.MltUt
744041* HI Prloary xlec/iinc oxide tcreenlm toner
•Ml tint
744041* 111 Prleary Hoc/sine oxide (Inter eacklne
OMltlne
744041* 111 Prleary line/sine oxide Sinter •Illnt/eruehlnt
eeeltmo
aOMW 4.* li IOf-4 Ih/Un to
303010 <1 lk/t«. I* >r«*ic«d
•.0201* Ib/toe le
oeulvalont produced
0.00124 Ik/ten I*
Controllod. derived fro* oolMlon fectort le e !>
Controlled «ltk kothouM. derived froe eeittle* factor
Controllod nub
(n • 21
kotJuun. dorlvod «roo ool»lon f«etor>
Controllod Hltk koihauo*. dorlvod «ro. oolxlon foctor
744041* 111 Prloary Hue/line oxide Uaeli kiln lutltlve. 103030 <2 Ik/toe InO produced Controlled .Ith b.tneuM. derived froo eeleelo* foctor
303010 4.4 x IOE-S Ib/tM InO Controllod -UK baehou.e. derived froe eel..Ion factor
744043* 131 Prleary line/line oxldo U.ali kiln product
•Mltleo
41
41
744041* 331
> xlnc/llnc oxide line ho)dint furneco
744041* 131 Prleary ilnc/iinc oxide line ore dryer
•eel tine
744041* 331 Prleary ilnc/ilne oxide line du«t procoM
•eel tint
744041* 111 Prlearv ilnc/Unc oxide line furnace preheateri
•Ml tine
<2 Ib/ton In oeulvalent
produced
2.2 x tOC-f Ib/ton In
equivalent prod
101030 <2 Ib/tM In •reduced
0.00571 Ib/ton In
eeutvalent produced
Con troll od »lth fcichouM. dorlvod «roo ut»lan tutor
Controlled .Ith vet scrubber, derived froo oelKlon
factor
Controllod >lth keehouee. derived free eeleelon factor!
Controllod -ttn beohoute. derived froo eolttlon factor
744041* III Prleary line/line oxide line eoltlno furnace - 301010 <2 Ik/ton in produced Derived froe oolMton factor.
41
•41
Cadetue
Cadelue
Cadolue
Cadetue
Cadelue
Cadelue
744041* 111 Prloary sine/line oxide line eetal powder erocee. 101010
•eeltlni
744041* III Prleary zlnc/xlnc oxide line tapplnt/ce.tlnt 101010
•eel tint
744043* 133* Prleary cadetuo •eeltln* Cadelue ca*tlnt furnace 303
744041* 111* Prleary cadelue iMltln* Cadelue koldln* furnace. 103
744041* 1319 Prleary cadelue •••ltln« Cadaiue eeltlnt furnace 103
744043* 111* Prleary cadelue »
Uncontrolled, derived froo eeloelon factor! 411
Uncontrolled, derived free oelolon factor 41.44.44
Uncontrolled, derived froo eel..Ion factor 43.44,44
Uncontrolled, derived froe eel..Ion factor 41.44.4*
Controlled tilth baohoun, derived froo eel»lon factor 43,44,4*
Controllod ulth vet ecrubber. derived froo oeliilen 41,44.44
(actor
744041* 111* Prleary cadelu
01 4.92 Ib/ton Cd produced Controlled tilth baehou.e. derived froe eet.clon factor 41.44,44
-------
Pa«a No. M
0*/2I/*0
POLLUTANT
Cadaliw
Cadallw
CadaluB
Cadalua,
Cadalua
Cadoliw
CaMlua
Canal ua
C.d.,u.
C.d.,u.
Cidalua
C.d.,u.
Ctdalua
Catdalua
CtdvluB
C*d*Jiu>
C«dfllUaV
Ctdalt U«
CM (1C
NUMM COM IMDUtTIIM. PHOCCM OIIIIKW MURCI
744041* III* Prlaary Cadalua Maltlna Cadalua tapvlM/CMtlM
744041* 111* Prlvary cadalua aMltlna Caatl«f/koldina lurnaca
744041* III* Prlaary cadalua .Ml Una Cd baohouaa
744041* 111* Prlaary cadalua aMltlna Cd aatal aaodar aackaalii*
744041* III* PrUary cadalua iMltlni Duat ck«r«ln«
744O41* 111* PriMry cadailw •aalkln* Pufllttwaa packint duak
call actor
744041* III* Prlavy ctdalua tMltUf Cv»»ua ataraaa allaa
744041* III* Prlairy cadalua ualtlna Prault dwartMnt
744041* 111* Prlau-y cadalua laaltlni furldollon davartaant
•tut
744041* 111* Prlatry cadalua »alttna PurlllcatlM aoMaa tank
744041* 111* Prlatry cadalua laaltlnf Solutions haatlna tank
744041* III* rrlaa (or llntar
cruihlna and raturna
744041* 111* Prlatry Ia4d aaaltlnt il«.l lurnaca
744043* 111* Prlatry laad aaalklna ll«»t furnaca
744041* 131* Prlairy laid oaltlnt Dro» ravarbarttary
• eld M«nt and tlntar
744041* 131* Prlairy laid aaaltlna Or. cruahlna
744043* 333* Prlakry laAd aaaltln9 Scrubbar for blast
*nd r*turnt
«CC COM UIIMION r«CTIM
1O| <1 Ik/tM Cd araducad
1O1 0.00714 Ik/tM Cd
101 0.03* Ik/tM Cd araducad
101 0.0* Ib/tM Cd araducad
101 0.21 Ib/tM Cd araducad
101 O.JS» Ik/tM Cd praducad
303 <2 Ik/tM Cd araducad
101 2.** Ib/tM Cd areducad
101 0.01*0* Ib/tM Cd
101 0.00754 Ib/tM Cd
araducad
101 0.7*4 Ib/tM Cd araducad
101010 0.000204 Ib/tM Pb
aroducad
30301002 4«.*4 Ib/tM Pb araducad
101010 S.29 > IOC-1 Ib/tM Pb
30301003 2.* Ib/tM Pb araducad
303010 0 041 Ib/tM Pb aroducad
10101004 0.7SS Ib/tM Pb aroducad
3O1010 2 K IOC~S ~ 7 B IOC'S
303010 7 * N IOE'5 - 1 * X 10C~4
Ib/ton Pb »rod
NOTM
UncMtrallaal. darlvad IrM aaUnlan lac tar
UncMtrallad. darlvad IrM M|»|M lactar
Oarlvad IrM MlaalM lac tor a (• • 21
Con troll ad Kith fcadwuaa, darlvod IrM ana MlaalM
iactar
UncMtrallad. darlvad IrM MlaalM 1 actor
CMtrrt,«,,^,v-«rMt«Ml..lM4«t«
Control lad vttk dry acrubbar, darlvad IrM ana MlaalM
lactar
UncMtrallad. darlvad IrM MlaalM lactar
Uncontrollod. darlvad IrM Ma aalatlM lie tor
UncMtrallad. darlvad IrM Ma MlaalM lactar
UncMtrallad. darlvad IrM Ma MlaalM lactar
Oarlvad Iraa an* MlaalM «ati«at«
UncMtrallad. darlvad IrM Ma MlaalM iactar
Control lad xlth a baaheuaa. atack ••••Una and
anelnaarjna astlaata
Uncontrollad. darlvad ira« ana aalaalan lactor
Uncontrollad. darlvad Iroa ana aajaalon lactar
MFOKNCC
41.44.4*
41.44.4*
41.44.4*
41.44.4*
41.44.4*
41,44.4*
41.44.4*
41.44.4*
41.44.4*
41.44.4*
41,44.4*
44.4*.*7
4*.»7
It
4*,*7
44. 4*. 97
4*.*7
44 44 97
44,44.97
-------
pee* Me. M
0*/2I/*0
CM (1C
MMM* COM INMMniRL PlkXfM
BIIMIOM MUKf
KC COM IMIMION r*CTM
Mam
Cadelue
Cadolue
Cadelue
Cadelue
Cadelue
Cedelue
744O41* III* Prleery lead oeeltlng Sintering (uedreltl
744041* 1141 Seconeery copper aeelklng
744041* 1141 Secondary copper aoeltlng
converter
744041* 1141 Secondary copper aeeltlng Total plant eel eelone
744041* 1141 Secondary lead Melting Heat furnace
103410 I.aw Ik/ten Pk produced uncontrolled, derived frM one MlaelM lector
1O400J *.01-O.II2 Ik/tM Cv
produced
Controlled ultk kethouee. oMllcokU only to fecllltlm
•nau ran oeterleU contain cadoluai
744041* 1141 Secondary lead eeeltlng
t*ry furMCl
104002 O.OOIM-0.0011* Ik/toe Cu Controlled ailtk kaghouae. appllcakle only to facllltte*
produced yhooe roei eaterlal* contain cadelue
104002 4 Ik/toe o> copper ocrap Control etatua unknown
30400401 2 * IOf-« Ik/tM Pk Controlled ultk three cyclone* • kagKouoe oteck
oaepllet « engineering eetleete
10400402 l.« x lOf-e Ik/tM Pk Controlled ultn cyclone • kaghouae atack aaeallng •
le.t?
44
44
41
M
Cadelue
Cadelue
Cadelue
Cadelue
744041* 1141 Secondary lead I
744041* II4I Secondary fine oooUIng Total plant eeUalono
744041* 1471 Cedelue electropletlng Entire procooe
744043* le»l lattery (nlckel-cadeluel Total plant oelaelMO
••tt«rv (nlc
••nuftctur*
744043* 4*91
10400402 ( II 10E-7 Ik/tM Pk
104001 0.01 Ik/tM In produced
O.O0009 g/hr/aep
104009 2 Ib/ton Cd charged
901001
0.001 ID/ton wintc >olld
w«*t*-dry ut.
Controlled Kith three cyclonea end kaghouoe M
Uncontrolled M
Uncontrolled, eeaourod *2
Survey of cooeantoo M
Controlled ky »rey-ba«le ecrukber. kaaed en eeterlal
balance tor eodel inclnereter
744041* 4*91 Municipal Mate
coebuatlon
744041* 4*SI nunlclpel «a»te
coobuatlon
744043* 4*91 nunlclpel uaato
744041* 4»S1 Hunlctpal «
coebuatlon
744043* 4*93
744043* 4*91 Ituntctpal uaate
coebuatlon
4993 Municipal waste
coebuatlon
n«s» burn. r«lr*ckory
(•cllltv
nodular tncln«r«tor
Rvfuia d«rlv«d full
Incinerator
X«fu«* dvrlvod
2.4So Ib/ton controlled
*artlculat« onloolon*
1.172 Ik/ton control lid
Mrtlculata oalsslon*
«.«2 Ik/ton controlled
>«rtlcul*to ••Itclon*
0.212 Ib/ton controlled
partlculate eelaalona
0.000* Ik/ton RDF
cootaltUd
0.004 Ib/ton KOf
coobuetod
3.1 x IOE-S Ib/ton HPF
coebuated
Controlled ky ISP. baaed M eource teata
Controlled ky ESP. kaaed on eource teata
Controlled ky ESP. baaed on aourco teat*
Controlled ky ESP. beaed M source teat
1001 RDF (u.l only, ESP control only, overall average
at severe! source overate*, ranee, li 0.00032 - O.OOlt
Ib/ton
I00« P.OF luel only, uncontrolled, overall average o(
aevorat eource averagoo
Spray drying alter acid gae and Pfl control, one data
point, lower detection Unit reported. 1001 P.DF fuel
only
III
-------
•mfM Mo. 17
ot/21 no
POLLUTANT
C*a»lu>
C.dcluo
C tOmtum
Octet u.
CtOmlum
CM SIC
MURK* com iMusraiM. MOCKS
744041* 4*SJ IhMlclMl «*«t.
COOtaMtlO*
744041* 4»SI DuitlclMl «M«t«
coabuvtloii
744041* 4H1 Munlcl.U VMt>
coobuvtton
744041* 4*S1 Itunlcl.U u..to
cooButMon
744041* 4*11 HuniclNl M«U
coobu.tlon
niiuioN sound
netful *r »t«rv*d-«lr
cooouttor
nodular •tarvotj-.lr
coabuttor
nodular oMco.a-alr
coobu.tor
nodular onc«>«-alr
coobuator
n««a burn. wator wall
Incinerator
KC COM IHIHION r*CTM MOTit
(01001 0.000* Ik/to* low* Mf control •">». «iMr*ll avorat* •* Mw«l ooure«
*<«•»•>•. rxlt* U 0.00017 - 0.0017 Ib/toi
IOIOOI 0.00(4 Ik/tM Im4 Uncontr«ll«d. ovmrmll •vmrmmm o< ««v«r«l Murci
•VV.QM. r*«w l« 0.002 - 0.007* Ib/ton
SOIOOI 0.00011 Ik/tM • n«w
•od«l to any *9« ••dtun
n«t« burn M*t«rwall
co«bu»tor( •••II •!•• n«w
to Any «t* •*diu«
n««i burn w*t«rwall
coabuitor. ••*!! »tt« n«w
•od«l to *nv *«* Mdlut*
n«tt burn y*t«rH«U
coMUu»tor , »•*! 1 tlzfl n«M
•od«l to *ny •«• avdluoi
soiooi o.oooil Ib/ton
501001 0.00011 Ib/ton food
501001 O.OOi Ib/ton
SOIOOI 0.000*0 Ib/ton food
C«p*eltv > 4OO to««/d*v. W control only. •v«-«ll
•vorooo of oovor«l BOUTCO •vwaoos. ran** 1* ••• •
10C-S - O.O0030 Ib/ton
000 tons/d«v. Mr*v dryin* *ltor «c.d «*•
•nd PM control .ovorall *v«. ol wvoral uurco *v«i..
r«n*o U O.OOOU - O.OOOJ* Ib/ton
CtoAdty < oOO tons/day, uncontrolled, ono d«t« oolnt
C«p*clty < «00 ton*/d*y. K«P control only, ovor.ll
•vor«oo ol o«v«r*l »ourc« •vorato** r«n«« !• 0.00011 '
0.00012
4.1 • IOC-S Ib/ton food C«»*clty < oOO tons/day, wr*y oyyln« aftor *cU •»•
•nd PH control. ovorUl «v«. o( •«v«r«l «ourco *v««..
r*nM U 2.4 K IOC-5 - 7.0 x 1OC-S
4.0 K IOC -5 Ib/ton <««d C*p«clty < *OO ton«/d*y. dry *orb«nt Injoctlon «ft«r
•cld «»• *nd PH control, ono d»t* point only
744043* 4*53 nunlciptl u«*t«
coabuttlon
n**i burn w«i«rw«ll
co*buttor, built b«for«
1»BO
501001 0.0032 Ib/ton food
CSP control only. ovorUl »v«r*9« of ••wor«l BOUTCO
*w«rA9«». r*ni« U 0.0024 - 0.004* Ib/ton
744043* 4*53 I,unlclp4l W*lt«
combustion
t1«»« burn w*t«ru»ll
cooibuttor, built b«*or«
501001 0.022 Ib/ton food
Uncontrollod. ovorall «w«r*»« of ••w«r*l oourco
*wor*«o«. ranao I* 0.0074 - 0.092 Ib/ton
744043* 4*53 HunJclpftl
tU»» burn H«tory«ll
coo>bu«tor. built b«for«
19BO
501001 7.2 x IOC-5 Ib/ton <«.d Dry aorbont Injoctlon a
-------
few Me. M
Ot/21/90
POLLUTANT
Cadelue
Cadet ue
Cadelue
Cadelue
Calclue
Calclue
Calclue
Caerolactae
Carbon dUulflde
Carbon dUulflde
Carbon dUulflde
Carbon eonoxtde
Carbon eonoxlde
Carbon eonoxl d*
Carbon monoxide
Carbon eonoxl de
Carbon tetrachlortde
CM fIC
•unoc* COM iNoutniM. mocfu tniMioN MUPX*
74*041* 4911 nunlclpal naat* net* bure. refrecterv
ceebuatlen facility
744041* 4*SJ (euate tludte FluUliei-bee furnace
Incineration
744041* 4951 Senate eludge Multiple keartk furnace
Incineration
744041* *O* Hoapltal «a*te Incinerator
Inclneretlon
7440702 2951 Aaehaltlc concrete Plant atack
production
7440702 2951 Aaehaltlc concrete riant *tack
production
7440702 2991 Aaphaltlc concrete riant atack
production
105*02 28*9 neeonlun aulfata notary dryer
•reduction - ceprelactae
by-product
75150 2824 Synthetic fiber* Sonera! eeUalane
production - vl*co*e
rayon
71190 28«* CC14 production - CS2 Separation unit
chlorlnatlon
75150 2895 Carbon black eanufacture Rain precea* puree vent
- ell furnace
tlOOlO 2911 Petroleue refinery fluldlied Bed catalytic
cracker unit regenerator
*10080 129* niner*! •eel nlnaral wool cupola
•anuf acturtng
«10080 1112 Iron and ateel production flectrlc arc furnace
Ulloy ateel)
(carbon ateel)
*30080 3312 Iron and ataet production Electric arc furnace
{carbon ftteal)
54235 Uaite oil coebuatlon u.tl. oll-flred bollera
«ISu ellllon Btu/h) or
act COM mum no*
fOIWt •.0001 Ik/tM feed
(0100504 0.00141 Ik/tM dry eludoe
5010050* 0.01*0 Ik/ton dry eludge
(0200901 35.2 x 10* -4 Ik/tM feed
10(002 1.71 « lOC-f Ik/tM
concrete
10(002 2.7* x 10C-7 Ik/tM
concrete
109002 I.I » IOE-II Ik/tM
concrete
1012100* 2.42 Ib/hr
10102901 SI Ib/ton tlbere
3O11020I 4 Ik/ton produced
10I009O4 40 Ib/ton carbon black
produced
10*00201 I*. 2 kt/e-1 of fre*h fuel
throughput
10501701 4-112 Iba/ton of elneral
wool produced
10300904 4,*-«.( Iba/ton of atael
produced
30300908 0.54*1.07 Iba/ton of
•teel produced
30300908 0.54-1.19 lb>/ton of
ateel produced
1 0.25 lb/1000 gal oil
burned
MOTIt *
(pray drylno after *ct*l we end ffl CMtrel. one date
••Ink Mly
Aver MM ef three teat a. tcrukker
Average ef II te*t*. acrubber. ranee f .1 M IM-4 -
O.I2e
Uncontrolled, teat dot*
Uncontrolled froe a elegle plant, avg. ef 2 velvet.
rang* It I.OI « IOf-5 - 1.42 1 IM-f Ik/tM
Controlled luneeeclf led) froe a *lnel* plant, avg. «f 2
value*, rente It 1.72 x IOC-7 - I.OI K 10C-7 Ik/tM
Controlled lunaveclf led) froe a alnele plant
8a
-------
Pete Me. It
OP/21 /PO
POLLUTANT
Carbon tatrachlorlde
Carbon tatrachlorlde
Carbon tetrechlorlde
Carbon tatrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorJde
Carbon tatrachlorlde
Carbon tatrachlorlde
Carbon totrachlorlda
Carbon tetrachlorlde
Carbon tatrachlorlde
CAS tIC
Muntu COM
§4235 2112
54235 2112
54215 2112
54235 2122
54235 2114
14215 214*
54215 2«4»
54215 284»
54215 214*
54215 214*
54215 214*
54215 214 P
54215 284*
54215 2B4>
54215 2B4*
54235 284»
54215 2B4»
INDUSTRIAL PROCISS
CMorlne production
(chlor-alkall)
Chlorine production
Ichlor-altatl)
Chlorine production
HypalenR production
CC14 production - C12
chlorlnatlon
CCM production - CS2
chlorlnatlon
CCM production • CS2
chlorlnatlon
CCM production - CS2
chlorlnatlon
CCM production - C52
chlorfnatlon
CCM production • CS2
chlorlnatton
CCM production - CS2
chlorlnatlon
CCM production - CS2
chlorlnatlon
CC14 production - CS2
chlorlnatlon
cAlortnatfon
CCM production -
CCM production -
hydrocarbon chlorlnolyala
CCM production -
IMSSIOH SOURCC
tall •*• ecrubblM
Fuiltlvea/tell eae
ecrubblng
Nitrogen trichloride
diluent
All eource*
Plantulde eetaalone
Chlorlnator
Chlorlnater
Loading tank car*.
bargee, trucke. etc.
Loadlne tank car*.
barge*, truck*, etc.
Proceaa fugitive
eel avion*
Procea* fugitive
Procea* fugitive
Procea* fugitive
Storage
C*rbon tatrachlorlda tank
Ctrpon tatrachlorlda tank
Crude tank (atoraga)
KC COM HUSSION FnCTOK
101001 I.I Ib/ton cklerlee
production cepeclty
10100* 7* Ik/ten chlorine
productuien Capacity
30100* 1.2 Ib/ton CCM u**d
4*5.000 Ib/yr
101040 220 Ib/ton CCM u**d
IO1 30201 212 Ib/ton CCM produced
30130201 11.4 Ib/ton CCM producad
101102 0.4S Ib/ton CCM produced
301302 0.072 Ib/ton CCM
produced
10I102BO 1.2 Ib/ton CC14 produced
101102*0 0.44 Ib/ton CCM producad
30130280 0.44 Ib/ton CCM producad
301 10280 0.2B Ib/ton CCM produced
407040 1.52 IB/ten CCM producad
407040 1.14 Ib/ton CCI4 producad
407040 0.174 Ib/ton CCM
produced
407040 0.1*4 Ib/ton CCM
MOTH
Uncontrolled, net ell Plante nee CCM
Uncontrolled, calculated by total eel**lon/tatal
capacity of plant* that u>* CCI4
Uncontrolled, net ell plant* uae CCM In thle nay
One plant only In U.S.
Induetry-hl de •*•* balence
Uncontrolled
Hefrlgerated condeneer
Uncontrolled
Kafrleerated condenaer
Uncontrolled
Quarterly l/n puep* and valve*
Nonthly l/n puee* and valvea
Monthly l/n valvee. double eechanlcal *e*le on pueee.
rupture dlek* on relief velve*
Uncontrolled
Uncontrolled
Rafrlgerated condenaar
Uncontrolled
MraMM
114
,14
114
114
141
1*1
143
1*1
1*1
1*1
1*1
1*1
1*1
1*1
141
141
1*1
hydrocarbon ch.orlnoly*ls
-------
fate No. »0
0»/2I/*0
•OLUITMIT
Carbon tetrechlerldo
Carbon totrechlorlda
Carbon tatracMorlde
Carbon tetrecklorlde
Carbon tetracklorlde
Carbon tetracklorlde
Carbon tetracklorlde
Carbon tetracklorlde
Carbon totrachlorlda
Carton tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon totrachlorlde
Carbon tetrachlorlde
Carbon tstractilorlde
Carbon tatrachlorlda
CM *IC
NUnKI COOt IWXMTtlM. rMctal
f*23f 2M» CCI4 production -
hydrocarbon chlerlnelysls
5*2)5 2M» CCM production -
hydrocarbon cklerlnolysls
1*23* 2M» CCM production -
kydrecarbon cklorlnolysis
(4211 2t«t CCH production -
kydrocarbon cklorlnolysis
942)1 2S*» CCM production -
hydrocarbon cklerlnolysls
(42)1 2e4» CCM production -
kydrocarbon.chlorlnolysis
5*231 2849 CCM production -
hydrocarbon chlorlnolysls
54215 214* CC14 production -
hydrocarbon cklorlnelysla
5*215 214* CCM production -
kydrocarbon cklerlnolyals
S42)S 204* CCM production -
kydrocarbon chlorlnelysls
54215 2I4» CCH production -
hydrocarbon chlorlnolysls
S*2U 2e*» CCM production -
hydrocarbon chlorlnolysls
542J5 214* CCM production -
hydrocarbon chlorlnolysls
542J5 2S4» CCH production -
hydrocarbon chlorlnoly»ts
54235 2849 CCH production - eatlxna
cMorlnatlon
54235 284* CCH production - ..tti.nt
ch 1 or 1 nation
chlorlnatlon
IIIIMION MUM*
Crude tank
0ay tanks
Day tanke
•lstlllatt*« celueej
MOM waste kaedllMt
disposal
Hex «aste kandlln*.
disposal
Loadlne barees. tanks
taadine bars*** tanks
Process futltlve
•slsslons
Process fueltlvo
••1 salons
Process fueltlve.
•Missions
Process fueltlve
•Missions
Ussto caustic
Uists csustlc
Cruda tank (storaea)
Cruda tank (storaee)
•CC COM
4070*0
4070*0
407040
301)0202
50)007
SOJ007
101102
301)02
301)0280
301)0210
101)0210
)0 1)0210
503007
50)007
407040
407040
407040
IIIIMION FACTO* NOTCI
0.02* Ik/ten CCM e.e 10C-4 Ik/ton CCH Steae stripper
produced
0.114 Ib/ton CCH Uncontrolled
produced
0.0092 Ib/ton CCH fUfrtaerated condenser
producod
0.72 Ib/ton CCH produced Uncontrolled, value Is for tuo tonka
MFOsD
1*1
1*1
1*1
Itl
1*1
1*3
1*3
1*3
1*1
1*1
1*3
UI
1*3
1*3
1*3
UI
1*3
-------
•ow Mo. 91
Ot/tl /*0
POLLUTANT
Carbon totrecMorldo
Carbon totrachlorldo
Carbon totrachlorldo
Carbon totrachtorldo
Carbon totrachlorldo
Carbon totrachlorldo
Carbon tatrachlorldo
Carbon totrachlorldo
Carbon totrachlorlde
Carbon tetrachlorlde
Carbon totrachlorlde
Carbon totrachlorlde
Carbon tetrachlorldo
Carbon totrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
CM (1C
MUM* COM
M1H H4*
14115 2Mt
54215 2(49
M23S 244*
54215 2049
542IS 2(49
54215 2149
54235 2149
14213 2049
542JS 2149
S4239 2B49
54215 2149
54215 2149
54215 2149
54215 2>49
54215 2149
iMumiM. MOCK*
CC14 producttoji » ojothaiM
chlorlnatlon
CCM production - Mthane
chlorlnatlM
CCM production - oethano
chlorl nation
CCM production • oothane
chlorlnatlon
CCM production - avethano
chlorlnatlon
CCM production - oethane
chlorlnatlon
CCM production - *oth«no
chlorlnatlon
CCM production • oath an*
chlorlnatton
CCM product 1 on * Mthano
CCM production * *«tnan«
chlorlnatlon
chlorlnatlon
CCM production - nothano
chlorlnatlon
CCM production -
•othanol/oothyl chloride
chlortnatlon
CCM production -
•ethanol/oethyl chloride
chlorlnatlon
CCM production -
•ethanol/oethyl chloride
chlorlnatlon
CCM production •
•ethane! /eethyl chl ori de
chlorlnatlon
DI1UIOM SOtMCI
ft*y t*jik»
DUtlllatlon ere*
overtone? Inort ta* vont
Loadlnt tank car*, bar too
•rococo 4u«ltlvo
M! colon*
Procea* fufltlvo
••laalono
Procooo JueltJvo
oolaalon*
Procot* {u«ltlvo
*•!•*! on*
Product *tor**€ tank
vent*
vent.
Recycled oethano Inert
•a* purge vent
Carbon tetrachlorlde tank
Carbon ttttrachlorldo tank
Crude tank (storage)
Crude tank (*tore9o)
•CC COM DIIiUON r«CTM NOTM
407O40 O.O» Ik/ton CCI4 produced Rolrleereted condonaor. ualtio 1» 4or too tank*
101125 0.104 Ik/ton CCM Uncontrolled
oroducod
401 0.40 Ik/ton CCM produced Uncontrolled
400 0.072 Ik/ton CCM Hefrlooroted condoneor
produced
10112514 (.44 Ib/hr Uncontrolled
10112514 1.52 Ib/hr Quarterly l/n puopa and valuea
10112(14 2.42 lo/hr flonthly I/I) »uopp and valvoe
10112514 1.41 Ib/hr Honthly 1/H valuea. double oechanlcal aoale on puope.
rupture dlako on relief valvee
50100 . on con re
407040 t.Zt Ik/ton CCM produced Uncontrolled
407040 0.192 Ib/ton CCM Halrl§ei a ted condeneer
produced
I01I2SII <0.004 Ib/ton CCM Uncontrolled
produced
407040 2.71 Ib/ton CCM produced Uncontrolled
407040 0.42 Ib/ton CCM produced Kmtri eerated condenaer
407040 0.00 Ib/ton CCM produced Uncontrolled
produced
KHMMC
I4J
141
141
141
141
141
141
141
141
141
141
141
141
143
141
141
-------
•a** H*. »a
Ot/21/M
NUJUIMIT
Cerbe* tetrecMerlde
Carbon totrecklerld*
Carbon tetrachlorld.
Carbon tetracklorld*
Carbon totracklorldo.
Carbon tetracMorlde
Carbon, tetracklorld*
Carbon totracklerlde
Carbon tetrecklerlde
Carbon tetrecklorldo
Carbon tetrachlortde
Carbon talrachlorlde
Carbon tetrachlorldo
Carbon totrachlorldo
CM (1C
Munm COM mumiM. rMctw
M2JS 2M» CCM »r**KtlM -
MtkaMl/Mtliyl cklM-ld*
CklVlMtlM
(tin 2M» CCM production -
Mtkuwl/Mtkyl chlorld*
cklM-lkatlM
•4211 2to» CCM .roducllo* -
••Mitmt/Mtkyt chlorlo.
cklorliiallM
M2IS 2Mt CCM .reduction -
Mtkuiat/Mtkyl cklorldo
cklorlnatlM
S42IS 2I*» CCM .roductlon -
Mthtnal/Mthvl cklorldo
cklarliutlon
S423S 2l»r«((ln
•reduction
942U 2l4t Etkylono dlcklorldo
.reduction - balanced
.recall
54219 »•* Ithylana dlcklorlda
.reduction - balanced
•rocoai
34Z35 2B4» Etkylono dlchlorlde
production - balanced
.rocei*
54219 284f Cthylano dlchterlda
procctt
muioM waft
Loadlm lank carl.
karoo*, truck., etc.
Loadln* tank cara.
barao.. truck*, otc.
•roceao fuflklv*
ooloaiono
Procoao futltltfo
oolaalono
frecoao futitluo
oolaalons
•reco.s tutltlv*
ooli.lono
tur«o tank
Sum tank
Kacfded oathano Inert
*aa .uroo wont
All aourcoa
Colvien vonta
Colu.n vontf
Liquid waito storage
tec COM tninioH MCTM Mmt»
UIU2 I.M Ik/too CCM produced Uncontrolled
301102 0.194 Ik/to* CCM Halrloorated condonaor
oroducod
IOI102IO 1.04 Ik/kr Uncontrolled
I01102M 0.42 Ik/kr Quarterly I/H pua»a and valve*
I01102M 0.42 Ik/kr Hontkly l/n vuoos and vatvo*
101 102*0 0.2 Ik/kr Bonthly l/n valvoa. double eechanUal Mai* on .uo*a.
ruptur* dl*k* on r*llol valvo*
407040 O.IM Ik/ton CCM Uncontrolled
produced
407040 0.0044 Ik/ton CCM Refrtooratod condenur
produced
10112511
-------
Pan* Mb. n
0*/21/*0
POUUTANT
Muraoi COM IMUITIIIM. HWCIM
HUMID*
KC COM MIMIOM FACTO*
Carbon tatracklerlde
Carbon tetrachlerlde
MM
2M» Ithyleno dlcMorleo
production - balanced
2M» fthylm dlchlorld*
•roductiM • balwicod
Oxycklwleatle* vent
air oroce»
OxychlirliutlM VMt
air «roco««
MI 12*01 1.4 Ib/ten OC produced Uncontrollod. kith value e« rent* IO.M-2.4)
10112501 0.041 Ib/ton IOC produced Tbernal exldlior. hi oh value e« ranee IO.OIU-0.04U
141
Carbon tetrachlortdn S42IS 2M»
Carbon tetracklorlde
Carbon tatrachlorlde
Carbon tatrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon tetrachlorlde
Carbon totrachlorlde
MUf 2U*
Carbon tetrachlerlde f42IS 204t
Sa21S 2la»
S«JJJ 214*
Ethyl one Mcklorlde
•reduction - balanced
•receae
Itkylene dUfclorloo
•reduction - balanced
proceaa
Ithylene dlcblorlde
production -
oxyhydrochlortnation
Itkylone dtchloride
production -
oxyhydrocklorlnatlon
Fluorocarbon 11/12
production
MZ3S 21«» PUorocarbon 11/12
production
i«2II 2I««
54JJS 2la»
S4JJJ 214*
riyorocarbon It/12
production
Fluorocarbon 11/12
production
Porchlaroothylona
production
OHvchlorUatlM wit
onyiin >r«c«>
OayckkorlnattM v«t
oxyvan orocoia
10112501 O.M Ib/ton IK produced Uncontrolled, Men value o« ranee CE rroducad Uncontrolled
Carbon tetrachlorjde
Perchloroathflene
•reduction - EOC
Chlorlnatlon
Dryina coluan
101 US20 0.124 tb/ton PCC »roduc«d Uncontroltad
-------
Pace No. M
0*/21/tO
POLLUTANT
Carbon tetrachlorlde
Carbon tetrachlerlde
Carbon tetrachtorlda
Carbon totrachlorldo
Carbon totrachlorldo
Carbon totrachlorldo
Carbon totrachlorldo
Carbon tftrachlorlde
Carbon tdtrachlorloo
Carbon totrachlorlde
Carbon totrachlortda
Carbon totrachlorldo
Carbon totrachlorlda
Carbon totrachlorlda
CM (1C
NUMf* COM IMM1MN. MOttM HIIHION HUM
-------
raoe No. M
Of/21 /M
POLLUTANT
Carbonyl aullldo
ChlaroaiM
Chlardana
Chloric acid, aadluo ««lt
Chlorine
Chlorlna
Chlorine
Chlorine
Chlorine
Chlorine
Chlarlna
Chlarlra
Chlarlna
Chlorlna
Chlarlna
Chlorlna
CMorlne
CAS
MUM*
443MI
5774*
1774*
777SO»»
7712505
7712505
7712505
7712505
7712505
7712505
7712505
77I2SOS
7712505
77I2S05
778250$
7782505
(1C
COM
2ttS
4m
4«
2411
2411
2112
2112
2112
2112
2112
2112
2112
2(|2
2112
2812
20 12
INOUtTIIM. PMCtM mlMIOM tOUKf
Carbon kltck aanulKturo lulu pracaoa puraa wot
Mvaaa elude* Fluldl«ed-b*d
Chlorine production Lleuetcctlon blow •••••
(cnlor-.U.II)
Chlorine production Lleue««ctlon blau •••«•
(chlor-.lkall)
-------
Pate He.
Ot/21/tO
•OUOTMn
CM (1C
tuna COM ikWNiMM. MKSM
«« COM OUMtM MCIW
ChlerlM
Chlorine
77*2101 2M» KM and
porckloroetfcyloM
production - propane
chlorlnatlon
77I2SO9 2Mt CCI4 production • C92
chlorlnatlon
7712509 t*4t IplcKlorohydrln
production by
trv«r
IwwitlM unit
MIMMI 20.«0 U/ton w«ducoj4 Control r«tlM wilt
Iw«r«tla. direct
chlorlnatlon
lOlOOf O.OM Iko/ton opocltlty Uncontrolled oolxlono
•tool
lOIOOtOI 0.11 - 0.41 1 til/ton Uncontrollod ool»lo«>
corkon ttool
lOIOOfOI 0.01* - 0.024 Iko/ton Uncontrollod ooloolono
corbon ttool
1 2.44 Ik/ton cool kurnod Ctlculotod fro ln
-------
'ape Mo>. »7
e»/2i/to
POLLUTANT
CklorobonioM
—— —
ChlorobwiMM
€ttlM*abmi«M
Ch.*vot>*nx*fl*
Ch J 0ratMft.t *M
Chtorob«nz«n«
Chlero6«n»n«
Chlorob-mi-n*
CMwotomz.**)*
Chlorotrtntan*
Ch|oro6*nz«n**
Ch.OT*ob*ni«n«*
Chi orob«nzt]n«*
Chi erob*nz«nc*t
Chlorob«nzan«.t
CM »IC
NtfflKX COOK INOUmiM. AMCNI
IMfOT 4741 Rail tu* c«r cUi
I.MM7 4HS lluii.c.Ml iMftU
CO*tHJlt.MI
101*07 4»S3 ItuillciMl Matt*
CMtM»tiWI
101*07 4*33 Hunt Cl M! »*«t«
COoAuttlMI
101*07 41*53 ItunUlMl **»t«
CMbutkftM
{MM? 4*53 ItunlcfMl M«t«
cMtMitloi.
101*07 4*93 nunlclMl •»•.»*«
108*07 4*53 HunUU«l MAtt.1
CO*bUflUOn
101*07 4*S3 «««••« fludtw
10.1*07 4*53 •*«*•« fludtw
tncln«r*tio«t
101*07 4*53 U.it.-.ttr trttAtx
4*53 nunlclp*! w.i«t«
combustion
4*53 rtunlcl»«l t*»tt«
co**buitlon
4*53 Hunlcl»*l «tt«
combustion
4*53 ftuntciMt «**t«
co*bu«tlon
4953 HunlclMl »**>t*
co*buttlon
1 OIIMtON COURCC
M|M ' Intir* procMS
tncln«r«tor
Itodulw •t«rv«4**lr
coatfutter
LAI* AM •••• burn r*twy
.ateruall coebuator built
after 1*10
Larto «aaa burn rotary
waterwall coobuator built
after 1*10
coabuator. aeall alzo new
•odel to any ate oedluo
naaa burn watorwall
coebuator. built before
Haaa burn watorwall
coobuator. built before
1*10
Fluldlzed-bed furnace
Multiple dearth
int 'OTU
recovery facility
Citlatlno eaaa burn heat
recovery facility
naaa burn, nonheat
recovery facility
naaa burn, nonheat
recovery facility
nodular Incinerator
tCC COW CMIMIOK FACTO*
4*00} «.M4« Ib/tenk car
MIOOI 1.7 • IOC-S Ib/tM
SOIOOI J.4 K lOC-f Ib/tM
SOIOOI «.4 x IOt-« Ib/tM food
501001 a. 4 x IOt-4 Ib/tM feed
SOIOOI (.1 x lOt-t Ib/ton feed
SOIOOI O.OOOI2 Ib/tM feed
SOIOOI 2 x IOE-S Ib/tM feed
S0100504 2 x IOE-S Ib/ton dry
eludM
50100504 0.0024 Ib/tM dry aludoe
SOI0070I 1040 Ib/tM of
waato cotbuetad
501001 4 x IOE-S Ib/tM ef xaate
coebuated
SOIOOI 0.4 x IOE-4 Ib/ton of
waate coebuatad
501001 4 x IOE-S Ib/ton of xate
coebuated
501001 1.4 x 10E-5 Ib/ton of
waate coebuated
MOTH
(olailen MaaurooMt
IMS Kir fuel Mly. CM* control only, one data point
only
UncMtrelled, overall aver a to of aeveral aouree
overawe, ranee la 2.* x IOC-S - 4.4 x IOC-S Ib/tM
Capacity > 400 tona/day, HT control Mly. ovorall
averaoo of aeveral aource avaraoea. ranee la S.4 x
IOE-4 - 7.0 x IOC-4 Ib/tM
Capacity > 400 tona/day. uncontrolled. Mo data point
only, detection Holt reported
Capacity < 4M tona/day. ftp control Mly. ovorall ave.
of aeveral aourco avea. . rente le 2.4 x IOC-S - 1.04 x
IOE-4 Ib/tM
ESP control Mly. ovorall averaoo. of aeveral aource
averaM*. ranee to I.I x lOf-S - 0.0021 Ib/tM
Uncontrolled. MO data point Mly
One toot, ocrubbor
Averoe of five teate. acrubber
laaed on eele. oodellna for hypoth. »OTU. repreaento
Controlled by dry alkaline acrubber I fabric filter,
aaauaea *5X control efficiency
Controlled by ESP. baaed on aource teate
Controlled by dry alkaline acrubber t fabric filter.
aaaueea 95X control efficiency
Controlled by ESP. baaed on aource taata
RCPCICM
n
IM
IM
IM
IM
IM
IM
IM
101
101
S*
III
111
111
111
III
-------
Faoo Me. *•
0*/»/*0
•OLUmWT
Chlerebenienee
Ck] ordbeMofte*
Cklerebonieneg
Chlorobontenes
Cktorebenieneo
Chloroethane
Chleroethane
CM SIC
buna COM iMousniM. mats
4*51 nuntclesl Msto
coebustlen
4*51 Hunlclpol Mete
coebustle*.
4*51 nunlclpal uaste
ceebustlen
4*51 nunlclpal Mete
coobuetlon
4*51 nunlclpal MSt*
ceebustlen
75001 214* nc,t.|4ehyde production
75001 2*4* Ethyl chloride production
fMUION tOUKC
nodular Incinerator
Projected or
state-of-the-art MS*
burn keat recovery
facility
Projected or
state-of-the-art MM
burn heat recovery
facility
Refueo derived fuel
Incinerator
Kelu.a darlved fuel
Incinerator
Off -gas vent
Separation unit
KC COM BIIMIQN MCfO* HOnf
MIOOI I • IM-4 Ib/ton of (taste Controlled by dry alkaline scrubber t fabric filter.
ceebusted assuees tfl centre! efficiency
S01001 1.71 « IW-* Ik/ten of Controlled by It*, based en source test
Meet* ceebusted
S0100I 1.1 i IOC-4 lk/t*« of Controlled by dry alkaline ecrubber t fabric filter.
uaste ceebusted essuees Ml centre! efficiency
SOIOOI 2.1 « IOE-4 Ib/ton of Controlled by IS*, based en source teet*
Haete coebustad
501001 I.I « IOE-5 Ib/ton of Controlled by dry alkaline scrubber t fabric filter.
uaste contrasted SIMMS *St control efficiency
101 12014 2.2 Ib/ton acetaldehydo Controlled, lev pressure scrubber, data free one plant
301125 5 Ib/ton produced Centre! uncertain, based en eao* balance and tests
Mn*ni
ui
ill
in
in
in
141
Of
Cklereethane
Chloreoth.ro
Chleroethane
Chloroethane
Chleroethine
Chleroethane
Chleroethane
Chleroethane
7500J 214*
7500J 2M*
75001 214*
75001 284*
75001 2B4*
75001 2140
75001 284*
75001 284*
by hydrochl or motion
Ithyl chloride (reduction
bv hydrechlerlnatlen oi
ethanel
Itkvl chloride production
by hydrechlerlnotlon oi
ethanel
Ithvl chloride production
by hydrechlerlnatlen ol
ethylene
tthrl chloride production
by KydrocMorlnitlon at
ethyl one
Ethylene dlchlorlde
production
Ethylene dlchlortda
production
Ethylene dlchlorlda
production -
oxyhydrochlor1 nation
Totraothyl le4 *• vary c«n*wv«klv*i ••tlMta. b*««d on MCni 49
••{••ion f«ctorc
301125.5 5.14 Ib/tort i>roduc«d Contro, st*Cu« uncl«*r, b*>«
-------
Ot/21/M
HXJJJINn
CM SIC
MMfft COOC INOMTftl* MOCttt
•niMfON fOUMt
•CC COBff DIIMIIM MCTM
CklvMtkMM
ChlwMtktiw
CklcrMtkUM
«•»—
CM ore! ere
Chi orol ore
Chlerofere
CMorolore
Chi or of or a
Chi or of ore
75003 2*4* Totraothyl load Proceae • general
production
7S003 4*93 SoMato studs* ItultUU hearth fur HOC*
Incineration
75OO3 4ffS3 Uaatowator troatoont POTU
47443 2411 Secondary 11 her mil It Dejnk * UHO papers
47443 2411 Secondary fiber ollla Oelnk - fine paper*
47443 2411 Secondary fiber olll* Oolnk - tl**uo papor*
47443 2411 Secondary ftber etll* Defnk - tissue papor*
47443 2421 Pulp/paper Mill, Matched Kraft
Integrated paper board, coarso papers
Integrated paper board, coarso papor*
47443 2421 Pulp/papor Mill. Dissolving Kraft pulp
47443 2421 Pulp/papor olll. Dissolving Kraft pulp
integrated pulp
integrated bleached papers
Integrated bleached paper*
301042 U Ib/ton totraothyl load SoMd) CM Tonas «Ct Kol**lo« Inventory data for ono
produced source
•0100504 0.0014 Ib/ton dry eludfe One teot. ecrubber
•0100701 1340 Ib/ton el ethyl oa*ed en eel*, eodollne lor hypoth. POTU. represent*
chloride In Inlluen average POTU that treats Industrial Hastowater
307 0.72 Ib/ten total During wastewator troatoont
product*
307 0.024 Ib/ton total Alter Maoto«ater troatoent
product*
307 0.32 Ib/ton total During Ma*tawater troateent
product*
307 0.0134 Ib/ton total After wastewater treatment
product*
307 0.44 Ib/ton total During waotowater troateent
product*
product*
307001 0.24 Ib/ton total During naotowater treatoent
product a
307001 0.024 Ib/ton total Alter waste water treatment
products
products
products
products
products
products
products
45
lot
W
144
144
144
144
144
144
144
-------
few «•. 100
Ot/21/M
POLLUTANT
Gkleretore
Chlorofore
Chlorof ore
Chlereforo
Chi or of or.
Chlorolore
Chlorof ore
Chlorolore
Chlorolor.
Chi or of ore
Chlorolor.
Chlorof or.
Chi or of ore
Chlorof or.
Chlorof ore
Chlorofore
Chlorofore
CM tie
MUM* COM INDUSTRIAL POOCH*
47441 2411 Pulp/pater •III.
l.teeratod
47441 2421 Pule/paper elll.
Integrated
47441 2011 Ascorbic acid production
47441 2114 Phareaceutlcal
•anufactur*
47441 204* Acataldehyde production
47441 214* Chlorelore production
tany eethod)
47441 2»4» Chlorolore production *
•ethane chlerlnatlon
47441 214* Chlorolor* production -
•ethane chlorlnatlon
47441 214* Chloroform production -
•ethane chlorlnatlon
47441 214* Chlorolore production -
•ethane chlorlnatlon
47441 214* Chlorolore production •
•ethane chlorlnatlon
47441 214* Chloroform production -
•ethane chlortnatlon
47441 214* Chlorolore production -
•ethanol/CIUCI
chlorlnatlon
•ethanol/CHlCt
chlorlnatlon
••th4.no! /CH3C1
chlorinAtlon
47*43 2B«f Chloro»«th*n« production
- ••th.mti chlorlnttton
474*3 2849 Chloroacthftna production
- ••th*nol/CH3Cl
chlc.rin4t.lon
tnlltlON «OUKI ICC COM BUNION FACTO*
lull It. papertrad* pulp 107 0.7* lk/te» total
and paper producta
tulllte eapersrede pulp 107 «.l4t Ibfteej total
and paper products
Plantuldd eelsslens JO 1040 4.»2 « IMS Ib/yr
Plant.lde eelsslona 101040 120 Ib/tee Chlorolore
uaod
Oll-s» vent 10112014 0.1 Ib/ton eotaldehyde
Handllno llo.dln. of tank UII2S 0.7 Ib/to* loaded
trucka and tank cars)
Bl.tllUtlon iraa 501 US 10 0.014 Ik/ton total
a«ersanci> Inert eas vent chloroeethanes prod.
Hendllnt/dlseosln* lleuld S0100701 0.42 Ik/ton Chlorolor.
ua>ta produced
neth.no Inert puree vent 10II2SII 0.0044 Ib/ton total
chloroeothanee prod.
Process fugitive 10112514 4.11 Ib/hr
Process lufltlve 10112514 2.42 Ib/hr
antsslons
storage tank emissions 407040 1 Ik/ton total
chlorOMthanos produced
Process futltlve 10112514 1.01 Ib/hr
a.l lalons
chlorooathane produce
••cycled .athano Inert 10112511 0.0044 Ib/ton total
gas purs* want chloronethanas capa
lnart-«i puree vent lor 10112510 0.0112 Ib/ton total
cond«n*«r aaioclated with chloroaathanaa prod.
chlorofor. dlttlll .
worn '
Durlne tia»t«ut«r treal»ont
Alter M*.«teM4ter ir«at»eAt
•
-------
»«M No. 101
Of/21/M
CM SIC
NURKIt COME INBUSTftfM. AtOtfM
CH1MIOM
«ce COM oimioN FACTOR
Chlar*««
M4f IthylOAO dUMorloa
production * fctlancod
S lkn«i fW rrwlucwl UnconlrolM
IM
CMorotore
Oiloraw<
2(4* tthvlana dUklarlda
production * kalancad
•rocaaa
2t4> Itkylana dlcnlarlda
production - kalancad
Qicychlortnatioft vont
4ir proco»
101I2SO1 I.I U/ton IDC »raduc«4 Hlduit v«lu« rwort«a In r>«r«tc« uncentrall*4
6.014 Ik/Ion IOC »ro«uc.d Hlihnt «roduc
-------
Peee No. 102
oe/xi/to
POLLUTANT
Cklorofora-
Cklorefere.
Chlorofore
Ckloroforn
Chlorofore
Chlorofore
Cnloroforn
CMorefore
CMoroforo
Chlorofore
Chlorofore
Chlorofore
Chlorofore
Chlorofore
CM »IC
Munm coot iMumiM. r*ocni
47441 204* lletkylOM eWorld.
production - ketkene
47441 2*40 Ke thy lone cklorlde
production - eothane
cklorlnetlon
47441 2MO n. thy lone cklorlde
production * ketkyl
chloride cklorlnatlon
47441 2140 ttatkylene chloride
production - eethyl
chloride cfclerlnatlon
47441 2D4» Itothylene cklorlde
production • eethyl
chloride chlorlnatlon
47441 204* Perchloroetkylone end
trlchloroetkylene
production
47441 20»» I.l-Dlleocyenate
production
47441 2i»* Oxvkluhenoxir.lne and
1.1-dlloocyenate
production
47441 JO** Oxykl.phenexar.lne
production
47441 4*11 Coollnl tower*, utility
47441 4*11 Coollnl tower., utility
47441 4*41 Water treatoont
47441 4*51 landfill
A74A1 4«S1 fi«u*a« •! udaa
UIIUION $OUMt
Inert nee puree
wmtSeroduct recovery
Storeee
fulltlve eel. .lone
Inert oee puree
v.nt/r>reduct recovery
conaenmor
Skoraee
Uxtewator etrlpper
Plantwlde eelMlono
Deaeration of eeueoue
waate
Plantwldo eelolon.
Cool! no towore - once
throuth ayatee.
Cool ln« tower. -
Chlorlnatlon of drlnklns
walar. evaporation
L«od(lll «n
KC COM INIttlON r*CTM MOTH
WII2f 1.0 « IM-I Ik/ton Derived free el to vl.lt
product
407040 *.I7I Ik/ton product Derived fro* elte vl.lt
MII2SI4 0.4*4 Ik/ten product Derived «roe olte vl.lt
JOII2J 0.014 Ik/ton product Derived «rea elte vl.lt
407040 l.ts Ik/ton product Derived froe elte vlolt
Ml 125 0.24 Ik/ton Controlled with 2 conden.ere. eey not epply to ell
perckloroethylene PCE/TCI plant.. .00 reference
produced
S.t x 10E-4 Ik/eec C«rbon edurptlon
0.0022 Ift/t Uncontrolled
0.0011 Ik/. Carbon adiorptlon
0.00142 U/IOC4 lal Uncontrolled
coollni water
4. 25 16/IOE4 ill cool In, Uncontrolled
water
1.14C x 10C-7 Ib/lal eun
wa.tewater dl.c
1.42 x IOE-4 Ik/lOCl o*l
water chlorlnat
5 0.41 x IOE-4 Average of ht«he«t values for 20 landfill. In S.
volue./voluee landfill California
II
II
11
lnctn«r*tton
-------
Pew No. 101
Of/21/M
POLLUTANT
Cklorolore
Cklorofore
Chlereeethane
Chloreeothana
Cklereeethane
Ckloroeotkane
Cbl orophenol
Oiloroohonol
Ckloroplienol
Chloroehenol
Cnlorophenel
Chlor ophonel
2-Cnl erophenol
2-Chl orophenol
2-Chl orophenol
Chlorophonola
CM
Minn
47441
47441
74171
74171
74173
74171
251 47100
2S147IOO
2S147000
25147100
25147100
25147000
95571
95571
95571
IIC
COM
4m
4953
214*
2 049
2449
4*51
4*51
4*51
4953
4951
4*51
4953
4 7*5 3
4*51
4953
4953
INDMTilAL Moon
Incineration
Uaateuater troatoont
AcetalMye. .reduction
Ckloroootkone production
- eetkaoe chlorl nation
Chloreoothane production
- eetkanol/CHWI
cMorlaatlon
Incineration
coebuetlen
llunlclpal Mate
coobuatlon
nunlclpal uaito
coobuatlon
llunlclpal Mate
coobuatlon
llunlclpal note
coobuatlon
nunlclpal Maeta
coobuatlon
Incineration
5euato aludoo
Incineration
nunlclpal uaete
coobuatlon
MISSION MUM*
Multiple hoartk lurMf*
POTU
Oil-... v«t
xecyclee eetken. Inert
Inort-.aa puree vent lor
condonoor aoaoc. •/ ootk.
chlor. prod, recov.
Multiple heartk lurnaco
Refuae derived fuel
Incinerator
Hodular otarvod-olr
coobuator
Lar.o oaaa burn rotary
wataryall coobuator built
after 1910
Lar.e oaaa burn rotary
Metaruall ceebuetor built
alter 1910
tlaaa burn Maternal 1
coobuator. aoall aizo na«
oedal to any ate oediuo
flaaa burn Mataruall
coobuator. built before
1910
Hultlple hearth furnace
POTU
icc coot HUSSION ncrai
10100104 0.0071 Ik/ton eV» tlodoe
10100701 t»40 Ib/ton of cklorolore
1* Influent
10112014 2.X Ik/ton acoteldehyde
IOII2I1I 4.01 Ik/ton totol
ckloroeetkonee ca.ec.
30112510 1 Ib/ton total
chtoreoethanee prod.
50100504 0.01012 Ib/ton dry oludea
501001 0.0002 Ib/ton «Df
coebuatod
501001 1.4 x IOC-S Ik/ton food
501001 9.2 x IOC-4 Ik/ton lead
501001 1.2 x IOC-S Ib/ton leod
501001 O.OO013 Ib/ton loed
501001 0.0012 Ib/ton loed
eludte
50100504 <2.4 x 10E-5 Ib/ton dry
eludta
50100701 40 Ib/ton 2-chlorophenol
In Influent
uaate coobuatad
NOUS
Avorate el tlx teate, .crabber
•aaed en eel a. eodelln. lor kyeotk. POTU. ropreaenla
aver aoe POTU tkot treat. Induatrlal uaataxator
Controlled, lou pre.eure ecrubber. data Iron one plant
Uncontrolled, booed on Inforoatlon auppled by one
producer
Uncontrolled, kyootk. lac. product no 2SX eethyl
chloride. 4IX HC. 251 chlorofore. t 21 carbon tot.
One teat, ecrubber
1001 RDF fuel only. ISP control only, one data point
only
Uncontrolled, overall averaoe of eeveral oource
avaraeo., rente It 2.2 > 10E-S - S.I K IOC-S Ik/ton
Capacity > 4OO tone/day. CSP control only, overall
averate of aeveral oource everateo. rente la 1.0 x
IOC-4 - 1.04 x IOC-S Ib/ton
Capacity > 4OO tone/day, uncontrolled, one data point
only, detection Holt reported
Capacity < 4OO tone/day. CSP control only, overall
avaraoe of aeveral uurco evoraee*. ranee la 4.4 x
IOE-5 - 0.00024 Ib/ton
CSP control only, overall average ol aevoral aource
avaraoee. ranee la 1.4 x 10C-5 - 0.001* Ib/ton
One teat , ecrubber
aae on ee a. e e nt or ypo . . rep
MFIOItNCK
101
5*
141
71
72
101
ISO
1*0
110
110
110
110
101
101
40
-------
••M Ma. 104
Ot/tl/M
POLLUTANT
OlBraahMala
Ckleroehenele
Cklereehanala
ChloroehonoU
Chloreehenol.
CMoroeh.noU
Chlereehenole
ChlaraehMalg
CMoroeh.noU
Cfclareerena
CMereerene
Chlereerene
Chlereerene
Chloroprene
Chlereerene
Chleroerane
Chloreprene
Chlaroerene
CM SIC
MUMS* COM IMUSTMM. PMCCtt INIMIOM SOWCI
4fSI nualcleol Mat* bletlM •*» aura beet
ceakwtlM recovery facility
4X1 Municipal Met* tleee aura, aanhett
ceekuatlM recovery facility
4t»l IkMtctaal iiaita llaee burn, aonha.t
ceekuetlM recovery facility
4M1 IkMlcloal Mete nodular Inclner.ter
4t5J IkMlcloal veete Modular liulaeretar
caabuatlM
4*n HunUieel wata Prelected or
burn heet recovery
facility
4»S1 Municipal veete Projected or
coabuatlM .t.»a-of-the-ert aaee
burn heet recovery
facility
4*S1 nunuleal -it. ..fv.e derived fual
CMbuetlM Inclnerater
4*S1 nuMcteat Mete Itaiuee derived fuel
caakuetlen Inclneretor
I24VM 2S21 Pelyvlnyl chloride (uipenilM ereca>4.
ereductlen entire elent
I2«»»8 2822 NeeerMe aenuiectura Ittck pelykettlee
I24»M 2822 Neoerene a«iucture Chleroprene vent
I24«tt 2822 Neoerene euui<»cture Dryer «»h.u«l
12«»»i 2822 NeoprMe ainufictura £«uH>oo etorege tutke
I24»<8 2822 Neoprene euuiftcture H«.lt t«nk
I24»*8 2822 Neoprene ..mificture Jit vent icrubber
124*98 2822 Neoprana aanufkctura *Kvclm chloroprene t«nK
SCC COM tMSSIOM MCtM
MIOOI 4 « IOC-S Ik/tan e» Mate
ceebueted
101001 e.j x iOf-4 Ik/tM el
neate ceakuated
SOIOOt t x IOC-S Ik/tM at «««ta
SOIOOI 1.4 M lOE-i Ik/tM af
$41001 X * IOC-4 Ik/tM af i»»te
caekueted
J0100I 1.4 it tot-s Ik/tM af
901001 2 x. IOC-4 Ik/tM o( mite
ceabvited
901001 1.4 x IOC-4 Ib/tM ef
"••'• "ebueled
101001 t it IOC-S Ib/tM ef «»ta
co^ited
10I01W1
-------
•aw No. 101
0*/2l/tO
POLLUTANT
CM or oar one
ChloroorofM
Chloroerene
CMoroereno
Chlerooreno
Chroeluo
Chroeluo
Chroolue
Chreoluo
Chrooiuo
Chrooiuo
Chrooiuo
CM fit
Nuran coot INDUSTRIAL rwctM BUitio* COMCC
12«*M 2*22 Nooereno eenulacturo ItrUeere
I2*»M 2122 Neooreno oeMifecturo • Tank car vont>
I2«*M 2122 Neoarone oamilacture Vacuuo coluoa Jet
12*»M 2122 Noworono aanufectura Valorization
10102*11 1.2* Ib/ton KoooroM tnelneorlne Judiaeent 121
301 Jt 0.42 Ib/ton neoorone fntlneerlnt Judgeeont 121
10102* O.M Ib/ton neoerene In»lne«rlnt judeeoont '"
10102* 0,07 Ib/ton neoerene Enetnoerloi Judiaeant 121
1012* O.OM Ib/ton nooerone fnelneorlel Judoeoont 121
1 502-3720 lb/IOC12 Itu Uncontrolled, calculatod baaed on onelnoerlno judeeeent I*
1 2M-21SO lb/10E12 Itu Controlled Kith oulttclone. calculated ba*od on 1*
1 141-10*0 lb/10EI2 Itu Controlled «lth EIP. calculated baaed on enelneerlno I*
Judeeeent
1 41-305 lb/IOCI2 ltd Controlled Kith xrubber. calculated baaed on 1*
enalneerlno Judeeeent
1 2420-1720 lb/10C12 Itu Uncontrolled, calculated baaed on onelnoerlno judoeoent M
1 1400-2150 IO/10C12 Itu Controlled Htth oultlclone, calculated baaed on I*
anolneertne Judeeeent
Judeeeent
engineering Judeeeent
1 2230-1720 U/10CI2 Itu Uncontrolled, calculated baaed on enelneerlno Judoeeent 3*
enalneerlne Judoaeent
s
i
5
-------
Pete It*. 104
oe/21/M
POLLUTANT
CM »IC
NUMt.) COM IMMtftML MOCK*
MIMION
»CC CON tmtSION FACTO*.
NOT!*
744O47J Cool coekmtlMi
Chroelue
Chreotue
Chroelue
744047J
Cxi ceokuetlen
744O47J CM! coebuetlon
Coal COOkuetlen
744047S Coot coobuotton
Coal coekuetlon
7440471 Coal coebuetlon
7440471 Coal cookuotlon
c**t-ftrM) t
k*H*r«.
4M-IOM IWIOftt Itu CM troll 04 ntUi MT. ciUuUtotf luootf M onolnoorino
tathrult* mlu«rU«<< «•» I
batton lxll«r>.
Anthrtclti »ultMrl»4 dry I
bettM k«llw«,
utll/couwc/loduitr
bottom b«ll.
utl I /cuurc/loduitr
Artkhr«clt« »uly«rli«d
bolt o« tolKri.
utl 1 /coaa«rc/lnduatr
•Itualfieui coAl-llr«d
cyclon* bollw.
ut 1 1 /cMMrc/l ltduitr
Blkualitou* coal-llr«tf
cyclon* bollor.
uti I /co»«rc/tnduitr
tltu.lnoui co« S*
244-10S lb/10112 Itu Controlled «lth ocrubbor. cilcuUtod b«««d on
onolnoorlno judoooont
2I2-IS70 lb/10C12 Itu Uncontrollod. olculotod b«»od on onolnoorln* judoooont 14
I22-M4 IWIOEI2 Itu Controlled «lth oultlclono. colculotod bo»od on
ontlnoorlno Judoooont
40-447 Ib/IOCU Itu Controllotf tilth Itf, celcuUt.d b»««d on onolnoorln« M
7440471 Coil coebuetion
7440471 Coil coebustlon
744047] Coil coetoustlon
744047] Coal co«bu«tlo
744047] Co«l
• Kualnou* Co«l-llrod I
cyclono bollor.
utl 1 /coaoorc/lnduitr
•ItuMlnous co*l-llroil 1
oulvorlxod dry bottoo
boll«r«, utll/co«iorc/lnil
•llualnout co*l-llrod 1
pult/orlitd dry bottoo
bollort. utll/coooorc/lnd
•itualnous coftl-flrod 1
pulverized dry bottoo
boll«r«. uttt/cooo«rc/t(td
BltuMlnout co«l-flr«d 1
pulvarliad dry bottoo
boiler*. utll/coa««rc/lnd
17-12* Ib/lOCU Itu
721-004 U/10EI2 Itu
JSi-447 Ib/IOCU Itu
Controlled with •crubbar. Ct.lcul*t«*4 on
•n«l »••»-.(.• judf«ii«nt
1290-1570 lb/IOC12 Itu Uncont
judoooont ]4
Controllod vlth oultlclono, ctlculited tanod on
onflnoorlnf Judgooent
Controlled with ESP, calculated based on enolneerlne,
Judaoeent
102-12* lb/10E12 Btu Controlled with ccrubber, calculated baaed on
engineerln« lud«ee«<\t
-------
Paw M*. 107
0»/21/*O
CM *1C
MUHKR COOK INDUtTftlM. MtOCCM
BIIMIOM MUM*
sec COM ninioN FACTO*
NOIIt
MFtXUICC
ChreeUuoi
7440471 CM!
7440471 Coal coaeuatlon
7440471 Coal contention
MtwlMUe « wily, centre!l»d ultk M
<4brlc .
MI-477 lk/10CI2 Itu Controlled «ltfc ISP. calculated kited on onelneerlnt M
tn co*l-Hr«d 1
bttllart. Utll/CMMTC/lAd
•ttuatnou* cA*t-firad 1
Mr Oder •taker bollwi.
u 111 /ctr
I.S-S.S lb/10£12 Itu
Indue, t co«eerclal koller eel>. o( Cr»< only,
controlled ulth 2 eechan. eat In (erle*. aourc
7440471 Coal coekuatlon
Llinlte co«l-
-------
Pod M*. l«
Oe/21/tO
•OLUmiMf
CM *IC
NUmOt COM IMUITCIM. MOCCM
IHIMIOM
tCC COM fMSflON MCTM
NOTU
Chroeluo
Chreelue
744*471 CMl CMktMtlM
7440471 CM! coobuetlo*
7440471 CM! CMktntlM
7440471 C»«l CMtuitlM
7440471 Col
7440471 Co.l co.6u.tlo
Lienite. C0*l-llr*4
eulverlled try kettoo
boiler.
utu/coeeerc/leduetr
IMO-IMO Ik/10112 Itu Uncontrolled, ceUuletod besed on enolneerlne Judiseent M
Uonlte co«l-llred
tuluorlied dry bo t toe
ballw.
Lltnlt*
boiler.
utlI/coeeerc/ledustr
Llo/ilte coel-fired
eulverlxod dry bottoo
boiler.
Llknlto co«l-fired
pulverized uet bottoe
bollere.
utll/coeeerc/lnduetr
Llonlto coel-flred
•ulvorlxed uet bottoe
•M-IOM Ib/IOElZ Itu
Contr«ll«d vltk wiltUlMM. MlcuUtdd b«l*d M
•niliiMrln* JudwMnt
4ZI-SI* Ik/10112 Itu Controlled xlth I«». celcuUted keeed en enclneerln* M
le
I 1220-IMO Ib/IOCU Itu Uncontrolled, celculeted beeed on enilneerlne judeeeent to
121-114 Ik/10112 Itu Controlled "Itk ecrukker. ctlculeted keeed on
704-IOM lb/IOCI2 Itu
Controlled "ltd oultlclone, ulcuUtod k>»d on
ontlnoorlno Judiooent
7440471 Co«l tombuHlon
7440471 Cod co«fru«tlon
7440471 Co«l co«buctl«i
ut11/cooeerc/lnduitr
Llenlte co
-------
feoo Wo. 10*
Of/21 /tt
POtUflMNT
Chroejluo
Chrooluo
Chroolue)
Chrooluei
Chrooluei
Chrooluo
Chreelue
Chroelue
Chrooluei
Chrootuo
Chrootuo
Chrooluo
Chrooluo
Chrooluo
Chrooluo
CM
Hun***
7440471
7440471
744O471
7440471
744047]
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440473
7440473
SIC
COM INDUf mi*. MOCfef
Coel cookuetlon.
reeldentlel
Coel Coobustlon.
rosldentlel
Coel coekuotlon.
resldentlel
Coel cookuotlon.
residential
Coel coobuetlon.
residential
Coel cookugtlon.
residential
Ceel ceokuetlen.
residential
Industrial
Cooling towerg.
Indue trlel
Cooling towere.
Industrial
Cooling towere.
Industrial
Cooling towere.
Industrial
Cooling towers.
1 ndustrlal
Cooling towers.
Industrial
BlfttlON fWMCf
Anthracite coel -< trod
eel lore
lltuelnous coal-fired
boilers
•ollere fired by coel
•ollere fired kv Ceel
tree Interter roeton
•ollere fired kv Ceel
free northern plain*
region
lollere fired kv coel
free rocky oounteln
region
Lignite coel -fired
boll ere
tubkltu.ln«,. ...1-flr.d
Cooling towere with low
efficiency drift
ellolnetor
efficiency drift
Cooling towere with low
efficiency drift
ellelnator
Cooling towers with low
efficiency drift
ellelnator
Cooling towers with low
efficiency drift
ellelnator
Cooling towers with low
eliminator
Cooling towers with low
efficiency drift
.H.ln.tor
tCC CODC fnltflO* MCTM NOTft
172 Ik/10112 It*. Uncontrolled, highly verleklo. celculetod ketod en
ontlneorlng Judgeoent
1S7 Ik/10112 Itu Uncontrolled, highly verleklo. celculetod besed en
engineering Judgeeent
U7 |k/10t!2 Itu Uncontrolled, celculetod beeed on engineering Judgeeent
241 Ik/I0tl2 Itu Uncontrolled, calculated based en engineering Judgeeent
•1.1 Ik/10112 Itu Uncontrolled, calculated keeod en engineering Judgeeent
21* lk/IOCI2 Itu Uncontrolled, celculetod keeed on engineering Judgeeent
IK Ik/10112 Itu Uncontrolled, highly variable, celculetod keeod en
engineering Judgeeent
114 lk/IOC12 Itu Uncontrolled, highly variable, calculated beeed on
engineer Ing Judgeoent
.441) coel H20 1/oln, Cr04-»ee cone. In reclrculatlng HJO
Ccr*.01149X HUM ICRo4 H Ecr" Cr oeloglon rete • eg Cr/oln. ft'roclrcul reto of
.441) cool H20 1/oln. Cr04*ppe cone. In reclrculetlng H20
Ccr..0071 » P. » (C*a4 » Ecr- Cr oelsslon rate - eg Cr/eln. R-reclrcul rete of
.441) cool H20 1/oln. Cr04-ppo cenc. In reclrculatlng H20
x g
20*
-------
».M M*. uo
Ot/21/tO
POLLUTANT
CM tIC
MMtt COM 1WMTIIIM. MOdM
•MMION MUKI
«cc COM
MOTH
CkTMliM
Chromium
Chrwlw
744M7J Cwlln* tMMTI.
l*dutlon
OI«kllUt<
kollw.
ukl l/c
dintUI
OUtllliU «ll-«lr«d
bolUr.
utl I /ceMWC/lndu«tr/r«l
d*Atl>l
•tt-tlon
S«u«M tludo*
Inclntntlon
tludo*
tnclnvrttlon
S«u*t« ilud9*
tncln«r«tkon
utll/ca««rc/lndu»tr/ro>l
d*ntl«l
•••ldu»l oll-4lr«d 1
boil.r.
utl1/co«««rc/lnduitr/r*tl
dtntl.l
Fluidli«d-b«d (urn«c« 501
ControlUd »lth tff. c«lcul*t«l b«««l« h««rth 4urn*c« 501 0.007 • O.«l lb«/ton dry Uncontrollod ••lc«lon«. *vmr»9m of S t»tl M«« 0.21 203
Ibft/ton
-------
Pae* Ho. Ill
0»/21/»0
POttUTMT
Chreelu*
Chreelue
Chroelue
Chroolue
Chroelue
Chro.Ua
Chroaiua
Chroaiua
Chroal ue
Chroaiua
Chroaiua
Chroeluo
Chroelue
Chroelue
Chroeluo
Chroelue
Chroelue
CM SIC
Nunm cow IMUSTHIW. MOOM
744O471 Sen*** elude*
Inclneratlee
7440471 Vaata ell coebuatloe
7440471 Wood ceobustlen.
raaldantlal
7440471 221 Woven fabric fleletileo
7440471 224 Woven fabric flnlahlne
7440471 22« Uoven fabric finishing
744047] 22« Woven fabric flnlahlne
7440471 25 Wood coebuatlon.
Industrial
7440471 29 Wood coebuatlon.
Industrial
7440471 25 Wood coebuetlon.
Industrial
7440471 211* Chroalc acid production
744047) 211* Chronic acid production
7440471 211* Chroalc acid production
7440471 211* Chroalc acid production
744047] 211* Chroalc acid production
7440471 211* Chroalc acid production
7440471 2*31 Asphaltlc concrata
IMIMIM MUKC
Multiple beartb fureace
Waste ell-fired belter*
«M» •llllon tttt'M or
Woodsteve vltkout baffle
Curlne ev*n - resin
finish
Meat settlne
tenter fraeas - raaln
Thereosal drains
Horizontal r*turn tub*
lalancad draft ulckaa
etoker-flred Industrial
boiler
lalancad draft Kick**
stokar>flrad Industrial
bol 1 ar
Chroelc acid filter
Chroalc acid fitter
Chroalc acid reactor.
•el tar, flatter
aaltar, 1 later
Packaaln*
Plant stack
KC COM BHHHN rYsCfai
tot O.OOOS - 0.0071 Ike/ten
dry elude*
1 0.17* Ik/1000 eal ell
burned
O.OOIt Ib/ton need burned
130001 t x 10C-4 Ik/toe fabric
1)0001 1.4 a IOC-S Ik/ten fabric
110001 0.00104 Ib/ton fabric
110001 2.4 « IOC-4 Ib/ton fabric
10200*0* 20.17 lfc/10CI2 Itu koat
Input
10200JO* 0.0001 Ib/ton fuel or
0.010 ns/J
1 020O*0 1 0.0001 Ib/ton fuel or
0.014 ns/J
301 Z.I Ib/ton rau eaterlal
processed
101 0.02 Ib/ton rau eaterla!
procasssd
301 0.4 Ib/ton ran eatarlal
procasssd
301 0.02 Ib/ton rau eaterlal
proceassd
301 1.4 Ib/ton rau aatarlal
procaaaad
processed
S0500J 1.24 » IOE-10 Ib/ton
NOTfft
Controlled by Met scrubber, aver at* ef • tests wu
0.0052 1 be/ toe
Uncontrolled, baaed en eat eel one date and enalneerlna
Judeeeent. variable
Uncontrolled, based on one study, nonbaffled stove
burnlno ereen pine
uncontrolled, avereee ef three teate
Uncontrolled, based en teet date, total Chroelue
Uncontrolled, averaee ef four tests
Uncontrolled, averaeo of three teats, total Chroelue
Saeple results, 1 riant, veod floorate • .114 ks/a.
boiler has 1-sais deslen u/ftvaah relnjectlen.
uncontrolled
Dry uood, one plant, partlculate control si/eechanlcal
collector (cyclone), eood feed rate 0.2* key*, boll.
off. SI. IX
collector (cyclone!. Mood feed rate O.S4 le/a. boll.
off. 41.31
icrubbar. aa total Chroelue. llkaly to be Cr VI
Uncontrolled, aa total Chroelue. likely to be Cr VI
Scrubber, aa total Chroelue. llkaly to be Cr VI
Uncontrolled, aa total chroelua, likely to be Cr VI
•*7iNCN
MI
IS
51
SZ
52
52
52
17*
177
177
Ul
Ul
Ul
Ul
Ul
Ul
170
production
2 v«lu««. r*n«€ It 7.57 * IOE-I1 - 1.71 x IOE-10 Ib/ton
-------
few Ml. lit
0»/II/M
CM SIC
Mumat COM ikBurmiM. »Roctu
nilUION MUMS
KC COM tnlUlON MC1M
MIC*
tsnxoisx
ChrMlua
CHTMtUO,
744O471 mi HspheltU concrete Plent
production
744O47I 1241 Caeent eeaulacture • dry
•recess
CeeaM aeaulscturc - dry Kllsj
process
7440471 1241
Klin
•recess
7440471 1241 Ceaevt asaulsctura - dry Kiln
7440471 1241 CeaMt asnulecture - net Clinker cooler
process
7440471 1241 Ceeent
7440471 1241
7440471 1241
- net Clinker coaler
Clinker cooler
aenufecture - »et Dryer/arlnder
7440471 1241 Ceeent unulecture - ust Kiln
:ture - uet Kiln
7440471 1241
7440471 1241
7440471 32*7 Refractory production Fusion i
Uncontrolled *><*> * slnolo plent, evt. el 2 velum.
renM Is 1.10 x 10I-* - 1.12 x lOC-t Ib/ton
Uncontrolled. Includes luel Missions, es totel
ChrMlua
Includes luel Missions, ss tatel ChrMlua,
uncontrolled
30)004M 1.1 ll lOf-S Ik/ton csaont Includes luel Missions, ss totsl chrMiua, CS*
Includes fuel Mission*, es tettl chrosilun). ffobrlc
•liter
1OS002 1.21 • IM-t Ik/tan
1O50041I 0.01 Ik/tM ceoent
produced
30500404 0.02e Ib/ton cea«it
1050O404 t.O x lot'
produced
10500714 I x IOf-0 Ik/tM Cdaent Fabric Illtor, Includes luel, es totsl ChrMlua
bed. Includes luel . ee totel chrooiuoi
IOS00714 0 x 10C-4 Ib/ton ceaent
produced
10500714 4 x 10C-4 Ib/ton cooent Hot scrubber. Includes luel, es totsl ChrMlua
produced
10500717 0.0014 Ib/ton ceoent Uncontrolled. Includes luel Missions, es totel
producsd chroalue
10S00704 0.024 Ib/ton cooent Uncontrolled. Includes luel Missions, es totel
produced chroalua
J05O070* 2.2 lOC-f Ib/ton ceoent ft»,
produced
totsl chroalua
30SO0700 1.4 x IOC-S Ib/ton ceosnt Fabric filter. Includes luel ealsslons, as total
produced chroalua
10S ISO Ib/ton refractory Uncontrolled, ss total chroalua
produced
170
lei
HI
141
7440471 12*7 Hofractory production Fusion castlnn
cruih/size/dry
7440471 12*7 Delrsctory production Fusion
10S 14 Ib/ton relractory Controlled 177(1, ae total chroolua
produced
305 74 Ib/ton relractory Uncontrolled, ss total chroolua
produced
744047} 32*7 Refractory production Fusion
flnlthing
7440473 32*7 Refractory production fretting pi
firing kilns
II tb/ton I
produced
0.2 Ib/ton refractory
produced
Controlled (7711. as total chroelua
Uncontrolled, as total chroolua
-------
P»M M>. Ill
Q*m/M
rOlLUTMIT
ChTMlu*
ChrMlua
throat IM
~—
Chrattiu
ChTMilM
Chroilu*
a"~""
ClWOOilU
CtlTOflilM
Chroelua
Cnroxlu*
Chro«luM
Chro.lu*
Chro«lu«
Chro«lu«
Chro.lu.
CM
Numm
7440471
744047}
7440471
7440471
744O471
7440471
7440471
7440471
7440471
7440473
7440471
7440471
744047)
7440473
744047J
744047]
744047]
tie
COM
12*7
12*7
12*7
12*7
12*7
12*7
12*7
12*7
12*7
3297
12*7
1112
1112
3312
3312
3313
3313
INOUSTtlAL FftOCCSS
Refractory product to*
Refractory production
Refractory production*
chrose*aaeneslto brick
Refractory production*
chroee-eeenaelte brick
Refractory production*
chroee-eaonealte brick
Refractory production*
Chroee-eeenestte brick
Refractory production*
chroos-savneslte brick
Refractory production*
chroee-eeeneilte brick
Refractory production*
chroelc OHide brick
Chroolc OKlde brick
Kef rectory production*
chroolc OKlde brick
Steel production
Steel production
Steel production
Ferroalloy production
HUSSION SOURCC
Freest**, process* *r*
Press! ftp process* era)
crueh/sis*/dry
firyer
««•<«'•"•"•«.•
fVeee/fCiu brtck dryer
Preee/f In* brick klin
*-.../«„. .,.«-
Raw eat oriel stores* silo
nil line
Spray dryer
Ar eon -oxygen
decerburfiation vettel*
all oft
Clectrlc arc furnecei
carbon and alloy tteel
•1 xed product*
Clectrlc arc furnecei
•ttinlett and specialty
tlectrtc ere furnace.
•CC COM MISSION FACTOR
309 190 Ifc/tea) r*fr*ct*ry
produced
309 94 Ib/ton refractory
produced
309 0.003* Ib/ton raw
•eterlat procetted
309 0.04 Ib/ton row *at*riel
•recessed
309 0.00074. Ib/ton TIM
•atorlel processed
309 0.000** 1 b/ton raw
•a tor lei processed
309 0.002* Ib/ton row
•eterlal processed
309 O.OOS4 Ib/ton raw
•atertal processed
309 0.»4 Ib/ton raw oatertal
processed
309 0.*4 Ib/ton raw oat or lei
processed
309 0.*4 Ib/ton raw eaterlal
processed
30300* 1.04 Ib/ton steel
produced
30I009D* 0.04 Ib/ton tteel
produced
3030O904 0 48 Ib/ton tteel
produced
30300*04 3.2 Ib/ton eteel produced
30300701 0.02* Ib/ow-nr enersv
con*un«d by furn*ce
NOTtS
Uncontrolled, a* t*t*l clwoelu*, oay over it ate
uncontrolled oalsslont
Contralled *44»>. at total citro*l
-------
•«M "»• »«
0*/2I/*0
CM SIC
MM** COM INDUSTRIAL FHOCISS
CNIMION 90UKM
SCC COM HUSSION FACTM
NOTf*
H1I ForrKbrioliM production
bv oloctrlc arc turnM.
proc.I.
Sill rorrocbraaivo production
by «l«ctrU «•< iyrnu.
proc.i.
l«rrocbr«M-«illc«i
product
C*fltin«,
l«rrochro*c product
7440471 1111 F«rrochro«lu. production
by .loctrlc *rc (urn.c.
proc...
Cloiod lurn»c«.
4*rroclwo».-.ll Icon
product
1311 FerrochrMjuo production
by electric *re furnaco
1111 ForrwhrMtlM production
by oloctrlc *re lurnac*
1311 Ferrochroolu. production
by .loctrlc we furnAc.
»roc«.l
lltl r«TKhr..luc vroducklen
by .tKtrlc vc lurn*c.
IvrecnroM-llllcon
product
Cru>hln«/(Tlndlnt.
hi9h-c«rbofl fwr.chr0<
product
Dry. cru.li. .1*. w.
M1004I7 0.071 Ib/tM »r^uct Cowe.it. •< cMtrcll^ Md iMC«itr«tl^ MUTCM. ..
t.t«l chrMlua
10100.17 0.14 Itt/ton product Cowo.lt. o« contrail^ «id uncontrallcd tourc... •«
t.t.l chrMluo
10100702 4.4 M 10E-S lb/(lwfir Scrubber. •* total chrooliM. a HUM* cbroolun Is 0.4S
•1 controllod Ml
10100. 0.12 Ib/twi product Cowo»lt. o« control!.* «nd unc«\tr«ll»tf MUTCM, 4.
tat.l chr».lu.
301004 0.42 Ib/ton product Cowa.lt. o« controllod «nd uncontrollod MUTCO.. ..
tot.l chrooluti
10100.11 0.41 Ib/ton or* prac.iHd Cownlt* «« tontroll.d 4nd uncontroll.d. •> tat.l
chrooluo
fgrn.c.. chroo. or./llM 10300704 I.It Ib/Hyhr
..It
Uncontrolled, ai total chroolu*. avwiMO chroeUua l»
151 ol Ffl by Motfht
Chroalua
1313 F«rrochro«lu* production
by oloctric «rc *urn*e«
3313 Forrochroal u« production
by oloctrlc *rc *urn«t
3313 Forrochro«U« production
by «t«ctrlc »rc furn*c«
proc«*«
Furn.c.. 10100704 1.102 Ib/rWir
I.rrochroo.-.!1Icon
product
Furnac.. hlpn-ctrbon 10300704 ».5» Ib/IWhr
f.rrochroM .nd chort. Cr
product
Oo.n lurntc.. 30300.01 0.007 Ib/IMir
<«rrochrOM.-.l1 Icon
product
3313 Forrochro.tu. prodwc
by .l.ctrlc «rc (urn
prac.ll
30300*01 0.001 Ib/llMhr
4«rrochrc..-«lI Icon
product
3313 Farrochroatu* production
by electric *rc furn*c*
procofi
3313 Forr.chro.lu. production
by .Lctrlc «re iurnfcc*
proc.ct
Ot«n . nlth-orbon 30300* 0.004 Ib/Hxhr
IvrrochroM. product
Avor.*. ol 0.2-0.71 rwio.. .. tot.l Cr uncontroll.d.
«»u»» Cr I. 0.4-I.4X o« Ffl o«l»lon. by «t.
Uncontrollod. •• tot.l ctlroalu.. ..luo.. chrooluo I.
I4( a< Pfl by Mloht
IUM. 0.4X tat.l
controlk.d PH I. chrootu.
Fibrlc (liter, controll.d chro.lu.. <»uo.. 0.41 tot.l
control I.d Pit I. chro.lu.
»u.«> 141 Pit It enrollu. Ul
F.brlc (llt.r. » t
chro.lu. by M.lvht
• lu... MJ Ml If
-------
pace NO. us
Ot/21/tO
POLLUTANT
Chroeluo
ChroeliM
Chroolue
Chroelue
Chreelue
Chroelue
Chroelue
ChrOelUO
Chroelue
Chroelue
Chroelue
Chroeluo
Chroeluo
Chroeiuo
CM
NunMl
7440471
7440471
7440471
744O4TS
7440471
7440471
744O47I
7440471
7440471
7440471
7440471
7440473
7440471
7440471
7440473
SIC
COM
nil
III!
1111
nil
1111
111*
111*
113*
111*
I33t
14
34
14
34
iMowmiM. nraciM
•wrochrooluo production
by oleetrle we fureaco
Fwrochroeluo production
by electric we furnace
»ra«»
Fwrochroelue production
by electric we furnace
proceoo
•wrochroeluo production
fay oloctrlc we furnace
preceao
Fwrochroelue production
by electric we furnace
procoaa
Chroalte oro reflntne
Chroolto wo roflnino
Chroolto oro roflnlno
Chro«lto ero ro41nln«
Chroalto oro roflnlni
Chrooo »l*tlnt.
docoritlvo
Lt«M«M""
^.r"-
Chrooo olttlnt,
docorit 1 vo
ChroB* »latlno. htrd
BIIMIM $OUK*
0>on lumtco. ollk-CWbM
forrocbrooo •roduct
Rocol»t/«toro or* in
•tack »tl«
Troot *•! ton illoy »ltb
Cl to Udlo, hloh-cwboi>
twrocfcrooo oroduct
Trotktno colton olloy
•1th Cl In Utflo.
< orrochrooo-ftl 1 Icon
product
Uol«h/roco»od
101 0.0001 Ib/ton wo
oroco««od
lot 01 00 I ».7 > toe-l lb/hr/*o»
30>OIOOI 2.* » IOE-1 Ib/hr/M*
50*01001 0.00244 Ib/hr/lt2
30»OI001 S.7 x IOE-* utod, used fluorocarbon fuoo oupproaaant
of tank, uaod fluorocarbon fuoo tfuppreaaant
N«K chrooe. «ve. of 1 vatuo*. baaed 'on current
<«oporoa> uaad, used fluorocarbon fuoe auppreaaant
Hex chrooe, awe. of 3 valuaa, bated on aurfaco area of
Total chrooe, average of 1 value*, bated on aoperaa
uiad, uncontrolled
MraniM
lol
141
141
141
141
141
141
141
141
141
IIS
135
IIS
13!
135
135
*r«a. uncontrolled
-------
f*W Ha. lit
O*/ll/*0
POLLUTMIT
ChraaliM
— -
Chrosilusi
ChreeUiM
ChroaiuBj
Chro*iu*
ChrocluB
ChroBlua
Chrostiua
Ctiroftlusi
ar-"-
Chroalua
Chraalua
Chraalua
Chrtatua
Chrealua
Chroatua
CM
HUM*
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440471
7440473
7440471
7440473
7440173
tic
COM
14
1471
1471
1471
4»U
4»l 1
4t»
4»SI
4*S1
4»SI
4*51
4*53
4*53
4*53
4*53
4*53
4*53
INOMTIIIM. MOCCM nistiM (ounci
Chraa* alatlM. a«r«- Putin, taak
Chraaa alatlaa. Chraalc acid anoaillac
dacar.tlva t*nk
Otroaa al«tla«* hard *Utlnt tank
Caallal tauaro. utility *r.«h tutar caallm twar
Cool In. taoar.. utility frmiti u«tar cool In. tmar
IkuilclMl u»t< lncln«ritar >t«ck
caabuifclMi
RunUlMl »««t« HultUla havth (urn.c.
nunlcl.al «««t« nultl.la h««rth lurn«c«
coabuttlan
Huniclpil «««t« »otkln« b«r ar.ta
—'-""' ""
ftunlctpal Haste Hefu*e derived fuel
coeouatlon Incinerator
ffunlclsal waste Refuse derived fuel
combustion Incinerator
nunlclval waste Refute derived fuel
coebustion Incinerator
HunlciMl waste nodular st*rved-alr
cOMbustlon coabustor
Hunlclpal waste nodular starved-alr
coebustion coabustor
c»*ibuitlon coabufttor
SCC COOt HUSSION FACTO*
30901001 1.04 M I0i-f Ik/lMf/Mp
30*01001 0.002 * 0.004 Ib/hr
30*01001 0.00012 Ib/Hr/M ft
30*01001 1.44 M IOf-4 lb/hr/*ta
tank area
30400701 S.7 lb/10I12 8tU
30400701 0.13* Ib/lOCU Btu
5010OI 0,004 Ib/ton eunlc. solid
waste-dry wt.
50100101 0.0078 Ib/ton solid vaste
Incinerated
501O0101 0.00*2 Ib/ton solid waste
Incinerated
incinerated
501001 0.0004 Ib/ton solid waste
Incinerated
501001 0.022 Ib/ton RDF
coabusted
501001 0.013 Ib/ton ROT
501 00 I 0.00044 Ib/ton RDF
coebusted
501001 0.0002 Ib/ton feed
SO 1001 0.0014 lb/H0 feed
501001 0.003 Ib/ton feed
MOTW
Total dvoaM. *veraee) fKter for uncontrollod »letln«
tanks
Cstleated toy MM balance, uncontrolled, based on tank
capacity.
IstlMtod by MB* balance, uncontrolled, based on tank
surface area
Ranw 1.33 N 10E-S - 1*2 x 10C-4 and 8.82 x IOt-5 *
2.44 x IOC-4. as Cr 4«, uncontrollod
Drift loot ranee of 0.1-0.21. based on source tests, as
total cnrOBluo
Drift loss ranee of 0. 0002-0. 0051. based on source
tests, ft* total chrooiuet
Controlled by spray-baffle scrubber, based on aiatoriel
balance for oodel Incinerator
Refuso only, wot scrubber, total chro*lue
Refuse end sludoe, wet scrubber, total ehrooiuej
ft*, total chroelu*
several source averages, rane« Is 0.000* - 0.044 Ib/ton
1001 RDF fuel only, uncontrolled, overall averaee of
Ib/ton
several source averages. 100X RDF fuel only, range Is
3.4 K IOE-5 - 0.0013 Ib/ton
CSP only, overall average of several source aver«9«m,
ranpe Is 2.8 x 10E-S - 0.00038 Ib/ton
RfFIMj
IIS
2O»
20*
Ul
Ul
Ul
*l
Ul
Ul
141
141
180
1*0
180
1*0
180
1BO
-------
•••a No. I IT
Of/»l/eo
MUUTMir
CAS fIC
MUMM COM IMOUSTilM. MOttM
OIIISION
KC COM MIMION MCTM
Chromium
Chromium
Chrooluo
7440471 OS* Municipal naeU
CeabUatlOT
7440471 «M1 MmtUiMl uaeta
Coebuetloe
7440471 4W1 Municipal Mate
coebuetloil
7440471 4*91 Municipal Mate
coebuetlon.
7440471 4WJ Municipal Mate
coebuatloe
7440471 4*91 Municipal Mete
coebuetlon
7440473 4»5J Municipal Mete
coobuetlon
7440471 4»S3 Municipal uaeta
coaouatlan
744047] 4»S1 Municipal Mete
ceebuetlon
Netful ar *xcM*-4lr
coebuotor
Me** burn. ueter veil
Incinerator
«» kum
H«t«riull co^xiitw built
•M«r I»IO
LWM •«•• burn rotary
»>t»r»*ll cMbu>tor buitt
«t(«r 1»0
L*r«« •••• burn rot«ry
u«t«ru>ll CMfeuitor built
«(t«r 1MO
n«» burn w«twu«ll
co»bu«ior, »•»!! •!>• n«u
•odcl to any «•* ••dlua
n**« burn u«twu«ll
coabustar, ••all alsn nau
•adal ta any aaa aadlua
Itaia burn uataruall
CDabuakor. avail aix* naif
•edal to any aoa oadtu*
Haaa burn uataruall
coabuator, taall also nau
•odal to any aaa aadiua
tolOOl i * lot-t Ib/ton la«d
(OtOOt «.007 Ik/ton <*•«
fOtOOl 0.00011 Ib/tM fax*
501001 0.022 Ib/tM faad
(01001 O.OOOJO Ib/ton «aad
501001 0.001 Ik/ton »aaa
501001 O.O0013 Ib/ton (aad
101001 0.0040 Ib/ton 4OO tona/tfay. ft* control only, avarall
avarato ml aavaral aourca avaraoaa. ranw It 1.4 «
10C-( - O.OOOI Ib/ton
Caaaclty > 4OO tana/day, uncontrolled, ono data aolnt
only
Capacity > 400 tona/day. away dry In* aftor acid taa
and Pit control, ouarall av». o« aovoral aourco a»ta..
ranoa ta 0.00044 - O.OOOtt Ib/ton
Capacity < 400 tona/day. uncontrollod, ona data point
only.
Capacity < aOO tona/day. £!» control only, avarall
avaraoa of aovoral aourca awaraoaa. ranoa la i.4 x
IOC-S - 0.00020 Ib/ton
Cap. S3 Municipal uaata
coetoatlon
501001 I.* x 10C-5 Ib/ton total Chroalua
Incinerated
-------
PeM No. Ill
0*/2l/*«
POUUTAHT
CJlTMllW
Ckr-l-
CArMlua)
CAT Ml HO
CnrMlua (Cr «•»
CHTMlvo (Cr *•»
Chroalua ICr *»»
Chroalua (Cr «•>
Chroalua ICr 4»
ChrMlu (Cr «'l
CJ.ro.lua ICr «D
Chroalua (Cr «•>
Chro.lua (Cr «o
ChrMlua (Cr «•>
Chroalua (Cr 4<)
Chroalua (Cr 4»>
Chroalua ICr 4<>
CM tie
MUM* COM INMTMM. MOCtM HIIMIOH MUKC
744047] 4»«J tone** aludaa Fluldl>ad-bad furoaca
7440471 4M1 Savaaa dud.* nultlpla hearth fureec*
7440471 4»J1 Senate alvdM nultlpla haarth
Inclaaratlaa Inclnarator
7440471 00* Moapttal Mat* laclnaratar
lAClnaratlM
1M402** 14 CkrMa Platlna. hard Platln* tank
1IS402** 14 Chraaa platlni. hard Platln* tank
105402** 1471 Chroaa platlM. Platln* tank
IIS402** 1471 Chraee platlni. Platlnt tank
115402** 1471 Chroaa platlni. hard Chroalc acid anodlilnt
tank
1IS402** 1471 ChrOM eletln*. hard Platln* tank
1 15402 1* 1471 Chroaa platln*, nard Platlnt tank
115402** 1471 Chraaa platln*, hard PI. Una tank
115402** 1471 Chraaa Platlnt. hard PUtlnt tank
115402** 1471 Chraaa Platln*. hard PUtlnt tank
115402*9 1471 Chroaa platln*. hard PUtln* tank
IIS402** 1471 Chroaa platlni. hard PUtln* tank
«CC COM
MIOOM4
MIOMM
M100SO*
M200SOf
10*01001
10*01001
10*01001
10*01001
10*01001
10*01001
10*01001
30*01001
30*01001
30*01001
30*01001
30*01001
30*01001
DUMION r«CTM
*.2 « IOC-4) Ik/tM dry
O.OOOOI Ik/tM dry tludw
O.OIS4 Ik/tM Mild naata
Inclnaratad
7.22 x IOC-4 Ik/tM
2.M x 101-4 Ib/hr/aaa
2.4* x IOC-4 Ik/kr/ft2
1.0 x 10C-I lk/aap hr
].« x 10E-* lk/aap hr
0.001*1 Ik/hr/ft2 tank
araa
I. 00 x IOC-7 Ib/aap hr
1.01 x ioc-7 Ik/aup hr
1.21 x IOC-4 Ik/aaa hr
1.7* x IOC-7 lk/aap hr
I.*4 x IOC-7 Ib/aap hr
Ib/aaP hr
1.30 x IOE-7 Ib/aaa hr
Ib/aap hr
MOTH
Avaraa* •< tbrM taata. acrubbar. total chravlui
AvaraM •» II taatt. acrubbar. total chroalua
Control lad. aa total chTMluo
Uncontrallad. taat data, total ckroailuo
Avoraw of 1 valuoa. fcaaod «n aavoroa uaad.
uncantrallad
AvaraM a« I valuaa. kaaad an tank aurfaca aria.
uncontrollad
AuaraM of) tlx taata. con troll ad by foaa klankat fuaa
auppraaaant »lth uattlnt a*ant. ran*a la 7 x IOC-* -
I.I x lOC-t Ib/aap hr
AwaraM of alx taata. uncantrollad. ran*a 1* 2.* x
10E-4 ta 4.4 x lOC-a lk/aap hr
Uncontrollad
AvaraM of alx taata. controlled ky doublo packad-bod
acrubbar follouad by chavron bladaa.
Avaraaa of alavan taati. control lad kv llntld
packad-bad acrubbar
icrubbar
Avarata of thraa taata. controlled by oaah pad alat
alialnator «/2aeta a< chavron bladaa followed by 2 pada
Avaraia of three teata. controlled by oaah pad olat
all.lnator - one aaah pad
allalnator - two pada
Averaae of three teata. controlled by Chevron-blade
•CFCRO
101
101
1*1
1*7
ISS
in
20*
20*
Ul
20*
tt*
209
20*
20*
209
20*
209
-------
paw NO. n»
M/tl/M
POLLUTANT
CM
•1C
COM INOWTRIM. PlkXtW
UIIMIOK KUtcf
*cc CON DIIMION r*cn»
NOW
Cnraalu*
Chra*tUB *ctorv
facility
lUa* bur*, tutor Mil (01001 U.W2 Ib/ton controll.d Control lad by IIP. baaad on aourca taata
111
CtiroaluB (Cr «•>
1*1402** 4*51 Municipal Mat*
uttlon
M- IlKlAWttV
WIOOI 1.414 Ik/tan cantrallad Control lad by IIP, baaad an aourca taata
aartlculata aal*
ChroalUB («•!.! ka/hr. controlled
Chryaana
Icrap tlra, opan burnlnf Tlr.a In axparlaantal
burn hut
O.IOS la/tan tlra
SUB af PAH analy on IK axtrat. af IAO-2 taat I flltar
coapont. ahrad condition • 2" by 2* placa. burn
r.t*»l.l ka/hr. controlled
rap tlra, opaft I
0.174 Ib/ton tlra
SUB af PAH «n«ly on IK axtrat. of IAD'2 taat t flltar
coapont. fthrad condition • 2* by 2* placa. burn
r«te«1.7 k«/hr. controllad
Scrap tlra, opan burnlna Tlr.k In aKparlaantat
burn hut
0.10* Ib/ton tlra
SUB of PAH analy on IK axtrat. of IAO-2 taat t Illtar
co*pont. shrad condition • 2" by 2" placa. burn
r>ta>2.1 k«/hr, controll.d
21S01* 25 Wood coabuitlo
induttrlal
••l.ncad draft Mlcket
•tok.r-ftrad Induitrltl
boll.r
10200*04 I X 10E-* Ib/ton
Craan wood, ona plant, ptrtlculata control u/Bachanlc«l
collactor (cyclona), Mood fold rita 0.94 kf/a, boll.
.«. 41.11
Coal tar craoiota
4*001 5.18 lb/tink or
Ealvftlon B«*iuraaant
-------
•*M Ho. 120
00/21/oa.
POLLUTANT
Cafcelt
Cobalt
Cobalt
Cobalt
Cobalt
Cobalt
Cobalt
Cobalt
Cake oven aal**lo
CM (1C
Muran COM iwumiM. MPXSM DIIMIW (OUMCC
74404*4 Heed caebuttlen. Uoodtteve idUuMt kellle
retldantltl
T44O4M 12* Uovee labrlc lint thine twin* ewe* - reel*
II el in
74404*4 224 Uoven labrlc llnlthln* Heat tettln*
74404*4 224 Uovon labrlc II el thin* Tenter Irene* - rail*
llnlthln*
74404*4 224 Uovee fabric llnlohln* Tharooool dyalaa
74404*4 21 Hood coabuttlon. ttltncod drelt "Icket
Induttrlol ttokor-llred Induotrlol
boiler
74404*4 21 Mood coekuttlon. •« lanced dralt nickel
Induttrlel etoker-llred Induotrlol
boiler
74404*4 4#S3 Itunlclptl Motto Incinerator etock
coebuttlon
no III2 Coko production. Coke event - charting
«cc COM minion MCTM
1.2 a IOC-4 Ik/ten wad
kuread
110001 J.» li »0f>» Ife/kon labrlc
110001 1.4 X lOt-f Ik/tan labrlc
110001 1.72 » IOt-4 Ik/tan
lebrlc
11OOOI 1.02 M IM-f Ik/ton
lebrlc
10200*04 0.0002 Ik/tan luel or
0.007 no/I
10200*04 1.74 X lOC-f Ib/ton luel
or 0.0007 no/J
SOIOO1 0.0001 Ib/ton eunlc.
tolld Mttte-dry ut
10100302 O.I to 1.10 Ik/ton coal
Uncontrolled, kotod on one ttudy. nonbollled otova
burnln* area* Pino
Uncontrolled, tvoraoe ol three tettt
Uncontrolled, bated en toot dote
Uncontrolled, ever too ol lour toot*
Uncontrolled, evartoe al three toot*
Dry wed. on* plant, part Icul ate control n/eechanlcal
colloctor (cyclone), wod lead rote 0.2* H/t. ball.
ell. SS.31
Croon wad. one plant, partlcultte control w/oachtnlctl
collector Icyclonel. wod loed rate 0.14 k*/t. boll.
all. 41. »
Controlled by oprer-bellle tcrubbor. bated on notarial
balance lor aodel Incinerator
For 1-S eiin*. uncantrallod cher*ln*
•tram
M
12
«2
52
52
>77
177
M
2*
by-BroduCk rocowory
Coko even Mlul
Coke oven Ml
Coke oven ealetlont
Cooper
1112 Cot. production.
by-oroduct rocovory
•rocotft
1112 Cok« (reduction.
by-oroduct rocovory
•recotf
1112 Coko oroductlon,
by-product rocovorv
procmtm
Cokl coobuttton
Coal coebuttlon
Coko ovono * dooro
Coko ovono - lido
Anthr.>cit* eo*.-Mr»eJ
cyclon* tt>tl*r«.
utll/cMMrc/lndutikr
Anthrtc.tt. CO»\-*ir«d
cvcton* bolt*r*.
utI1/coM**rc/.nduttr
U10010I 0.24 to O.J Ib/ton cool For 10 ta 7S1 loeklna door*
10100114 0.004-0.04 Ib/ton coil For 20 to 40S laokln* lid*
Coko event - o
-------
Paid Ho. Ill
0*/2I/M
pttxuTMrr
COM or
Carter
Caopar
Caooor
Copper
Caooor
Cower
Cooper
Capper
Coooar
Caooor
Cooper
Capper
CM (1C
MuntW COW INDUSTRIAL PMdM
7440SOI Coal coobuitlon
744050. Coal *«*«.«..
744050* teal coobuatlon
744050* Coal coobuatlon
7440501 Coal coabuotlan
7440501 Coil coobuotlan
7440501 Coil caabuotlon
7440501 Coll caabuotlan
744050* Coil co.bu.tlon
7440501 Coil caebultlan
7440501 Coil coobultlon
7440501 Coil coabultlon
7440SOI Coil coebuitlon
UIIMION (OtKI
Anthracite, coal-llrcdl
overload itokor boiler a.
utl 1 /coeaerc/leduetr
ouorleed atoker bollera.
Anthracite ceal-«ir*d
overdid itokor boll era.
Anthnclt* coal-llrod
ruluarlxad dry bo t toe
botlera. utll/coooerc/lnd
Anthracite coal-llrod
oulverliod dry bettoo
Anthracite caal-llrad
oulvorlsod dry bottoo
bollero. utll/coooerc/lnd
nnthnclte caal-ilrod
aulverlied dry bottoo
bollora. utlt/cooeerc/lnd
oulverlied net bottoe
bollera. utll/coooerc/lnd
Anthriclte coil-llred
>ulverlied net bottoo
boll in, utll/coooerc/lnd
Anthrielte coil~f!rod
•ulwirlxid wet bottoo
bollera. utll/coHarc/l/id
Anthriclte ceil "fired
•inidir ttoker bollaroi
utll/comrc/lndu>tr
Anthriclte coil-
-------
Page io». 122
01/21/M
POLLUTANT
CM SIC
Nuntn COM INOMTIIM. raocnt
KC COM BtltSIM MCTM
NOTt*
Comer
744010* Cut CeotMeUe*
7440SOI CM| toebuatlen
7440541 Cut coebuetlo*.
7440SOI Coal COebUOtle*
MtlMlMIM CMl-«lr««
CVCIWM toll«r.
utl I /n«Mrc/lii*i*tr
cvclxi* boll«r.
utl I /cMMrc/ln*»tr
i C4*l-«lr*d t
<4 «toK«r Mllv.
14
•7-S03 U/lOClt fttu Controlled -UN wltlclono. calculated b*»«d on
2X Ik/IOCIl lt«
Controlled «lth ttP. b4Hd Ml »ourc« tut*
M7-I340 lb/IOCI2 Itu Uncontrolled, beeed M «lcul«ted «nd eeeeured ealeele
lietori
Cooaer
Cooper
Cooper
Cooper
Cooper
7440501 Coal coebuetlon
7440S01 Coal coebuatlon
7440501 Coal coebuetlon
744050* Coal coobuotlon
7440501 Coal coebuetlon
7440501 Cobu«tloA
7440501 Co4l c»bu«tlon
744050a Co«l co«buitlon
7440508 Coll eo.bu.tion
lltualnou* coal-«Ir«d I
overfeed fltekw b«U**-,
utl 1 /coM«rc/tndu»tr
•ttue.nou* co*l*llr«d I
ev«rf««d fttohw bollor.
utll/coewwc/inductr
•ituainous co«l-l|r«d 1
vulwwiieid dry botto*
boiler*, utll/COeiMrc/lnd
Vltuainou* ceal-flr*d 1
tfulwwtxttd dry totto*
boll.w«. utll/coaMTC/lnd
•Itueilnou* co*l-*lr*d t
pulv«rti*id dry t>otto«
bolleir*. utll/coMBarc/ind
•Uualnouc cot.l-llr*d t
ejulv.rli.d dry botttM
t.otl«r», utll/coMarc/tnd
llltuoelnou.! co*l-4tr*id 1
pulv«rli«d M*t bottom
t*oli«r». ull./ct>4.B*rc/.nd
lltualnou* eo*l-*lr«d I
pulverized w«t botto«
boilers, uil1/co«««rc/tnd
lltuelnou* co«l-*li-ed t
pulverized wet bottoa
boIlere. utl1/coaaerc/lnd
340-503 lb/10E12 Itu
1D/10C12 Itu
Controlled ulth eultlclone. celcullted beeed en
en«lneerln« Judfleeent
Controlled ulth It*, colculeted boeed en enflneerlnf
Judeeeent
Uncontrolled, boeed en eource teete
Controlled Kith eultlclene. celculoted beeed i
engineering Judfeeent
Controlled «Itn ESP. booed on eourco teote
«*0-WM Ib/I0tl2 Itu
141-204 lb/10CI2 Itu
141 lb/IOCI2 Itu
SOI Ib/lOCIl Itu
1*4 IO/IOCI2 Itu
24 U/IOEI2 Itu
573-141 lb/IOEI2 Itu Uncontrolled. colcuUted b«>od on onelneerlnt judooeent
Controlled with eultlclone, calculated baaed on
engineering Judgaaent
Controlled ulth ESP. baaed on aource teata
-------
p**o NO.
0*/2I/*0
POLLUTANT
CM *IC
NUrUEK COM IMUoTMM. MOCm EHUIION SOUDCf
KC COM OIIMIOM r*CTM
HOTIf
Coopor
COOMT
Co»oor
Coopor
»4405Ot, CM! coobuotlon
744050* CMl coobu.tto*
744050*1 Cool
7440504] Coil co*bu>tlo*
7440501 Co.l coobu.tlon
7440501 Co.l coobuitlon
7440501 Cod
lltuelnou. CMl-llPo* I
wo.dor itokor tailor*.
uktl/coooarc/llXuotf
atokw b«il«r«.
•Itu.lnou. coil-tok«r bsll«r.
utl I /c
Llgnlto co.l-llrod
oworfood .tokor bailor,
ut11/coaoorc/1ndu.tr
Llonlto co.l-ftrod
•ulvorlzod dry faottoo
boll.r,
utlI/co..«rc/lndu.tr
Llanlto co.l-ftrod
oulw.rlzod dry bottoo
bol1«r,
utl1/co...rc/lndu.tr
Llvnlto co.l-flrod
oulv.rlxod dry bottoo
boll.r.
1040-1420 Ib/IOtlJ l«u Controllod «
-------
Feee Me. 114
Of/ll/*0
•OLUItANT
Copper
Copper
Copper
Ceeper
Copper
Copper
Copper
Copper
Capper
Copper
Copper
Copper
Copper
CM «IC
Nunm COM MoumiM. moccn mission sauwx
7440M* Ceal coebuetlea Llpnlte coal-fired
pulverized dry kettee
•tlln.^./l^rtr
744O50I Ceal ceebu.tlee Lignite coal-fire*!
uttl/couoerc/lnduetr
7440500 Ceel (eebwetleej Llmlte coal -fired
bollere.
utll/coeeerc/lnduetr
74405OI Ceal coebuptlM Llgnlt* coal-fired
utll/coeeerc/lnduetr
7440501 Ceel coebuitlee Limit* ceal-«lr*d
epreador etokor bollere.
utl 1 /coeaerc/lnduetr
7440SOI Ceal coebuttlon Llwtte c»»l-«lr*4
apreader atoker bollera.
ut 1 1 /coeoerc/lnduetr
7440501 Ceal ceebuetlon Llinlte coal -fired
apreader etoker bollere.
7440501 Coal coebuetlon. Anthracite ceal-flred
7440501 Coal ceebuatlen. lltualnoua coal-fired
reeldantlal bollera
74405O* Cool coebuatlen. loller* fired by coal
residential froa Interior region
7440501 Coal coebuatlon. lollare fired by coal
reeldential fro* northern plalne
rafllon
7440501 Coal coebuatlon. lollcra fired by coal
realdantlal froa rocky oountaln
region
fCC COM tlllSMON F»CIO«
41 Ib/IOSIl M»
Contrelied ultn scrubber, celculated
enilneerlne Judieeent
111-240 Ib/IOCIZ Itu
12* lb/IOC12 Itu
ll« I6/10CI2 Itu
117 Ib/lOCIl Itu
140 lb/10E12 Itu
10* lb/IOC12 Itu
151 lb/10E12 Itu
Controlled «lth Mr. calculated baud an an«lne«rln«
1010-14*0 Ib/I0fl2 Itu Uncontrolled, calculated beeed on an.lnaerln.
S»7-M4 IbrlOCIl ttu Controlled Kith eultlclone, celculated baaed en
III Ib/IOf 12 Itu
717-17JO Ib/IOCIl Itu Uncontrolled, calculated baaed en engineer In* Judgeeent
Contreltee »lth aultkclone, calculated baaed on
engineering. Judgeeent
Controlled ulth fSf>, calculated beeed on englneerln
Judgeeent
Uncontrolled, highly variable, calculated baeed en
engineering Judgeeent
Uncontrolled, hi only variable, calculated baeed en
engineering Judgeeent
Uncontrolled, calculated baled on enolneertne Judeeaent
I on engineering Judgeeent
Uncontrolled, calculated baled on aneineerin* Judeeeent
I on engineering Judgeeent 14
-------
P«M NO. lit
0»/2I/*0
CM SIC
Nunwi cocc iHoutniiM. raoctM
inlMION MUMS
ICC COM BIIMION FACTO*
Coopor
C»ppor
Coppor
Copper
Copper
Copper
Cappor
Cappor
Cool coobuotlon.
rooldentlol
Cool coebuotlen.
rooldontlel
Oil coobuetloe
T44OSOI Oil coobuetlon
7440SOI Oil coobuetlon
7440901 Oil coobuotlon
7440SOI Oil coobuotlon
7440500 Oil coobuetton
7440S08 Oil coebultlon
7440501 Oil caobuPtlo
Uood coobuatlon.
7440508 1011 Iran arc »rotot»tn«
Llenlte ca«l-
-------
»a«a Me. 124
Ot/2l/*0
CM *It
NUINI COW IMUtniM. mOCIM
tMltMON
KC COM IMIMIM f«CTM
NOTIS
Cappar
Cappar
1021 Copper era
ellll«e/praceillp,e
lutlrti WK««
7440500 224 Uavaa fabric «l«UMi>e Cwlnt aven - reela
Ml
0.004 Ik/tM *r*
proc«>*d
110001 0.001 Ik/ton I0>rlc
CMtr*ll*d. WMTM* •« MtlMtM fW »bOut M plWItl
UnCMtr«ll*d. avtraw ol thr«« tnti
7440500 224 UavM Isbrlc flnlshlnc Halt eattlnt
7440500 224 Uav« fabric llnlshlna Tenter treeos - I
J10001 1.22 > lOt-i Ib/tM
«»brU
ttacontrpllod. Mud M t««t d«t«
110001 1.2 x IOf-4 Ik/tM tsbrlc Uncontrolled, avereaa el «aor testa
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
7440504 224 Uovwi fabric fUUMne TherMCol dvelft*
7440500 29 Uood coetueUon. Horlxontal return tube
Industrial
7440501 25 Uood co-toustlon. ialanced dra.t Mick.)*
tAduttrlel «tok«r*4ir*4 i«du*ArUl
boll**-
744050* 25 Uood co-iHiitiPd. laltnced *-«U wicket
Induttfl*) »tok«r-«lred Industrial
bolUr
7440504 241t Copper auUate production Entire proce*«
7440501 2fl»5 Carbon black Manufacture n.l A proceu puree vent
- oil furnace
7440504 3312 Iron and steel production lafU OKyeen furnace
operation*. 4-aKM* process
*Mltin«/r«
-------
Pae* Wo. 127
09/21 m
POUUTAMT
COM***
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Coo per
CAS
HUrtKIt
7440*0.1
7440508
7440900
7440508
7440508
7440501
7440508
7440501
7440508
7440508
7440508
7440508
7440508
SIC
COM
HI*
3312
9312
3112
3312
3312
3312
3313
3311
3313
3313
1111
3331
INDUSTRIAL PROCESS
Iron Mid vteel production
Iron *nd steel •reduction
Iron *vtd steel •reduction
Iron end steel production
Iron Mid steel production
Iron Mid steel production
Iron Mid steel production
Ferroalloy production
Ferroalloy production
Ferreclloy production
Ferro«lloy production
Pri..rv c«..r „,«„
MlfflON SOURCE
Electric ere fvmeca)
operation*.
charilne/taeelne/tleoolne
Open h.arth furnace
operation*.
eeltlneVrof Inlnt
Open heartA furnace
operation*.
eeltln./reflnlnt
Sinter planta/alnter
dl*char«e
(Inter plant./. Inter
dl.charee
Slnterln* operation*.
vlndbox aMhautt
Slnterln* operation*,
wlndboK eMhauat
Fenn (101)
Fed (501)
Foil (751)
Electric arc furnace.
open, f erroean.aneae
Cl*ctrlc furnace
SCC COM
waootoe
MIOOtOI
WIOOPOI
J0300il4
30300«14
303008 II
30300113
10100*15
10100*01
30300402
30300701
30300510
30300512
MISSION FACTO*
•.004 Ib/ten eteel
•.04 Ib/ten ateel
0.0004 Ik/ton Mr contoAt 0.2*11. cerbgM *t.Ml
Uncontrolled, copper content Q.14X
Controlled - CSP. copper content 0.1*
Uncontrolled. co»eer content 0.104..
•*Bhou*e. co**er content 0.104X
Uncontrolled. eHor coerM Pfl re»ov«l . copper content
0.104*.
Wet ESP, eo«>per content O.I04X
Uncontrolled, open «urn*c«
Uncontrolled, ooen/cloced furnecc. b*thouse *chlev«*
Uncontrolled, open/closed
-------
Pew Ho. 12*
0*/2I/*0
POLLUTANT
Copper
CO...T
Coppor
Cooper
Copper
Cooper
Copper
Copper
Copper
Cooper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
Copper
CM
HUNK*.
744050*
744050*
744050*
7440SO*
7440501
7440SO*
744050*
744050*
744050*
744050*
744050*
744050*
744050*
7440508
7440500
744050*
7440501
744050*
SIC
cage
mi
1111
111*
in*
111*
in*
111*
in*
in*
1141
1141
1141
1141
1141
1141
4*51
4*51
4>51
INDUSTRIAL PMCfSS
Prlaerw coooer eualUnf
Prlnerv capper geeltln*
Pr.eery ...d ».•«...
Prleery laed eeoltlng
Prleery leed eoeltlng
Prleary tine
production
Prleary sine **lek>
production
Prleary line (slabl
production
Prloary zinc (slab)
production
Secondary copper seel ting
Secondary copper eeeltlng
Secondary copper saeltlng
Secondary copper seeltlng
Secondary copper seeltlng
Secondary copper seeltlng
Municipal waste
coebustlon
Sewage sludge
Incineration
Sewage sludge
Incineration
EMISSION SOURCE
Dultlple hearth reeeter
Revorkoratory furneca
•last furnace
Refining) furnace
Sintering
Roaster - electrolytic
plant
Roaster -
pyroeetellurglcal plant
Sintering -
eyroeetallurglcal plant
Vertical retorte -
pyroeotallurglcal plant
Cupole - Insulated copper
wire
Cupola - Insulated copper
wire
Cupola - ecrap
copper /brass
Cupola - scrap
copper/brass
Movorboratory furnace *
brass/bronze
Reverberatory furnace ••
brass/bronze
Incinerator stack
Fluldtzad-bad furnace
Multiple hearth furnace
SCC COM
IQUHMHH*
MUOS07
10301001
101010
1O10IOOI
101010
101010
1030 JO
10303005
10400211
10400211
10400212
10400212
30400215
501001
50100504
50100504
EMISSION neCTO*
0.44 Ik/ton COM. ore
procaeeaa'
O.S Ik/ton cone, or*
processed*
O.OOU Ik/ton Pk produced
I.M » IOS-1 Ik/ton Pk
produced
0.002 Ik/ton Pk produced
*.0 Ik/ten In produced
*.0 Ik/ton In produced
O.OO4 Ik/ton In produced
0.002 Ik/ton In produced
1.2 Ik/ton eaterlal
Cher god
O.OS Ik/ton eaterlal
charged
0.1* Ik/ton eaterlal
charged
0.012 Ib/ton eaterlal
charged
charged
0.24 Ib/ton oaterlal
charged
0.011 Ib/ton eunlc. solid
waste-dry wt.
4.2 x 10E-4 Ib/ton dry
sludge
0.0211 Ib/ton dry sludge
NOTES
Control lad. keead an eeeuaad Cu content i Ptl foe., ESP
echtevee **S central, essuae Cu content IS Ht
Controlled, kaeed on assueed Cu centont e Pit lee.. ESP
achieves *»» control, assuee Cu content IS wt
Control lad. copper content 0.2»I
Cantrollad, cooper content 0.04S
Controlled, copper content 21
Controlled, cappar content I.7S
Controlled, copper content I.7S
Controlled, copper content 0.041
Controlled, copper content 0.0141
uncontrolled, capper content O.SS
ISP. copper content O.SS
Uncontrolled, estleated copper O.SS
Estleated copper O.SS. ESP
Controlled by eprey-baffle scrubber, based on eeterlal
balance for eodot Incinerator
One test, scrubber
Average of five tests, ecrubber
seVfMW
SJ.»7
n.tT
SI
SI
(I
(I
51
SI
SI
Sl.»7
SI,»7
SI.»7
51. »7
53 97
"
101
101
-------
Pate He. 12*
0*/2I/*0
CM (1C
Nunm COM iNoutTRiM. rwKMf
iniiiioN uunci
tec cow mission ntcTOD
MOTH
Copper oxide
Copper oKide
11171*0 3112 Iteel production
11171*0 >112 «t««l production
Mia v««i - M
r«lln« cycle
Eloctrlc *rc lurn4C«
10300* 0.0*4 Ike/ton Meclalty Uncontrolled emissions
•leel
10100901 0.0014 • 0.002 IDS/ton Uncontrolled emissions
carbon ateel
Iff
If*
Copper OKide
Copper oxide
Copper OKloe
13171*0 1112 Steel production
11173*0 112 Iron foundrUi
1117180 112 Iron foundrlee
»S4*7 4»S3 U««t«mt«r tr«t
Cloctrlc 4rc 4urn*c«
••ltln«/r«llnlnt
fl«ctrlc «rc lurn*c«
ch«r«« wid t*» cvcl*
Eloctrlc »rc (urn«c«
Mltln«/r«ilnln8
3010090* O.OIf - 0.04 Ike/ton Uncontrolled eel sal
carbon stool
M400304 8.014-fl.OW Ibf/ton of Uncontrolled eelsalons
Iron produced
30400104 0.14-0.14 Iba/ten of Iron Uncontrolled eeleslono
SOI00701 12 Ib/ton o-croiol In
Inlluont
•»od on win. nodollnt for hy»oth. MTU, roprounto
•voronn POIU th«t tro«ti UduttrUl Motnutor
ft
I04H5 Oil
tw tr««tunt
Cretylaldehyde
Crotylaldehyde
417010) 2I4S *»t««/»hMnot
10119480 0.0024 Ib/hr
Controllod
-------
**«•• No. ISO
0*/21/*0
POLLUTANT
CllOOnO
CM-MHO
Cu-ono
CUMnO
CUMAO
1 .3-Cyc.a*>ont*dlono
l.3-Cyc.Oi«ont4diono
1 .3-Cyc.opont*dl«no
1, 3-CycloponUd.o-.no
Dlb«nsU,h>*nthr*ic«n*
Dibonioi'ur.in
Dlb«nzofur*fl
D.b*"30fur*n
CAS SIC
NUtlKft C00€ IMtXMTRIAL MOCCtt
*M2I 2-4 CUMM (trotfuctlon
•MM 2tM Cuoono production
•MM 2-4* AcotOAo/*honol
•«nul«ctur«i froo ctMono
tM2l 204* Acotono/ohonol
Oftvnufatcturo froo cuMnti
•M2I M4» Acotono/vhonol
oamjiUcturo froo cuoono
S42»27 tcrw tiro, ot*on burnln*
$42*27 Scr«» tiro. «t««n trurninti
$42*27 Scro tiro. o»«n burnln»
942*27 *cr»»» tiro, o+on burnlnf
93703 *cr*» tlr*. e**ft burnlnt
13244* 4*53 nunlcU»l w««to
COBbU«tlO«l
132*4* 4*53 rtunlci**! u«tt*i
co*>bu»tlon
132*4* 4*53 rtunlelp*. **it
C .or-HatlM VM,
*tor*to t«Ak voiitt
ci>-bln«d
Tlroc U oMtorloofit.l
burn hut
Tir«» In OrVorloont*!
burn hut
Tlr.,» Ifl cx#«r.»*nt.>.
burn hut
Tir«oj In ox»>orio«nt.\l
burn hut
burn hut
T.r*jf) in oK»»rlo«itt«l
burn hut
Extatln* »*•• burn h«*t
rncowcry facility
r •cover*' facility
CMlstlnti r*fu««-d*>rlw«d
fu«l Ucllitv
KC COM Bllff ION rnCTO*
MIISoOO 0.02*7 Ik/kr
Ml If 410 0.03*4 Ik/kr
3010*151 O.2I Ik/tM Mraool
eroducotf
3010*1(1 1.72 Ik/tM phenol
3010*111 O.Ota Ik/ton thenol
eroducod
0.0*1 Ik/tM tiro
0.1*0 Ik/tM tiro
0.134 Ik/tM tire
0.020 Ik/tM tiro
0.004 Ik/tM tiro
501001 l.»2 > IOC-4 Ib/kM of
uaek* coebuaked
501001 1.2 > IOC-7 Ik/kon of
waako coebuaked
501001 4 K 10C-4 Ib/ton of »»te
coebuaked
conbuaked
MOTES
UnCMkroIlod MlealM lector lor • beew llould
UMM trolled ulaalM lector lor o lleht llould
Con trailed Uondenaatlon) . baaed M enalneerlno
Judioeent
Conkr oiled fadaorptlM or condanaatlon) . baaed on
Induatry sourcaa
Controlled
1/4 to 1/4 ol e tire, uncontrolled
VOST oaeeleo kurn rote - 4.43 ko/hr. chunk condition* •
1/4 t* 1/4 ol a tiro, uncontrolled
Sua ol PAH analy M lie ontret. ol IAO-2 toot t filter
coopMt. ohred condition > 2* ky 2* piece, kurn
rato-1.7 kc/hr. controlled
Controlled ky CSP. kaaed on aourco teata. oola*lon* •
2.3,7.1-TCDO eeulvelont
Dry alk. acrubbar ft labrlc filter contr.. aeaueea >5I
Controlled by CSP, bated on lource te*t*. oolMlon* a
2.3.7.1-TCOD equivalent
2.3,7.1-TCDD equivalent
contr. off 1C., eela. • 2.3.7.1-TCOO ogulv.
M7IMN
214
214
If
If
1*
212
212
212
212
212
212
III
III
111
111
111
111
-------
Pat! N». Ill
0*/2I/*0
POLLUTANT
CM tIC
Munm coos iwutniM. rmcitt
inlUlON tOUKt
«CC COM BI1WIOM r«CTM
nan*
DIbanjoluran
Dlbeniofuren
Dloaniofuran
Dlbeniefuran
Olbenzofuran
IJ244t 4»H Municipal w»t«
CMbuttlM
IJ2a4» 4*SJ Municipal Mat*
coobuatlon
IJ2««» 4*51 Municipal vaata
conbuatlon
IJ2«4» 4*S1 Municipal Mate
coebuatlen
IhMkiltr iKl
IJ2a4» <»5J
coabuttlon
w liiclMr*Ur
burn boat recovery
facility
Projected or
atate-of-the-art eeeg
burn hoat recovery
ProJ.ctid or
•t«l<-ol-th<-»rt
fOIOOl I. JO ii 10i-7 Ib/tM of Controlled by IIP. baaod M Mure* taata. eelealMe o
I 2,J.7.«-7CDO equivalent
it*
501001 I M IOI-* Ib/tM of uaete Dry alk. ecrubber t fabric flltar centr.. aaaueeg tfl
canbuatad centr. afflc.. eala. • 2,3.7.1-TCOO eaulv.
SOIOOI 1.14 » IOC-7 Ib/tM ef Control lad by ISP, baaed en aourca teata. eelaalgna *
2.1.7.1-TCN) equivalent
SOIOOI I * IOC-> Ib/tM ef vaate Dry alk. acrubber S fabric filter contr.. aaaueea MI
CMbuatad centr. afllc.. eela. • 2.I.7.I-TCBO aaulv.
WIOOI 2.4 * I0€-* Ib/lM •«
Control I nd by ISP. b«««d on MUTC* t««ti. «l»lon<
2.3.7.1-TCDD •o.ulvtlant
Dlbanzofuran
Kunlcl»*l >u«
coabutklon
901001 !.• » IOE-7 Ib/tM e>
w««tfl Cft«bu>tnd
Cry u«« «I
contr. nfflc.. mmlt. • 2.S.7.I-TCDO nulv.
Dtbansafuran
tw tr«tnnt
facility
rotu
SOI00701 IMO Ib/ton dlbenzofuran laaad M eela. eedallnc fer nypoth. POrU. repreaenta
U Influent auaraM POTU that treata Inouatrlal «aatevater
I,2-01broeo*tAlna
I0»»3< 421 T.nt truck truiuort
Tank truck loaded Kith
product - aMtreee loaae
40iOOI 4.1 > 10C-7 lb/1000 ••! Calculated frM eaa.
tranaportad
l.2-0lbraaoath* «th,
dlbroaldc In Inllu.n
•«»*d on ••!«. m>d«llnff for hypotn. POTU. r«pr€<«nt«
ta«ator
1,2-Dlt»-oao«tt>*ne
I0a»4 5171 fiaaollna loadlnt o< tank Sel.ih loadlni
404002 1.37 H IOC-4 lb/10£3 gal Calculated free eaaollne vapor eatleataa
throughput
I0a*34 5171 Caiollna loadlna
404002 *.4l » 10£-S Vb/I0€3 i
throughput
1.2-Dlbroaoethma
10a*34 5171 Catollna loading o< tank Sub.ar«ad loading -
trucks at bulk plant* dadlcatad nornal lar
5.47 x lOC-S Ib/lOEI gal Calculated
-------
'•M Ha. 112
0»/2t/*0
POU.UTANT
I.I-Dlbroeoathan*
l,2-Dleroaesth*n*
1,2-Dlbroeaa-thana
1,2-Olbroaaethana
1 ,2-Olbroaoothane
1,2-Dlbroeaathana
l,2-0lbraao«thano
I ,2-Dlbroaoath*na
1,2-Dlbroaoathana
1,2-Dlbroeoathan*
1,2-Olbroaoathana
1,2-Olbroooathana
1 ,2-Dlbroaooth«na
1,2-Dlbroaoathana
1 ,2-Olbroaoathana
CM (1C
NUneC* coot iwutmiM. MocMf tniMioM MUM*
104*14 (171 Saaollw leading el tuk (ubaertoe1 leading; - vaaor
trucks at bulk plants balance service1
104*14 (171 Easollne loading of tank (*Uok leading -
trucks at bulk toralnala dedicated noraal ggrvlc*
104*14 (171 CoollM losdlng el t«nk (pU>« loading - »*por
truck* at bulk toralnal* balanco sorvlcg
IO4»14 (171 6««olli>« loading o< t«nk (uboorgod loading -
truck* at bulk l«r«ln«l« dadlcatod nora.l larvlca
1O4*14 (171 Cauiltm loading ol tank Subnrgod loading - vapor
trucks at bulk torolnals balanca sorvlcg
104*14 (171 Casallng sturag* at bulk Uorag* tanks - bro.thlr..
IO4»14 (171 Caaolln* storan at bulk Storago tank* - draining
104*14 (171 Casolln* starag* at bulk (toraga tanks - lining
104*14 (171 Caaolln* otoraga at bulk Fluad-roaf staragg tanka
104*14 (171 Caiollna storaga at bulk Floallng-raof atoraga
1O4*I4 (171 Carolina storago at bulk Flo
-------
Paaa Ho. 11]
Of/21/fO
rOLLUT*NT
1.2-Dlhreeeethene
1.2-Dlkroeeetnue
1.2-Dlkreeoethane
01 butyl phthaleta
Olkutyl •hth.Ute
1 ,2-DlcMorohemene
1.2-01 ehlorot.ni.fi.
1.2-DlcMorebenzene
1 ,2-01 chlorohenx.ne
1 .2-01 chlorokenzone
1 ,2-Dlchlorob«nzan.
1 . 4-Dlchlorobenz.n.
1,4-DlcMerobonz.n.
1.2-DlcMorob.nz.n.
CM *IC
MURK*- caw iNDutniM. MOCIU DIIHIOM touKf
IO*»J4 **4I taeallM eteraae a* ieleali fllllae •*
.ervlca undarwound taitka
I0*a]4 5541 CatoUm atereta at SukMraad fllllM •«
••rvica vtAtlons undtfrgrAund tMlka
1M*)4 SS4I CiMllM brlc i I«nt«- lr.«.« - r»ln
(tnl.h
»S50l 2114 fhvMcwitlol rrM«» «»li>lwii
•anuLctura
MS01 2<«S Olchloro.nllliw<1.4> Fuslttv. ..l.ilont
rrpductlon
»5501 2I«S OUhloro»nllln.(3.4) Proc.o ..l.llon.
production
•5101 2)49 DicMoro«nllln. Itor.w tank .».ilon>
oroductlon
»5501 2I«S DUhlorob.ni.n. Fugltlv. ul»lo»>
production
tSSOl 2I4S Olclilorob Proc... ••Jtflon*
production
production
WC COM DIIUIOM FACTM
4MOOWI l.4» II IOt-4 Ik/1000 «.l
throughput
40400M2 ».fl « lOC-t lb/1000 «•!
throughput
40*001 I.I x 10f-f Ik/1000 ••!
330001 f.2 * lOf-4 Ik/tw Ubrlc
110001 0.002* Ib/tofl f*krU
1010*0 0.2*0 Ik/ton
l.l-dlchlorokwixon*. u«.d
101 0.* Ib/ton
1.4-dlcMor.«nllln.
produc«d
101 I.I Ib/ton
I.4-dlchloro«nllln.
produced
4070*0 0.1 Ik/ton
1.4-dlchloro«nllln.
produced
101 101 I.S2 Ik/ton
l.I-dlchloroMnzon.
produced
101101 4.*4 Ik/ton
1.2-dlchloro«*nz«n«
produc.d
1.2-dlchlorolMnz.n*
produced
301301 2.04 Ik/ton product
produc.d
JO! 301 11.42 Ik/ton product
produc.d
produced
101121 0.1 Ik/ton dy* produc.d
HOTM
CalcuUU* lro» WMIIM v«»or MklMtm
C«lcuUt*d «ro» t*Mllra vwer wtlutM
Calculated froa taaolln* vapar aatlaataa
Uicontrallad. kaaetf on t«t data
Uncontroll.d. taat data
ru«» katancd (Indu.trK Kid.)
Eananl Mtlaataa, no >p«cHU. on control
Canaral actlMto. no aaecUlce on central
Ganerel aatleatee, ne Apeclllca an central
•*»4 an data *roe alta vl.lt. «« apacKlc* oa
control.. Ilkaly te ka Mih u.lua
t»»*d en d*ta free alta vlalt, ne apacKkca en
control., llt.lv te ka nidi v.lua
controla, Ilkaly te ka Men u.lue
C.tla.ta k»»*d en data free .It. ul.lta, apacKIca en
control net aualUkla. likely to ka Men ualua
E.tia.ta k«.ed en data free alta vlvtt*. .pacific, an
control not av.ll.kla. Ilkaly te ka high v.lua
control not ftv.lltkle. llk.lv to ka high value
G.n.r.l a.tleate. no .pacific, on contrela
12
12
-------
P.M No. 114
0*/21S*0
POLLUTANT
1 ,2-BUklorotMnsono
1 .l-tick|grokon*«no
1.2-0lchlorok*nzano
1.4-Dlchlarobanzana
CM tIC
Nunm COM
MMI 2Mf
•WOt 2k*(
•5501 4741
104447 4t51
iNDumiM. raocn
•yo mik**!*
Dvo ayfttko*!*
••II tank c*r clo
SWaM (lutfM
1 tnlMION MURCf
ProcoM oolMloo*
(toraM tank ootulon*
Miln* Kntlro procoM
Fluldlzad-bad turnaca
ICC COO* HIIMION FACTOR NOTIt
MII2I ».tO Ik/ton *Vo producod fonorol o*tlMto. no *poclan>ana
1 .2-Dlchlorak••
lnciil4VatioA
141711 4MI SWUM (ludM
J4I7JI 4t5J (MOM lludM
InclnvUtan
»S50I 4»5J IM IludM
IkilUMl kurtk lurMC*
•lutfw
WHOOSO* 0.01213* >k/t*n dry Ono »aat. Krukbor
•ludM
fluldllad-kod iwnac* 5010050* «no
IM447 4*51 U«it«««t«r tr«t«nt
§41731 4»53 H. In
Inlluant
•«§•< on oolo. xxMllhf v*r«M P4TU tk*t tro*t> Industrial luitOMtor
l»«d Ofl «•!•. oodolln* «or nymth. POTU. roprMont*
*vbrlc . dlract
chlorln«tlon
495] (au»9a iludM
Inclnaratlon
30112535 0.002 Ik/tan praducad Control uncartaln, baaad on taita and aaaa kalanco
-------
•ate Me. IIS
0*/2I/*0
POLLUTANT
D! entered! ben sofurene.
total
1.2-Dlckloroethane
1.2-Dlckloroethane
CM SIC
MUntU CODE INMSTMM. MtOCCif EMISSION SOUK* SCC COM IMIUION FACTO* NOTU
4»SJ Senate) elude* Multiple hearth furnace SOIOOSM 1.474 x IOE-7 Ik/ten dry Averaee of tub teete. ecrubbor
Incineration eludte
107042 Internal conbuetlon notor vehicle* 2 I.IM x 1OE-S Ik/ten Calculated kaaed en enelneerlnt Juda.eent
entlnee - •oblle leeded tee burned
107042 2121 rolyvlnyl chloride Suapenelon proceaa. 1010IMI I x IOE-S Ik/ten PVC Bated on a eodel •lent. 1*71 dete, I.I x IOC! Ik
production entire plant capacity, control etetue not certain
l.2-0lchloroetk*n«
1.1-DUtilaroethaM
1.2-Dlchloroethane
1.2-Dlchlaroethane
1.2-Dlchloroethanc
107041
M2I FdlvwHIdd rubber
production
fntlro orac<«
TSI4.I 214* Ethyl chloride production Separation unit
by kydrochlorlnatlon
107042 214* Ethyl chloride production Precoee vente
by hydrochlorlnatlon of
ethylene
107042 2«4» Ethylene aelne production Entire proceae
MIOZoOl 47.0 Ib/ton polyeulflde ControlIof. bated on enflneerlnt judeeeent
rubber produced
107042
2B4* Ethylene dlchlorlde Colunn ventt
production * balanced
J01UI 12! Ib/ton produced
101I2S1S II.* Ib/ton ethyl
cklorldo produced
1010)4 It. II Ib/ton tthyleno
aelne produced
301 12S 4 Ib/ton EK produced
Control uncertain, baaed on MM balance end teett
Control atatue unopecKled, aaoretate oatleate kaeod on
national oelaalone end production aatleatea
Facllltlea ueln« typical control! for 1*74. aoereoate
eit. baaed on national eel«. t produc. e«t.
Uncontrolled, baaed on hypothetical plant vttk total
EDC production capacity o( 1.12 x IOEI Ifc/yr
tl
ti
II
II
1.2-Dlchloreethane
1.2-Dlchloroethane
1,2-DlchJoroetnane
t,2-0lchloroethane
1.2-OUhloroethane
1 ,2-Dlchloroethane
107042 2>4«
107042 2>4*
107042 2(4*
107042 214*
107042 2(4*
Ethylene dlchlorlde
production * balanced
procoae
Ethylene dlchlorlde
production » balanced
procaa*
Cthyleite dlcnlorlde
production * balanced
proceca
Ethylene dlchlorlde
production * balanced
procaaa
Ethylene dlchlorlde
production - balanced
proceaf
107042 214* Ethyl. n« dUhlorld*
Coluon wonts
Dlract chlorlnitlon w«nt
Olr«ct cnlorln«tton wont
Blr.ct clilorlnMlon vont
Oxychlorlnatlon. air
proceaa.
abaorber/etrlpper
Oxychlorlnatlon. air
301125 <0.12 Ib/ton CDC produced Controlled by thereal exldlier, hypothetical plant «/
total EDC produc. cap. of 1.12 x IOEI Ib/yr
30112502 2.14 Ib/ton EDC produced Uncontrolled, beeed on hypothetical plant «lth total
EDC production capacity ol 1.12 X IOEI Ib/yr
I01I2S02 <0.
-------
rape Ho. 114
0»/2I/»0
POLLUTANT
1.2-Dlchloreethane
l.2-0lchloreeth*ne
l.2-0lchloroethano
1.2-Dlchloreethene
l.2-0lchloroethane
1.2-Dlchloroethane
1.2-Dlchloroethane
1 ,2-Olchloroethane
1.2-Dlchloroetheno
1 ,2-Dlchloroethene
1 ,2-Dlchloroeth*ne
1 ,2-Olchloroethane
CA* IIC
NUn«ai CODC INDUSTRIAL PMCIM
1070*2 2Mf I thy lone dlchlerlde
production - kalancod
erocea*
1070*2 2I«* tthyl one dlchlerlde
production - balanced
proceaa
1070*2 2Wt Ithylene dUklorlde
production - balanced
procee*
1070*2 2l*o Ithylene dlchlorlde
production - belanced
proceaa
1070*2 2I«* Ithvlene dlchlorlde
production - balanced
proceaa
1070*2 2o*t Ithylene dlchlorlde
production - balanced
procea*
1070*2 2I«* Ithvlene dlchlorlde
production - balanced
procet*
1070*2 21** Ithylene dlchlorlde
production - b*l*nced
procoea
I07O«2 21** Cthylene dlchlerlde
production - b*l«nced
•roceae
1070*2 2I*» Cthylene dtchlerlde
•reduction - balanced
•roceta
1070*2 2I*» Ethylene dlchlorlde
•reduction - balanced
•roc ese
1070*2 2»t» Cthylana dlchlorlda
•reduction - balanced
•roce-a
1070*2 2B69 Cthylene dlchlorlde
production - b*l«nc*d
•rocet *
UUoalON MUM .
OxychlorUatloa). air
orocaaa. relrleeratod
condanaer
Oxychlorlnatlon. air
proceaa, relrlooreted
condenaer
Oxychlorlnatton. exyoon
proceae
OKvchlorlnatloo. oxyoon
procaaa
Oxychlorlnatlon. oxyoen
eroci-e
Precate lueltlvo
eeUilox*
Proc**a fupltlvo
eelaalon*
blotraeteent
Stor«9* went*. In-proceaa
Storage went*. In-proceaa
Storage wente. In-procefa
Stora«a venta. produced
Stor*g- venta. produced
ICC COW fMlttUN FACTM
*OI|2MI «.• Ik/ton IK produced
10112901 <0.0t* Ik/too IDC
produced
10112901 0.*24 Ik/ton (DC produced
101 12901
-------
Pete No. 117
0*/21/M'
POLLUTANT
1.2-mckIorMtkeno
I.l-Olchioroetnane
I.I-OI chloroethane
l.l-BI chlaroethene
1 . 2-Dlchl oroetkene
l.Z-DtchlerMtneno
l.Z-Dlchloroeth>ne
I,2-01chloroetntlon
75341 204* Detkyl chlorafera He
-------
re** MO. m
Ot/21/TO
POLLUTANT
1 .2-Blchloroethan«
1.2-Dlchloroethano
1.2-Olchloroethane
1.2-Dlchloroethane
1,2-Dlchleroetheno
1,2-OlcMoroetlieno
1.2-Dlchloroetnene
l.2~Dlchleroethane
1,2-Dlchloroethana
1,2-Dlchloroethene
1,2-Dlchloroethano
l.2-DlchloroetliDlchlor0ethano
1,2-Dlchloroethane
1.2-Illchloreetnano
CM SIC
NUHICII COM INBMTKIM. MOCCM
1070*2 2M» PercMoreethylene
production
107042 2«*» Trlchloroethylene
production
I07M2 2Mt Trlchleroethylene
production by
oxyhydrochlarleetlon
process
1070*2 214* Vinyl chloride ooneeor
production
107042 2l*o Ulnvl chloride nono«or
production
107042 214* Vlnylldono chloride
production
107042 2*11 Gasoline klendlno it
refineries
107042 2>ll Cool In* klondlnc at
refineries
107042 421 Tank truck transport
107042 421 Tank truck transport
107042 421 T.nk truck trlud«o
Inclnoratlon
107042 4953 Sou4«o lludoo
InclnorAtlon
107042 4»5] U>it«.it«r tro«nt
fniisim IOUKI
HydrocorfeM cnlorlnolyoU
procoM. Mil M«to
kondllnt
Cntlro procoo*
*b«>rpUO«
HOAwv ond* lro«
dlttllUtlon colWM
M«*vy ondt fro«
dlitllUtlon coluon
Cntlro procooo
Stor«to *nd nandlln* of
(DC lOC-f lb/1000 «•!
transported
404001 4.11 X 10C-4 lb/1000 f'l
transported
5010050s 4.4 X 10C-4 Ib/ton dry
sludge
50100504 1 X IOE-S Ib/ton dry
sludoe
50100701 720 Ib/ton etnylene
dlchlor. In Influent
HOTIf MFBoJMM
Contr*vepwr kel. »ye. 1 carbon odsor./bypothet. plant fl
prod. I.IXIOU Ik/yr PCI t 4.4x1017 Ib/yr CCI4
Controlled, asjoroeate estloate based on notional fl
eeletlane, end production eetleate*
Control unclear . kamed on oass balance and te»tl«» «f
Uncontrolled, basts unspocUled »l
Controlled by thereal Incineration, calculated based en II
entlnoorln* Jydioeent
Controlled, oooreeate estleete based on national (1
e«l*4len* end production eetlnalem
Control atatus and basis unepeclfled II
Control status and bade unspecified fl
Calculated free1 oeoellno vapore oetlnatee 90
Calculated fron easollne vapore estleatee M
Calculated Iron eesollno vapora estleates SO
One test, scrubber 101
One test, scrubber, both Isoeers 101
•ased on ents. oodellna for hypoth. POTU, represente 9t
§
i
-------
Pa** No. IJ>
0*/2I/*O
POLLUTANT
1 .2-01chl»ro*thana
1.2-OfchIoroathana
1.2-Dlchloroathana
1.2-DUhloraathan*
1.2-Dlchloroathana
I .2-01 chl oroatnana
1.2-Dlchleraathan*
1.2-Dlchloroathana
1.2-DUhloroatheno
l.2-Dlchloro«tnana
1 .2-01 chl or oa than*
1 >2-Dlchloroethane
, c oroa ana
l.2-Dlchloro*tnana
. - c oroe
CM IK
NuniEII CODE INDUSTRIAL PHOCItt
1070*2 117 Caullna leading •« tank
car/truck tilth ludad
gaullae
1070*2 S17 Caiallaa loidtng a< tank
car /truck ulth 1 aided
ga*eiiee
1070*2 5171 ta.ollne laadlae ef taut
truck* at bulk plant*
1070*2 5171 Caullne lo.dln* of tank
truck* at bulk plant*
1070*2 5171 C**allna loidlng of t*nk
truck* *t bulk plant*
1070*2 II 71 Caroline loading a< tank
truck* at bulk plant*
1070*2 SI71 taiellna loadlnf of tank
truck* at bulk taralnal*
107042 5171 Cesolln* loadlnt ol tank
truck* at bulk twalnal*
1070*2 5171 Caullna laadlni of tank
truck* at bulk taralnal*
1070*2 5171 Caaolln* etorate at bulk
plant*
Plant*
107042 S171 C«*ol ln€ •tor*9' *t bulk
uUnti
107042 5171 C»»i>lin» it or 40* t*d nor**) ••rwlc*
t>»l.>*h to»a.n« - vtpor
d*dlc«t«d nor -1*1 ••rvica
tub*>«rt«d leftdlni - v*t»or
b*<4iac« ••rvtc*
Stor*9« taUik* • bf«*th.nf
10..
to****
Stora** tank* - filling
loa.a*
Flxad-roof ctoras* tank*
- breathing lo**e*
• «
* *
KC COM fDIMIOH raCTOet NOTE*
40*00144 O.OOI* Ik/IOEI wl Uncantralled, calculatad ba*ad an angleaerln* Jo*
tran*f*rrad
40*0011* 0.002245 la/IOEl aal Uncontrolled, calculated ba.ed an engineering Jud
transferred
404002 0.001402 lo/IOEI gai Calculatad free gaaollna veper aitlxate*
throughput
404002 ».* x IOE-4. Ik/IOEI g
404001 5.78 x IOC-4 lb/IOC3 gal Calculated free ae*ollne veper* astlaata*
tr*n*ferrad
404001 ».* x IOE-4 Ib/lOE) gal Calculated free •••aline vaaora *>tleate*
tr*fl*4errad
404002 I.I4 x IOC-8 Ib/lOEI aal Calculatad froe gaaellne vapar o*Ueate«
throughput
404002 2.35 x 10C-8 lb/10C3 *al Calculatad 4roe gasoline vapor eatlaat**
throughput
throughput
throughput
x ga a u a ga
* *
gaaua aganae
KreWPKC
peMat II
geaant ft
fO
50
(0
50
SO
(0
' so
so
so
so
so
so
so
so
so
s
5
-------
Pate No.
Of/ZI/M
CM (1C
MUflK* COM IMMCTIIM. PMCCM
inltSION fOUKf
KC COM INIMION MCTM
NOTtt
1.2-Dlchloroetkena
1.2-Dlchloroothana
107042 M4I Ceaellee earketUe
ectlvltlea
1070*2 ((41 Caeollee eerketliie
activities
;lees r 4O*O04 O.OO014* Ik/100* Ml Calculate* free Meal lee vapor estleataa
CalculatMl IrM MaollM war «tlMt«
40*004 0.0014* Ik/1000 Ml
thrwakvut
tranalar
Unco.tr.ll.d. calculatatf MMd an antlMarlM Judiiaint (I
l.2-0lchlorooth«na
1070*2 ((41 Cool I He eerketlne,
activities
Vehicle refuetlnt 40*00401 0.000171 Ib/IOCl Ml Con trailed, calculated eased en enetnaorlne Judee.ent
operations, dlaplaceeant leaded Ma transfer
II
1.2-Dlchloroethuie
1.2-Dlchleroath>ne
107042 ((41 Cool I !<• oarkatln*
actlvltlea
1070*2 ((41 EMollne storaM at
aervlce etatlons
Vanlcls rafuallni 40*00402 0.000111 Ib/lOCI lal Uncontrolled, calculated bated en onslneerlns JueveoeA
operations, aplllaee leaded Me tranafer
Illllni ol
40*0010* 4.42 « IOE-( Ik/1000 Ml Calculated «roe Maallne vaaar aatleataa
thrauehaut
l,2-0lcliloroatht
••rwlc* •t«ki«n»
(fl*>h
undirground t«nkc
40*00101 0.001(1 Ik/1000 Ml
threuaheut
Calculated free Maeltne vaaer eatleataa
1.2-DlcMoroathine
1070*2 ((41 tliollix ltor<» tlon procao. 101125 I.I Ib/ton of PCC and TCC Uncontrolled, kaaad on data froe one producer
drylne coluM vant produced
1.2-Dlchloroatnylana.
15*405 206* Parchloroathylana
production
Chlorln.tion of athylene 30112521 0.15 Ik/ton of PCC
dUhlorlde produced
proc/dlttlllation vent
Uncontrolled, kftead on data free ona producer
-------
Paee No. HI
POCUITMtT
CM *IC
nunm coot iwumiM. moat*
CnlltlOH MUKC
fCC COM OIIUIOM r«CTM
1.2-Blchleroethylono. 1M4M 2M» l-orrtloroetkyl.
- productlo*
1.2-1)1 ckloreothylono.
1.2-Otchloroethylon*.
1.2-Dlckloroethylene.
lf*S*2 Ji*» Perchloreotkyle
trtchloroethylo
production
19*5*1 21** Perchloroethylo
production
IJ45»2 2M* rercMoroethylo
production
2.4-Llchloro-»-nllroanlU 2*13414 22* Woven f«krlc flnlaMn*
2,4-Dtchlore-«-nltro*nlll 2*11414 22* Uavon fabric flnlahln*
Cklorinetle* ft otkrloo* Mil MM 2.2 Ik/tM •* fCC
dlCRlorldt
»roc/Mutrol!M » dryl*«
•TOO wont
lorlMtlM wocon. U1I2S 0. 12« Ik/ton •* fCI
dlotlllitlon vont Ki (reduced
Uncontrollod. b ono producer
Cklorlnitlon ol otkylnno MII2S2I O.M« Ib/tKl o< PCI
dlcklorld* produced
proc/dl*tltl*tlon vent
Chlorln*tta« o4 ethylena JOUI5ZO O.U IWtoe •< rCI
dlchloride produced
proc/naulrtllz* • drying
*re* vent
CurIn. oven - reiln 110001 O.OOti Ik/ton «»orlc
(Inlth
Tenter t
2.4-DlcMorophenal
2,4-BIchlorophenol
2.4-Dlcliloroplienol
Otchloroproptne
Olethyl >nth••<•* iludoo
Incineration
120B12 4tSl U«t«...t«r trottunt
24*311*7 21** Propylene OKlde
production ky
chlorohydrlnatlon
•4**2 224 Uovan fabric llnlthlne
•4««2 22* Uov.n fabric flnlahlnf
144*2 22* Uovan fabric tlnl>hln<
4*»1I7 Scrap tire, op.n burnln
Flutdl>ed-ked furnace 50100504 <7.4 x IOC-5 Ik/ton dry One teat, ecrubker
iludva
Multiple hearth furnace JOIO0504 <4.* x lOC-f Ik/ton dry One teat, ocrukoer
aludM
H. 10C-4 Ik/ton fabric Uncontrolled, teat data
130001 • K 10E-* Ib/ton fabric Uncontrolled. aw*ra9* of two teata
0.14* Ib/ton lira VOST aaaplea burn rate - 0.* k»/hr
2" by 2" place, uncontrollad
52
212
-------
Fa«* kto. 142
0*/2I/*O
FOUUTAUT
CM
•1C
COM INOUmlM.
OIIMION MMCf
|CC COW DIIMION r«CTM
NOW
Olhvdral
01hydrcl
Dlhydrolndon*
4M11T
4MII7
4*4117
4*4117
4»4lt7
BlhydrolndojM
Scrap tlra. epee kuraln* lire* In exparloectel
burn hut
Scrap tlra. open kurnln* Tlree In experlaMtal
burn hut
Sere* tlra. open burnln* Tlrea III experlaental
burn hut
Scrap tlra. wen burnln* Ttrea I* experleental
bur* hut
Scrap tlra. open fcurnlni Tlree In experimental
burn hut
Sera* tlra. oo«n buralnt Tiros In
bum hut
0.044 Ib/te* tlra
•.070 Ik/ten tlra
0.2M2 Ib/ton tlr«
O.404 lk/tw Ur«
0.1M Ib/ton tlra
0.011 Ib/ton tlra
VO»T MWplM bur« r>M - I.I k*/kr. »hr»d condltlen
1- by a* •!«•. WK«itr*U*d
VOST Mvln kura r«t« - 1.4 M/hr. Miratf condition
2* by 2* »!««. uncontrollmd
VNMT •«•»!« bum r«t« - 0.0 kt/nr. Kirrt condition
2* by 2* »!««. uncontrollxl
UMT *H»|M kura r.t« - O.f ki/kr. chunk
1/4 t« l/> >< • tlr<. uncentratUd
votl ttmflft bum r«t« - 1.7 k«/hr. chunk condition*
1/4 to 1/4 «« • tlra. uncontrolled
VOST >«*l« burn rat* - 1.27 t«/hr. chunk conditio
1/4 I* 1/4 •« a tlra. uncontrolled
212
212
Dlaothyl »htl»l*t*
BlHthyl (htkalit*
II1II1 224 Hovon ««brlc 10C-9 Ib/ton dry One teat, acrubbar
elude*
2.4-OleethyUhanol
Oleathylatyrene
105«7*
Incineration
nultlpl* hearth furnace
27974010 1149 ncetone/rhanol Cuoene teroxldatlon vent
aanufacture free cuaana
5010050* <3.4 x IOC-9 Ib/ton dry One tait. ecrubbar
alud*a
10120202 0.0001 Ib/ton phenol Controlled (not apeclfledl. ba»d on ••wlln*. 1*77
data, average lactor*
4,4-Olnltro-o-creaol 914921 4*9!
Incineration
Fluldlied-bed furnace
90100904 <».4 x 106-5 Ib/ton On* teat, acrubbar
•lud**
4.4>Dlnltro-e*cr*iol
914921
S*u»* aludte
Incineration
la hearth furnace
50100S04 <1.I2 M 10E-4 Ib/ton dry One taat, acrubbar
aludge
2.4-Dlnltro»h«nal
912*9 4tSl S«..9« aludae
Incineration
Fluldlzed-tad furnace
SOIOOSOt <0.001172 Ib/ton dry On.
aludaa
-------
rota Me.
Ot/21/M
I4S
POLLUTANT
CM
tic
COM INOUtniM.
tniMiou MUM
tec COM BIIMION MCTM
lloctyl
Moctyl pnthalate
llphonyl ether
II7IIT
II7II7
Incineration
4M1 feuaea aludea
Incineration
2Mt Phtkallc anhydride
•reduction *
MIOOM4 t.K « IOt-4 Ib/ton dry
tlode*
Bultlple kearth funuci IOIOOSO* 0.002* Ik/ton Dry >lu4» Awaw •< tM t«tl. KrubMr
ruittlM wl»lM«
MIDI* 0.012 lb/tw M »r«k>c.hth*Ut«
1I1I4I 224 Uouon <«krU fln|ihln« Ih«r«o«ol dv«ln<
110001 1.44 » IOE-4 Ik/ton
librlc
Uncontrollod. avor««« of two
fitvlnyl konxcno.
IIOMTB)
1121740 224 Uovon fabric flnlahln*
Curlnt ow«n • rooln
flnlih
131X101 0.00121 Ib/ton f«brlc Uncontrollod. ono t««t
Olvlnyl bonsono, (otitod
l*ooor«>
1121740 224 Uovan fabric flnlahlne
Tontar fraoo* - rosin
II nun
110001 1.4 x IOC-4 Ib/ton fabric Uncontrollod, avoraoa of tvo toata
f»lchlorohydrl»
UlcMoronydrln
I04IM 2*
1041*1 21
eptcnlorohydrlH uae aa a
foadatock In batch
proceaaaa
EpIchlorohydrlH uae a* a
faadatock III batch
procaaaoa
fualtlva oolaalona
Procaaa vonta
M.2 Ib/ton of
oalchlorohydrln uaad
1.12 Ik/ton
oalchlorohydrln uaad
laaod on aoereoato oela. 4 thruput oat., rapraaanta no
partlc. «ac.. baaod on SOCHI «OC eela. fac.
laaod on onreaati oolaalona and throughput oatleatoa.
rapraaonta no particular facility
EpUMorohydrln
1041*1 21
Cplchlorohydrln uao aa a
faadatock In batch
procaaaaa
Storaaa facllltloa
(Includaa atorago tanka
and tranafar oparatlona)
101 0.*4 Ib/ton of laaad on aooroiato oolaalona and throughput aatloataa.
oplchlorohydrln uaad rapraaanta no particular facility
EolcMorohydrln
2121 Epoxy raalna (conttnuoua
procaaa) production
Storaaa tank aolaalona
407 0.4 Ib/ton of product Control atatua unapoclflad. baaod on OAO plant'a
asttoataa
Eolchloronydrln
26*21 Epoxy raalna (contlnuoua
procaaa) production
Storiaa tank ealaalona 407 0 Ib/ton of product
Tanka vontod to balloon haador. baaod on ono plant'a
aatlaataa
Eplchlorohydrln
2121 Epoxv raalna tcontln
procaaa) production
10IOIB47 0.01 Ib/ton of product »fll afflcla
only
Eolchlorohydrln
Eplchlorohydrln
production
Fugltlva aalaslona
30I305BO 1.24 Ib/ton Uncontrollad, ba»d on SOCHI VOC aalaalon lactora
oplchlorohydrln produced
-------
•••a No.
Ot/ll/tO
KLLUTMIT
CM
COM iNDurraiM. MOMM
HtlMIM tOUK*
tec COM mwigN mem
ftlcnlorohydrla
Eplchlorohydrln
talcklarohydrla.
I04M*
iOUM MM
faUMarakyoVU
•reduction
•reduction
I04IM *•«» Eplchlorehydrlp,
•reduction ky
kydrocklarlliatloa
procaaa vaato.
turna, (Mtlittn
llacludaa otaraaa tonka
and transfer «r«rtr»l m\»t»»
wlchlarohydrli >radMC«< ii«itaiuild< ••!•. tottU t »«tlonyllanc« tn* tntlm
115020 <0.001 Ik/tan
IMcentralUd. t«t d*t*
ftkyl acryleta
Ctkyl alcahal
ftkyl alcohol
ftkyl alcohol
Ethyl alcohol
2-fthyl hexanal
Ethyl atyran*
M - Ouwick •kurkv af«-l»
I40HS 2W» Acrylic «cl« »r>ductl
krepylvn* •xltfA
44175 205 ttkarlaa
44171 205 lakarlaa
44175 20*4 Ulna oekla*
44175 20*4 Vine atklne Fereent1
faraankad
110001 0.0042 Ib/tan Ubrle
11O001 0.00*2 Ik/tM fabric
Uncantrallad
Uncantrallad
Uncantrallad. far • 12 dearee Fahranhalt tank
Uncontrolled, for a 10 dearee Fehranhalt tank
Uncontrollad, ona tact
Uncontrollad. avaraaa of two tasta
52
52
Ethyl atyrana
fthyl atyrana
fthylbaniana
Ethylbeniene
2*104101 224 Vovan <
-------
•at* No. I4S
0*/2I/*0
POLLUTANT
fthylk*n«M*
(thylbMzene
EthylbMzene
Ethyl beniene
Ethyl benzene
Ethyl benzene
Cthyl DMcen*
I thylbMzene
EthylbMzan*
Ethyl benzene
Ethyl benzene
Ethyl benzene
Ethyl benien*
y
Cthylbenzena
CM *IC
NUntU CODE INDUSTRIAL PROCESS EMISSION SOURCE
IO04I4 Scrap tlr*. e*M burnln* Tlrea 1* oxperlOMtal
burn hut
100414 Scrap tlr*. OPM burnln* Tlrea 1* uperleMtal
bur* hut
100414 Scrap tlr*, OPM burnln* Tlrea In oxnrlOMtal
burn hut
100414 Sera* tlr*. OPM burnln* Tlrea 1* *w*rloMtal
burn hut
100414 Sera* tlr*. OPM burnln* Tlr*a In experimental
burn hut
100414 Sera* tlr*. OPM burnln* Tim In exporloental
burn hut
100414 Scrap tlr*, open burnln* Tlrea In *Hp*rlo*ntal
burn hut
100414 Sera* tlr*. OPM burnln* Tlru In experimental
burn hut
100414 Scrap tire, open burnln* Tlrea In experimental
burn hut
100414 Scrap tlr*. OPM burnln* Tlrea In experimental
burn hut
100414 Scrap tiro. op*n burnln* Tlrea In •xperteantat
burn hut
100414 Scrap tlr*. OPM burnln* Tires In experimental
burn hut
100414 Scrap tlr*. open burnln* Tires In experimental
burn hut
100414 HI Agricultural Uaed black plastic
sec COM mission r*CTM
0.«*4 Ik/tM tlr*
0.131 Ik/tM tlr*
O.S47 Ik/tM tlr*
0.2*3 Ik/tM tlr*
0.114 Ik/tM tiro
0.4OS Ik/tM tlr*
0.1*1 Ik/tM tlr*
1.341 Ik/tM tlr*
4.37* Ik/tM tiro
0.574 Ib/tM tlr*
0.102 Ib/tM tiro
0.212 Ib/tM tlr*
0.0*3 Ib/tM tlr*
0.040 Ifa/ton tire
0.077 m«/o3
NOTE*
IAD-2 •Ktract* U/Hf (Mini*. CbMt CMdltlM e |/4-l/«
o< tlr*, burn rate e 1.7 kt/fcr. uncMtrolled
IM-2 extract* »/rtS analval*. chunk CMdltlM • I/4-l/«
af tlr*. kurn rat* • 2.3 k*/hr. uncontrolled
VOST aaeplea burn rat* - I.S ko/hr. ahrad condition •
2* ky 2* piece. uncMtrolled
VOST aeeplea burn rat* - 2.3 ko/hr. shred condition e
2* ky 2* Piece. uncMtrolled
VOST esnelee burn rato - 0.* k«/hr. ahred condltlM •
2* ky 2* place. uncMtrolled
VOST eemplee burn rat* - 1.3 k«/hr. shred CMdltlM >
2* by 2* Piece. uncMtrolled
VOST aemples kurn rat* - 1.4 ke/hr. ahred condition •
2* by 2* piece. uncMtrolled
VOST aemples kurn rat* - O.t ka/hr, shred CMdltlM • '
2" by 2* ploc*. uncontrolled
VOST seeeles burn rat* - O.S k*/hr. chunk CMdltlM* e
1/4 to I/* of a tiro. uncMtrolled
VOST samples burn rat* - 1.7 k*/hr, chunk conditions •
1/4 to l/« of a tlr*. uncontrolled
VOST aemples bur* rat* - 3.S k«/hr. chunk CMdltlM* •
1/4 t* 1/4 of e tire. uncMtrolled
VOST aemples burn rat* - 1.27 ke/hr. chunk CMdltlM* •
1/4 to 1/4 of a tire. uncMtrolled
VOST aemples burn rate - 2.27 ko/hr. chunk conditions •
t/4 ta 1/4 of a tire, uncontrolled
VOST aeeplea burn rate * 4.43 kff/hr, chunk conditions •
Experimental slmuletlM. plestlc sheet • 1 Ib. . EC/FID
test iron VOST •aoplaa. ran** la 0.021 - 0.124 me/el
212
111
piratic crop covara
Ethylbenxen«
Ifl Agricultural
Induitry-ileld burnlni o<
plaatlc crop cover*
Unu»d black plaatlc
0.040 O|/e3
Cxperleental aleulatlM. plaatlc aheet • 1 Ib.. EC/FID
tut (roe VOST aanplei. ranee la 0.013 - O.Oia eg/nl
Ethylbanxene
100414 24M Uood precervln*
Incineration ol mate 307005 Not detectable
Controlled ulth baohouie
-------
Pee* No. 144
KLUITMn
CM IIC
MUM* COM MUMMM. PMCtM
IMtSIOH MUM
«CC COM MIMIM PMTM
Mm
Ithylheniono
fthylkenzena
ftkylbanione
Ithylkeniene
Ithvlkenzene
Ethyl benzene
fthylbeniene
Ithylkeniene
Ethyl ene
Ctnyl one
Ethyl ene
(thyl one
Ethyl ene
Ethylana
Cthylene
Ethyl ene
Ethyl ene
100414 24*1 Weed erewrvlm
100414 IMC Hcetooe/Phenol
Benufecture free cueene
100414 2(*( Acetone/Phenol
eanufacture free, CUOMO
100414 2*11 retreleun refinery
100414 4>SI (euaee eludte
Incineration
100414 4*91 leuaie elude*
100414 4*51 UaatMater treateent
100414 SS4I tualln* earketln*
actlvltlea
74151 21* Ithylene production
74151 21* Ethylone production
74ISI 21* tthylona production
74(91 21* ethyl me production
74151 2f* Ethylane production
74851 21* fthylene production
74851 28* Ethylene production
74B51 28* Ethylene production
74BSI 2B* Cthylane production
thereat «pan> evaporation <• at/Ml (a* vented
Cleavaa* lection vent* Ml 202 11 1.0 « IW-* Ik/ten phenol
(cooclned)
Cueene pet-oxidation vent UI20202 «. 000(4) Ik/ton phenol
riuldlaed catalytic JO* O.J77 Ik/hr
creckln* unit, fueltlvea
riuldlzad-bed furnace SOlOOSO* 4 « lOC-f Ik/ten dry
elude*
nultlel* keartk fur nice S01005O* 0.0027 Ik/to* dry clud**
roiu 50100701 1120 Ik/ton ethyl keniene
In Influent
vehicle rofuollafj. vapor 40*00101 O.OItB lfc/«al of *••
Ion puapod
Futltlvo Minion - 1011*74* 0. 00411 Ik/hr
Fuiltlve eaiaalen - 1011*74* o.OH Ik/hr
aaepllne connection*
Fugitive Minion - 3011*74* 0.1*4 Ik/hr
Fuiltlve Minion - 1011*74* 0.00*1 tk/hr
opan-andod Una!
Full tl vi Million - (at 3011*74* 0.2407 Ik/hr
praiiura relief valve
Fun II vi oolnlon - 1011*74* 0.00050 Ik/hr
vll vai
Futltlvo Minion - 1011*74* 0.01** Ik/hr
Fugitive oolnlon - 1011*74* 0.01B* Ik/hr
Vllvn
leal I
Controlled lunipaclUed) . kaaed en teat data. 1*77
data, averate factor*
Controlled (not opeclfled). baaed en aaeplln*. 1*77
Baaed on •elantod Million atreaai content
1
One talt. Krukker
rive teat*, ecrubker
(nod en eela. eodellne for hypoth. rOTU. repreaent*
Lilted a* eelaalen rate far
athylkonxene/2.>-dleethylheptano
Uncontrolled Minion factor
Uncontrolled eellalon factor
Uncontrolled Minion factor
Uncontrolled eataalen factor
Uncontrolled Minion factor
Uncontrolled oolnlon factor for a heavy lleuld
Uncontrolled Million factor for a llont lleuld
Uncontrolled oelnlon factor for a *n
0
129
125
•2
101
101
I*
*
214
214
214
214
214
214
214
214
214
-------
Fat* It*. l«f
0»/21/M>
FOLLUtajIT
Ethylon*
Ethylon*
Ethylon*
Ethyl on*
Ethylono
Ethylono ilytol
Ethyl*n* oxide
Ethylon* oxld*
Ethylon* oxld*
Ethylon* oxide
Ethylono oxide
Ethylone oxide
Ethylene oxld*
Ethyl *n* oxide
Ethylon* oxide
Ethylon* oxld*
Ethyl*n* oxld*
CM SIC
MMt* COM IMUtniM. FMCSM OI1H10N MWCC
74191 2*4 ItkylOM production Fuoltlvo ooUolM - p*M»
Mai*
74191 2«4» Acetic anhydride Reaction by-product •*•
production
74191 214» ItkylOM dlcklorldo Abeoratlon
production - direct
chlorlnatlon
- oil lurnac*
74191 tot Hoapltal M*to Incinerator
Incineration
10721 1 4741 Mall tank car clainln* Entire proco**
752H 20 FooditvM luntoetlon P~u*ltlve eeUplono
7SJ11 20 FoodatuH luollttlon FroceM venta
75211 20 foodituH fu*l*atlon Uaatauator eelaalone
75211 20 FoodatuM ll»74a ».127» Ib/kr Uncontrollod o*4*alo* «oct*r lor « Itont lleuld1
Mil 3102 X.* Ib/ton acetic ia.ed on data Iron thro* plant*
anhydride produced
10II2S02 4.2 Ik/ton produced Control uncertain, baaed on teat* and oao* balanc*
10100SO4 I.I Ib/ton carbon black la*od on t**t data
111029 <0.02 Ib/ton 0.0007 Ib/tant car E*l»lon M**urooont
tOO Ib/ton othylm* oxide Uncontrollod. bleed on lourco teito
u*ed
4M Id/ton othylon* oxide Uncontrolled, baaed en oourc* t*at*
uaed
1000 Ib/ton othylene Uncontrollod, ba»od on oourc* t*at*
oxld* ua.d
too Ib/ton othylono oxld. Uncontrollod. baaed on aourc* taata
ya*d
1400 Ib/ton *thyl*n* Uncontrolled, baaed on aourco teat*
oxld* u**d
30117402 0.01-2 Ib/ton Uncontrolled, baa*d on aourc* teat*
30117402 0 Ib/ton Controlled by catalytic oxidation or oeereency <|are.
•ource teat*
34 < .
301174 0 Ib/ton Controlled by racycla or ecrubb*r ulth Incineration or
30117421
REFtHtHCK
214
152
**
»7
1*7
07
44
44
44
44
44
41
43
43
43
by *ir-OKld«tlon process
-------
Fata Ha. 14*
Ot/tl/tt
MUUMMT
CM *IC
aum* COM IMRUmiM. MWCM*
fMSttON SOUKS
tec COM tmttiM
MOItt
ftkylena axlde
tthylena e*l*e
Itkylana Mid*
TSUI 2M» ftbylaM Okie* ^reduction Itrlapar v«it
kv alr»a*iidatlae] aracaaa
TS211 tM* ttkvlena axloe aretfuctta* Carbon dlealoe
ky exyaan-oxldatlan vant
aracaaa
Ml 17411 * Ik/tM
1OU741» •.OOftta-l.t Ib/tM
C«itr*U*d ky kolldr,
«i Mure* t«.t»
mil 2M9 Kthyl«M •*l<* *r**.«U.M CwboA d|.uU.M .taMTaMr 30117110 0.12 l»/tM
Uncontrolled. k*Htf oil MOtiMwInt
hvrotlntlcal >l
J15020 400 Ib/ton atkylana onlda Uncontrollad. b»ad on aourca taata
u«ad
315020 520 lb/ton/ko*pltal bad Uncontrollad, baaad on aourca taata. Inappropriate to
u*a tkla lactor for Individual kotpltala
-------
P*W No. IO
0»/2l/»0
CM *IC
•mot COM iNMtniM. raocns
MISSION SOMCf
«CC COM ttllNIOM MCTOX
MOTI*
fthylono oxldo
Ithylono Mid*
Tflll SO42 Hoaoltot otorlll»atla« Fudtlvo oolooioM
75211 0042 Hooaltal otorlIllation Froccoo Mate
JI5010
WO Ik/to* otnylono oxldo
ourckaaod
uncontrolled, kaood M OOMTM «o»U
IIS02O (00 Ik/ton otfcyloflo oxldo Uncontrolled, baaed M eewce t«U
•4
IthVlone oxide
TS2H M<2 Haw freem wit*
J1JOJO MO IkStM/hoMittl
Uncootrallx). b«««l on uurco t«.t». InworaorlMo to
uu tkl« «xtor lor Individual h«*lt>l*
Cthylono oxldo
(tkvlono oxldo
(tkvlono oxldo
7S2II IM2 HowltO •torllliatlon Proco« vonto
7S2II 1042 Howlttl otorlll»tlon U««t..«t«r ooloolono
7I2IS 1042 Howlttl •torllliatlon y»t..»t*r oolMlon
1IS020 1W Ik/ton otkylono oxldo
•urchtiod
1100 Ik/ton otkylono
oxldo u«od
315020 1440 Ik'ton/kowltil Md
Uncontrollod. koood on oourco to«to
Uncontrollod. kaood on oourco tooto
Uncontrollod. kaood on oourco toota. Inaooroorlato to
uao tklo factor for Individual hoaaltalo
Ithylono oxldo
75211 1042 Howltal atorllliatlon U««t«««t«r ooilalont
140 Ik/ton othytano oxlda
yurchaaod
Uncontrollod, kaaod on oourco tatta
Itkylono oxldo
(tkylono oxldo
Cthylono oxldo
Ctnylono oxldo
Fluoranthono
Fluoranthona
Fluorantnano
Flueranthana
7S2II 1042 HoolUl •torlllior.
tablo-toa
7S21I 1042 HoMltal atorlllzar.
taklo-toa
75211 1042 Hoaaltal Itorllliar,
tablo-to*
752lt 1042 HoolUl atari 11 jar,
taklo-toa
Futttlvo oolaalona
Fuoltlvo oolaalano
Procaaa * •onora!
racaaa * oanoral
204440 Scrat tiro, o>an burnlni Tlrat In axtorloantal
burn hut
5crap lira, o»an burning lira* In axsarloant*!
burn hut
400 Ib/ton othylona oxlda
uaod
100 Ik/ton otnylano oxlda
aurchaaod
1400 Ik/ton othylono
oxldo uaod
1240 Ik/ton othylona
oxldo aurchaaad
1.04S Ik/ton tiro
0.7*4 Ik/tan tlra
0.7*1 Ib/ton tlra
0.543 Ib/ton tlra
Uncontrollod. kaaod on ontlnoorln* judoooont
Uncontrallod, kaaod on onolnoorln* Judaooont
Uncontrollod, kaood on onolnoorln* Judtooont
Uncontrollod. kaaod on onolnoorlno Judoooont
turn of PM4 analy on IU oxtrat. of 1*0-1 toot 4 flltar
coapont. ahrod condition • 2" ky 2* ploco. burn
rato'l.l ko/Hr. control lad
Suo of PAH analy on ll« ontrat. of >AO-2 toat t flltar
coapont. ahrod condition • 2* by 2" placo, burn
rata'l.t kfl/hr, controllad
5uo of PAH analv on 114 aiitrat. of ««D-2 taat t flltar
coapont. ahrad condition • 2* by 2* placa. burn
rato-1.7 ko/hr, central I ad
Sua of PAH analy on 114 axtrat. of >M>-2 taat t flltor
coapont. ahrad condition • 2" by 2" ploca. burn
rata-2.3 ko/hr. controllad
Fluortnthana
204440 25
Hood coabuatlon.
Induatrlal
Horizontal raturn tuta 10200904
1.8 x 10E-4 Ib/ton
(dry b«il«>
-------
Pee* No. 1*0
o»/2i/*o
POLLUTANT
CM (1C
iunm CMC iwwmiM. men*
KC COM MIMIM FACTO*
wn*
FIueraAtheM
Fluoranthene
FI
Flu
Fluorene
2O*440 2f Mood, coetxietlee.
Induatrlal
20*440 IS Mood coebuotlM.
Industrial
l«7>7
M7I7
1*737
laleoced *•«•* ulckee
otokor-flred Induatrlel
boiler
lelenced *ralt ulckee
etoker-llred Industrial
bolter
10200*0* «.« x IOt-« Ib/tM <(Ml
llKtV IcvClOM). MOtf <l
burn hut
Scrt* Ur». «••• burnln* Tlr«> I* •x»«rlM«t>l
burn hut
Scra» tire. •*«! burnlnt Tlrat In •Mvlnantal
burn hut
10200*0* 2.1 x tOC-I Ik/ton luel Dry uood. one plant, partlculate control M/eechanlcal
collector (cyclone), vood ieed rate 0.2* ke/a, boll.
ell. fS.31
0.722 Ib/tM tlr«
O.tll lb/t«i tlr«
0.«*2 Ik/ton tlr<
O.tSI lfc/t«i tlr«
0.411 Ik/ton tlr«
IAB-2 extract* •'•>» M«ly>U. •nr<4 condition • 2* by
2* olKm. bur* r«to • I.] kc/hr. uncontrolled
>*0-2 otrtctl »/H» Malyolo. •Drod condition • 2* by
2* plocoo. burn r*to • I.I ko/hr, uncontrolled
InO-2 oxtrut* u/nt on>lvil«. chunk condition • 1/4-1/4
ol tiro, burn rato • 1.7 ke/hr, uncontrollod
«nO-X extrtct* u/nS *n«ly>l>. chunk condition • 1/4-1/4
ol tiro, burn r«to • 2.3 kfl/hr. uncontrollod
Sue ol F«H u*ly on II* extra, el IM-2 t«t t Illtor
coMont. ihred condition • 2* by 2* olece. burn
r«t«-I.I kt/hr, controlled
212
•era* tire, open burnlne Tlraa In experleental
burn hut
O.JOt Ib/ton tire
tun o< PnM «naty on lie eiitrat. ol IAO-2 teat 4 Illtor
cowont. enrad condition • 2* by 2* elece. burn
rata-1.1 ke/hr. controlled
Icrap tire, open burnlne Tlraa In experleental
burn hut
0.4*4 Ib/ton tire
Sue ol MM analy on lie extrat. el IAO-2 teat t filter
cowont. ehrod condition • 2* by 2* etece. burn
rate>l.7 ke/hr. controlled
tcraa tire, eeen burnlne lira* In eneerleental
burn hut
O.X47 Ib/ton tire
Sun ol PAH analy en IU oxtrat. al IMi-J teat 1 Itlter
caeaont. ahrad condition • 2" by 2" alece, burn
rete-2.3 ke/hr. controlled
nnleal lead
delluorlnatlon
nnla«l leed
delluorlnatlon
Tharaal delluorlnatlon
proceaa
Thara*! dalluorlnation
•rocaaa
1*0 Iba/ton P20S
Uncontrolled aelaalona baaed on a eaterlal balance
0.04-0.4* Iba/ton P209 Controlled but device not apecllled
U»I441I
nnlotl leed
delluorlnatlon
alxlne and drylnl
O.OII Ib./ton f205
Controlled by a wet acrubfaar
f\ula bad. oll-4tra«
caUlnar
0.0004-0.0010 Iba/ton of Controlled toy a wanturl acrubber. averaee o* * teat
rock throughput runt waa 0.001* Iba/ton throuehput
Fluoride
14*84488 2874 neaonlun phoaphtta
production
Ory«r/coolar
30103001 0.03 Ib/ton phoaphata Controlled (not apacllladl
produced
-------
Pete tte. isi
0*/2l/tO
POUJ/TANT
CM SIC
Nunoc* coot tMumiM. nractu
oimiw MUMS
tec toot nnssioM ncnn
Fluoride
UtO«M MM AeeXMlue pftooelieto
ereductleo)
U»I44M 2W4 Aeeenliie) ehoeehate
production
14*144** 2174 Phoaphate lertlliter
eanulacturlnt
l4*t44M 2174 phoephata fertilize)
•aiMifecturlnej
Frotfuct
MI0340S O.»l Ik/to
oroducod
Controlled (not »P«el«l»d>
'aeeoeletor-eranul 10103002 O.OS Ik/ten pheephato Controlled (net epeclfledl
oter produced
Daactor-eranulator/dryer/ 301014 O.OZ43-O.OSS Ike/tee, el Ctrl by • venturl ecrubker • e*rey-creeellaei packed
cooler vent*, dlaeeonlue P20S produced acrubbera. av* 13 teata 0.0341 Ike/ten P205
J010U01 0.00041-0.OOII Ike/ten el Controlled by a uenturl icrukker. tvertee o< • tetti
F20S produced Me 0.0007 Ike/ten F20S
BwoMtrlc
hot y«l I /product
coollnt t«nk,
*7
Its
its
Fluoride
I4*I44M 2(74 Ptioapkate fertilize
•anulacturlnt
I4*(44BB 2B74 Pheaphate fertilize
eanufacturfne;
I4*(44(B 2B74 Pheephate fertilize*
y»lu« pond luiltlv*
•(••tone
J010JO 0.14 Ik/ten F20» Input Controlled mth e pocked ecrukber
30102* O.OOCJ-0.0005 Ik/ten »20S
Input
I010U02 O.I-S.2 Ike/ocre-dey
Aeeueee ' concentretlee o( 12000 Pftl In pond. Kind
•peed verlee free 1-4 H/tec. *0 F tee«
Ufl44M 2174
fiypvua pond fugitive
10IOU02 0.2-7.1 lke/>cre-d«y
A»uee« F cencentretlen el 11-44 PPI ebeve pond
I4»I44M 2074 Phosphate fertilizer Tee aln.la-tank reactor*. 10101401 0.0040-0.0112 lk*/ton ol Controlled kv tue leelneeeent ecrukber* In eerie*.
•anufacturfnt - net ehoaehorlc acid plant P20S produced averaeo el 1 toot* uae 0.00*1 lb*/ton P20S
proceae
UM44M 2174
Conwentlon*!
•utl-coepkrteent tonk
re«ctor. phosphoric ocld
pKnt
10101401 0.007-0.01*4 Ibe/ton ol Controlled by way-concurrent packed ecrubber. averaee
P20S produced ol S teat rune ua> 0.0117 Iba/ton P205
U»*44B* 2*74 Phoaphate fertilizer Conventional 10101401 0.0014-0.01*4 Iba/ton ol Ctrl by opray-croaelloe packed ecrubber. rue rep IS
eanulacturlni - oot eutl-cowarteent tank P20S produced teat runs / 3 fee., auf rate 0.00*1 Ib/ton P20S
proceaa reactor, phoaphorlc acid
UM44BI 2174 Ftiowhorlc «cld
production
JOI014 0.01-0.02 Ib/ton P205 Controlled »lth a packed •crubber
Input
14*I44BB 2B74 Suparphoaphate loranular Cur I nil bulldlni
triplet production
10102*07 0.04 Ib/ton '205
Uat (crubber <*71). baaod en teat data
14*B44BB 2B74 Superphoaphato
-------
•aee Ho. IS2
Ot/2l/*0
MUJmNT
Flu.
Flu.
Flu.
Flu.
Flu.
Flui
Flu.
Flu.
vide
vide
vide
vide
vide
vide
vide
vide
Fluoride
FllM
Flui
Flu.
Flu.
vide
vide
vide
vide
Fluoride
Fluoride
Fluoride
Bl ...ula4da
CM
MUM*
I4*S44M
I4M44M
14M44M
I4M44M
14M44M
I4t*44*8
14M441S
Utl44SS
14*144(1
I4M44SS
14tl44SS
14tt44SS
UtS44SS
le*a448S
14*14481
1 A«S44BB
SIC
COM
2174
2174
2174
2*74
2*74
2*74
2*74
2174
2*74
2*74
2**t
322
322t
3251
32*
32*4
17*4
IHDUSTRIM. FdOCtSS
Superphespbate 0.022-0.230 Ike/ton of
F2DS produced
30102*05 0.03S-O.I4S Iba/ton of
P20S produced
301014 O.OOOS Ib/ton F2OS Input
30501301 S Ik/ton charts
30501404 20 Iba/ton ol (lass
produced
305012 2 Ib/ton rax eaterlal
proceaaed
305003 1 Ib/ton brick producad
30501201 0.12 Iba/ton of ejaaa
produced
proceaaed
mm
Controls not epeclllod
Controlled by sprey-croseflev pecked scrubber, oversee
ol 7 tests Mas 0.0002 Iks/ton F2O5
Ctrl by t venturl. I cyclonic, » 1 apray-croaatlou
packed scrubber. av» el 1 toots 0.211 Ib/ton FJOS
Ctrl ky venturt ocrubbers ft spraycroeefloe) packed
ecrubbero. evs) el 10 tests 0.121 Ib/ton I>20S
Uncontrolled
Met scrubber <*7I>
Uet scrubber <»7I) . based on toot data
Controlled by 2 cyclonic scrubbers In series, oversee
of 4 tests MS O.I It Iba/ton F20S
Controlled by a venturl scrubber, packed-bed cyclonic
scrubber. av» of 7 tests 0.1*5 Iba/ton P20S
Controlled Kith a packed scrubber
Uncontrolled
Uncontrolled, bated on United teat data
uncontrolled, appllea to tunnel or periodic kiln. ta*.
oil. or coal fired
Uncontrolled eolaalont. uool flborolaas furnace
UFttCI
1*0
its
its
its
t7
t7
»7
its
its
174
t7
t7
»7
»7
»7
-------
•n* MO. 1*1
POLLUTANT
CM (1C
Nunon COM INOU*T*.IM. FMCH*
DIIKION $OMCt
IU COM BMMHN CACTW
Fluoride
»»rld.
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
I4M44M 1112
I4M44H JJI2
Ut(44M 1112
l4*t44M 1114
14M44U 1114
14M44H 1114
I4M44M 1114
14*I44M 1114
I4M44M 1114
I4M44M 1114
I4*I44M 1JJ4
14*14411 1114
14*14411 III4
149044M 1114
I49B44M J3J4
u»maa jjj4
149B4488 3334
Stool production
Stool oroduct Ion
Primary aluolnti*
production
Prloary •luolnu*
production
Prloary •lu.lnw
production
Prloary aluolnu*
production
production
Prlaary aluelnu*.
production
Prloary aluminum
production
Prloary alualnua.
production
Prlaary alualnua
production
Prlaary *luiilnuii
production
prl alary Alunt nun
production
Prlaiftry eilualnuej
production
Prl*.iry alualnua
production
production
floctric ore lurHM«/AOO 30300* t.74 ibc/ton o|o«l Uncontroll*.! oolMlon*
vo«>ol str«.w.> coobtn««3
ATOOA oxytm W300* O.J7 lb«/ton stool Uncontrollod wiwlon*
Ut«lnl**s *tooli
floctric «rc lurn*c« 103OOMS O.OO4 - 0,7 lb*/ton stool Uncontrollod oolciloni
Anodo b*kiB»j IUTAMO 3030019S »** IWton -olton M Uncontr*U«d. *4.««ou< fluorld*. b*«*d on t**t d*t«
oroduct
Anod* fa* kin* 4tirn*c* 103O0105 O.I Ib/tM wit on Al Uncontrolled. p*rtlcul*ta lluorldo. b**od on to«t dot*
product
Anodo b«klii« «urn*e« 30300105 0.04 Ib/ton •olton Al 6*«oous fluorld*. b«*od on tost d*t«, opr«y tOMor
product
product
product
Anodo b*ktn« 4urn*co 30300105 0.03 Ib/ton oolton Al P*rtlcul«to fluortdo. b«*od on t»t dat*. CSP
product
Anodo o*Mn» furnaco J0 1001 OS O.OOf Ib/ton oolton Al 6«oous fluorldo. b*««d on t«ftt d«tft, dry «lu«ln.v
product ccrubbor
Anodo bkfcU* 4urn»co 3O3Q&10S 0.002 Ib/ton oolton Al Pcrt.cuUto fluorldo* b*>«d on tost d*t», dry 4liMln«
product ccrubb.^
Horizontal Sodorbor* stud 30300102 22 Ib/ton oolton Al Uncontrollod, tasoous fluorldo, basod on tost data
call product
Horizontal Sodarbart atud 30300102 12 tb/ton oolton Al Uncontrollod. partlculat* fluorlda, basod on t*st data
call product
cal 1 product
call product
Horizontal Sodarbart stud 30300102 !•.• Ib/ton «oUan Al Gasaous fluorldo. oolaslons to coll actor, faasad on tatt
call product data
call product taat data
in
it*
in
•7
»>
•7
ay
tr
*7
»7
•7
»7
»7
S
I
-------
Pad* He. 114
O»/21/tO
POLLUTANT
Flu.
PlW
Flu.
PlW
Flu.
PlW
Flu.
PlW
•rldd
irldo
irldo
•ride
>rldo
irldo
>rlda
vlda
Fluorlda
»lw
PlW
Flw
Flu.
irldo
irldo
irldo
irlda
Plwrlda
Fluor Id.
Fluor Id.
Fluorlda
CM
auwn
U««44M
UM44M
ia»44H
UM44M
U«*44M
lafl44M
Utl44U
UTI44M
la»!44M
t*M44M
I4M44M
latl44K
U»I44II
I4M44M
IIC
COM
3334
3334
3334
3334
3334
3334
3334
3314
3334
3334
3334
3334
3114
1114
1114
1114
1114
imumiit. MOCIM
Prloarv alWlOJUP)
productlM
PrlMry aluoliwo)
production)
PrtMry alttaipjuoi
productlM
Primary aliMlnu*
production
prloCctt.,"*"""
Prloarv .luotnua
production
prlaary aluolnuoi
production
Prloarv olualnuo.
production
Prlnary aluolnuo
production
Prloarv aluailnum
production
Prloarv aluolnuo
production
Prloary alunlnun
production
Prloary aluolnuo
production
Prloary aluolnuo
production
Prlo.ry aluolnun
production
Prlo.ry alunlnuo
production
Prlo.ry aluolnuo
production
tnllllON (OUKI
HorUontal (odorkort otlad
coll
Horizontal tedorkarc Mud
coll
Horizontal tcdarkor* stud
coll
Horizontal wdarbarf atud
coll
Horizontal (odorkor* atod
coll
Horizontal fodorfcart atud
coll
Horizontal Sodarkart atud
coll
Horizontal Sodarbor* atud
coll
Horlxontal fodarbort atud
coll
Horizontal todarbor* atud
coll
Prabaka call
Prab.ka call
Prab.ka call
Pr.b.ka call
Fr.b.k. call
Pr.b.fca call
Pr.b.ka c.l I
«CC COM
30300102
30300102
30300101
M300I01
30300102
10300102
JOJ00101
10100102
10100102
10100102
10100101
10100101
10100101
10100101
10300 101
10300101
1010O101
tHIMIOM r*CTM
7.f Ik/tM Mlton M
product
1.? Ik/ton Mlton M
product
0.4 Ik/ton Mltoa M
product
1.4 Ik/tM M! tan *l
product
•.2 Ik/tM Mlton M
product
0.1 Ik/tM Ml tan M
product
1.0 Ik/tM Ml tan M
product
0.1 Ik/tM Mlton nl
product
0.4 Ik/tM MltM At
product
0.2 Ib/ton Mlton Al
product
4.7 Ik/tM MltM Al
product
S.a Ik/tM MltM Al
product
0.4 Ib/ton oolton Al
product
0.1 Ib/ton Mlton Al
product
product
1.4 Ib/ton oolton Al
product
1.4 Ib/ton »olt.n Al
product
MOTCS '
•OOMU* flow-Id*, apray tOMr. kaaad M toat data
Partlculato , acrubbor plu. I»P, kaaod M ta.t data
PtrtlcuUto. acrubkar plua ISP. kaaod M tmt data
Eaaaoua, Mtt CIP. kaaad M taat d.ta
Partloulata, Mt IIP. kaaod M toat data
C.«aoua, dry aluolna acrubbor, baaad on toat data
P.rtlcul.to. dry aluoln. acrubbor. baaad M taat data
fiaaaoua lluorldo. kaaod on toat data, croaa flaw packad
bod acrukbor
P.ckad bad .crubbor
a.cond.ry .crubbar
Partlcul.ta iluorldo. b.aod on to.t d.ta. dry plu.
•acondary .crubb.r
touar
.pray tOM.r
ffnxtt
»7
•7
»7
»7
»7
»7
»7
»7
»7
•7
t7
»7
»7
»7
»7
»7
-------
Feee Ho. ttf
Ot/21/M
rOUUTANT
Flu
Flu
orlde
•ride
CM
WMM»
14M44M
14M44H
Fluoride 14*14411
Flw
Flw
Flw
Flw
Flui
Flw
Flw
Flu<
•ride
pride
•ride
•ride
irlde
irlde
irlde
irlde
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
Fluoride
I4M44H
I4TI44M
I4M44N
14*14410.
14*1448*
14tl44M
14*14418
14014411
14*14411
14*14411
14*14411
14»I44B1
14*14481
14*I44BB
SIC
COM
S3S4
3134
1114
1334
1114
1114
1334
1114
1114
3334
1114
1114
1114
1114
1114
3134
1334
MoutniM. FHOCUS
rVlearv tluoUnyei
•reduction
FVlBprp* elwoliNW
production
Frloory aluotnuo
production
•reduction
•reduction
Frloory aluelnue
production
Frloary aluelnue
•reduction
Frloory aluelnue
•reduction
Frteory aluelnue
production
Frloary aluelnue
production
Frloary aluelnue
Production
Frloary aluelnue
production
Frloary aluotnuo
production
Frloary aluelnue
production
Frloary aluotnuo
production
Frloary aluolnue
production
Prloary aluelnuo
production
CnlUlQN MUM ICC COM tJUMION FACTO*
Frcbake coll WJOOI01 I.I Ik/ ten
product
•retake- cell MM01M O.f Ik/ten
product
Frebake cell 1O3OOIOI J.I Ik/ton
product
Frekaka coll 303O010I 1.4 Ik/too
product
Frokake cell 301OO10I 0.4 Ik/ton
product
Frebake celt 30300101 24.0 lk/te>
product
Mite* M
•at ten Al
eolte*, M
Mite* Al
Ml ten Al
i Mlten Al
Frobake celt 30300101 20.0 Ik/ton eolton Al
product
Frekake cell 1030OIOI 22.1 Ik/tot
product
Frobake cell 30300101 1».0 Ib/tof
product
i Mlten Al
i Mlten Al
Frobako coll 10100101 22.1 Ik/ton Mltm Al
product
Frobake cell 10100101 4.2 Ik/ton
product
Pr.b.ka coll 10100101 0.2 Ik/ton
product
Probate coll 30300101 0.4 Ik/ton
product
Prabaka call /fuel tlva. 103OOIO1 1.2 Ib/ton
product
Pr.b.ka col 1 /fualtlvaa 10300108 1.0 Ib/ton
product
Vortical Sodarbore atud 30100101 11 Ib/ton i
call product
Vortical Sodarbare atud 30300103 11 Ib/ton i
call product
Mlten Al
oalten Al
oolten Al
eolton Al
eolton Al
niton Al
10 It an Al
NOTE*
Fartlculato flu*
Caaoaua fluoride
scrubber
1
ride, koped on teat data, opray to*Mr
, kaaad on toat dote, floatlno bed
KFfJCN
-
f7
FartlcuUte fluoride, booed en ta.t date, ftoattnt bod »7
scrubber
taseouo fluoride
dry ocrubker
'articulate fluo
filter dry ocrub
Uncontrolled, «a
. booed MI teat data, coated ket filter
ride, kaped on toat date, coated bap
DOT
aaoua fluoride, based en toot date
Uncontrolled, partlculate fluoride, kaoed en toot data
Baseoue fluoride
collector
Fartlculote fluo
collector
Caaoouo fluoride
Fartlculate fluo
cyclone
Caaoouo fluoride
acrubbar
. kaeed on test data, eeloolono to
ride, kaped on toot data, eeloolono to
, kaoed on toot data, oultlple cyclone
ride, kaoed on toot data, eultlple
, kaaed on toat data, dry aluelna
Fartlculato fluoride, baaed on toat data, dry aluelna
•crubbor
Gaaoouo fluoride
. baaed on toot data
Uncontrollad. aaoaoua fluoride, baaod on teat data
Uncontrolled, partlculato fluoride, baaod on teat data
»7
f7
"
»7
*7
»7
F7
»7
»7
»7
»7
*7
»7
»7
-------
Poo* Me. 114
0*/21/*O
POLLUTANT
Flu,
Flu,
Flu.
Flui
Flu.
Flu,
Flu,
Flu,
Flui
•ride
srlde
•ride
wide
•ride
irlde
irlde
•ride
vide
Fluoride
Flu,
irlde
Fluoride
Flu,
arlde
Fluoride
Flu,
•rlne
Fluorine
Fluorine
CM
Nunoto.
14*04400
14*84488
14*84480
14*04400
1 4*04400
14*04400
14*04400
14*04488
14*04400
14*04408
14*04400
14*04488
14*84488
14*84488
7782414
7702414
7782414
OK
COM
M14
1114
1114
1114
1114
1114
,114
1114
1114
1334
1114
1114
1114
1114
2874
2874
2874
INOUOTIIAL PDOCni
Prlnory elueleue
•reduction
Prleory oluelnue
•reduction
Prleory eluelnue
production
Prlnory eluelnue
»r eduction
Prleory oluelnue
production
Prteory Iluelnue
production
Prlesry oluelnue
production
Prleiry oluelnue
production
Prleory oluelnue
•reduction
Prleiry oluelnue
•reduction
•roductlon
Prleiry oluelnue
•reduction
Prleiry Iluelnue
•reduction
Prleiry Iluelnue
•reduction
Phosphoric ocld
•roductlon - eet prociss
Phosphoric ocld
•roductlon - Met precis*
Phosphoric icld
MINION OOUOCf
Verticil Soderbere •tool
cell
Verticil lederboro etud
cell
Verticil Sederberf stud
coll
Verticil Oederbero stud
coll
Verticil Soderbere, stud
Mil
Verticil toderberi stud
coll
Verticil Soderbere stud
Mil
Verticil Soderberi stud
coll
Verticil Soderbere stud
Mil
Verticil Soderberf stud
coll
Verticil Sodorbero stud
coll
Verticil (oderbero otud
cell
Verticil Soderbere stud
colt
Verticil Sodorbere. stud
coll
Condsnsor
Cyptue settling ponds
ftuctor
OCC COM
M300IIO
IO3001IO
10100101
MMOIOI
10300101
J010010I
J0100103
IOI00101
J0300101
10100101
10300101
10100101
10300101
10100101
1010140]
30101402
10101401
HUSSION PACTO*. NOTtS •»»»
• r oiii • n n L - - - —..-!. i ----,„ -•-----------.•-—« .•••••j— •.---— i i . •-•»•
4.» Ik/ten
ereduct
l.f Ik/ten
•reduct
O.I Ib/ten
•reduct
0.1 Ib/ton
product
I.I Ik/ten
•reduct
t.I Ib/ten
•reduct
20.1 Ifc/tei
•reduct
*.I Ik/ten
•reduct
O.I Ib/ten
•reduct
2.1 Ib/ten
•reduct
O.I Ik/ten
•reduct
0.4 Ib/ton
product
20.1 Ib/to,
•reduct
4.7 Ib/ton
product
eelten
eolten
eelten
eelten
eelten
eelten
M
Al
Al
Al
Al
At
I not ten Al
eelton
eelten
eelten
eelten
eolten
Al
Al
Al
Al
Al
i eelten Al
eolten
Al
41:2 Ib/ten icld
1.12 Ib/ton ictd
$4.4 Ib/ton
Fuoltlvee. eeeeoue lluerlde, kised en test dot*
Fuottlves. portlculoto lluerlde. keoed en teot dot*
Ciseouo lluerlde. dry iluelni scrubber, booed en test
dito
rirttculito lluerlde. dry oluolni scrubber, booed «•)
tost doto
Ciseeuo lluerldo, scrubber • ISP > eerey screen <
scrubber, biped en teot doto
PirtUulete lluerldo. scrubber • (IP » oeroy screen »
scrubber, biped en teot dito
Coloolens to collector, oeooouo lluerlde. blood en toot
diti
Celssleno to collector, eeeeous lluerldo. booed en test
diti
Ciseeuo lluertde. oeroy touer. booed on test dito
Portlculote lluerlde, oerey teuer. bosed on test doto
Ciseeue iluerlde. venturl ocrubbor. booed en test doto
Pirtlculite tluorlde. venturl scrubber, bosed on tost
diti
Cisoeus lluerlde. Multiple cyclones, booed en test diti
Pirtlculite lluorldo, eultlole cyclones, bised on test
Uncontrolled, bisod on eiss bilinco
0.7 icres ol pond needed to preduce 1 ton icld
Vf
»7
»7
»7
"
»T
»7
*7
»7
»7
*7
»7
»7
»7
*7
»7
»7
production - w«i »roc*«c
-------
raee No. 1ST
Oe/21/fO
•QLLUTAMT
Formaldehyde
Formaldehyde
Formaldehyde
Formaldehyde
Formaldehyde
Formaldehyde
CM SIC
MUnetft COM SMDUtTRlM. BftQCttt
SOOOO ArnmneU product Ion
SOOOO Coal combustion
SOOOO Internal combu*tlon
engine* - mobile
engine* - mobile
engine* - mobile
engine* - mobile
en* In** - mobile
SOOOO Internal combuttlon
engine* - mobile
engine* - mobile
SOOOO Internal combustion
engine* * mobile
engine* - mobile
en*lne* * mobile
engines - mobile
SOOOO Internal coBbuttlon
sn*ln«s - mobile
eneincs - Mobile
CnittlOM SOURCf
Intlre procese
Coal -fired boilers or
«ti 1 /commerc/lndu*tr/re*l
nut Mobiles Icetelvet)
Automobile* OioncatalyeO
vehicle*
Heavy-duty dleeol
vehicle*
vehicle*
notorcyclst, 4 -cycle
SCC COM OUSS10M FACTOR
O.OOOIt Ib/ten esehelt
produced
1 I70.S ID/IOCI2 itw
2 7.1 « IOC-0 * I. U* N
I0f>« Ib/mlle
Ib/gal
t o.oom u/Mi
2 0.00121 Ib/gal
2 O.O0309 Ib/gal
MOTtS
Con tret uncertain
Uncontrolled, basod en measured melt, factor*. InMi
data to characterise eels, by boiler type
•a**d on eml*e. te*t data, use lower value for low
mileage cars/higher value for high mileage cars
•lleage cars A higher value for high mileage cars
mileage care A higher value for high mileage car*
•lleaee car* A higher value for high mileage car*
•lleage car* A higher value for high mileage cars
Based on emlss. t**t data* us* lower value for low
•Ueage ear* A higher value for high mileage cars
mileage car* A higher value for high mileage car*
iaaed on emte. teet deta. use lower value for low
•lleaee, car* A higher value for high mileage car*
• Ueage car* A higher value for high •lleage car*
•lleage car* A higher value for high Mileage car*
Darlvad from total aldehyde emissions data
lOt
10*
10*
-------
Pot* *k. IM
O*/2I/M
MLLUTAHT
CM SIC
MURK* COM IHDUtTtlM. MUCH*
tnlMlOM
KC COM DIIMIOM fACTO*
NOTM
KFCMMCt
Forooldohydo
FoTMldokyd*
lotornot contention
ontlnoo - oobllo
loAoro.%1 codkutttoK
onolnoo - ototlonorv
IntorMl cookuotlon
onolnoo - ototlonory
Ut«rit>l CMbuitlM
•nvliw* • •trtlwiwy
Turk* wo» or Mttoa
>lrcr«it
«u turklM*
(••-llrod r*cl»r*c>tuc 2
•AfltltOfl
••••ltn« *»d 202
mdu«trl»l
t.oom
lorlwd «rM total aldohydo oolnlono *«t«
»,»« tb/lOCll Itu Mot Unconlrollod. calculated baoed on entlneerliiu lud*eo*nt
Input
11.211 Ik/10112 Itu koot Uncontrollod. colculotod koood on ontlnoorlnt Judtooont
Input
10.410 Ik/10112 Itu koot uncontrollod, colculotod kMOd on onolnoorlnt Judoooont
Input
104
10*
104
Forooldonydo
FoTMldohydo
Forooldohydo
Fornoldohydo
Foroaldohydo
cUI/ln>tltullo«*l 10100*
Natural oao
Htturol too
Ion Oooottlc
Hood cookuotlon
220.1 Ik/10112 Itu ho*t Control ototuo unopocKlod. koood on oourco tooto
Input
0*7 lk/IOCI2 Itu hoot Control ototuo unopoclllod. koood on oourco tooto
Input
11.12 lk/IOEI2 Itu holt Control ototuo unopocKlod. koood on oourco tooto
Input
Oll-
-------
Fate He. 1C*
Ot/21/tO
POLLUTANT
Forealdohyde
Forealdehyde
Forealdehyde
Ferial dehyde
Ferealdenyde
Farealdehyda
Ferealdehyde
Forealdehyde
Forealdehyde
Feroaleehvde
Foreatdohyde
Foreal dotiyde
Forealdohyda
Forial dahyda
CM *IC
NUnKR COK INDUSTRIAL FMCMI
SOOOO 01 Internal ceebuatlae
enelnee - noblle
SOOOO 01 Internal coebuaUon
anginal - eoblla
SOOOO 01 Internal coebuatlen
•ntlnea • eoblle
SOOOO 01 Internal coebuitlM
englnea • eoblle
SOOOO It Internal coebutUen
enelnaa • eoblle
SOOOO It Internal coebuaUon
anginal - eoblle
SOOOO It Internal coebuatlan
englnea - eoblle
SOOOO It Internal ceaDuatlofl
anemia - eoblle
SOOOO It Internal ceebuitlon
anginal - eoblle
SOOOO It Internal coebuitlen
onglnea • eoblla
SOOOO It Internal coebuitlon
anginal - eoblla
SOOOO It Internal coibuitlon
•nelnal * eoblla
SOOOO It Internal coebuitlon
anginal * aoblla
DliniOM tOUKI
lleial eevered
cenatructlon «»il»eant.
Mhealed tractor
Oleial rouered «are
eaulaiant. elacellaneoua
t...ll« ,<»»•«,
-------
Fete It*. 140
0»/2I/»0
•OUUIMTT
CM IIC
NUttO. COM INMimtM. FMCO*
BIIUION
ICt COM miWIM MCTO*
Forestdehyde
Foresldehyde
Forssldehyoe
Fereeldehyoe
MOM 14 Interne! (oetoustlon
MOM 1* InterMl ceebmtto*
MOM 14 Internsl coebustlo
•nelne* - eobtle
MOM 14 Internsl coebustlen
construction
construction dwloxnt.
•otor tradBr
ino ftoworod
conttructloA Mvlftttwntf
roll«r
CualtM »OMT•/•>>
(.00217 lb/s«l
BsrlvW IrM totsl slMydo ssilsslons data
Bsrtvod troo) toks> atoohydo soisslons d*t>
Dsrlvod fr«s> totsl (tdohydl oolsstons dst.
Ovlvcd 4rosi totsl aldohydo sslsslons dst*
Foreeldehyde
14 Internsl coebustlo
enolnos - eoblle
24»1 Fsrtlcle bosrd
esnuf scturlnf-uood
conktructlon o«ulo»ont,
wh««l tatsl sldskyos ssl.slons dst*
107M70I O.It lb/et( t 1/4* Survey e< eeresn orstlcle bosrd slsnts. sverses
Forest dehyde
SOOM 24*1 Fsrtlcle bosrd
esnulscturlno-tM
0.22 - O.t4 Ib/ni * 1/4* Survov »l tour stsnt* by Hst'l Council I Fsrtlcle bosrd
Frecsss vonts
I070070I O.S1 Ib/esl * 1/4-
1 *ssln HCHO In roslnit.7- ut 1, I sit
uncontrolled
211
Fores! dohyds
SOOOO 24S] Fsrtlcle bosrd
1070070] 0.41 - .4S Ib/esl I 1/4-
1 DsslnUb/lOO ID bosrd) 7.1. tlssi 4.1-1.7 nln/srss.
tsw I20F. EKCSSS HCHO In r*slni«.7- »( 1. I Fit
uncontrolIsd
Foresldenvde
24S] Fsrtlcls bosrd
•snufscturlnfl-w
Frocsts vsnts
10700701 O.«l lb/ssl • 1/4-
I Rs>ln
-------
Pa*« N*. 141
0*/21/*0
POLLUTANT
CM «IC
HUT*** COK INDUSTRIAL PftOCSM
HUSSION SOUKCI
SCC COM HUSSION fACTOA
MOTIS
For»ald«hyd«
Forataldahyd*
ForMldohydi
MOM 14*1 rtrtlcl* bur*
•onufoctvrlii.-Mood]
•rncmiM
SOOOO 24*1 Portlcl* bo«rd
•«nu<>cturln«-»ood
•reCMtlnt)
SOOOO 24*1 rorttclo botrd
•onufocturlnt-wood
•roco««lit4)
SOOOO 24*1 Portld* boord
•onufocturl na.-wood
•roc ooolno
SOOOO 24*3 PortUU bo.rd
until *cturln*-uood
procoislnfl
SOOOO 24*3 PortlcU bo.rd
•«nuf«ctur
rroc«*fl vent*
Prec*«« vant*
Procaia want*
30700701 *.3f U/Ml « 3/4"
10700703 0.31 Ib/M* • 3/4"
30700703 O.2S Ib/M* * 3/4*
30700703 O.S* Ib/aa« • 3/4*
30700703 0.7* )b/M» * 3/4*
307O0703 0.42 Ib/aal * 3/4*
1 *d*l»(lb/IOO Ik boordl 4.2. tlMi 4.t-i.7 iln/oro*.
tow 120F. EMM. HCHO III mini*.7 «t I. I lit
uncofttrad
1 *.r«>.
t«w I20F. Cxc«» HCHO I* rmHmt.1 vt I. 1 »)t
uncontrcd
I Mlla «.l. tlMi 4.1-1.7 .in/pr.«.
t«w 320f, E>c»« HCHO 111 r««lni».7 Kt I, I >lt
uncontrdd
I M«ln 1.1, tlm 4.1-l.i .ln/.r««.
t»r 3*0f. CKC.M HCHO In rd.lni 7.7 «t I. I »lt
uncontrad
I *«l«llb/IOO lb bo*rd> *.*. tlMi 4.1-1.4 •ln/»<-««.
t»» 14OF. f»c.» HCHO In roolni 7.7 Ht >. 1 »lt
uncontrod
I MUndb/lOO lb bo*rd) 1.0. tin. 4.1-1.4 >tn/or««,
t«« I40F. Inc... HCHO In r.iln. 7.7 Ht \. I olt
uneontrad
211
Foruldchyd*
SOOOO 24*3 f«rtlel« board
•«mi f «ctur 1 n
Procaia vant*
30700703 0.84 Ib/M* 8 3/4"
S ftaatfiUb/100 lb board* 8.0. tiaai 4.1-8.4 aln/praa.
t*o 340F. CKcata HCHO In raalm 7.7 wt S. I pit
uncontrad
For oal doh vdfl
SOOOO 24*3 P«rtUI* board
•u\u< *cturtn«-t*ood
Procaa* vanfes
30700703 0.22 - 0.33 lb/*af • 3/4"
X MaalnUb/lOO lb board* 8.4. tiaai 4.3-4.* ain/araa.
taw 320F. Eitcaaa HCHO In raalm 3.2 wt 1, 1 alt
uncontrad
r*orM!d€hyd«
24*3 f.rtlcl. bo.rd
•.nuf tctur1no-wood
orococtlnf
24*1 r.rtlclo bo.rd
o.nul.cturln«-wood
Procoto vonto
Procot. vontt
30700703 0.31 - 0.3S Ib/Ml * 3/4-
1 Ko.lnllb/100 lb bo.rd> *.l. tlooi 4.3-4.* nln/proo.
t«» 320P. CXCOH HCHO In r«lni 3.2 ut t. I olt
uncontrod
30700703 0.4S - 0.4* lb/««l
I HoilnUb/100 lb bo.rd) *.*. tlMi 4.3-4.* .ln/pr.i.
(«•!> 320F, E»co» HCHO In r.ilm 3.2 wt I. 1 .It
rorMldohydo
24*3 Pftrtlclo board
•*nuf «cturinf-wood
Procaca vents
10700703 0.7» - 0.11 lb/««l • 3/4' > HMlnllb/100 lb bo>rd)IO.O. llm 4.3-4.> mlntrrft.
t»p I20F. E»c.» HCHO In r.tln, 3.2 nt I. 1 pit
uncontr.d
For«ldco« HCHO In 211
ro.ini S.* wt X. 1 olt uncontrad
-------
Paaa Na. 1*2
0*/XI/M
POLLUTANT
CM tIC
Nunm COM MMtniM. MOCCM
mission towct
UC COM OIIUION PACTO*
Horn
SOOM
24»1 Partlcla kaard
aanu< Ktwlna-watf
aroCMaUf
24t* Partlela kaard
procaaalat
24»] Particle kaard
Praca.a vanta
fracu* vant«
Procaaa vanta
10700701 t.l lk/aa« • :
M70070I t.l lk/«l • 1/4'
10700701 l.t Ik/Mf * 1/4'
S F.aalallk/100 Ik kaard) JO. taap 2*4r. Cxcaaa HCHO la
rMlm 0.4 Mi t. I Pit uncMtrad
X M.laUb/100 Ik kaardl 10, tn» 2I4F. Ixca.a HCHO In
raplni O.S Ht X. I pit uncantrad
X HaaliiIlk/100 Ik board) SI. taap 2I4F. fxcaai HCHO I*
r«lm 0.4 «t X. I alt uncontrad
til
Faraaldahyda
SOOOO 24tl Partlcla kaard
Prac«i« v«it«
10700701 t.Z lk/aa< t 1/4*
X Kaaip.uk/I00 Ik kaard) II. taap 2I4F. fxcaai HCHO In
ratlni 0.4 lit X, I Pit uncaatrad
Faraaldanyd*
SOOOO 24»J Partlcla
SOOOO 24tl Partlcla kaard
froc... v«nt>
fracatt iMAt*
10700701 1.2 Ik/aal t 1/4*
10700701 4.0 Ik/aif 0 1/4*
I Malii Ilk/100 Ik kaard) II. taap 2I4F. Cxcaaa HCHO In
railni 2.* nt X. 1 Pit uicantrad
I llMlnllb/100 Ik kaard) 12. taaa 2I4F. Cxca» HCHO In
raalni 4.0 Mt X. 1 pit uncantrad
Faraaldahvd*
SOOOO 24»I Partlcla kaard
Prac«n v«nt«
10700701 4. a Ik/aaf a 1/4'
I KaalnUk/100 Ik kaard) II. taa* 2I4F. Cxca>< HCHO In
rallni S.7 lit X. I Pit uncantrad
SOOOO 24»J Partlcla
10700701 2.4 lb/a.« t 1/4"
X «««ln(lb/IOO Ik kaard) 0.4. taap IMF. Ixcaaa HCHO In
raalni JO «t X, I pit wicantrad
Faraaldahyda
Faraaldahyda
24»1 Partlcla kaard
pracaaatna
24*1 Fartlcla kaard
aanuf acturlnl-hw
Prac«> v*nt>
rroc<» v«nt>
10700701 2.1 Ik/aal I 1/4*
10700701 1.4 tb/aal • 1/4-
I *ailn1 Partlcla board
a«mi< • 1/4*
I ««»ln(lb/100 Ib board) 2.1, taap I1BF. Excaal HCHO In 211
ratlni 11 yt X, 1 pit uncontrad
-------
F.eo He. 141
0»/2t/»0
POU.UTAMT
FerMldehvde
Foreeldohyde
Fareeldehyde
Foreeldehyde
ForMldehyd*
Fareeldehyde
Pore.ld.hyOe
Foreeldeftyde
Foreeldehvde
Fareeldehyae
Foreeldehyde
Fera.ldehyde
Fore.ldehyde
Fore.ld.hyde
Fare.ldehyde
Fore.ldenyde
CAS fIC
NUnOC*. COM INOMtMM. PMCIM CHIM10N SOURCf
tOOM 24*1 Particle bo«rd Procee* vent*
proca**tno.
50000 24*1 Portlcl* botrd Pr»ce.« vent*
e*iwf«cturln*-eeed
proca**iAfl
SOOOO 24*1 U.forbevd MmtlMtur* Fro** oper.tlon
SOOOO 2121 Itolealne-lerMldohyde Fare.ldehyde .tor.**
r**ln production
SOOOO 2«2I H*l*elne-lorMldehyde Proe... - toner. 1
re*ln production
SOOOO 2121 Fnenal-'oreeldenyde r«.l« Foreeldehyde itor.ee
production
SOOOO 2121 Phenol -lor..ldehyde r«ln Prate** - eenerel
production
50000 2121 Paly.cot.1 roiln Fore.ldehyde otor.ee
production
(0000 2*21 •olyuatel re.U Froc*« - eener.l
production
50000 2B2I Ure.-foreeldeft*de re.ln Foreeldehyde •tore**
production
50000 2121 Ure.-lare.ldehyde re. In Proce.* - lenerel
production
50000 2145 Acetone/phenol Cle.v.oe lectton vent*
o.nul.cture Iroe cueene (cooblnedl
50000 2045 Fnth.llc uihydrld* PhtB.llc .nhydrlde
production condenvor*
50000 2B45 Fhth.llc .nhydrlde Phth.llc .nhydrldo
production conden.er*
50000 2845 Phth.llc .nhydrlde n.ln proce.* Inclner.tor
SCC CMC
10700101
107007
407
10101(42
407
10IOKOS
301011
301011
407
3010! 13 J
10120211
1O101*
30101 •
10101*
mission FACTO*
*.S Ib/e.l • 1/4-
0.47 ib/Mf el Mlerbavd
praduced
4.O4-0. 4 Ib/tea »» 171
loTMldehyde u.ed
O.M-I.O Ib/ton el 171
loraeldehyde w**d
0.04-0.4 Ib/ton el 171
lore.ld.hyde u*ed
0,10-1.0 Ib/ton el 171
lerultfehyee u.ed
0.04-0.04 Ib/ton el 171
lereeldehyde u*e
0.11-0.74 Ib/tan al 171
loreeldehyd. u.e
0.04-0.4 Ib/ton ol 171
lore.ldehydo u**d
0.1-1.0 Ib/ton al 171
loreeldehyde u*od
S.2 * 10E-7 Ib/ton phenol
p
4.2 Ib/ton PA proauc.d
0.14* Ib/ton PA produced
4.2 Ib/ton PA produc.d
NOUS
t HelUUkSlM Ib baerd) 4.0. teep IMF. Cxee*. NCNO In
re*Ui 11 ut I. 1 Fit uncontred
1 *..ln(lb/IOO Ib bau-d) S.7. too* IMF. Cxce>* WHO In
reelni II »t I. I pit aacentred
Aver.ee e*l**lon lector lor three dlllerent r**ln
•y»tw»
Uncontrolled, bull unclur
Uncontrolled, boot* uncle.r
Uncontrolled. b**i* uncleer
Uncontrolled. b**l* uncle.r
No Inloreetlon M* ev.II.bl* en the b..l> al the**
••tleete* or tha type* ol control Involved
No Inlereetlon MO ev.ll.ble en the be*l* al the**
o*tleete* or the typo* el control Involved
Uncontrolled. b.«l. unclev
Uncontrolled, b.el* uncUer
Controlled
-------
Pete «•• 144
Ot/21/M
POLLUTANT
CM IIC
Hum* COM iNMsmiM. PMCCM
(MIMION fOMCt
tCC COM WIMION MCTM
MOtft
FeTMloMwd*
2*41 Pkthallc anhydride
production • mepkthalo
IUU proceeo locUmretor JOI01P 0.14* Ik/tM M produced COTtrolled, te»t date ana] MOlneerlno JudoemMt
120
Foroaldohyde
Formaldehyde
MOOO
XMI Pktkollc anhydride
productlM - KylMO
Phtlullc Mkydrltfa
»r«ductlwt • Xylan*
•TKMl
IUU process Incinerator 3)0101* 0.141 Ik/tM fK produced Controlled, all aldehyde aaaumed to be formaldehyde
IUU proceas InclMTator 30101* 4.2 Ik/tM ** produced Uncontrolled, all aldehydes reported aa formaldehyde
(0000 2(4* 1.4-kutanedlol productlM Formaldmhyde etoraoe
0.01 - 0.4 Ik/tM 17X
Mo l« o« tkoie,
eetlMtoe or th« typoe of controlo involved
120
Formaldehyde
SOOOO 214»
>ro*Ktlon Fro<«t -
301250 tor»*
Foratldohvdo ttor***
Htndllrti
10112005
foroal. moln. prod.
0.04 Ik/tM of 171
*ar»«l . coin, produce
0.004 to/ton el 171
loro«l. eeln. prod.
0.02 Ik/ten al 171
loroal. coin, produce
Controlled by thermal oxidation, hypothetical plant
Kith formal, produc. tap. of ».« x 10C7 Ib/yr
Uncontrolled, baaed M hypothetical plant ailth
formaldehyde productlM cap. of f.»2 x 10C7 Ib/yr
Controlled by vont (crubber, hypothetic*! plent Kith
(ore.l. production CO. of ».»2 « I0£7 Ib/yr
Uncontrolled. b«i«d on hypothetlcel pUnt Kith for»l.
production cwiclty of ».»2 *. IOC7 Ib/yr
Formaldehyde
Formaldehyde
2l4f Formaldehyde production,
metal oxide catalyst
process
284« Formaldehyde production,
silver cetalyst process
301120 0.0008 Ib/ton of 371
formal, sola. prod.
10112005 0.74 Ib/ton of 37X
foreal. solution prod
Controlled by vopor recovery, hypothettcel plent Mtth
(ore.l. production c»p. of ».« x 10E7 tb/vr
uncontrolled, based on hypothetical plant olth
formaldehyde production cap. of ».»2 x 10C7 Ib/yr
Formeldohyde
2849 Formaldehyde production.
silver catalyst process
30112005
-------
Fate Dm. US
0»/21/*0
POLLUTANT
Formaldehyde
Formaldehyde
Formaldehyde
Formal dohydm
Formaldehyde
Formaldehyde
Formaldehyde
Forulaahyd*
Formaldehyde
Formaldehyde
Forealdehyde
Formaldehyde
Forealdahyde
Formal dahydo
Formaldehyde
Formaldehyde
Formaldehyde
CAS SIC
MfM* COM IMMTIMAt PMCCSt tnl5$IOPJ SOUKX
9OOOO 2«4» Foroaldohyde production. Absorkmr
•liver catalyst procesa
90000 214* formaldehyde production. Formaldehyde iterate
•liver catalyst process
90000 214* Forealdehyde production. Formaldehyde atorate
•liver catalyst process
9OOOO 214* Formaldehyde production. Formaldehyde etarace
•llvmr catalyst procass
90000 214* Formaldehyde production. Handllne
ellvor catalyat procesa
90000 214* Forealdehyde production. Hindi In*
•liver catalyst process
90000 214* Forealdehyde production. Product fractlonator
•liver catalyat process
50000 2S4* Formaldehyde, production. Product tractlonator
90OOO 214* Forealdehyde production. Product fractlonator
silver catalyst process
90000 294* Forealdehyde production, 5tartup vent
silver catalyst process
90000 294* Hexamethyleno-tetraelne Foroaldehyde atorame
production
90000 294* Henaeathylone-tetramlne Procais - oanaral
Production
90000 214* Pentaarythrltol Foruldahvde stars**
production
SOOOO 294* Pontaarythrltal Proc.cs - sanaral
production
50000 2.4* Trl.athy,ol.ro,.n. ror...d.hy<. .««•„.
Production
50000 294* Trlmethylolpropana Procaia - nnaral
production
50000 2171 Urea (solid) production Drue sranuUtlon
tee COM
10II20M
407
407
407
101 120
JOI120
101 12004
10112004
10112004
101120
407
10101425
40T
101250
101250
101250
10104004
UUMtON FACTO*
0.192 Ik/ton m< ITS
fmrmal. motm. mrmd.
1.04 Ik/to* of S7S
formal, •aim. produc*
0.004 Ik/tan of 171
formal, win. prod.
<«.OOI1 Ik/ton of 179
formal. Ml*, prod
0.02 Ik/ton of 171
formal . eoln. produce
O.OOOi Ik/ton ml 171
formal, sola. prod.
0.44 Ik/ton of 171
formal, soln. produce
0 Ib/ton of 37> formal.
0.014 Ik/ton of 171
formal, eoln. prod.
0.2 Ik/tan of 171 formal.
soln. produced
O.I Ib/ton of 171
<0.7I Ib/ton of 171
0.004-0.44 tb'ton of 171
2.4-5.4 Ib/ton of 171
formaldehyde used
0.02 Ib/ton of 171
0.141 tb/ton of 171
for»4ld«hyde u*ad
mm
Controlled ky flare, based M hyeothotltlcal plant nlU
formal, production cap. of ».*2 » IOE7 Ib/vr
Uncontrolled, kaaed on hypothetical plant Mlth
formaldehyde production capacity of *.*2 x IOE7 Ib/yr
Controlled by vent scrubber, hypothetical plant Mlth
formal, production cap. of *.*2 x 10C7 Ik/yr
Controlled kv thermal oxidation, hypothetical plant
Mlth formal, produc. cap. of *.*2 x IOC7 Ib/yr
Uncontrolled, kaaed on hypothetical plant Mlth formal.
production capacity of *.*2 x IOC7 Ik/yr
Controlled ky vapor recovery, hypothetical plant Mlth
formal, production cap. of *.*2 x 10E7 Ik/yr
Uncontrolled, kaaed on hypothetical plant Mlth
foroaldehyda production cap. of *.»2 x 10C7 Ik/yr
Recycle to absorber, kaaed on hypothetical plant Mlth
foroaldmhyde produc. cap. of *.*2 x 104*7 Ib/yr
Controlled by mater scrubber, hypothetical plant Mlth
formal, production cap. of *.*2 x 10E7 Ib/yr
Uncontrolled, based on hypothetical plant Mlth
forealdehyde production cap. of *.*2 x IOE7 Ib/yr
No Information Mas available mn the baals of theae
No Information Mas available on the baala of theae
Mo Information Mas available on the basis of these
No Information Mas available on the basis of these
astleataa or the typas of control Involved
No Information Maa available on the basis of these
No Information Mas available on the basis of these
sstlsatss or ths typas of controls Involved
•OTPXN
104
104
104
104
104
104
104
104
104
104
104
104
104
104
104
104
104
uraa producad
-------
Pee* No. U4
O»/lt/M
POLLUTANT
Forealdotiydo
Foreatdehyde
ForeeteMtyde
Ferealdehyde
Ferieldehyde
ForMldehyde
Forealdehyde
Ferealdohyde
Forealdehydo
Forealdehyde
Foreoldehyde
Forealdehyde
Forealdehyde
Forealdehyde
Forealdshyde
Foroaldehyde
Forealdehyde
CM tIC
NUnOf* COM IMMtmiM. PMCftS
10000 M71 Urn (sell*) production
fOOOO 2071 Urea production
IOOOO 2071 UTM (sol 141 production
SOOOO 2071 Uru <••!!«» production
(0000 2171 Ur«. (solid) production
SOOOO 2*11 Petroleue refinery
10000 2*11 Petroleuo refinery
SOOOO 2*11 Petroleue refinery
SOOOO 2>SI Asehsltlc concrete
production
SOOOO 32*4 Flu* •tt«Hl>tIaa I«M|
•!«•• 4ltMr production
SOOOO J2»« Fl«oo tlan >«>ol
fflatt llbor production
SOOOO 11** FUM »tt«nu>tlon Hoot
flaco llbar production
SOOOO J2»« Flu* ottonuttlon nool
•!••• flbor production
SOOOO 12*4 KoHry win vool •!•••
41bor production
SOOOO J2»» llotiry ipln Bool •!>•<
(lb«r production
90000 32>t »ot«ry «pln wol »l«n
ilbor production
50000 lit* «ot»rv do,>
Fluid cokor burnor
Fluldliod bod cittlytlc
crtcfcor unit roftftnorotor
IUuln< bod ITCO
roaanorAtor
FUnt «t«ck
«-ll product production .
totil lino
•-It product production,
curlni
Ductbo«rd production,
tattl lino
Ductboard production,
curlna and coollnt
Ouctboard production
N*«>/y d«n«lty product
production
R-lt/ft-ll production
ft- 14 product production,
curing and coollna
tec coos
JOI04OM
IOI04OIO
I010401O
10104011
10I040II
J040I20I
10*00201
10400301
105002
115012
115011
115012
115012
10501204
10SOI204
10501204
315012
IHIWION FACTOR
•.OOM lb/to» 4)1 polld
yroo produced
0.01* Ik/tM *i «olld
urvo »r«duc«d
O.OOOO Ib/ton o< >olld
ur«« prooTucod
0.004 Ik/ton o« Mild
urao produced
0.001 Ik/to* *f oolld
uroa produod
I.I* Ik/1000 obi froah
<.«d
4.14 lb/1000 kbl ltk CO boller/fSP. derived 4roe eelsslen
teat date for total aldehydes
Controlled Mlth CO fcoller/ES*. derived tree eelsslen
teat dote lor total aldehydes
laaed en 1 lei tod test data, cyclone/net scrubber
control
Controlled »UO an MWAF
Controlled >lth en HVAF
Controlled Kith an HVAF
Controlled ulth an HVAF
Uncontrolled* nay not represent all oreanlcs In exhaust
atroae
Uncontrolled, nay not represent all oreanlcs In exhaust
streae
Uncontrolled, Bay not represent all orsanlcs In exhaust
atroae
Controlled with a venturt scrubber
MFWB
10*
10*
104
104
104
104
104
104
*7
171
171
171
171
»7
»7
• 7
173
-------
P.M (to. l«7
OVII/M
POLLUTANT
Foruldekydo
'"••"-'«•
Fora.ld.hya.
'"""*-
'«*-"•
Foruldtfiyd.
'«•—"*
For*>Id*hydo
""•«**v-
Fornaldnhyoo
Fornaldohyd*
Fornal dattyda
Fornaldahyde
CM SIC
NUUC* COOf
SOOOO J2U
SOOOO J2».
SOOOO J2t»
soooo im
SOOOO 12».
SOOOO J2f*
50000 I2M
SOOOO J2»t
SOOOO 12»*
SOOOO J2»*
SOOOO 401
SOOOO 15
1NOU9TH1M. rftOCfS9
Rotary aptn iiooi tlaaa
ft bar production
•otary apln wool tiaaa
flbar production
ftotary apin anol tlaaa
fibar production
Rotary spin wool tlaaa
41 bar production
Rotary apln tool tlaaa
flbar production
Rotary aptn wool tlaaa
flbar production
Rotary apin wool tlaaa
Ubar production
Rotary apln MOO. •!*••
flbar production
Rotary apln wool tlaaa
flbar production
fibar production
Rotary apln MOO! tl***
fibar production
flbar production
Internal coabuatlon
analnaa * ooblla
Intarnal coabuatlon
antlnaa - aobila
combustion
combustion
co«bu*tton
CnlttlOH SOURCt
R-M product production.
«-lf product production,
curlnt and toolin«
(*-!> product production,
foratng
P.- II product production
P.- II product production
Haavy danatty incutation
production
Ouctbeard production
R-I« product production
R-ll product production,
fornint and curtn*
Curing procaaa
L.C...,,...
Imt tlrertft
r.cow.ry l.ctllty
r.cov.ry IftCtllty
r.cov.ry t.clllty
sec COM mission r*CTM
IISOI1 «.« Ik/to. «I*I(M4
M-educt
1ISOIJ ».l Ik/tM Unllked
M-«kKt
1ISOI2 «,* Ik/ton «Ul.li«d
»r»duct
JIS012 O.SO Ik/tM llnMi^
.rtduct
1IS012 O.I Ik/tM flnltlw*
product
I1S01I «.* Ik/tot M*l»h«4
product
I1SOU O.S Ib/ton «lnl«h.d
product
1ISOI2 0.* Ik/tan llnllh.d
product
IIS01I 0.4 Ik/ton Onlm.d
>r«4uct
product
30501204 O.JO Ik/tM /t«l
coabuatad
Mn.
Cwtr.llod mtk . MHturl KnikMr
Contrail^ «ltk • Mt scrubs*-
Contrall.d Mltk * Mt Krukbor
Controlled «ltk . Mt ISP
Controlled yltk M MMF
Contr.ll.d «ltk M liKlnoratio*
Controlled ultk . Mt ISP
Control l«l Kith o Mt ISP
Controlled «ltk * Mt 1ST
aizad facllitlaa
Uncontroitod. aworaoa ajolaalon factor for 4 dlfforont
alzad facllitlaa
aizad facilitUa
Darivad froai total aldahydo ooiaalon taat data
Darlvod fro* total aldohydo onlaalont dat«
aiauaaa tSI control afficiancy
in
171
m
171
171
171
171
ITS
171
171
171
-------
Paw Me. 141
Ot/2l/*0
potunoait
Ferealdehyde
Foreaidehyde
Foroaldehyde
Forealdehyde
Foreaidehyde
Foroaldehyde
Forealdohyde
Foroaldehyde
Foroaldahydo
Foroaldehyda
Foroaldehyde
Forealdahyde
Forealdehyde
Caaollno
fiaaollno
CM SIC
MunefR COM INDUSTRIAL PROCESS
SOOOO 4tSJ Municipal uaete
ceebuetlee.
SOOOO 4,«SJ Municipal laaate
coobuatlen
SOOOO 4»SJ Municipal eaate
coobuatlen
SOOOO 4t»J Municipal eaate
coebuatten
SOOOO 4fSl Municipal uaete
coebuotlon
SOOOO 4»SI Municipal oeeta
coebuatlen
SOOOO 4»SJ Munlcloal uaote
SOOOO 4»5J Municipal uaate
coebuatlen
SOOOO 4>S1 Munlcloal uaate
SOOOO 4tS] Municipal ueeta
SOOOO 4tSl Municipal uaate
coebuatlon
SOOOO 4453 Municipal waato
coobuatlon
SOOOO SOU Mpn.lt dlatrlbutlon/u>a
CIIIMION MUMX
rut* burn, tmiliiit
rKovcry fMltlttf
ftodultr IftctMTttor
nodul*r iHCiMTAtor
Pr*J*cti4 w
»Ut«-oit-th.j-«rt ••••
burn h««t r^covwy
«*c.mv<
rYBjijctad or
•te>i*-ol-th«-«rt ••••
burn hfj*t r*covwy
Refute darlvftd futl
iactnarAtor
M*fu«« dtirlvMtf #u«l
I net n«r « tor
lUfu** d«rlv«d fuel
lncln«r«ter
nodu.tr st«rv«tl-«lr
cosibustor
Houfttor
L*r«* •••• burn rot*ry
k**t«rM«ll c»«bii»tor built
**t.r i»ao
tlev** burn wktsrwfttl
cevbusitor. built b«lor«
Ent.r* proc«s»
n
Tknk truck lo*U«d with
SCC COM miSSIOM FnCtflol
SOIOOI t.OOM Ik/tee, of naete
SOIOOI 0.0014 IWtee. of uaate
coabueted
SOIOOI 1.4 x 101-4 Ib/tee of
•aate ceeeuated
SOIOOI O.OOS Ib/ton of Hoate
coebuated
SOIOOI 0.0004 Ib/taej of uaate
coebuated
SOIOOI 0.0022 Ik/to* of Mate
coebuated
SOIOOI 1.4 X IOE-4 Ib/ton o<
waate coebuatod
SOIOOI 1.2 x IOE-4 Ib/ton ROF
coebuetad
SOIOOI 1.0 x 10C-* Ib/ton feed
SOIOOI J.S x IOt-4 Ib/ton feed
SOIOOI O.OOS Ib/ton uo/Nt feed
SOIOOI l.S x 10C-S Ib/ton feed
0.004 Ib/ton aaphalt
applied
404001 0.00417 Ib/IOOO 9al
406001 0.00417 Ib/IOOO oal
tranaported
Mom
Controlled by dry alkaline ecrubbor S fabric filter.
aaauoea fM control efficiency
Controlled by ISP. baaed en aourca toata
Controlled by dry alkaline acrubbor t fabric filter.
aaaueee PSS control efficiency
Controlled by ISP. baaed en aource teat
Controlled by dry alkaline acrubbor S fabric filter,
aaaueee til control efficiency
Controlled by ISP, baaed ee aource teata
Controlled by dry alkaline acrubbor t fabric filter.
aeaueea tSS control efficiency
1001 UT fuel only, ISP control only, overall avoraoe
of eeverel aource avereoea. ranee la 1.4 x 101-7 - 1.4
x 101-4 Ib/ton
ESP control only, one data point only
Uncontrolled, overall aver.ee of towel aource
euareeaa, ranee It l.S « IOC-7 - t.l x IOC-4 Ib/ton
Capacity > aOO tone/day. ESP control only, one data
point only
ESP control only, one data point only
Forealdenyde aaauood to bo O.SX of THC
nveraoo of ranee detorelned froe engineering eetleate.
RvP • 10 pal a
Average of range detorotnod froo engineering oatieate.
RVP • 10 pal a
RfFDbO
III
III
III
II*
III
111
III
IM
1*0
ISO
1*0
ISO
«7
»7
-------
rote Mo. 14*
OOU.UTMIT
CM tic
•MtKK COM ittumiM. rmciM
tniuioN
tCG COM IH1UIOM FACTO*
HOTtt
«eeellm
Gasoline
Caaollnt
Caaollne
Caaollna
Caaollne
•OOMiv 411 Tank truck tranaport
100441* 421 Tank truck tranaport
Caeollne
•00441* «I71
•00441* §171
•00441* 1171
•00441* S17I
•00441* SI7I
•00441* 1171
•00441* SI71
•00441* SI7I
•00441* 1171
•O0441* SI7I
•00441* 1171
•00441* SI7I
100441* 5171
•00441* SI7I
§00*41» 5171
Caaollne loading at bulk
teratnale and bulk pi ante
Caaollne loadlnt at bulk
terolealt end bulk plants
CeaolUe loadlnt at bulk
terelnale and bulk plante
Caaollne loading of tank
trucke at bulk tlant<
Caaollne loading of tank
truck! at bulk plant!
Caaollne loading of tank
trucke at bulk planta
Caiollne loading o< tank
trucka at bulk planta
Gaaollne loading of tank
trucka at bulk teretnele
Caaallne loading of tank
trucka at bulk terelnala
truck! at bulk terelnala
Caaollne loading of tank
trucka at bulk terelnala
Caaollne atoraga at bulk
planta
Caaollne atorate at bulk
planta
Gaaollne atorage at bulk
planta
Gatollne storage at bulk
tarelnala
lank truck UHl
entreee loaaea
Tank truck mil ceded -
typical loaeet
•ulk tarelnal vapor
lulk tereUal vapor
eroceaeor
•ulk terelnel vaeer
proce!!or
tplaah laadlnt -
dedicated eoreal terulce
Splaeh leading - vapor
balance aervlce
I loading; -
dedicated noreal eervice
Subeerted loedlng • vapor
balance aervlce
Cplaah loadlnt -
dedicated noreai eervice
Splaeh ioadlnt - vapor
balance aervlce
Subaertad loadlnt •
dedicated noreal eorvtce
Subearted toadlnt * vapor
balance aervlce
atorage tank! * breathing
loaa
Storage tanke - draining
loaa
Storage tank! - filling
leases
Flfced-roof atorage tanka
• breath Int loaaea
40400151
«.H* Ib/IOM Ml
traoiportad
O.OJ4I lb/1000 ••!
tranlporlad
0.041* lb/1000 tal
•aaollu loaded
«. |« - ».» lb/1000 fal
•aaollao loadad
».0017 - ».O1 lb/10CO pa)
•MoliM loaded
11. fJ Ib/IOfI lal
thrmekout
1.11 Ib/IOCI eel
throughput
4.fZ It/IOtJ fal
throughput
l.ll Ib/lOn eel
throughput
11. fJ Ib/lOEl eal
tranaferred
l.ld Ib/IOEI tal
traniferrod
4.»J Ib/IOCI tal
transferred
1.1* Ib/IOEJ gal
tr ana I erred
2.47 X IOC-4 Ib/IOEI tal
threuthput
2 x IOC-4 lb/IOE3 tal
threuthput
5. Of « IOE-4 lb/10£J tal
throughput
0.212 Ib/IOEI gal
throughput
Averato of reeet detereleed free) engineering eetioatt. t7
KIP e 10 pel!
Average »f ranee dotorelnod froe engineering eetleate, »7
RVP a 10 gtie
Controlled by carbon ebeerber. average of 11 teetl. IN
rente nog 0.0021 - O.II lb/1000 tal
Controlled by refrigeration le*
Controlled by tkereal oxidation IM
Engineering eatleate. Rv» • 10 pala »7
Engineering eatleate. «VF • 10 gelt *7
Entlneerlnt eatleate. «vf • 10 pala »7
Inelneerlng eatleate. RV» • 10 gtte »7
Entlneerlnt) eatleate ualne «W of 10 gele *7
Entlneerlnt eatleate ualnt PNP of 10 gtte. »7
Entlneerlnt eetteete uelnt RVP of 10 tile »7
Entlneerlnt eitleate uelnl Rv* of 10 pala *7
Uncontrolled, entlneerlnt eetleate. eeauee fixed roof 9O
Uncontrolled, englneerlnt eatleate, aaauee fixed roof SO
Uncontrolled, entlneerlnt eatleate. aaiuee fixed roof 9O
Converted froe Ib/vr. aaauee 34S day! of operation.
equal throuthput for each tank
-------
•aw Ho. 170
Ot/21/tO
POLLUTANT
Caaollm
Gaeollna
Ciaallna
Eieallna
Eaaol Ira
«...„„.
Giaollna
Giaolln*
Giaollna
Giaollna
HapticMorodtbaniofunn*.
totll
Haptichlorodlbanzofurini.
totll
totll
H*ptichlorodlb*nzofurina.
totil
Heetichlorodlbanzofurins.
totll
CM (1C
NUnK* (OK INCUSTHIAL PMCIS*
•004*1* SI7I CaacliM ataraw at bulk
t oral ml a
•00*41* S171 Eaaallna ataraee at bulk
tar.lnil*
•004* 1> S17I ClaallM ataraaa at bulk
•00441* SS4I Ciiolln* aarketlna
actlvltlaa
•00441* S541 SiMlIM aartatlna
•ctlvltlee
•OO44I* SS4I Ciaalina airkatlnl
•ctlvltlat
•00441* SS4I Ciaallna atoraaa at
•orvlca otitlan*
•00441* 5541 Eiiollna atorita at
oarwlca atitlona
•00441* 5541 EieoUne Itoraaa at
•arvtc* •tatloni
•00441* SS4I Ci»ollna atariae It
aarvlca •titloni
24 rulp'piper alll. trait
pip*r r*cov*ry bolt*r*
1141 Secondary coppar *a*ltlna
4* Industrial cirbon
" ;;:;::r::;r
HUSSION SOUKC SCC COM (MISSION FCCTOR
n«ad-rool (taraaai tank* 404001 ».U1 lb/IO(I aal
- uorklai laaaa* tfcrauajHHit
riaitlm-raof atoriaa 404001 •.XII Ib/IOfl aal
tinka - ataraaa la«««a throuahput
Floitlat-raof ataraa* 404001 1.4* « 101-7 Ik/IOCI ••!
tanka - «orkl«a loaaaa throughput
*.lu*llnt oparitlon* - 404004 1.10 Ik/1000 aal
(aluallnt oparatlana - 404004 11.01 Ik/1000 ail
tfliplicaaant laaaaa thrauahaut
(uncontrollad>
Mluallnt oparitlont - 404004 0.4t« Ik/1000 aal
aplllioa throuahput
•ilincad aubMraad 40400104 0.114 Ib/IOOO til
'Illlna of undartrouAd tnr«uaftput
Splnh Illllnt of 40400101 II. S2 Ib/IOOO aal
underground tinka throughput
Sub>*ra*d fllltnl a» 404O0101 7.144 Ib/IOOO til
undararound tinka tlwouahput
link braithlnt and 40*001 1.0 Ib/IOOO sal
aantylna throuahput
Stick 307001 0.14 - O.SO na/dica * 11
02
Stick 104002 II.OOO na/daca • IS 02
Stick 0.41 ni/daca • 31 02
Stick S Not datactibla - 40
na/di» • 3< 02
NOTIS
ComOTtW lra« Ib/w. aaauoa MS tun *f aparatlaa.
Mual thrauahput tar auk ta*k
Conuartad fro* Ik/vr. laauM 34S diva *f operation.
awial thrauahput far aich tank
Canuartaat Iron Ik/vr. aaauao MS daya af aanratlen.
aaual tkrauannut far aacft tank
Cnalnaarln* aetlMta. KVP • 10 aala
fnaln*arU» aittaita, RVP - 10 aala
Inalnaarlnt aatlaata. «Vf • 10 aala
Cnilnaarlnc aatlnlta. DM* • 10 aala
fnalnaarlna aatlMta, HVf " 10 aala
Intlnavlm aatlaata. HUP • 10 aata
Inalnoarlna aatiaata. •«• . 10 aala
Thraa lacatlana taatad
Eatlnitad vilua Iron atick taat raaulta
Ttor 4 atack taatlna
Thraa locatlona taatad. doaa not Includa
2.1.7,1-laoaar. d*t*ctlon Halt <0.l u*/dica • II 02
so
•7
»7
»7
H*pt*chlorodib«nzofur«n*.
totatl
O Uir. r«cl»»tlon
.nclnfjr*t.on
230 n9/dtca t 31 02
E«tla*t.td v*Iu« frcM «t«ck t«*t rcftutt*
IIS
IIS
-------
raeo No. 171
Ot/21/M
CM
POLLUTANT HUnKK
Heotachlorodlbenzofurane,
total
Haptachlorodlbanzolurana.
total
Heptachlorodlbenzolurana,
total
Heetachlorodlbenzolurana*
total
He»tacMerodlbenzb-»-dle»
Ina. total
Haptacnlor odl banzo-p-dlox
Ina. total
Haetachlorodlbanzo-e-dlox
Ina. total
Hep tachlorodl banzo-p-dl ox
tna, total
Meptachlorodlbenzo-p-dto*
Ina, total
Haptachl orodl banzo-p-dl ox
tna, total
Meptachlorodlbenzo-a-dlox
Ina, total
Hap tachl orodl banzo-p-dlox
Int. total
Haptachl or odlbanzo-a-dlox
Ina, tot.l
Hap tachl orodl banzo-p-dl ox
Ina. tot.l
Haxachlorobanzana 1IB74I
Haxachlorobanzana 1U74I
Haxachlorobanzana 118741
tic
COM INDUSTRIAL PHOCtSS
4t Uood coebuetlo*
4tSI nunlclpal uatta
coebuatlon
4*SI nunlclpal waete
coebuetlon
tOa Hoapltal uaata
Incineration
2a Pulp/aarer all], kralt
papar recovery boll era
334* Secondary copper eeeltlao
4t Drua> and barrel lurnace
4t Induatrlal carbon
regeneration
4t Sewage aludg.
lncln*r*Uon
49 Ulr« rccUuUon
Incineration
4t» Uood coabufttlon
OSJ nu.iU.Ml ««t«
coevbuite'on
4tS3 Kunlclpal ...t.
conbuatton
lOa Hoapltal waato
Incineration
072 Fungicide application •
072 Herbicide application -
O.cthal
4»S3 Landfill oi HC1 wa.to
MISSION MUMS
Stack, Induatrlal
wx>d-llrad boiler
Haaa burn, «ater Mil
Inclnarator
Haaa burn, water Mall
Incinerator
Incinerator
Stack
Stack
Stack
Stack
Stack
Stack
Stack. Induatrlal
yood-ilred boiler
fla.a burn, water wall
Inclnarator
n.aa burn, water wall
Inclnarator
Inclnarator
Application proceaa
Application arocaaa
Fu«ltlva aalaatona
ICC COM MISSION rACTOP.
10200* «.t ne/dace • IX 02
i 2.H - 2MO nllUl t I2S
C02
S I.S48 > IOt-1 - l.al H
IOI-I Ik/ten feed
S0200SO* LOT II IOI-* Ik/ten lead
107001 O.I* - O.M n«/d«ce • IS
02
104002 IMO n«/d»ce * IS 02
S I.I nt/d.ce t IX 02
O.tO ni/d.ce • IX 02
S O.22 - 21 ne/d.ce * IS 02
S 110 ne/d.ce t IX 02
10200t It ne/d.ca I IS 02
S 4.41 - 2IBO no/Mel e 121
C02
S I. 41 x IOC-1 - 1.4a4 x
IOC-S Ib/ton lead
S02OOSOS 1. 45 X lOC-e Ib/ton laad
302 2 Ibe/ton lunelclde uaad
302 2 lb*/ton herbicide u»ad
50100* 1.4« x lOC-t tb/acra/day
NOUS
Salt-lade* wood. Tier 4) etack teatlne
• • 10, 4 locatlona, controlled with ae> ISP
• • a. 4 locatlona. controlled wltk en ISP
Uncontrell«d, teat data
Three locatldng tdeted1
(atleated value Iroe stack taat reaulta
Tier 4 etack teat eawltna
Tier 4 eteck taatlnt
Three locatlona taatad
latleated value Iroe etack teat reaulta
Salt-laden weed. Tier 4 atack taatlnt
n • 10. a locatlona. controlled with an ISP
n • 4, 4 locatlona, controlled wit* an ISP
Uncontrolled, teat data
Aaaueea content • 0.1S. all volatilized - woret caae
al tuatlona
Aaaueea content • O.IX, all volatilized - woret caee
altuatlona
Baaed an engineering eatleatea. aaaueee landllll
UFDetM
lit
lit
III
147
lit
III
lit
lie
It*
111
US
111
III
147
4*
4*
4*
condition., HCI volatilization
-------
Page No. 172
Of/21/to
CM tIC
Nunm COM iNDUtTiM. rracfM
OIIUION fOMCI
ICC COM IHIMION PoCTM
NOW
NexacMoroboAuno
Heftecnlorooeflzene
I.I.S.4.f.(-Mo»,ockloro-l.
1-cyclopentadlona
l.2.»,4.S.t-Ho»achlcroM.
1-cyclopontadlene
1.2.I,4.I.S-t»e»achloro-l.
3-cyclopentadlone
l.2.1,4.!.S-He«achloro-l,
1-cyclopentedlene
l.2.1,4.S.S-Hexachloro-l.
3-cyclopentadlene
l.2.1,4.S.5-He«echloro-l.
3-cyclopentadlene
1.2.1,4.7.l-He«achlerodlb
enzofuran
I.2.l,*.7.t-»e»schlor0dtb
onzofuran
I.2.1,7.l.»-Hexachlarodlb
enzofuran
Hexachlorodlbenzolur sne.
total
H«M«chlorodtb«nzofur*ni.
tatil
H«K«chloredlb«nzolur«n«.
tottl
IIOT4I tw*t«r trutMKt
1.44 * IOE-* U/Mr«/4*v »*M« w «n«lMirtM
condition!. NCI uaUtlllzitlon
MWUM* IwxMlll
(0100701
120 Ik/tM
kw4Ckl«rab«ia. I*
UfllMMl
M ««U. ••dell** lor kyootk. rOTU, ro»ro*Mt>
> rOTU lk.t trutm
2M* IU»Khlorocycla>olit>4t«» ChlortMtlM ructor vwtt Ml
•rodueklon
10.4 lb/to» »roduco4 »«««d wi onclMorlm Judonont
2M* M»»cMor»cvtlw«n»»al«n« fuitttuo
•roductlon Ml»lan
2*4* HoxKhtorocyclo>ont«dl«n« Storm
production
77474 207t roitlcldo MnuiwturUi Fuiltlv* ool»len>
77474 207* r«>tlcld< ••nuUcturlnt fr»c««« - ft«
4>S] nunlclnl n»to
conbuctlon
n«io burn. Httor IM||
Inclnorttor
n*t* burn, w«tof wall
Incinerator
nua burn. Httor vail
Incinerator
H«x«chl orodl benzol unfit.
tot.l
2a Pul»/»»r mill, trait Stick
paper recovery boll era
3341 Secondary copper malting Stack
49 Orun and barrel iurnace Stack
4t Industrial carbon
regeneration
Seuaae sludge
Incineration
Ml
4 Ik/ton *roducod
!»•< M o**lmortiil iudtooont
1.4 Ik/tod produced lited oil onglneerln* Judoeawnt
101031 0.2t Ib/ton uaed
101031 0.4S Ik/ton uaed
JOI03J 0.10 Ik/to* uaed
•ated Oil engineering Judvooont
•aaed on engineering Judneant
0.47 - II ng/M.3 0 121 n • 3. 1 locetlone. controlled iiltk « 1ST
C02
0.27 - 7.1 ne/Nol 0 121 n • «. 1 location!, controlled .ltd en It?
C02
0 - 4.1 ng/Nol • 121 C02 n > 4. I locations, controlled vltk on Itf
0.07 - O.J» ng/dec* • 31 Three locetlena leaked
02
304002 oOOO ni/daco 0 N 02 Catloatod value froo gtack teat results
tl
11
II
IS
II*
II*
II*
1.0 ng/dace 0 II 02
Her 4 atack teat gaopllng
0.5> ng/d»» t II 02 Tier 4 etack testing
0.10 - 12 n«/daco • II 02 Three locations teated. does not Include 2.1,7.1-1
it*
HeMachIorodlbenzolurana,
total
4* Utre reclamation
Incineration
49 ne/deco • II 02
-------
Ptto No. 173
Of/2l/»O
POLLUTANT
MexachlorodlbeiuoOirene.
tot.l
Hexachl erodl bentef urene .
tot.l
Hoxachlerodlbenzoo-p-dloxln
1.2.3.7.l.*-Hex«chlorodlb
enio-e-dloxin
Hexichlorodtbenzo-p-dlexl
nt. totel
Hexachloredlbenzo-p-dtoxl
at. tot.l
Hoxechlor odlbenzo-p-dl oxi
nt. tot.l
Hexachltrodlbenze-o-dlox|
nt. tot.l
Hex»chl orodl btnzo-p-dl oxi
nt. tot.l
Nex.cnlorodlbenzo-p-dloxl
nt. tot.l
Htx.chl orodl btnzo-p-dl oxi
nt. tot.l
Htx.chl or odlbenzo-p-dl oxi
nt, tottl
Htx.chlorodlbenlo-p-dloxl
nt. tot.l
Htx.chl or odlbenzo-p-dl oxi
nt, tot.l
CA« SIC
NUnlU COO* INOUtTIUM. PMCSS*
4» Uood ceebultloo
4MJ ItunlclMl Mete
coebuttlon
4»5J Itunlctpil y.lte •
coebuttlon
•04 Hotplttl yaete
Inclnerttlen
S74SMS7 <»IJ Municipal Mite
co-buttlon
3444S44I 4*53 Municipal Mite
coebuttlon
1*401743 4*93 nunlclp.l Mite
24 Pulp/paper elll, tr.(t
Piper recovery bollert
3341 Secondary copper taoltlne
4f Drue ind btrrel furnace
4* Induttrlll carbon
reeeneratlon
„ $«*„ .Ud^
.nc.rt«r«t.o«,-Hr.M* boilw-
n**» burn, wktw w«lt
tncin«r .ttor
n*** burn. Moji«r «»*ll
• l>c.n*r*ter
Inctn«r*tor
«*•» feurn, w«t«r MAii
incln«r*ter
n*»» burn, ufttw w*ll
incinwctor
n««s burn. M4t«sr y*tl
lncl»«-.ter
Stick
(tut
Stict
Stact
St.ct
St.ck
St.ck, Induttrlal
•ood-llred boiler
n.tt burn, w.ter u.ll
Incinerator
n.tt burn, water wall
Inclnar.tor
Incln.r.tor
sec COM tniwioM rwTo* HOTS*
10200* IS M/eea t 31 02 Silt-lade* Hood). Tier 4 eteck teltlne
( 1.12 - 3*M »i/Ne3 « I2t e • 10. 4 location!, controlled) Kith an ISP
C02
S 1.432 * ICX-I - 2.02 x n • e, 4 location, controlled ultk en ISP
IOC-S Ib/ton e.l m/Nel • I2X • • 4, 4 location*, controlled tilth an ISP
C02
S 0.17 - 11 *«/HeI * 121 n • 4. 4 location!, controlled] ulth an fSP
C02
» 0 - 4.4 n«/Ue3 * 12t C02 n • 4, 4 location!, controlled Kith en ISP
307001 0.0* - O.I* np/dtce • 31 Three location! teetod
02
304002 2200 no/dice • 3» 02 Iitteated value etack teet reeulte
f 0.7* «*/dece 0 IS 02 Tier 4 ttack teet lieellnt
O.M ne/d«c« * 31 02 Tier 4 etack tettlne
9 Not detectable - 7.0 Three location! teeted. detection llelt <0.t n«/dice t
ne/dtce • 31 02 31 02
10200t 4* n«/dice | 31 02 Silt-laden eoed. Tier 4 etack teitlni
C02
5 3.2 x 10E-S - 1.411 x n • 4. 4 location!, controlled »lth an ESP
IOC-5 It/ton feed
S0200SOS 0.7S * 10E-4 Ib/ton «.«d Uncontrolled, tett dlta
RSmOM
IIS
IIS
us
1*7
III
III
111
II*
IIS
IIS
IIS
IIS
11*
11*
111
III
147
-------
Fee* NO. IM
0»/2I/M
POLLUTANT
CM SIC
NUMKIt COM IHDMTIItM. HtOCItl
INIMION (OMCI
KC COM MINION FACTO*
MTU
t»J4U
Hydroeon chloride
Mydreoen chloride
Hydreeen chloride
Hydrooen chloride
Hydroeen chloride
Mydroeen chloride
Hydros*" chloride
Hydroeen chloride
Hydroeen chl or Id*
Hydreeen chloride
Hydroa«n chloride
1*1 nerlculturel
Industry-field kurnlni of
elastic ere* cowere
1*1 fterlculturtl
Industry-field burnlni of
pUstlc crop
«»24U 1*1
1*1
*«rl cut turd
lr>*i>try-«l«U kurnkni at
•l««ttc era* covert
Atrlculturtl
lndu«try-ll«l« burn I no at
•lafttic ere* covers
CM! cortKittlon.
tnduitrUl
Ca«l coobuttlon.
Indultrlil
C«l urtuitlon.
Inou.trl.l
Co«l
r«>lo>ntUl
Co>l cortuttlan.
ruldmtUI
Coil co^Hiit
r»ldl
U««t« oil combustion
7«47ulO 2il» Hydrochloric icld
process
211* Hydrochloric *cld
orocsss
7»»70IO 2BI» Hydrochloric >cld
••nufsciurs - by-product
proctss
7t<70IO 2BI» Hydrochloric (Cld
Usod ki*ck olMtlc
Unus«4 bt*c< pUstlc
Ussd klsck pUstlc
Unussd buck plsstlc
•ttu«li»eus C»«I
Industrlsl bollor
«ntr«cU« co«l Industrlll
bollsr
LISAlt* cost l«dustrl«l
bolt or
•llufllnous co*l
ro>ldsntlsl bailor
Anthrsclto cast
roildsntlsl boll or
Limits cost rosldontUI
boll or
U«ft« oll'Ured bollors
K150 .111 Ion Itu/hl or
sp»c« hsstors
Cntlrs procsss
By-product HCI
•y-nroduct HCI
Entire process
•.«*» mt/ml •« olsstlc
«.IM ee/«J •< pUstlc
«.0*0 e>f/el •< olMtlc
•.021 ce/e) •< olutlc
102002 7i.i >p«/IOC» ITU
102001 IS.I Ibs/IOf* ITU
102001 1.0 Ibe/IOC* ITU
«0.I Ibs/IOC* ITU
120 lbs/IOC» ITU
H.I Ibs/IOC* ITU
51.12 Ib/IOOO eel ell
burned
30101101 0-8.5 Ibs/ton scld
produced
J01011 3.0 Ibs/ton
301011 0.2 Ibs/ton
1.3 to 1.1 Ib/ton scld
produced
Cxeerlewtel eleuUtlee. pleetlc sheet • 1 110
Ib.,ostlutod free) evereee benions ens) toluetM response
(JWerlewiUI •leuletlon. pUstlc sheet • I
Ib. .estlettsd tree) evereee benxene end toluene reel
(MorloooUl slouUtlon. pUstlc sheet • I
Ik. .mtlMtee) «roe sverete beniene end toluene) n
210
110
iKperloentsI sleuUtlen. pUstlc sheet • I 110
lb..ostluted froe evereee benzene end toluene response
•seed en retoi ef oroductloe
lissd on ret* o* preductlee
•seed en rote «f eroducttoe
111
111
III
Uncontrolled, bteod on eelsslons dste end en«lneerln« 99
Judeeeent
(seed en rete of production, n/out flnel scrubber III. *7
l*ssd en rste of production, controlled Kith scrubber 111
-------
Pew Me. I7S
otmro
rOLLUTAHT
Hydroeen chloride
Hydroeen chloride
Hydroeen chloride
Hydroeen chloride
Hydroeen chloride
Hydroeen chloride
Hydroeen chloride
Hydreeon chloride
Hydroeen chloride
Hvdreoen chloride
Hydroeen chloride
Hydroeen chloride
Hydrovon chloride
Hydrogen chloride
Hydroeen chloride
Hydroeen chloride
CM SIC
Nunm coot
7447010 Mlt
7447010 2121
7447010 2122
744.7010 Mil
7447010 M21
7447010 214
7447010 214*
7447010 2B4P
7447010 2B4P
7447010 2B4»
7447010 214*
7447010 2S4»
7447010 3312
7*47010 4VI1
7447010 491 1
7447010 4911
INOUtTftlM. HtOCCtt flUUIOM UUACC
Mytfrockiwlc Kid bitir* »r«c«M
MiMJf«ctur« * »y*tl»Mt»
»r«c«M
PolyvUyl chlorite «u«ii«niloA »rocoH,
production witlr* »t*At
M*ot*r*fl4i MfwfMtur* Mu*ou« *M*t< v«nt
cona*n»»r
M«pr». „«,,.,»»,. Ucln^.tc,
PVeevlene oxide
Chi orobeniene prod. Abeorptlon
leono- t dl-). direct
chlorlnation
Cplchlorohydrln Separetton unit
production by
hydrochlorlnatlon
Ethyl chloride production Separation unit
by nydrochlor! nation
Ethyl one dl chloride Abeorptlon
production - direct
chlorlnatlen
netKKl chloroioro Heat tran»(er
production by
hydrochlorl nation
hethyl chlorofore Separation unit
production by
hydrochlorl nation
tower •
Coal coobuetton Boiler
Coal coebuatlon Boiler
tec COM tnmiON fncro* HOIM
0 to
-------
ret* He. 17*
Of/21/M
POLLUTANT
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
Hydrogen chloride
CM *K
NUntU COM INDUSTRIAL PMCEM
7*47010 4«ll Coel ceebuetlon. utility
7*47010 4tll Coal coebuitlon. utility
7*47010 4»S1 nunlclMl Met*
coebuitlon
7*47010 4rSl nunlclMl oa*l*
coebuitlon
7*47010 4*91 nunlctMl uael*
cookuetliM
7*47010 4rS! nunlclMl uaet*
coebuetlon
7*47010 4*93 nunlclMl uaet*
coebuetien
>*470IO 4»93 nunlclpal oaet*
ceebuitlon
7*47010 4»SJ nunlclMl uaate
coebuitlen
7*47010 4*93 nunlclMl uaete
coebuitlon
7*47010 4rH BunlclMl Mite
coebuitlon
7*47010 4»S3 nunlclMl uaite
coebultlon
7*47010 4tS3 nunlclMl uait*
coabuitton
7*47010 4>S3 nunlclMl Mite
coebultlon
7*47010 4»SJ nuntclpal uaite
coabuitlon
7*47010 4*53 Municipal Mite
coebultlon
7*47010 49S3 nunlclpal uaite
coebultlon
EMISSION MUKf
Anthracite coal utility
boiler
Lignite coal utility
boiler
Entire oroceee
Entire erocee*
fntlre croc***
Maaa burn. tt**t r*cov*ry
facility
naai burn, heat recovery
facility
nan burn, nonhoat
recovery facility
nan burn, nonheat
recovery facility
nodular Incinerator
nodular Incinerator
•alula derived fuel
Incinerator
Mefuie derived fuel
Incinerator
Incinerator
Incinerator
Nafuae derived fuel
Incinerator
Refute derived fuel
Incinerator
SCC COM HUMION FACTO*
101001 J».» 1**/10E» ITU
101003 1.0 lka/lOC» ITU
f 0.0*2-4. M Ike/to* refuie
> 1.4 Ik/ ten r*fu**
f 4 Ik/to* refute
SOIOOI 1.2* Ik/ ten of uaite
SOIOOI O.I Ik/ten of uaite
coebuited
SOIOOI 1.2* Ik/ton *f uaete
coobuited
SOIOOI O.I Ik/ton of uaet*
SOIOOI 7.1* Ik/ton of uaito
coebuited
SOIOOI O.I Ik/ton of uaite
coubultod
SOIOOI 1.14 Ib/ton of uaite
coebuited
SOIOOI 0.* Ib/ton of uaite
coebuited
SOIOOI 9.0 Iki/ton eeterlal
burned
S03001 9.39 Ibi/ton eater I.I
burned
SOIOOI 4.* IB/ ton RDF coebuited
SOIOOI 10.4 Ib/ton RDf coebuited
NOTE*
laied en ret* of production
laied en rat* of production
Depend* oei uaete content. coebuitlon condition*.
control dowlc*.
For wit* uhlck 40 not recover energy
For uait*-t*-*n*rgy facllltlei
No MCI control. be**d en eource toiti
Controlled ky dry alkaline ecrubber. anueei tOl HCI
control efficiency
Ho HCI control, baud on eourco teitl
Controlled by dry alkaline ecrubber. «*uee« tOS MCI
control efficiency
No HCI control , booed on eource teet*
1
Controlled ky dry alkaline ecrubber. eeeuee* *OI HCI
control efficiency
No HCI control , baaed on eource teete
Controlled by dry alkaline ecrubber. eeiuee* *OI HCI
control efficiency
IOOS ROF fuel only, ESP control only, overall average
of levorel eource averegee. range !• 3.4 - 9.2 Ib/ton
IOOS P.OF only, uncontrolled, overall average of leverel
lource average*, range 1* 4.1 • 19.1 Ib/ton
in
-------
rat* NO. w
Ot/21/tO
POLLUTANT
Mydroeon chloride
Hydroeen chloride
MydreMn chloride
Hytfreten chloride
Mydroeen clilor Id*
Hydroeen chloride
Hydrooen chloride
Hydraeen chloride
Hvdrooen chloride
Hydroaen chloride
Hydrooen chloride
Hydrooen chloride
Hydroaan chloride
Hydroean chloride
Hydroaan crtlorlda
CM «IC
NUniM lOOt INOUSTIIM. MMCUS
7*47010 4W nunlclpal Met*
contention
7*47010 4»SJ Municipal Mete
contention
7*47010 4»SJ municipal M*te
Contention
7*47010 4M1 nunlclpel Mete
contention
7*47010 4tSJ lhuilcl»t*
contention
7*47010 4tSI nunlclxl n»«to
contention
7*47010 4*
conteistlon
conbuttlon
7*47010 4»I Itunlclxl K»l«
conbuvtlon
7*47010 4«SI nunlclnl w»«t«
conbuttton
7*47010 4»S1 nunlelp.l MMto
conbutttion
7*47010 4>SI Punlclnl »••(•
conbu«tton
inmioN WKMCC sec COME
M«in onrlund lunl W1001
tnclnor*tar
Dodultr itu-vnd-Ur f 01001
conteittor
Hedulw >t*rvnd-c»*-*tr fOtOOl
conbuttor
llodultr nxco«n-*ir M1001
cofttentor
H<» burn. y»tnr Mil SOIOOI
tnclnwttor
»••• burn, tutor «•!! SOIOOI
InclnwAtor
L«ra« n*«t burn rotary S01001
u«tnr«*ll conbufttor built
•ustDr, tn*ll •!>• n*w
nodal to ftny A9* nodtun
n«*a burn w«tnru«ll SOIOOI
CdKbutlor. »»»U »i» n«M
n<» burn uoo>. ruiw U 1.2 - !*.« Ik/ton
Uncontrolled, ovoroll ovorion of cover*! oource
•vor**oo. ruioo I* I.M - I.I Ik/ton
Uncontrollod, •varoll *vor««o of oovorol nource
•vorooo*. ronw l« 0.70 - t.2 Ik/ton
IS* control only, overall ovor*«o of oouorol oourca
•VOTMO*. ronoa I* S.I - >.2 Ik/ton
Dry oarteMt Injection of tor *cld ••• ond PH control.
one d*t* point only
fSP control only, one dot* point only
Uncontrolled, one dote point only
Cipuity > *00 tone/dey. tiT control only, ovortll
•voraee of oeverel eource evor*oee. ronee le I.t2 • t.4
Ib/ton
CMtclty > 000 to2 * 11. 1 Ib/ton
Capacity < *00 tona/day, ESP control only, overall
Ib/ton
Capacity < *00 tona/day. apray drylm aftor acid eae
and PH control, overall av9. of aeveral aource avfle..
ranae 1* 0.138 * 0.9* Ib/ton
Cap. < *00 tona/day. dry aorbent Injection after acid
fla* and Pn control, overall av«. of aaveral aource
KFfMM
IM
IM
IM
IM
IM
IM
IM
IM
IM
IM
IM
IM
IM
IM
IM
S.. r*n«« U 0.14 - 2.2 Ib/ton
-------
Pate Me. 171
Ot/21/tO
POLLUTANT
CM SIC
HUneU COM IMMtnUM. PMCIM
IHIMIOM MUKC
tec COM IHIMIOM men*
MOTK
Hydratan chloride
Hydroten chloride
Hydreten chloride
Hydraten chloride
Hydreten chloride
Hydroeen chloride
Hydraten chloride
Hydreoon chloride
4*fl rtunlclpal »*et*
coebuetlen
7*47010 4»*J Municipal tw»t«
7«470I« 4»»J HunlclMl twit*
7*47010 4tSI nunlcl**! nut*
7447010 4«1 HwiUIMl >M>I<
7447010 4>53 IkutlclMl •»(•
7447010
4t5I (•»•!• (ludw
litclnw«tlon
Hat* bur* awterHell WIOOI IS Ib/te* feed
coebuetw. built before
ItM
naia bur* vateruall WIOOI 1.0 Ib/to* feed
coabuator, built before
1*80
Maaa bur* vateruall MIOOI 1.4 Ib/ton feed
coobuatar. built before
1*10
Daee bur*, refractory MIOOI 0.0*2 Ib/ton feed
facility
lUet bur*, refractory 501001 2.1 Ib/ta* feed
facility
naae burn, refractory MIOOI 1.2* - 4.2 Ib/ton feed
facility
uecoMrclled. «w data oeiet only
ffjf* control enly. everell averaee of eeverel eourc*
overate*, rante I* X.2 - 1.1 IB/ton
•ry eorbent Injection after acid tee and Ml control.
one date point only
tpray drylnt after acid eae and rtt control. one date
paint wily
flf* control only, overall ever*** of eeveral eource
everat**
(If* control anly. *v*r*ll rant* af eeveral eaurc*
everaaa*
IN
IM
ItO
110
7447010 4*SI (••>••• >ludM
Incinerator etack
Incinerator eteck
M100M* 1.1 Ib/te* dried eludt* Uncontrolled
S0100504 O.I Ib/ton dried elude* (crubbar
Hydreten chloride
Hydroten chloride
Hydroten chloride
Hydroten chloride
Hydroten chloride
Hydroten cyanide
Hydroten fluoride
Hydroten fluoride
7447010 4>S] U»t< Inclnvttlon
10* Ha«»lt*l «««t«
Incineration
104 Howltel «««t«
Incineration
B04 Hofeltll ««>te
Incineration
104 HotplHI oelte
Inclneretlon
2>4t Acrylonltrlle production
- iONIO irocen
Coil ceebuitlon.
lndu>trl>l
Co«l coaoultlon*
Industrial
LUuld ueete etarat* S01O070I I.I* Ibe/ton (tterlal
burned
Txo-chaobered Incinerator S020050S 20-12 Ib/ton uaate
1IS020 14.7 Ib/ton feed
319020 14. I Ib/ton feed
Incinerator
AbBorber vent
Lignite coal-fired
botlere
Anthracite coal-fired
boll en
115020 1.7 Ib/ton feed
Uncontrolled, rant* du* t* varlatlan 1* Mate, t*tt
an* facility
uncontrolled, avaret* eelaalon factor baaed an 20
facllltlae
Controlled ulth fabric filter, baaed en I facility
Controlled utth uet ecrubber. averaee **laelon factor
baaed on 1 facllltle*
101
1012540* 0.4 Ib/ton acrylonltrlle uncontrolled, baaed an data fro* plant* and IPA atudl**
produced
102001 1.2 lbi/10C* ITU
102001 7.2 lbi/10£» ITU
•aaed upon rat* of production
•aaed upon rate of production
-------
Paw No. 17*
0»/I1/»0
POLLUTANT
Hydroaan tluorlda
Hydroaan Uuorlda
Hydroaan Uuorlda
Hydroaan Uuorlda
Hvdraaan Uuorlda
Hydroaan Uuorlda
Hydrogen Uuorlda
Hydroean Uuorlda
Hydroaan Uuorlda
Hydroaan Uuorlda
Hydrogen Uuorlda
Hvdro«an Uuorlda
Hydroaan Uuorlda
Hydrogen Uuorlda
Hydroaan Uuorlda
Hydroaan Uuorlda
Hydroaan Uuorlda
CM ftC
HUnKIt CMC INOUSTIIM. PMCEfa
74*43*1 Coal coofeuatloa.
lndu»trl»I
74441*1 Coal coaouatloa.
raaldantlal
74441*1 Coal coabuattan.
raaldantlal
74441*1 Coal coeouatlon.
raaldantlal
74441*3 J»I» Hydrofluoric aclal
eanufactura
74441*3 211* Hydroiluorlc acid
aanuf actura
74443*1 2174 Olaaaonlua phoiphata
production
74441*J 2(74 Vlaoeonlue phoiphate
production
74441*1 2174 Dlaeeontue pnotpneta
production
74441*1 2174 Pheaphorlc acid
production
74441*1 2174 Phoaphorlc acid
production - wat procaaa
74441*3 2174 Phoaphorlc acid
production - Mat process
74441*1 2174 Phoaphorlc acid
production - utt procaaa
74441*3 2874 Suparphoaphata f granular
trlplal production
74441*3 2974 Superphoaphata (granular
triple) production
74441*3 1255 Detractory production
74441*1 1114 Prloary atualnim
production
DIIMIOM MUM!
lltuolaou* coal-flrad
boll art
llenlte ceal-flred
bollara
Anthracite coal-»lrad
botlara
lltualnoua eeal-llred
bollara
Tall «aa
fall gaa
Aaaonl at Ion-granulation
procaaa
noaonl at Ion-granulation
procaaa
firyar/coolor
Condanaar
Gypau* aafctllng ponda
Condanaar
Raactor
Ratctor/dryar
Raactor/drvar
•rUk 'Irlng kllna
Horizontal aodarburg atud
- Iu9ltlua
tCC CMC
I02OO2
M10U04
M10I204
101030
30103002
10103001
101017
3010140J
1010140}
30101401
10102*04
10102*04
10SOOI
1010010*
IMMICM P»CTO» NOTM
*.4) low/IOC* ITU laadd u*a» rat* •« praductlad
«.J4 lbl/10f> »IU
a.W Iba/IOf* ITU
4.17 tbf/IOC* ITU
IS lo/ton aclal Uncontrallad. avaraga o« data iar thraa planta
0.2 Ib/ton acid Cauatlc acrubbar. ayaraaa o« data
-------
Fage Ho. IM
0*/2I/*0
POLLUTANT
Hydro gee fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Hydrogen fluoride
Mwdroaan Jluarldfl
CM *IC
NUneC* COM
74441*1 1114
7*441*1 1134
7*441*1 1114
74443*1 1334
74441*1 1114
74441*1 1114
74441*1 4*11
74441*1 4*11
74441*1 4*11
74*41,1 4,51
74*41*1 4*51
74441*1 4*51
74441*1 4*51
74441*1 4*51
74441*1 4*51
74443*3 4*53
74443*1 4*53
IHOUfTIIAL PMCIM
Prloery elueleue
production
Frleary aluelnue
(reduction
Frteary aluelnue
(reduction
Frleary allujlaue
•reduction
Frleary eluelnue
(reduction
production
Coal coebustton. utility
Coal coebustlen, utility
Coal ceebuatlon. utility
coeoustlon
HunlcKal «aste
co-cult Ion
nunlclpal waste
coebustlon
combustion
nunlclpal waate
coebustlon
nunlclpal waste
coebuatlon
coabustlon
IMIallON MUKI
Horlaontal loderkero etue)
cell
V t f - fugitive
eel salons
Vertical eodorkero (tud
cell
Frebaked fugitive
eelaslono
Frebaked reduction cell
Anode baking furnace
Lignite coal-fired
tollers
Anthracite coal -fired
boll era
•Ituelnoua coal -fired
bollara
Refuse derived fuel
Incinerator
nodular 4tarved-alr
coebuator
nodular atarved-alr
coabuator
nodular excess-air
coabustor
naaa burn, water wall
Incinerator
Larea ease burn rotary
watarwall coebustor built
altar U60
uatarwall coebustor built
altar 1*80
(CC COM OIIMIOM FACTO*
M100I02 l.f Ike/ton
101001 10 4.* Ike/to*
M100I01 0.* Ike/ton
10300100 I.X Ike/ton
M100IOI 4.* Ibs/ten
30300105 0.12 Ike/tee.
IOIOOI 1.2 Ike/101, ITU
101001 7.2 Ibe/lOE, ITU
101002 ,.4 Iks/IOC* ITU
501001 0.01* Ik/ton RDF
coebusted
501001 0.001 - 0.0*1 Ib/ton feed
501001 0.041 Ik/ton feed
501001 0.0014 Ib/ton feed
501001 0.012 Ib/ton feed
501001 0.07* Ib/ton feed
501001 0.041 - 0.110 Ib/ton faad
501001 0.00*4 Ib/ton feed
HOTfl
lased ixee rate, ef (reduction
lased upon rat* ef production
laaed upon rate X (reduction
lased MOO*, rate ef production
lased ueee rate: ef (reduction
lasod UCOA rate of (reduction
•ased tape* rate ef (reduction
•ased upon rate ef (reduction
•ased ueon rate ef (reduction
1001 RDF fuel only. IM> centre! only, one data point
only
Uncontrolled, overall rang* ef several source averages
Uncontrolled, overall average ef several source
averegoe
Uncontrolled, one data point only
Uncontrolled, one data point only
Capacity > 400 tone/day. ISF control only, overall
average of several source averages
Capacity > 400 tons/day. ESF control only, overall
ranee of several source averages
Capacity > 400 tons/day, apray drying after acid gas
MF1MNCC
IM
III
III
III
III
III
111
111
III
IM
IM
IM
IM
IM
IM
IM
IM
W4t«ry4ll coftttufttor t»ullt
*H.r 1*80
»ntf Pn control, ov«rklV «v«r*«« of »«v«r4\ »t>urc«
•v«r*>«»
-------
Paa* No. Ill
0*/21/*0
POLUniWT
Hydroton fluorlda
Hydrete* fluarlda
Hydroten fluarlda
Hydroaan fluorlda
Hydroten fluorlda
Hydrotan fluorld*
Hydraaan fluorlda
Hydroaan fluarlda
Hydroten fluorlda
Hydroten fluorlda
Hydroaan fluorld*
Hydroaan aulfida
Hydroaan .uHlda
Hydroaan .ulfid.
Hydro«.n .utfld.
CM (1C
MM** COOI 1NMMTP.IM. MtOCttl IHIMIOM tOWCt
74*43*3 4*53 Itunlcla.l yaata Ltrt* a... bum rotary
caabuatle* y. tar Mil coaouator built
aftar 1*10
7**43»I 4*11 flunlcltal Mate II... bur* y.tery.11
ceatouatton coabuator. eeall alia now
1*443*3 ««3 Municipal y..ta It.. a burn yitary.lt
coabuctlon coabuetor. aaall alia now
aodal to any a*« a«dlua
7**43>3 4*S3 Municipal vaata tl..a burn y. tery.il
coabuatlon ceabu.ter. aaall alia nay
aodal ta any ata eadlue
7««43»3 4*13 nunlclptl vatte M... burn y.tery.ll
ceebuatlon coabu.ter. aaall alia nay
aodal ta any ate aadtua
74*43*3 4*53 Itunlclaal uatte H«m« burn t»tar«all
coabuatlen conbu.tor. built bafora
1*00
7««43>3 4*S3 Itunlclaal yaat* n..a burn y.tariull
coabu.tlon coabu.tor. built bafora
1*80
7««43*3 4>S3 Itunlclpal yaat* H««a burn, refractory
coabu.tlon f.clllty
74*43*3 4*93 nunlclpal vtlt. n.K burn, refractory
coabu.tton f.clllty
74*43*3 4*53 dunlclp.1 y..t. n... burn, refractory
coabu.tlen f. ditty
74*43*3 4*53 flunlclf.l «..t. ft... burn, refractory
coabu.tlon l.clllty
77130*4 Fl.h aroca.ilni alant. Fl.h .cr.p cookara -
fr..h
77030*4 Fl.h aroca..ln* .l.nt. Fl.h .cro cookere -
• t.la
77B3044 2*11 PuU/p.par .111, kr.lt t.tth diM.tar tbloy)
KC COM IMWION FnCTOH NOTM
WIOOI 0.0071 - 0.011 Ik/toe. Cwaclty > 400 tana/day, aaray drylna altar acid aaa
feed and Pfl control, overall rant* •< tower al aourca
(OIOOI 0.044 - «.O4t Ik/ten feed Capacity < *OO tana/day. IV central only, overall
ranee of aeveral eeurco averatea
S0100I 0.04* Ik/ton feed Caaaclty < «00 lone/day. Uf control only, overall
aver.ee af aaver.l aourca averatee
SOIOOI 0.00032 - 0.0031 Ik/tan Capacity < «00 tona/day. oaray dry In* after acid oat
toed and Pfl control, overall rante of teveral .ourca
aver ate*
SOIOOI 0.002 Ib/tan feed Capacity < *00 tone/day, taray drylnt after acid t*t
and PH control, overall averata af teveral .ourca
avereeee
SOIOOI 0.010 Ib/ton feed ESP control only, one data paint only
501001 0.011 Ik/ton feed Uncontrolled, one data point only
IOIOOI 0.003 Ib/ton feed fpray drylnt after acid taa and PH control, one data
paint only '
501001 0.012 Ib/ton feed ESP control only, overall averate of aavaral eourc*
aver .tea
.varata.
SOIOOI 0.005 Ib/ton feed Uncontrolled, one d.t* point only
30201201 0.01 Ib/ton fl»h Uncontrolled
30201202 0.2 Ib/ton ften Uncontrolled
503O0204 * f 10E*4 Ib/hr/ton
burnlna coal rafu.a
30700101 0.0"0.2 Ib/ton of product Ooer.tlnt condition, .uch a. coabu.tlen taapa and fual
tWIMM
IN
IN
IN
IN
IN
IN
IN
IN
IN
IN
IN
»7
»7
13*
S
Kill #«p*r pro
typ«» Account lor ih« bro*
-------
P«oe Mo. 112
04/21 /to
POLLUTANT
Hydrogen aulllde
Hydrogen aulllde
Hydrooan autlldo
Hydrooen pull Ida
Hydrooan aulllda
Hydrooan aulllde
Hydrogen aulllde
Hvdrosen aulllde
Hydrooen aulllde
Hvdreeen aullide
Hvdrooen aulllde
Hydreoen aulllde
Hydrogen aullld.
Hydrogen aulllde
Hydrogen aulilde
Hydrogen aulflde
Hydrogen aulllde
CM
MURKS)
77110*4
77110*4
77110*4
77110*4
77110*4
77110*4
77110*4
77110*4
77110*4
7711044
77110*4
77110*4
7703O44
7783044
7713044
7783044
7783044
fIC
COM
2*11
2*11
2*11
2*11
1*11
2*11
2*11
2411
2411
2*11
2*11
2411
241 1
2411
2411
2411
2411
IMDUSniM. PKOCKI
Pulp/paper •III, trait
•III paper proceaa
Pulp/paper •III. trait
•111 paper procoaa
Pulp/papor •til. kralt
•III papor proceaa
Pulp/papor •III. trait
•111 paper procoaa
Pulp/papor ottl. kralt
•111 paper procoaa
Pulp/papor •til. kralt
•III papor proceaa
•III papor proceai
Pulp/paper «lll. kralt
Pulp/papor •111. kralt
•III paper proce.a
Pulp/paper elll. kralt
•111 paper proceaa
Pulp/paper elll. kr.lt
•111 paper proca..
Pulp/paper "111. kralt
•III paaor aroca.a
pulp - aulllta pulping
Pulp/paper .III. kralt
pulp - aulllte pulping
Pulp/paper •!!!. kr.lt
pulp - aulllte pulping
Pulp/paper (III, kr.lt
pulp - aulllte pulping
HtiniOM MMCI
latck dl teat or
(bood wont)
Iroun stock xaakorla)
laaal vantt
Contlnuoua dteeater
Olrect contact evap.
(oxldtaad black Itauort
-------
rate Ma. Ill
09/2I/9O
POLLUTANT
Hydrogen aulflda
Hydrogen lulflde
Hydrogen eulflde
Hydrogen aulflda
Mydrceen fulflde
Hydrogen «ul(ld«
Hydrogen aulflda
Hydrogen fulflde
Hydrogen fulfido
Hydrogen fulflda
Hydrogen fulflde
Hydrogen fulflda
Hydrogen tulflda
Indene
Indene
Indana
CM SIC
NUMC* COM INOUtTIIM. FOOCISS
77110*4 2*11 Pulp/paper elll, kraft
pulp - aulflte pulping
77110*4 2*11 Pulp/paper a>lll. kraft
pulp - aulflte pulping
77110*4 2*11 Pulp/paper elll, kraft
pulp - aulflte pulping
77«0«4 2*11 Pulp/paper elll. aralt
pulp - gulflto pulping
77110*4 2(24 Synthetic fiber*
production - vl*co*e
rayon
77110*4 21*9 Carbon black oanufacture
- oil furnace
77110*4 2199 Carbon black eanufactura
• oil furnace
77110*4 2895 Carbon black eanufactura
- oil furnace
77*10*4 2*11 Potreleue refinery -
77110*4 2*11 Petrol eue refinery -
aulfur recovery pi ante
77110*4 2911 Patrolaue refinery -
•ulfur recovery planta
77110*4 2*11 Patrolaue rerloary -
77810*4 32»« ninaral uool
oanuf acturlng
IMSS10N IOIMCI
Noflcontect recovarv
bailer ulthaut direct
contact evaporator
Aecevery bailor end
direct evaporator
Seelt dlatolvlaf tank
lurpentlng condonaer
General eelaalong
CO boiler/Incinerator
Flare
ll.in proce** purge vent
Twe-etage ctaua recovery
gaa unit
Clau* recovery proceaa
ulth beauon tail gaa unit
Claua recovery proceac
with wel lean-lord
•crubbar
?hrae-ftag« Claua
Kp-1 tall gaa unit
nlnarai wool cupola
burn hut
burn hut
burn hut
SCC COM Dilation FACTO* NOTM
107001 •.! Ik/too air-dried pulp Apply idm recovery furnace la operated optically to
central TM
W700I04 12 Ik/tan air-dried pulp fur venturl ocrubbor or Or. can be reduced SOI wltp.
black llguor oxidation
M70010S 0.2 tb/ton oir-drled pulp fur untreated, eean pad or ocrukker. can be lowered 11
lev aulflte tutor uaed In tank
10700107 0.01 Ib/toa air-dried Untreated
pulp
10102901 4 Ill/ton flbera Uncontrolled. Ion auallty factor
101009 0.22 Ib/ton carbon blac* laaed on ta«t data
produced
101009 2 Ik/ton laaed on teat data
10100504 *0 Ik/ton carbon black teeod on teat data
produced
IOIOI2 0.045 lb*/ton of aulfur Single teat value
food
101012 0.00* Iba/ten of aulfur Average of I teat run*
feed
aulfur feed
101012 t.I Ibf/ton of aulfur Average gf I teat rune, aulfur la froe carbon dl fulflde
30501701 1.0 Iba/ton of etnaral Uncontrolled eelpalona. average of 1 teata
wool produced
0.7178 Ib/ton tire IAO-2 eKtracta M/ttS analyala. ahrad condition • 2" ky
2* piece*, burn rate • 1.1 kg/hr. uncontrolled
0.579 Ibstofl tire 1AD"2 eKtracta w/nS analval*. *hred condition • 2* by
•VfJoDM
97. 171
97. 171
97. in
n. in
»7
97
»7
•7
194
194
It4
IM
117
212
212
212
§
I
-------
Peee No. IK
0*/2I/*0
CAS
(1C
Hunm COM iNDutniM. PMCIM
HIUSIOM tOMCf
«CC CMW IHIMIIW PACTtt
lndeno(1.2.I-cd>eyrene 1*11**
lndene(1.2.I-cd>oyrene IMJtS
Indwell. 2.1-cd>ovrene I»JJM
lndeneU.Z.3-cd>eyrene I*1I*S
Scree tire, eeen kurelno Tlree U exeerleeetel
burn but
Scree tire, eeen burntne Tiro. In exeerleeeitel
burn hut
Scree tire, eeee burnlno Tiro. In oxperleentel
burn hut
Scree tire, eeen burnlne Tire. In exeerleentel
burn Hut
icree tlr«. eoen burnlnf Tire. In exferloentel
burn hut
».t77 Ik/ten tire.
0.1*1 Ik/tM tin
0.141 Ik/to* tire
0.11* Ik/tM «lr«
0.070 is/ton tin
lnO-2 extrecte n/W M«lymU. Ckwit condition • I /«-!/« 212
•I tlr«, burn r«t« • 2.) k*/hr.
(u. •« PAH M«lv M IU «xtr>t. •« IAD-2 tnt t lllt«r 212
cwant. >»r«4 condition • 2* M 2* •!««. bum
rl.l kt'kr, cantrellod
turn •» PAH Moly Ml IK ««tr.t. •« IAO-2 tnt t filter 212
conoMt. »hrod condition • 2- by 2* •!««. burn
r«t«>I.T tw/kr> control I od
Sun Qt PAH oMly M 1(4 o«tr«t. ol IAO-2 t«t i flltor 212
coo»«it. (hrotf Condition • I" by 2* Hmt*. burn
r*U»X.I kl/hr, controlled
11411110 M Uood coobu«tlon.
IndustrKl
Morliont*! r«turn tub*
10200*0. 1*4.7 IB/10C12 ItU koit
Inout
fu*ll riMlltt. I »l»nt. «ood ilevrtto • -114 ••/*,
bailor k« !-•»» d.«lon «/«l»»«n r.lnjoctlon.
uncontrolIod
1tobutvr»ldohydo
I«obutyr«ldchydo
11411110 2S Wood CMbuitlon.
InduitrUl
19431110 2S Mood coobuitlon.
InduotrUI
IS4U110 2*41 A.eheltlc concrete
•reduction
IS41I1IO 2MI «»heltlc concrete
•reduction
1S4II1IO 10* Howltil u«it<
Inclnorctlon
Uood combust I on.
rifldmtlil
Uood coobuvtlon.
rnianvtttl
Coal coobuttlon.
InduitrUl
•tltncod dr>e<
•tokor-«lred lndu»trl«l
boll or
rum iUck
PUnt >t«ck
10100*0* 0.0014 Ik/ton luol
>0.24 n«/J
I0200*0o 0.0104 Ib/ten 0.1» nt/J
IOS002 1.72 « IOC-7 Ib/ton
concroto
105002 4.71 x IOC-* Ib/ten
concrete
113020 <0.010I Ib/ten food
2.1 Ib/ton wood burned
1 Ib/ton vood burned
10200202 0.001. lbr«*d.r .tokor w«tortub«
boll.r
10200204 0.0084 Ibl/lOCi ITU h.«t
Input
Uncontrolled eel••Ion.
-------
Pa»e Ho. IIS
O9/21/90
POLLUTANT
Lead
Lead
L..d
Lead
Lead
Lead
Lead
Lead
Lead
Lead
Lead
Lead
Lead
Lead
Lead
Lead
CM (1C
NUIKIt COM IHOUiniM. PttOCUS
7419921 Coal ceobustlo*.
Industrial
7419921 Ceal coebustlen.
Industrial
7419921 Oil coetwetlen
7419921 Oil coebuttlan
743992) Oil coabuttlen.
Industrial
7419921 Paved read*
7419921 Paved roada
74I992I Paved roads
7419921 feueeo sludge
Incineration
7419921 Sevaeo sludge
Incineration
7439921 Senate sludee
incineration
Industrial
7419921 25 Uood coabuatlon.
Industrial
7439921 2S Uood coabustlon.
Industrial
7439921 2951 Aaphaltlc concrete
production
7439921 2951 Amhaltlc concrete
HUSSION SOUflCf
Cnalnerata ttekar
uatertuba boiler
Underfeed (taker
uitertube bailer
Industrial, ceeeerclal.
and residential bailer*
Utility bailer
Oll-rlrad bailer
Duat reontrainaant
Entire aaurce
Vehicle exhaust
Fluldlied-bad furnace
Fluldlied-bed furnace
Multiple heartk furnace
Balanced draft ulckes
stoker-fired Industrial
bolter
Balanced draft wlckea
stoker-fired Induatrlal
boiler
Plant stack
Flint Stick
Sec COM BUNION FACTO*
102002 0.000* let/IOC* ITU heat
input
1020020* O.OOO* lba/IOC« ITU neat
Input
1 0.9 Ik/10112 Btu
101004 21 Ik/10112 ltd
102005 0.0001* ibeVIOM B7U heat
Input
«.«! x IOC-S le/vahUlo
eil*
1.412 x lOi-4 Ib/vahlcla
4.41 x 10C-* Ib/vahlcla
eile
SOI 0.0002 - 0.005 Ibe/tan
dry tludtt
SOI O.OS2 Ibs/ton dry sludge
SOI 0.02* - 1.77 Iba/tan dry
tludee
1020090* *2**l lb/IOC12 Btu heat
input
1020090* 0.00022 Ib/ton fuel or
0.007 no/t
1020090* 0.00040 Ib/tan fuel or
0.01S ng/J
305002 1.9fl x IOC-11 Ib/ton
30S002 9.9 « 10E-IO Ib/ton
NOTn '
Uncontrelled ealttlene
Uncontrolled eel talent
Uncantrallee), calculated baaed an enelneerUe
Judgaaant. ateuned uae distillate all
Uncontrolled, calculatad baaed an engineering
Judsaaant. aaauaad uea real dual all
Uncon troll ad aaleelane. baead an 1 teat
Calculated baead an data available far 1975-197*
Based ea field Maaureaanta far I97S-197*
Projected aaleala* factor far 1990. calculated baaad ea
coeposlte vehicle aaaratlan
Contrail ad by net acrubbar
Uncontrolled aelsslons, tingle teat
Uncontrolled aelsslons, average of ( teats uaa O.S3
Ibs/ton
Saeple resultt, 1 plant* aieed fleurate • .S14 kg/a.
boiler has 3-patt design eYrtyeeh relAjectlan.
uncontrolled
Dry need, one plant, partlculata central u/aachanlcal
collector (cyclone), need feed rate 0.29 kt/l. ball.
eil. 55.31
collector (cyclone), awed feed rate O.S4 kt/t. boll.
eff. 41.31
value*, range It 1.7 x IOC-II - 4.2S x IOC-II Ib/ton
Uncontrolled froe a alngle plant, average of 2 values.
MfYMNCS
tit
tit
M
M
11*
122
122
122
201
203
201
17*
177
177
170
170
10C-IO - I.I X IOE-9 Ib/ton
-------
rot* Mo. IM
0*/2I/M>
CM fit
Nunm COM iNoumiM. raoctn
(flllilON MUKf
KC COM INIMIOM r*CTM
74It*2l III2 ftMl •reduction
«r»on o*y«w WJOOt *.«]» Ike/to* etoel
decerkurlletlM VMral
(•UIMeii gteoil
IM
74JM2I III! Stool production
74I**2I 1111 Forroelloy production
Iloctrlc ere Iurn.ee/A00 10100* 0.11 Ike/to* (tool
we..ol etreeee cooklned
Electric arc furnace. UM0702 *.0e Ik/ao-kr energy
ee.led. elllceoaneanaee ceneueed ky furnace
M«ltllH IU>t
C/tl»t tod r«v«rtar>tory 1040040] 0.00*4 lk*/ton
Co«U• 0.0047 - 0.0141 Ikl/tan
741**2I list Solder eenutecture
741»21 14* littery lte.d-.cld>
e.nuf*cturo
741*>2I 14* littery lle.d-ecld)
Enltra »rec«»
I040OT O.I -0.4 Ik/ten !•»«
on on* ftourc* toot »nd oAotnoorln* ••tiotto* Iro*
throo othor Iwllltlo*.
Le.d oxide production 10400SOI 0.0024 - 0.014 Ik/ton Controlled ulth a kaghouee. leed acid katterlee
Italtln* »roc«««
10400$ 0.11* Ik/ton l««d
Uncontrollod. k«»od OA Ml •ntlnoorin* oitlMt**
•eld ktttorlM
741ft21
l«t»«ry
•«nuf *ct
74I9t2l 14tl lAttary ••nufactura
I0400S2I 1.72 Ik/too ei l«4d
Lod ox in* till - ktrton 10400J24 0.4* lb«/ton e<
pruc«»« throughout
Uncontrollod. l««d «cld k«tt«rlo>
Controlled by • kiohouu, lo>d outdo >Unt not
k«ttorlo«. lo>d Mid btttorloi, r.nM U 0.11 - 0.74
Ib/ton
14*1 l>U«ry >«iulld< b«ll olll
I0400SOI 0.0027 Ibi/ton ol
throughput
Controlled by • o«*houu. lotd «cld fcittorln. r«n»o
0.0021 - 0.002* Ib/ton
74}»*2I }4*l littiry o«iu<»turo
r«cl«ofttlon
30400S10 0.101 Ik./ton ol le.d Controlled ky caec.de ecrubber «t .verage efficiency of
feed M.JI. le.d ecld b.tterlee. r.nge le 0.044 - 0.142
ID/ton
741»*2I 14*1 lnd
•l»«r ch.nglng
1040090* 0.4$* lbi/1000 b.tt.rl.. Controlled by baghou.e at .ver.ge efficiency of *7.n,
produced le.d .eld ta.tterlee. r.nge le 0.424 - 0.4*4 Ik/1000
Slitting e.chlne
-------
Faaa MO. in
Ot/21/tO
CAi (1C
NurtMit coos INMMTIIIM. rmcco
KC CON HUSSION men*
MOTH
laad
Load
743tt21 Mtl lattary aanufKtura
743M2I Mtl lattory oanufutura
743W2I Mtl lattery aanufactur*
743tt2I 3atl lattary aanufwtura
IllltU* MCklM
I0400SO* 0.24 ika/IOOO kattarlaa
•raducad
Srld caatlM and ol.lna 30400SO* O.M1 IkaVIOOO kattaria
arodocad
Srld caatln* and «ull 10400M* 0,0*1 Ik»/10M k*tt«rl«
Crl< cotlnt
S04009M 0.00 Ibl/IOOO ktttvlM
CMtr*ll«d by kMhMM at *W>M •fllclMKV •< tO.n. ItJ
lud *«d k4U«ri«
cuitrdlW at «w«w •fflclancy •« It. 71, It]
laid acid kattarln, ranaa la O.OJO - 0.004 Ik/1000
ktttarla*
Rata-clon* cwitrallad at avaraaa aKIclancy a< t4.2I. 1*1
lud acid kattarln. ranaa !• O.OSJ - 0.041 Ik/1000
k«ttarlm
Rota-clan* cantrallad at avaraaa alllclancy ai t4.II. Its
laid acid kattarlaa
743tt21 Mtl lattary aanufactura
Thru »rac«» lw«tl«n JD4O0504 9. Ill
wwitiM »ro*ic«d
Contrallad ky kaaliauaa with avaraaa afttary au«i4tctura
743tt2l Mtl littary ••nul.ctura
Thraa »roca»a forjutlon 30400504 1.11 Iba/tan af laid
aoaritlon throughput
J0*00507 1.72 Ika/ton o« lalda production 1040OS 0.02 Ihi/ton of la
-------
P.to Me. IN
0»/21/tO
POLLUTANT
Loed
Loed
Lud onlde
Lud o«lde
Lud o«lde
Lud e>ld«
Lud oxide
Lleonone
Lteonono
Lleonene
Lleonene
Lleonene
Lleonene
Lleonono
Lleonene
Lloonene
LlBonan*
CM (1C
Nunm cooc iNoutniM. Mocm IHI««ION MUM*
74!**2I «»ll Coel coebuttle*. «eeldentlel heller*
rnldentlel
741M2I KM Ho*plt«l Meet* locleereter
Incleeretlen
111714(1 1112 (tool production Electric ere turetce -
cherte end tej» cycle
HUM* 1112 Stul production WO vetoel - eelt end
refine cycle
1117340 1312 Slnl production Electric we iuruc* -
Mltln«/r««lllln«
III7JM I3Z Ire* leundrln Electric »rc iuruce -
chftr«e «nd t«» cycle
I3I7U* 132 Iron «eundrle> Electric *rc (ur/nce -
e In e««erl«nt«l
burn hut
llUtl Scrw tire, men burnlnt Tire* In enrerleent*!
burn hut
I3BB43 Scr*» tire, open burnlnt Tire* In eK0erleent«l
burn hut
bum hut
138841 Scr» tire, wen burnlnt T|r.. In e»perleentlecet, burn rete • I.I ie/hr. uncontrolled
IAO-2 extrectt N/nt enelvtlt. chunk condition • 1/4-1/4
e( tire, burn rote • 1.7 kt/hr. uncontrolled
UOiT tte»l« burn rete - l.f k«/kr. shred condition •
2' by 2* olece. uncontrolled
VOST •M*|OI burn rete - 2.1 kt/hr. thred condition •
2* by 2* piece, uncontrolled
VOST ueolee burn rete - O.t kt/hr. shred condition •
2* by 2* »lece, uncontrolled
VOST •••vie* burn rete - 1.1 ke/hr, thred condition •
2- by 2- tloce. uncontrolled
VOST ueolot burn rate - 1.4 kt/hr, thred condition •
2' by 2* piece, uncontrolled
VOST •«wle* burn r«t. - O.I kt/hr, throd condition •
2- by 2* piece, uncontrolled
VOST people* burn rete - O.S kt/hr, chunk condition! •
MFDbD
M
1*7
IN
!*•
IM
1M
IM
212
212
212
211
212
212
212
212
212
212
1/4 t« 1/4 ol • tire, uncontrolled
-------
rat* No. lit
Ot/21/tO
CM (1C
NUnKft COM INDUSTCIM. rHOCIM
iniuiON taut*
KC COM
NOTU
netn*alu*
nalelc anhydride
nalelc anhydride
Halelc enhydrlde
IUM1 Scrap tire, open kurnla*
74399S4 29S1 nepheltic concrete
production
7439954 J95I AspheltlC cencr.te
production
10III4 IMS Phthellc enhydrld*
production • naphthalene
proceap
2MS rhthatlc
production - ntfththelene
process
Tirn In MMTlMUt*!
burn Hut
1tr«* tn
burn hut
305002
».0*7 tk/tM tlr*
O.OX1 Ik/tM) tlr*
•.• x
concrete
J.»« K IOf-7 lb/t««
VOST eaeplea kum rat* - 1.7 «*/hr. chunk candltlone e
1/4 t* I/* of a tire, uncontrolled
VOST seeelos bura rat* - 1.27 «e/hr. chunk cendltlona e
1/4 to 1/4 •« e tire, uncontrolled
Controlled (unspecified)
-------
•aee He. 1*0
0*/2I/M
CM SIC
WJnoU COM IMUmiM. PdOCIU MIUION tOUKI
ICC COM DIIUION FACTO*
Hantanou
7419945 CMl CMtantlM
741*949 C*«l coebuvtlen
743994J Cul ctlan
741*945 C»l uebuttlon
74399*5 Cul coebultlan
7439*45 Cut contention
741994* C»l ca*Bu*tlon
AntkrKlt* c**l-flr«4
cycled* kallvi.
Utl 1 /CMMTC/IUdlMtr
Ant hr>cl«« cul-flr**
cvclon* b«ll*rft.
Utl 1 /CMMTC/tlldUltr
Anthracite coil-llr*d
•ulvorliad dry bettee
bailor!, utll/ceeoerc/lnd
Anthracite coal-tired
•ulvorllid dry bottoe
bailor*, utll/coeeerc/lnd
Anthracite cul-flred
boll*r*. utll/coeeerc/lnd
Anthracite coal-. utll/coeeerc/lnd
Anthracite coal-fired
oulwerlMd net bottoe
IH Ik/10112 Mil
71-135 Ib/IOCU lt«
Controlled k4tk ftr. C4lcul«t*d b*Md •• *nftMdrlM
Controllod vltb Krutobw. c>lcul»t«d Mud
«n«tn**rli>* Juo»«»«tit
1070 Ik/10112 Itu Uncontrolled, calculated baled on
Judoaoent 14
1430 Ib/IOf 12 Itu Contralled Kith eutttclane. calculated baud on
Cantrollld -ltd ocrubbv. Mlculotod k*ood on
14
441 lb/IOCI2 Itu Controlled ulth (IP. calculated baaed en entlneorlnf
17 Ib/I0fl2 Itu
I 112-1070 Ib/I0(l2 Itu Uncontrolled, calculated bated en entlneerlnt Judteeent M
Hantano**
7419*45 C««l contention
7419*45 Cul coebuitlen
7439945 Cokl co*t>u»ttBn
Anthracite co*l-'lr*d
•ulv*rli*d net bottoe
boiler*, utll/coeeerc/lnd
Anthracite coal-llred
•uW*rlx*d u*t bottoe
botlw*. utll/coe«rc/lnd
Anthracite coal-«rc/lnduttr
c vet on* baU*r,
utl ) /co***rc/lndustr
32-419 Ib/I0il2 Itu
490-1300 lb/IOCI2 Itu
Controlled ulth EST, c*lcuUt*d b»*d on enflnoerlni
Jud««.«nt
Uncontrolled, ba**d on eeaaurttd *nd calculated eel**lon 14
-------
fata No. l»|
0*/2I/*0
CM IIC
NUIUB. COM INDUSniM. niOCIU
fHIUIOM mud
KC COM nifSIDN r*CT«
MTtt
Itanoaneeo
flanoaneee
Itenoenoae
74im« Co«l coebuatlon
741»MS Coal coebuatlon
74J9MS Coal ceebuatlon
cvclxii ball«r.
i>tl I /to— «-c/l«*i»tr
cyclftna boilw.
utt I /u*Mrc/lii*i*tr
I *22-«7 Ik/IMIS Itu Controlled uitk eultlclone. calculated baaed M
Ifl U/10C12 Mo
70-111 Ik/l«CI2 Itu
Controlled «ltk CSF. b»»d on MUTU tmt*
Contr.11.4 «ltk «ru66*r.
M
M
neneeneeo
Hanoaneae
rtanoeneee
743*»eS Coal coebuatlon
74J»t«S Co*I coebuatlen
74im« Coil cookuttlon
MJ»»«« Ce.l
lltu.lnoui ce«t-*tr>4
•utv«rlz«d dry botte*
2tW Ib/lOf 11 itu
MI MUTC* t««t»
lltuilaoui ca*l- cxl-ltrcd
•ulixrlud Mt kottM
1IM tb/IOflt Itu Controlled ultk •ultlcloni. k«Md on controlled ,
uncontrolled eeUelon te.t deta
lb/10C12 Itw
14 IWIOCI2 ftu
Controlled »ltN It*. b«ed en eeurce: te«t»
Controlled Bltk ecrueber. baled en MUTCI te»t«
•01-2*10 lk/IOEI2 Itu Uncontrolled, calculated baaed on enalneerlne Judeeeent M
7tlM>
7<3tt45 Coil cortu.tlon
Ce«l co«bu»tlon
iltualneo* cfl«l~f
•ulw«rlud u
bolUri. utll/cu«rc/Ind
i coal-fired I
Bulv«rl>«d
boll«r>. ut
§tolt*r boflcr*.
}77-IJM> Ik/10112 *tu
177 1»/IOCI2 Itu
Centrelled xltk eultlclen*. calculated baled i
•nvineertn* judveeont
Controlled xltk (eP. baaed en eeurce teat*
2170 IWIOC12 Itu Uncontrolled, baaed on aource teata
llaneaneta
74J»»»5 Call coibuttlon
74I»»«5 Coil c«bu»tion
lltualnoua coal-fired I
•praider atokar bollar*.
utlI/co^Marc/lnduatr
lltualnoua ci»l-flrad 1
•l>r«4dar atokar boiler*.
util/co»erc/lnduetr
1M-1010 lb/10E12 Itu
11-471 lb/10E12 Itu
Controlled ulth eultlclem. baaad on eeaaured and
calculated evlaajon lactora
Controlled wtth CS*. baaed on »aaaur«d and calculated
aetaalon factora
-------
rate Me. l»l
09/21/90
POLLUTANT
CM SIC
MJHKR COM IMUM1UM. MOCIM
(MIUION
KC tout HUM ION FACT*
NOTM
74399*1 Cool coeeuotlo*
74399*5 CM! coebuotlo«
74199*5 CMl coobuottoe
74199eS Coal coebuatle*
74399*5 Coll coeeuatlon
74399*5 Coll contention
74199*5 Co«l coebuatlon
74399*5 Coal
Co«l coabuction
Lltnltt c
l-«lrod
cvclon* bollori.
utl 1 /couorc/lnduitr
Llonlto cul-'lroa'
•ulv«rl>od ovy bottoo
bollor.
ut 11 /cowrc/lnduitr
Ll»nlt( co«l-«lr«<
pulworllod dry battoo
bailor,
ut I I /caoaarc / Induttr
Llonlto co«l-flro<
rulwwliod dry battoo
bailor,
utl I /ceooorc/lodustr
tlonlto co«l-tlM*rtii« iudnoont
Uncantrollod. colculotod boood on onolnoorlnt judoooont
Controlled by eultlclem. calculated baaed en
efialneerlea. Judfeaent
Controlled by IV. calculated baaed on enalneorlno
Controlled by ocrubbor. calculated baaad en enflneerln
Judaaeent
4.410-U.ISO Ib/IOCU Itu Uncontrolled
flanaaneao
7<3»»*5 Coil ei»bu>tlan
tlanlto co«l-llrod
^ulwerlxod wot bottoo
boilort,
utll/coooorc/lnduttr
2050-7580 1D/IOEI2 Itu
Controlled with eultlclene,
analnaerlfiv Judaaoant
Co«l coabuitlon
I.l9nlto co«l-ftrod
pulv«rlx«d w«t bottoo
9«5 lb/IOCI2 Itu
Controlled with 1ST, calculatad b«aad on onolnaorlno
judflaoant
utl) /co«»«rc/!ndUftr
-------
faee He, In
0»/2l/tO
CM
•1C
POLLUTANT
tunic* cone INDMTCIAL nwccn
OIIMION
KC CODC BHMtlM FACTOR
NOW
74)t*ef
naneanaae
llantanaae
74jee«t
74)eM5
CMl coebuetloe
CMl Coebuatloe
CM! ceebuetiMi
Coal coetouatlon.
roaldantlal
Coal ceabu«ttoA,
r»ldtntl
-------
rate Me.
0*/2I/M
POLUITMir
CM SIC
NUMCI COM IMUeTMM. MOCfU
(HIMIOM
tec COM tfliMiOM rftcm
Oil ceebuitle*
Otl coebuetlee
Oil coebuetle*
Oil ceebuatlon
Olttlllate ell-fired
boiler.
utl I /coe»erc/l«duatr/rail
dentlal
Hoeldual ell-fired
boiler.
utll/coaaerc/lnduetr/real
dontlal
Hail dual ell-fired
boiler.
utll/coeaerc/iliduatr/roal
dentlel
Realdual ell-flrod
boiler.
utl1/cowi«rc/lndu«tr/ra«l
I.M iwioiia M«
Ik/IOfU »tu
II.M Ik/IOCIt ttu
1.72 Ib/IOCU Itu
Control 1*4 nit* Krubtar. calculated b*M* M
Unc«ntr«ll«d. calculated ba>a4 on •ndnavIM Jud««»ant
Control I •< Hltk •ultUlona. calculated baud M
Controlled Mttk Iff. calculated kaead en entlnnrlne
Judoeaent •
Oil coebuatlon
Kealdual ell-flred I
boiler.
utl1/coeeerc/lnduatr/real
2.M IWIOCI2 Itu
Controlled Kith icrubeer. calculated kaeed en
enilneerlne Judeeeent
7«3»f«5
7 1.0 Ik/tan wood burnad
Industrial 10200* 1.0 Ib/ton weed burnad
Flrealaca 1.0 Ik/ton wood burnad
Uoodttova 1.0 Ib/ton wood burnad
UooJttove or fireplace 1.0 Ik/ten burned
Uooutxova ulthMit baffle 1.1 > 10E-4 Ib/ton wood
burned
Cenaral e.l.lloni 305 Neilldble
Curing oven - realn 110001 1.4* * 10E-4 Ib/ton
flnltn fabric
Halt aattlng 130001 2.2 x 10C-S Ib/ton fabric
(U.Uhln» ftbrlc
Centre! etatue MlMecIf ted. fcaaed en eaUelon factor f4
for reeldentlal yoodatevea
Control etatue unanecl'led. baaed en eetaalon factor *4
for raaldentlal ueedatewee
Control atatua and kaala uneaectfled *4
Uncontrolled *4
Uncontrolled, baead en one etudV. nonbaffled (tove *•
burnlnv eraen etne
Mien irade ere ne lonier elned In U.S. II
Uncontrolled, average of three taata 92
Uncontrolled, baaed on teat data 52
s
t
-------
lUfH Ma. I*S
Ost/21/fO
H.U.UTANT
IU/.MI....
fUfifMtH*.!
no\n««n*c«
IUnf«n*».i
n*fit«n.»M
fUnt.>n«»«
rUi>9*>n»*i
n*>n9*.na»
fUn9 ...!•«•
n*n9e>n««.i
n*n9«n«»«
fUnt*na»«
n*>n ••»*»•
n*nv »(%•«*
fUng*n.«ft«
n«n9o.n*»«
n*n«*n.it.a
fl«n0«n*TC*T
CM
MUriMJt
7«w«
743*t49
743M45
743f*49
7OWI
743»»*$
74JM45
74Jf»4S
74J»»4S
,43,,«
741tt.S
74UMS
741*teS
7«t»»S
743»»4S
7434M5
741tt4S
741,,4,
CODE
lie
III*
lit*
HI*
III*
111*
111*
211*
211*
211*
111*
211*
2t5l
2»51
1241
1241
1241
1241
INOMTMM. PftOCIU
Uovon fabric finishing
Chenlcal application*
Manganese cheat cat
production
nanganase cheelcal
production
nanganese cheelcal
production
production
(synthetic) production
(synthetic) production
(synthetic) production
(synthetic) production
(synthetic) production
(synthetic) production
Asphaltlc concrete
production
Asphaltlc concrete
production
Ceeent eanufacturs
Ceeant eanufactura
Ceeent eanufactura
Ceeent eanufacture • dry
process
IIIIMIOM MUCCI
TkornoMl dyeln«
Intlr* *roc*g*
Ore drytng/*rlildlM
Ore drylng/orlndln*
Ore roasting
Or yer / or 1 nder
Dryer/erlnder
Packaging and liandllM
Packaging and handltnl
Roasting
Roasting
Plant stack
Plant stack
Clinker cooler
Clinker cooler
Clinker cooler
Oryer/grlnder
KX COM
DOOM
Ml
J01070
301070
101070
301070
101070
101070
1 301070
I 301070
101070
501070
105O02
105002
105
105
105
10500tll
million FACTO*.
I.I M lOI-» Ib/ten fabric
1 Ik/ton mod
l.» Ib/ton of natorlal
precesssd
O.OO* Ib/ten of natorlal
110 Ib/ton of natorlal
processed
O.ll Ib/ton of natorlal
processed
l.t Ib/ton of eat or 1.1
processed
0.00* Ib/ton of naterlal
processed
1.4 Ib/ton of oaterlal
processed
0.0054 Ib/ton of eater! al
processed
110 Ib/ton of naterlal
processed
0.12 Ib/ten of utertal
processed
1.01 x IOf-10 Ib/ton
concrete
5.72 « 10£-t Ib/ton
concrete
5 « IOE-4 - a.l « 1OC-5
Ib/ton caeant
2.3 x 10E-5 - 4.S > 10E-5
Ib/ton ceeent
2.1 k IOE-5 Ib/ton cxant
produced
0.041 Ib/ton count
produced
MOTH ' '
Uncontrolled, average of throe test*
lased on engineering estleates
Uncontrolled, calculated based on engineering Judgeeent
Controlled bv fabric filter, calculated based on
engineering Judoooent
uncontrolled, calculated eased on engineering Judge* ont
Controlled by fabric filter, calculated baud on
engineering Judgeeent.
Uncontrolled, calculated baud on engineering Judgeeent
Controlled by fabric filter, calculated based on
englnoerlni Judgeeent
Uncontrolled, calculated based on engineering Judgment
Controlled by fabric filter, calculated based on
engineering judeeoont
Uncontrolled, calculated baud on engineering Judoeeent
Controlled by fabric filter, calculated baud on
engineering Judgeeent
Controlled (unseeclflodl froo a single plant, average
of 1 values, range Is 1.43 « 101-10 - 4.4 « IOE-10
Ib/ton
Uncontrolled free a single plant, average of 2 value*.
Controlled by fabric filter, calculated based on
engineering Judgeeent
Controlled by gravel bed. calculated based on
engineering Judgeeent
engineering Judgeeent
Uncontrolled, calculated based on engineering Judgeeent
ItTIMN
ft
II
107
107
107
107
107
107
107
107
107
107
170
170
107
107
107
107
-------
Page Me. If4
0*/2I/*0
rOLLOTAXt
CM SIC
bUHf* COM IMaJtTPlM. PDOCtSS
iMIUlOH COUMCt
*CC MM (HIMIOM MC1M
HOT!*
741994S 1241 Ceeent eanufacture - dry Kill
jottetH t.m ik/un cwwi
1*7
llanganeee
1241 Ceeent eanufacture • dry Kile
eroceaa
74I9MS 1241 Ceeent eanufacture - dry Kile
erocoeo
741444S 1241 Ceeent eanu'acture - »et
ereceee
7419943 1241 Ceeent eanufacture - net Kile
oroceae
741994S 1241
1241 Ceeent eanufacture - net Kiln
eroceea
741994S 1112 Col
74I994S 1112 Iron and ateel
Coke even battery
on General eelaalone
743994S 1112 Iron and ateel oroductlen Iron blaat furnacaa.
caathouae eelaalona
7439943 1112 Iron and ateel production Iron blaat furnacea,
caathouae aelaalona
743994J 1112 Iron and ateel eroductlon Iron blaat furnacea.
JOSOMM 2.1 x tOI-f - 1.2* II
IOt-4 Ik/ten ceeent
10S00404 I.I x IOI-S - 1.24 x
IOt-4 Ib/tM ceeeet
USOO? 0.414 lk/t«i
Coo trot 1*4 by ISP. cilcuUUd baud on «»ln«orlng
Controlled by <«krlc Illtor. MlcuUtod baud on
M5007W 0.114 tk/tM c«Mnt
Uncontrolled, colculotdd k*Md on oatlnoorln* Jmimnt 107
IMcontrollod, colculotod bMod M onilnoorlno Juaionont 107
1090070* 2 x lOf-S - 1.42 x IOC-4 Controlled by IIP, calculated baaed on engineering
Ib/ton ceeent judgeeent
30S0070*. 4.* x 10E-S - 1.12 x Controlled by fabric filter, calculated baaed on
IOC-4 Ik/ton craent englneerlee judeeeent
101001 0.02* Ib/ten coal burned laaed en engineering eetleatee
101 0.04 Ib/ton Iron and laaed en engineering eatleatea
ateel aroduced
1010012* O.OOOle IB/ton of Iron Controlled by runner covert b elckue hooda te fabric
filter, calculated baaed en engineering Judge.
IS
IS
lOlOOU* O.OOIS Ib/ten of Iron Uncontrolled, calculated baaed en engineering Judeeeent 107
107
Uncontrolled, calculated baaed on engineering Judgeeent 107
74I»»«S 1112 Iron and ateel •reduction Open hearth furnace
•eltlno/reftning
74I*t«5 1312 Iron and ateel eroductlon Open hearth furnace
oparttlona.
30100401 0.071 Ib/ton of elg Iron Uncontrolled, calculated baaed en engineering Judgeeent 107
3030090) 0.001 Ib/ton of elg Iron Controlled by CSP, calculated baaed on engineering 107
Judgeeent
743aai5 3112 Iron and ateel production Open hearth furnace
operfttione. roof aontta
7419945 3312 Iron and atael aroductlon Opan hearth furnace
301009 0.0004 Ib/ton of rig Iron Uncontl
303009 0.00024 Ib/ton of »lg Uncontrolled, calculated baaed on engineering Judgeeent
Iron
107
107
langanefe
7439945 3312 Iron and »t«*l production
101009 4 x IOC-4 Ib/ton of tig Controlled by aide-draft hood to fabric filter.
Iron calculated baaed on engineering Judeeaont
-------
Pit* No. 1*7
0»/JI/»0
COM INDUSTIIM. PMKXSS
flllSSIOM MUKI
tCC COM OIIM10N r*CTM
Mont
743Sml 1311 tree. And stool production Slntortnt operAtlons.
•Inter dlschArte (broAke
end hot ocreen)
3312 Iron And stool production Slnterlnt eeoretlon*.
sinter dischAree. Ckreske
And hot screenl
743*MS 3312 Iron Md steel production Slnterint operitton*.
•Inter dlschAroe (krssk*
And hot screen)
713t»4l 3312 Iron Md stsel production Slnterlnt oporitloM,
wtndboM And dlscherte
743*MS 3312 Iron Md otool production Slntorint eporAtlonl.
303001 0.01 Ik/tee, of sinter Uncontrolled. CAlcuUtod OAssd en entlneorlnt JudtoeMt 107
30300* 0.0012 Ik/ton o« olntor
JOJOOS 0.007 Ik/ton 0« llntor
303(KW O.OOM Ik/tOH at olntor
Controlled kv lAbrlc filter, colculoted kosed en 107
ontlnoortnt Judteeent
Controlled ky orifice scrubber. CAlcuUtod OAsed on 107
entlneerlHf Judeeeent
Controlled kv fAkrlc filter. CAlcuUtod OASed en 107
entlneerlAt Judteeent
30300813 0.134 Ik/ten of sinter Uncontrolled. CAlcuUtod koMd on entlnoorlnt Judeeeent 107
743t»*S 3312 Iron And stool production Slntorint oporotlons,
windboM OKhAust
743*»4S 3312 Iron Md steel production Slntorint operAtlons.
wlndbox OMhAUSt
743***S 3312 Iron Md stool production Slnterlnt operAtlons.
ulndbox OMhAUSt
743»**S 3312 Iron And steel production Slntorint aporotlons.
UlndbOK OKhAUSt
3312 Iron And (tool production Ctntorlnt ooorAttonft.
oi(h«uot
30300113 0. IO4 Ik/tan ol olntor
743t»*S 3)11 Stool production
743M4S 3112 Stool production
3312 Stool production
7«3»>45 3312 Sto«l production
SAAIC OKyten furnAce
oporAtlens, SOr* eonltor
SA*|C OMyaon furnACO
op.r.llont. Q-tOT ,ro,
ooltlnt/roUnlnt
Bttlc oxygon furnoco
op«r*tlonA, cKAralnt
BAA|C oMyton furnACn
ofiorAtlonA. hot ootAl
After cooroe portlcle reeavol. colculoted kooed on
entlnoerint Judoaeent
107
30300(11 0.01*2 Ik/ton ef sinter Controlled kv dry ISP, CAlcuUtod koted on ontlnoerlnt 107
30300SI3 0.001 Ik/ton of olntor
Controlled kv vet ISP, c Aleut At Ad kAOed en or.«ln«rln«
Judtoeent
107
3030Oit3 O.O054 Ik/ten ef (tnter Controlled kv scrubber. CAlcuUtod kosed on entlneorlnt 107
30100SI3 0.012 tk/ton o« olntor
303Ou» O.OOS Ik/ton ef stool
30J
-------
•ace No. 1M
O*/2I/K>
CM
(1C
caw itnimiM. mocfit
tniMIOH UUHCI
KC CUM tTilMIW FACTO*
74im* 1112 iteel production
Ilectrlc arc furnace
MMO» t.tta Jb/ten •« aroduct IMco>tr«IIW. calculata4 baaad •» anilaaarln Ju«o««ajit 107
rleneeneee
Manaaneee
743ms 1112 «t««l production
741**tS 1112 (teel production
743»M! 1112 »teel production
74]**«S 1112 eteel production
741*»«S 1112 *leel production
74I**«S 1112 eteel .reduction
74J»*e9 1112 «teel .reduction
74I**as 1312 fteel .reduction
Ml t/r«
•I ley »t««l
Clactrlc arc fumaca
•aaratlona.
•alt/ra/ala«
cartoon ataal
Clactrlc arc furaaca
operation*.
•al t /ra« /char«a/taa/al ae
carbon ataal
Clactrlc arc lurnaca
o»aratlonaf
•altlna/rallnln* carbon
ataal
Tep-bloun baatc axyoan
lurnaca, Baltlnv/rafinins
Tea-blown baalc oNyaan
lurnaca. aal tlna/raf Inlna
Tea -blown baalc aKyaan
furnaca. aeltlna/raf Inlnt
Tea-blown baalc OKyflan
furnace, aaltlnf/ral Inlna
10100* *.017« Ib/ton a4 areduct
Cantrallad by fatal bulldlm evacuation ta fabric
filter, calculated baaed en eniUeerlna Judiaaint
W100» l.n Ib/tan *t eroduct UncentrolleJ. calculated baaed an enalnaarlnf Judaeoent 107
lOIOOt O.OOIf Ik/tan af areduct
Controlled by OK ulna charhln«/erlndtnt/alitn«
by electric arc furnaca
.roce.a
3311 Farrea*n9anete .reduction L«dle treateent
precast
0.41 Ib/ton of Itn areduct
O.U Ib/ton of no product
7.S Ib/ton of nn aroduct
Control etatua unaaaclflad. calculated baaed i
anfllnaarlnf) Judeeaent
Control atatua unaaaclflad. calculated baaad i
enelneerln0 Judeeeent
Control atatua unaaaclflad. calculated baaed i
enelnearln* Jud9aaent
107
-------
Caoa No. I**
09/21/90
NLLUTMIT
CM *IC
MUnK* COM IHDUtTtlM. PDOCCU
«CC COM inittlON F«TMI
743994S Jill Ferroeanieneeo aroductlen Oaen i
by electric arc furnace electric furnace
eroceee
741994S 3311 Ferreeaneanaae production Open i
by electric arc furnace electric furnace
103004 ll.t Ib/toii »f oroduct
303000 4.14 Ik/Nft concueed ay Uncontrolled, baaed on tf-<2 date lor ferroalloy
lure., operation product lee
107
743994S 1111 Ferroaaneaneae production Open i
by electric arc furnace electric furnace
74I994I 33IJ Ferroeaneenaea production Open
by electric arc furnace elec(
30100* 0.4 in/toil el product Controlled by acrubbera. calculated free) aource teata
el total pertlculate eel eelone
1010O4 O.llt Ib/nun conaueed by Controlled by acrubbera. calculated tree aource teata
fur*, operation ol totel partlculata eelaalona
107
743994S 3313 Ferrooentaneae production Sealed aubaereed-erc
by electric arc furnace electric furnace
lt.2 lb/ton el product Uncontrolled, baaed on *f*-« data lor ferroalloy
production
107
7439*4$ 3313 Ferroeantanaae production aeelai
by electric arc furnace electric furnace
303 *.4t Ib/NUh coneueed by Uncontrolled, baaed an *f»-42 data lor ferroalloy
lurn. operation production
7439945 3313 Ferroeaneaneae production Sealed aubeereed
by electric arc furnace electric furnace
303 O.OOe Ib/nun conauead by Controlled by acrubbera, calculated Iroe aource teata
lurn. operation of total partlculata eelaalona
107
743»*4S 3313 Ferroeanianeae production (ael-aeali
by electric arc furnace electric furnace
procaaa
743*949 3313 Farroeantaneae production Sael-aaalad aube<
30300701 S.2 lb/ton ol product Uncontrolled, baaed on «>-42 data for ferroalloy
production
3030O701 2.31 Ib/nut conaueed by Uncontrolled, baaed on AP-42 data for ferroalloy
furn, operation production
107
743*»4S 3313 Farroeaneanaae production Saal-aa«led aubaartad-arc 30300701 0.01 lb/ton of product Controlled by acrubbara, calcul
by alactrlc arc furnaca alactrlc furnace of tetat partlculat* eelaalon*
743<*4S 3313 Farroaanuneaa production Sael-aa>l*d aubear>eil-arc 30300701 0.037 Ib/nUh cenauead by Controlled by acrubbara. calculated free aource teata
by alactrlc arc furnace alactrlc furnaca furn. operation of total partlculate eelaalona
procaa*
107
743*945 3313 nan9«neea-bearlnff Cruanlne and <
ferroalloy prod/alactrlc
arc furnaca proc.
743*9«5 3313 nanpjnaaa-bearing Mccajpt and a
ferroalloy prod/alactrlc ore
arc furnace proc.
303 0.90 lb/ton ef tin ore Control atatua unaeeclfled. calculated baaed on
proceaaad engineering Judeeeent
303 0.90 lb/ton of tin ore Control atatu* unapaclfled, calculated baaed on
proceaaad engineering judeeeent
-------
fooo Mo. 200
M/21/«O
POU.UTMIT
eoneoe
nonooneo.
non«oneoo
non,on...
n.n..n...
nonionooe
Mon onooe
nknv»n»o
n*m •*"••*
rUn«*ne»*
rUn94.no**
„„,«,...
Don .n«.«
CM SIC
Munm com
7430000* 3311
7430MS III1
74UO.S nil
743mS HI!
74ims nil
745ms nil
74ims mi
74im< 1111
74imS 112
741*>«9 312
741»»«S 112
743»»»5 312
74imS 112
741**tS 112
741W5 112
IWUSTIIIM. •MCMS
fleeeen.*o-keerleo.
ferreelloy ored/electrlc
ore fumoce oroc.
SI 1 Icoeeneenooo
production bv electric
ore furnoce oroceoe
Slllcoeeneeneeo
production bv electric
ore furnoc* orocooo
SI 1 Iceeoneoneoe
production bv electric
ore furnace oroceso
,Ulc<.on..n...
Sl.Uo«M««n«*.
production by electric
•re furn*ce procet*
Slllco.on«ono ore Control ototu* unooeelflod. colculotod booed en 107
C.otlno Ml 0.24 Ib/ton of He eroduct Control ototuo unopeclflod. colculotetf booed oe 107
onolnoorlne Judoeeent
Cru.hlfio/»rlndl«t/o4atn» 101 0.11 tb/toe of «n product Control ototuo unopocltlod, colculotod booed en 107
eoelneertn* Judeeoont
L«dlo trooteont 101 4.0 Ik/ton of Hn oroduct Centre! ototuo unopoclflod. colculoted booed on 107
onolnoorlni Judtooont
O»on ouboortod-orc 1010040$ 0.11 Ib/nuh conoueod by Controlled kv ocrubboro. colcutoted free oourco toot* 107
Soiled oubMreod-orc 101 0.002 lb/nu» conoueod bv Controlled bv ocrubbor*, colculoted free oourco toot* 107
.Uctrlc furnoco furn. ooor.tlon of tetol oortlculote eeloolono
Sool-ooolod ouboereod-orc 10100702 0.012 Ib/ton of oroduct Controlled bv ocrubbor*. colculoted fro* oourco toot* 107
eloctrlc furnoce of totol oortlculote eeloolono
Sool-ooolod oubeoreed-orc JOJO070I O.OOt Ib/mik conoueod by Controlled kv ecrubbere. colculoted fro* oourco toot* 107
eloctrlc furnoco furn. operation of tetol oortlculot* eelnlon*
CupoK 10400101 0.2S Ik/tea of Iron Uncontrolled, colculotod booed on endneerln* Judeoeent 107
Cupol • 10400301 0.12 Ib/ton of Iron Controlled bv **ot cop, colculotod booed on on*lneertno IO7
judoaeont
Cupol • 10400101 0.075 Ib/ton of Iron Controlled bv leelnvoeont ocrubbor. colculotod booed en 107
onfllnoorln* Juaoeeent
Cupolo 10400301 0.012 Ib/ton of Iron Controlled bv Men enerey ocrubbor, colculotod booed on 107
onelneerln* Judoaoont
Cupolo 10400301 0.003 Ib/ton of Iron Controlled bv fobrlc filter, colculotod koood on 107
entlneerln* jud*e.ont
Eloctrlc ore turnoce 10400304 O.IS Ib/ton of Iron Uncontrolled, colculotod booed on onilnoorln* Judoooent 107
Eloctrlc ore furnoco 10400304 0.0015 Ib/ton of Iron Controlled bv fobrlc filter «»»«! . colculotod booed on 107
onglnoorln* Judgooont
s
i
-------
P«9« No. lot
09/21/90
POLLUTANT
CM IK
MUMCR COM INDUSTIIIM. PMCflt
EHIMION SOUICf
•CC COM {MISSION MCfM
NOTES
7439941 112 Iron leundrle.
7439945 132 StMl feundrlm
7439945 332 St«el loundrte.
7439945 132 Steel Iwmdrlu
7419945 132 Ste
743994S 332 St.
743994S 3321 Iron ler.y) leundrl
7439945 349 l.ttery (dry coll)
7419945 349 Kttwy Idry C.ll)
e«nuf.cture
7439945 149 l.ttwy (dry C.ll)
e.nuf.ctur.
7419945 149 l.tt.rv Idry i
••nut.cture
7439945 349 l.ttwy (dry C.ll)
•«nuftcture
7419945 149 l.ttwy (dry C.ll)
Induction fwTMcej
Iloctrlc ere Iwm«c4j
Electric .re furit.ce.
(l.ctrlc we e* *nd ht>ndltnt
10400301 0.022* Ik/tM •* Iran
IO400701 0.»2 Ib/tM 4)1 tree)
10400701 0.024 it/ton .< iron
Electric we «ur««c* 10400701 0.013 Ik/ton e« Iron
10400701 0.0001 Ib/tM 44 iron
30400705 0.004 Ik/too •« Iron
104001 O.JOf Ib/ton Mt.l
304 30 Ib/ton of MtorUl
proc***«d
0.03 Ib/ton of ••twl*!
Unco.tr.llo4. c.lcul.tod b.Md on on9lnowln9 Judii.ont 107
UncMtroll^. c.lcul.tod o...d on mlnMrli* Judtuwit 107
Control l.d by IV. c.lcul.t.d b.l.d on 4WflAMrlllt 107
Jud«.>ont
Control I.d by wnturl Krubbor. c.lcul.t.d b.M4 M 107
onglmwln* Juan..nt
Controll.d by «»Drle Illtw. c.lcuUt.d b...d on 107
on9lmwlnt Jud9.MOt
UnCMitr.ll.d, c.lcul.tod b»od on on.lnowlnf Jud9«Mnt IO7
l..od MI 4M9ln«orln« octlo.to* >'
Uncontrolled, c.lcul.tod b..od on «n»ln.wln9 Jud««««nt 107
Con troll «d by fabric filter. cUculatod batod on
analnaorlno JudaatMnt
t.O Ib/ton ol utwl.l Uncontr.ll.d. c.lcul.tod b.i.d on onolnoorln* Ju .ludg.
Incln.r.tlon
7439945 495] 5.U.9. lluds.
Incin.r.tlon
&t.ck. «luidlx.d-b.
-------
P»«* Ho. 202
0»/21/fO
rOLLUTANT
fUAfMA***
n«n««A««« 9*149
n*nt»«n«*« OKlda
R*Afj*n*ui OMieU
.1a>nfj..n.»*i oxlttm
n»n«Ana«« ox.d*
n..nt»««** «Kitf«
IWcury
Itorcury
flfjrcury
tlcrcury
n«rcury
rtejrcury
tlfjrcury
CM SIC
MUtKM COW INDUSmiM. MOCIU
74}»t*S §0* HoMlt.il k»«t«
ln«U«r*ti««i
111734* Ml 2 StMl eNVductteW
131714*5 3312 «t««l product! 0fl
1 11714* 3312 St«l product.*!
III7J4* S3I2 StMl .w«K*u cycle
Ilactrlc we lurnace -
eeltlne/reflninf
Ilactrtc arc furnace •
ealtlnt/raflnlnt
flactrlc we furnace •
charte and tap cycle
flectrlc are furnace •
charge and taa cycle
Clectrlc we furnace -
Anthracite caa, -fired
ballara.
utll/cenaarc/lnduatr
Anthracite coal -tired
bollara.
utl 1 /caeaarc/lnduatr
Anthracite coal -fired
ballara.
utl 1 /conearc/lnduatr
Anthracite coal-fired
ballara.
utl 1 /coMarc/lnduitr
lltualnoua coal-fired
Dollar,
lltualnoua coal-flrad
bollar.
utll/coeaarc/lndu«tr
boiler ,
utl 1 /coaaarc/lnduitr
«CC COM DtlUlIM FnCTOI
IMOOSOf 1.4 » 101-4 Ib/ton
MMO* 2.1 Iba/ton eeeclaltv
ateel
MMOtM O.OOM - 0.24 Iba/ton
carbon ftteel
WlOOtOI O.O* - 4.1 lea/ten cwben
oteel
MlOOtOI 0.0* - 0.24 Ibt/ten
aaaclalty atoel
lOJOOMt 0.00*4 - 0.012 Iba/ton
carbon steel
IO400104 2.1 Ibt/ton of Iron
produced
10400104 2t Iba/ton of Iron
•roduced
1 II lb/IOCI2 Itu
1 VII lb/IOCI2 Itu
1 l.l-I.I lb/IOCI2 Itu
1 II 1D/IOCI2 Itu
1 14 lb/IOCI2 Itu
1 14 ID/IOC1J Itu
1 8-14 lb/10C12 Itu
Norn
Uncontrolled, teat elate
Uncontrolled eelaalona
Uncontrolled eel eel one
i Uncontrolled eelaalona
Uncontrolled oelaalana
Uncontrolled eelaalona
Uncontrolled eelaalona
Uncontrolled eelaalona
Uncontrolled, baaed en enetneorlnt Judiaeont
Controlled by If. baaed en onilnoerlni Judneont
Controlled by ecrubber. baaed on enflneerln* Judiaeent
Controlled by eultlctono. baaed en onflneerlne
Judtanent
Uncontrollod, baaod on enalnaerlnv Judaaeant
Controlleal by eultlcyclone. baaed on anojnowlne
Judaaeant
Controlled by CSr*. baaad on analnaarlnv judtaaant
U7
IM
It*
J»
-------
•
-------
•aoo. No. 204
Ot/2l/*0
tit
com iNoutrniw. mociti
Horcurv
T4J*»7»
741t*7«
74J*m
latanal CMkUOtlOO)
onflows • otatlonary
Intonial cookuotlM
onolooa • stationary
Internal cookuatlooj
oneinos - stationary
Natural too cookuotlo
rclal/lnstltutlo
Oil cooouatloo
Oil co*buatl«n
Oil cwbuatlM
Oil to»tu»tlon
Oil cotbustlM
Oil co«buatlon
Oil cenbultlen
unman
ICC COM INKS ION r*CTM
Daclarocatlo* MflM •
dlatlllato oil «wl
Eao turklno * natural tao
fuol
C» turblno - otatlllato
oil l
tfantlal
Dlitlllato oll-«lrad
bolIar.
utl I /coMorc/lHduotr/roal
dantlal
Dlttlllato oll-tlrad
bailor.
utll/conorc/lnduatr/roal
oonltal
Daildual oll-
-------
Pat* Me. 2X
Ot/ZI/M
MU.UTMIT
Mercury
Mercury
Mercury
Mercury
Mercury
Mercury
Mercury
Mercury
M-cury
ftarcury
Nwcury
n«rcury
n«rcury
H*ircury
n*.rcury
rtorcury
>t
CM
NUneU
74J»»74
743»»74
743t»74
J43»»74
743>t74
741>P7«
743»t74
743»»74
743»»74
743»»74
743»»74
743f»7*
7434*74
743»»7»
743»»»*
743»»74
(1C
COM
0721
10**
12
lilt
2112
2112
2(12
2112
2112
2812
2812
2112
2112
2»5I
INDUSTRIAL nUClgt
Mint application
Uood ceebuatlen,
reeldentlal
Agricultural eer.ylng
Mercury elnlne
Coal refuae Pile kwnlne
Oil anala retortln*
Chlorine production
tchler'elkalll
Chlorine production
Chlorine production
(chlor-.lk.lt)
Chlorine production
2 produced
101001 0.2 to 1 Ik/100 ton CI2
301001 O.I Ik/100 ton CI2
301008 4 Ib/tOO ton CI2 producsd
1.12 x IOE-S - 1.21 x
IOE-2 Ik/ton
4.70 x IOE-4 - 4.75 x
10C-1 Ik/ten
30S002 fron a alngle plant* average
of 2 valuaa. range la l.l x IOE-10 - 1.1 X lOE-t
range 1* 1.9 X IOE-* - 2.4 x IOE-*
wncei
in
Co)
US
IIS
13*
40
IIS
IIS
US
US
US
US
IIS
141
1*1
170
170
-------
Paoo Mo. 20o
Ot/21/90
POLLUTANT
Mercury
Itorcury
Mercury
Itercury
Itorcury
Itorcury
ttor cur y
Itorcury
rtoreury
Horcury
Horcury
Horcury
Mercury
Hercury
Horcury
ftorcury
CM SIC
NUTIM* COM IMNMTRlnL FftOCCM
,„„„ „„ r^u „„
741*»7* 1111 Ferroalloy production
741**7* 1111 ferroalloy production
741997* 111* Prloery eercury
production
74J997* 111* frleary Mrcury
production
74I*»7* 111* Prleary oorcury
production
7419*7* 3141 Secondary oorcury
production
7419*7* 1141 Secondary nercury
production
7419*7* 1* Electrical »»>r,tu>
oanuf ecture
741»*7« I**l littery eanufacturo
utility
741997* 4*1 Natural oa. coebu.tlon -
utility
741997* 4*1 Natural .•• CO.Outtlon -
utility
741*97* 4*1 N*tur«l ••• coobuctlon -
utility
743997* 49S3 Aunlclptl wait.
tOIMIOH tOMCI
Kloctrlc ore lum««d«
op.*. forro*«iff«iM««
lloctrlc ore 4um*c«.
tUctrtc vc «ur««c«.
•ul->»lod. «orro.HUon
Mooing operations
Retort operation
i«lt«r »t«ck
Entlr* proce.s
Entire proce...
production by VACUUM
dlttllUtlon
Handllnt o* He or It.
coapounds
Entire proce..
oth.r source.
U
-------
p.»( uoj/ni 8*00-0 IOOIOS
uovqi ZltO'O - ZSOO'O «l Murj -»»j»/tr
J»A» >e MlJ*Af HtJ»nO M|IM IO-I1U03 JSJ
p»»J UOV4I JBOO'O IOOIOS
M|u
uo>/41 KIIOO-0 - t-301 x Z't «l
*lAt
oei
JflV uo)/qi ItOOO-0 IMIOt
ZiOO'O • ZCOO'O M
1001
IOJJU05 JS3 M|UD
1/01/Q1
AJ«« (0
o» loot
J0« UOJ/m BZOO'O IOOIOS
uoijfnq.03
100IOS !•"»
>H tot
•ii
)••» »JKO« uo p»X| 'MI "4 (>»I[OJ)uo3
^lifl i»)/qi SOO'O IOOIOS
o|»)M Mt|n>nJ>d
HOJ1U03 MV41 »'£ IOOIOS
iuei uo»/ql tf-» IOOIOE
•u
A9MI9IH*
•uofltfM »3>fn9f}j*d
P»HOJJUOJ uo»/q| »-n
I 00 (OS
•it
UO BMt« •«] Aq B«||OJ)UO]
wt'tt tOOlOS
HU03 IH IOS >MII<» 'J»»II»
IOOIOS <(JO»«J»»J -ujnq »>u
•>»m |>d|9iunu
•ti
Aq p»uoj)i
P.HOJ)UOJ MV4I Wtl IOOIOS
e»
uoj/ql WOO'O IOOIM
tllON
W1MJ MtniUl 3003 33t
NOHJIH3
SH30IM ivimsnoNi 3003
313 SV3
-------
SSI no| »fttu. B.j»qqnj3ft |tuo|)u»Auo> 'p»)M»* XOOI «»»n««y »ftpn|t AJP uovqi MOO'O 90SOOIOS
•6pn|m »et».s
KIO'O - »BOO'0 «t
p»( uoi/ql ZIO'O 100IOS
>UO • JOJ1U05 |M PUt U|0« t)»P »UO
PI" •«•»•• uo|»»f«l »u»qjo« » *u|/jp ittJd*
ttOO'O - KOO'O »1 MIKJ ••MTJWW »jno« |>j*n*m »o
••A. ||*JMO MtUO |OJ)U03 Ml •<»?/•««» 00* > A*|»«3
i *Atp/»uo* 00* > M19V4V3
uovqi itOO'O - ZSOO'O «l »««J
•t* p|» -»»»t lU|AJp MJM Mtp/.UOJ 00* < <»l««3
MHO VM04 <>j»itM »o MtJM* ||>j»na MIM |«J)uei
•J0(»q >||nq 'J0i«nq«o5
put uovqi ZZOO'O IOOIOS ||»«j»»t« UJnq "tH
08«l
put uo»/q| »100'0 IOOIOS l|tnj»>tii ujnq t.tu
«n|p»« mt9 Au» o« l»poa
nmu >x|» ntBt 'jo)«nq«o3
put uovqi »ZOO'0 IOOIOS ||»Bj»»t« ujnq «««M
put HOt/ql »»00'0 IOOIOS |I»«-»>»« ujnq ..tu
•n|pMi Mt AU9 t
MBU VZI* l|t« *JO)«t
i IZOO'O IOOIOS |t««J«»t» ujnq
uoj/91 OlOO'O IOOIOS
ujnq
OKI •">»'
tOOIOS AJUOJ ujnq •»• MJ>1
' «>vqi Ziioo-o looios n»« •<•»•• •••"<« «"M
p>»( uovqi «-JOI x I IOOIOS
PM« uet/ql SIOO'O 100101
t-l»»> J»|npo((
-------
Page No. 209
09/21/90
POLLUTANT
Mercury
Mercury
Mercury
Mercury
Methanol
Methanol
Methanol
Hetnanot
Hethanol
Hethanol
2-IWtho«yethano!
2- <2-Methoxyethoxy)
ethanol
1 -Hethoxy-2-propenol
Methyl acetate
CHS SIC
NUMBER CODE INDUSTRIAL PROCESS
741**74 4*53 Sevan sludse
incineration
743*974 4*51 Savage sludge
Incineration
743*974 BO Phareaceutlcals
compounds application
741**74 B021 Dental preparations use
47541 2841 Charcoal manufacture
47541 2841 Charcoal manufacture
47541 2841 Charcoal manufacture
47541 284* Dimethyl terephthalate
production by mathanol
esterlflcatlon
47541 284* Dimethyl terephthalate
production by eathanol
esterlflcatlon
47541 284* Clycol ether production -
mathanol process
10*844 284* Clycol ether production -
•ethanol process
11177! 284* Clycol ether production -
•ethanol precast
107*82 74** Tank truck cleaning
7*20* 284* Terephthallc acid (crude)
production
EMISSION SOURCE
Sludoe incineration
furnace
Incinerator
Entire process
Handling losses
Batch kiln
Continuous furnace
Overall process
Recycled and fresh
methanol storage tank
vents
Recycled and fresh
eethanol storaee tank
vents
Vacuum systee vent
Vacuum system vent
Vacuum system vent
Entire procees
Reactor vent
SCC CODE EMISSION FACTOR
50100504 0.0070 - 0.004 lit/tern dry
eludes tncln.
0.003* Ib/ton sludge
charged
400 Ib/ton of Hg applied
20 Ib/ton of H« handled
10100401 22 Ib/ton charcoal
30100404 7.4 Ib/ton charcoal
30100401 144 Ib/ton charcoal
manufactured
301031 0.24 Ib/ton dimethyl
terephthalate prod.
301031 0.024 Ib/ton dimethyl
terephthalate prod
10125102 0.124 Ib/ton olycol ether
produced
IOI2S302 0.188 Ib/ton elycol ether
produced
30125102 0.124 Ib/ton elycol ether
produced
4*004 0.002 Ib/truck cleaned
30101102 14 Ib/ton crude TPA
produced
NOTES
Mater scrubber ctrl , eff ranglne free •«->«. avt 5
tests 1.4* (/Metric ton dry sludge Incinerated
Unspecified, emission factor la average for 25
facilities
Uncontrolled, baaed on engineering Judgeeent
Control status unspecified, based on engineering
Judgement
Controlled, afterburner, engineering Judgement
Controlled, afterburner, engineering. Judgement
Uncontrolled, range of 134-152 Ib/ton, engineering
Judgement
Uncontrolled, baaed on hypothetical plant operating
8740 h/yr end having S.»J x IOEB Ib/yr capacity
Controlled by vater absorber, based on hypothetical
plant operating 8740 h/yr t S.]9xlOES Ib/yr cap
Uncontrolled, approximation based on data from one
Plant
Uncontrolled, approximation baeed en date from one
plant
Uncontrolled, approximation based on data from one
plant
Emission measurement
Uncontrolled
REFERENCE
1*7
148
113
111
124
124
124
42
42
142
142
142
»7
42
nettif! ethyl tetone
nethvl ethyl ketone
Methyl ethyl ketone
78*11 247 rapor coatlne
Coatlne line
78*31 2845 Hcetone/phenol Cleavaee fact I on vents
•anufacture free cumene (combined)
78*11 2845 Rcetone/phenol Cumene perexldatlen vent
manufacture from cumene
t.OI x IOC-5 Ib/ft paper
coated
10120211 1.4 x IOC-S Ib/ton Phonal
30120201 0.10 Ib/ton phenol
Based on one sampllne proeram. sampled at discharge of
afterburner
Controlled (unspecified) , based on test data, 1*77
data, •verave factors
Controlled (not specified), baaed on sampllne. 1*77
date, averaee factors
125
-------
Page No. 210
0»/21/»0
POLLUTANT
nethyl ethyl ketone
nethyl methacrylate
netnyl thlophene
nethyl thiopnene
nethyl thiophene
nethyl thlophene
3-netnvlbutyreldehyde
1-nethyl-l-cyclohsxen*
1-nethyl-l-cyclohexena
1-nethyl-l-cyclohexene
1 —Methyl - 1 ~cvcl ohexene
|-nethyl-l-cyclohexene
1 -nethyl -1 -cvcl ohexene
1 -Hethyl -l-eycl ohexene
tletnylene chloride
nethylene chloride
Hethylene chloride
nethylene chloride
CAS SIC
NUTOER CODE INDUSTRIAL PROCESS
78933 4*53 Senega sludge
incineration
Scrap tire, open burning
Scrap tire, open burning
Scrap tire, open burrring
Scrap tire, open burning
5908*3 28*5 Acetone/phenol
manufacture froe cuoene
S»M»1 Scrap tire, open burning
5*14*1 Screp tire, open burning
5*14*1 Scrap tire, open burning
5*14*1 Sera* tire, open burning
5*14*1 Scrap tire, open burning
5*14*1 Scrap tiro, open burning
750*2 Aerosol packaging
750*2 Aerosol product* use
750*2 Degreadne operations
u*lng IK
750*2 Degreaelng operation*
EMISSION SOURCE
nultlpla hearth furnace
Tires in experimental
burn hut
Tires In experimental
burn hut
Tires in experleental
burn hut
Tires in experimental
burn hut
Cleavage section vents
(combined)
Tires In experimental
burn hut
Tires In experimental
burn hut
Tires in experimental
burn hut
burn hut
Tlreg In experimental
burn hut
Tiree tn experimental
burn hut
Tlree In experimental
burn hut
Entire proees*
Entire process
Cold cleaner
Cold cleaner
SCC CODE EMISSION FACTOR NOTES
5010050* 0.01074 Ib/ton dry sludge Average of three tests, scrubber
49004 0.071 Ib/truck cleaned Emission moasureoent
2* by 2* Piece, uncontrolled
0.051 Ib/ton tire VOST samples burn rata - O.t kg/hr, shred condition •
2" by 2" Piece, uncontrolled
0.0*3 Ib/ton tire VOST aamplee burn rate - 1.3 kg/hr. shred condition •
2" by 2* piece, uncontrolled
0.04* Ib/ton tire VOST sample* burn rate - 1.7 kg/hr. chunk conditions •
1/4 to 1/4 of e tire, uncontrolled
30120211 1.7 x 10E-4 Ib/ton phenol Controlled (unspecified), based on test data. 1*77
0.0534 Ib/ton tire VOST samples burn rate - t.S kg/hr. shred condition >
2" by 2* piece, uncontrolled
0.02S Ib/ton tire VOST saeples burn rate - 2.3 kg/hr. shred condition •
2* by 2* Piece, uncontrolled
O.lls Ib/ton tire VOST samples burn rat* - 0.* kg/hr. shred condition •
2* by 2* piece, uncontrolled
0.07* Ib/ton tire VOST samplee burn rate - 1.3 kg/hr, shred condition •
f by 2* piece, uncontrolled
0.053 Ib/ton tire VOST samples burn rate - 1.4 kg/hr. shred condition •
2- by 2' piece, uncontrolled
0.151 Ib/ton tire VOST lample* burn rote - O.I kg/hr. «hr*d condition •
2* by 2* piece, uncontrolled
0.241 Ib/ton tire VOST samples burn rate - 0.5 kg/hr. chunk conditions >
1/4 to 1/4 e< * tire, uncontrolled
It. 4 Ib/ton nC consumed Uncontrolled, based on aggregate emltslons/coneumetlon
for 10 ouMtlonnalre respondent*
2000 Ib/ton HC contained Uncontrolled, band on engineering Judgement
In product appl
40100X02 1710 Ib/ton fresh Uncontrolled, considers recycle, based en material
(virgin) IK used balance
40100302 1740 Ib/ton froth Contr • 0.7 freeboard ratio « drainage rack »l 15 sec.
REFERENCE
101
»7
212
212
212
212
125
212
212
212
212
212
212
212
74.75
4*
74
74
using nC
(virgin) 1C u>ed
oraln time, consider* recycle, eater, balance
-------
Page No. 211
09/21/90
POLLUTANT
Hethylene chloride
nethylene chloride
nethvlene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
tlethylene chloride
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
75092 Deoreailng operation*
uiino nc
75092 Deoreailng operation*
Uflng nc
75092 Oeereavlno operation*
u*lng nc
75092 Degreavlng operation*
u*lng nc
75092 Paint stripping
75092 Paint itrlpplng
75092 Paint stripping
75092 2121 »la*tlc* proce**lng
75092 2851 Paint (tripper
formulation
7S092 2M9 Acetaldohyde production
75092 21*9 Chlorooethane production
- oethane chlorlnatlon
EMISSION SOURCE
Conveyorlxed vapor
dcereaier
Conveyorlxed vapor
oeoreaier
Open top vapor de«rea*er*
Open top vapor deorea*er*
DIP tanki at durable
good* eanufacturer*
01 p tankl at durable
good* Manufacturer*
General eol*«lon*
General »olvent u*e
Entire proce**
Off-ga* vent
Recycled oethane inert
gas purge vent
SCC CODE EMISSION FACTOR
40100224 1920 Ib/ton fre*h
(virgin) nc u*ed
40100224 1B20 Ib/ton freih
(virgin) DC uied
40100204 U«0 Ib/ton «r««h
(virgin) nc u*ed
40100204 17BO Ib/ton freih
(virgin) nc u*ed
402 1200 Ib/ton nc contained
in Itripper u*e
402 400 Ib/ton nc contained
In itrlpper u*ed
402 2000 Ib/ton nc contained
in •tripper u*e
401 2000 }b/ton u*ed
301018 2000 Ib/ton u*«d
301 100 Ib/ton of nc consueod
30112014 0.2 Ib/ton acetaldehyde
30112511 0.102 Ib/ton total
NOTES
Uncontrolled, considers recycle, Material balance
Controlled by carbon adsorber or refrlg. freeboard
chiller, consider* recycle. Material balance
Uncontrolled, consider* recycle, eater. al balance
Controlled by refrigerated freeboard chiller, consider*
Uncontrolled, ba*ed on eater lal balance* for 3 auto
eanufac. facilities * I aircraft Mint, facility
Controlled be water seal and 13 »«c. drain tie*.
atsuee* 401 ee let Ion reduction
Uncontrolled based on Questionnaire response* for auto
plant* and engineering judgement
n«u*e all 1* eventually released to atoowhore
Uncontrolled, bated on aggregate eetlutee of eel**ion*
and conpuMptlon et formulation facllltlee
Controlled, lev preuure Krubber. date from, one plant
Uncontrolled, bated on Information euppled by one
producer
REFERENCE
7e
7*
7t
7*
157
157
157
13
13
157
143
71
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethvlene chloride
75092
75092
21*9
2M9
Chloroeethane production
. Mthanol/CHlCl
chlorfnation
fthylene dlchlorlde
production •
oxyhydrochlor. of
ethylene
Ethylene dlchlorlde
production -
oxyhydrochlor. of
ethylene
nethane chlorlnatlon
Methane chlorlnatlon
Inert-«a* puree vent for 10112510 O.OH Ib/ton total
conden*er a**oelat*d with chleroeethane* prod.
nc dUtlllatlon
Abporptlon unit
Separation unit
Fuejtlv*. e»i**lon*
Inert •*• pwee
vent/product recovery
30112501 <«.00* Ib/ton (K
produced
Uncontrolled, hvpoth. fee. produclni 251 eethyl
chloride. 4tS HC. 2SX chlorofore. I n carbon tet.
Control etatue and baeie unepeclfled
301IJSOI O.OOJ Ib/ton CDC produced Control «tatu« end bade unweclfled
J011M14 0.*4 Ib/ton product
30112511 0.21 Ib/ton product
Derived fro* elto vlllt
Derived free cite vUlt
II
13
-------
Page No. 212
09/21/90
POLLUTANT
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
nethylene chloride
CAS SIC
NUHBER CODE INDUSTRIAL PROCESS
75092 2B*9 nethanc chlorlnatlon
75092 28*9 Hethyl chloride
chlorlnatlon
75092 2B«9 nethyl chloride
chlorination
75092 2B«9 nethyl chloride
chlorlnatlon
75092 28*9 nethylene chloride
production
75092 308* Polyurethane foae
(flexible glabatock)
production
75092 3084 Polyurethane foae
(flexible glabatock)
production
75092 3084 Polyurethane foae
(flexible alabatockl
production
75092 3084 Polyurethane foae
(flexible alabatockl
production
75092 3084 Polyurethane foae
(flexible alaMtock)
production
75092 3084 Polyurethane foao
(flexible alabatock)
production
75092 3084 Polyurethane foae
production
75092 3479 Printed circuit board
eanufacture
75092 3479 Printed circuit board
eamifKture
75092 3711 Paint atrlpplng
EMISSION SOURCE
Storage
Fugitive eelaaiona
Inert gaa purge
vent/product recovery
condenaer
Storage
Entire proceaa
Equipment leak eelealona
Procaaa ventg (foae
tunnel, curing area!
Procaeo ventg (foae
tunnel, curing area)
Storage tank eelaelone
Storage tank eelaalong
Entire aroceaa
Photoreolot etrlpplne.
Phot or eel at atrlpplng
Spray booth ealntenance
at eutoenblle eeeeebly
Planta
SCC CODE EMISSION FACTOR
4070*0 2.04 Ib/ton product
30112514 0.94* Ib/ton product
30I12SII 0.052 Ib/ton product
4070*0 4.92 Ib/ton product
30112510 4 Ib/ton IK produced
3010189 34 Ib/ton of nc conaueed
30101B9 10 Ib/ton of IK conguoed
3010189 1940 Ib/ton of IK
congueed
3010189 840 Ib/ton of IK conguoed
30101894 4 Ib/ton of IK conguoed
30101894 1 Ib/ton of K conguoed
3010189 2000 Ib/ton IK loneueod
40100302 1800 Ib/ton fregh
(vlreln) 1C uged
40100301 15*0 Ib/ton fregh
tvtrelM 1C vtea
40201405 1400 Ib/ton IK contained
In gtrlpper ege
NOTES
Derived froe otte vlglt
Derived froe glte vlalt
Derived free glte vlalt
Derived froe alto vlalt
fteflecte 1983 eontrola. baaed on 1983 aggregate eela.
production total a for IK producer*
Uncontrolled, baaed on SOCni VOC eelgalon factorg and
euegtlonnalre roaponoog
Controlled by leak detection and repair, baaed on
engineering judgeeent
Uncontrolled, baaed on facility euegtlonnalre reeponaea
and onolneerlne; Judeeeent
Curing area venta uncontrol.. foe* tunnel ventg
control, by encl. » carbon adaorb, engineering judg.
Uncontrolled, calculated free eueatlonnalre reapon***
ualne nP-41. eeuatlon*
Controlled by refrigerated condenaer, baaed on
engineering Judgeeent
Uncontrolled, bagod. on engineering Judgement
Uncontrolled, baaed on eaterlal balance
Controlled by carbon adaorber. baaed on eatorlel
b*\em.
UAcontrolled. baoed on euegtlonnalre regponoe* and
OMinoorlng Judejeeient
REFERENCE
13
13
13
13
49
73
73
7J
7J
7J
73
49
74
74
1ST
-------
Page No. 213
09/21/90
POLLUTANT
He hylene chloride
flethylene chloride
tlethvlene chloride
nethylene chloride
Methylene chloride
flethylene chloride
nethylen* chloride
flethylene chloride
flethylene chloride
l-nethylnaphthalene
l-nethylnaphthalene
2-n*thylnaphthaleno
2-flethyl naphthalene
CAS SIC
NUHBER CODE INDUSTRIAL PROCESS
75092 4953 Seuage sludge
incineration
incineration
75092 5149 Cheelcal distribution
facilities
75092 5U9 Cheelcal distribution
facilities
75092 73B4 Photographic file
processing
75092 753 Degreaslng operations
using nC
75092 753 Degreeslng operations
using IIC
75092 7*41 Paint stripping
75092 9711 Paint stripping
90120 Scrap tire, open burning
90120 Scrap tire, open burning
9157e Scrap tire, open burning
9157* Scree tire, open burning
EMISSION SOURCE
Aircraft (eilltary and
commercial)
Fluldized-bed furnace
Handling omissions
(filling losses)
Storage tank emissions
Splicing glue
Carburetor cleaners
Carburetor cleaners
Furniture stripping
(household and
commercial)
Installations
Tires In experimental
burn hut
burn hut
burn hut
Tire* In experimental
burn hut
Tires in *xperi**nt*l
burn hut
Tlrmt in *xft*ri**ntei
burn nut
SCC CODE EMISSION FACTOR
490 IsOO Ib/ton nC contained
in stripper use
50100504 1.4 x IOE-4 Ib/ton dry
sludge
chior. in Influent
4 2 Ib/ton IK distributed
2000 Ib/ton IK in
ppliclng glue applied
40100302 17BO Ib/ton fresh
(virgin) HC used
40100302 1S20 Ib/ton fresh
(virgin) DC used
490 2000 Ib/ton IK contained
in stripper use
in stripper used
0.459 Ib/ton tire
0.981 Ib/ton tire
0 477 1 b/ ton ti re
0.451 Ib/ton tire
0.747 Ib/ton tire
t.lafJ Ib/ton Ur*
NOTES
contro ed, as on •• er • a ance*
One test, scrubbor
Based on eel*, Modeling for hypoth. rOTU, represents
aver*** POTU that treat* Industrial vtittwater
distribution estle. for dlst. facilities in 1»B3
Uncontrolled* based on nationwide •Missions and
distribution estieates for dtstr. facilities In 1983
Uncontrolled, based on engineering Judgeeent
Uncontrolled, consider* recycle, eateri*! b«iance
Controlled by water cover, consider* recycle, eaterlal
balance
Uncontrolled, b**ed on engineering Judgaeent
Instillation* using dtp twite*
XnD-2 extracts w/IIS analysis, shred condition • 2" by
2" pieces, born rate * 1.3 kg/hr. uncontrolled
IAD* 2 extract* w/IIS analy*!*, *hred condition • 2* by
2" piece*, burn rate • 1,3 ke/hr, uncontrolled
Kf\D~2 extract* u/HS anal yf is shred condition • 2" by
J- pieces, burn rat* • I.I Hs/hr
»AD-2 extract* «/nS analysis. *hr*d condition « 2- by
2* Pieces, burn rat* • 1.1 «g/hr. uncontrolled
IAO-2 extracts WHS analysis, shred condition • 2* by
2* Pieces, burn rat* • 1.1 »*/hr. uncontrolled
IAO-2 extracts u/ttS analysis. Chun* condition • l/4-l/«
of tire, burn rat* • 1.7 »s/hr. uncontrolled
REFERENCE
157
101
101
f*
40
*9
•9
7»
7*
IS7
1ST
212
212
212
212
212
212
-------
Page No. 2M
09/21/90
POLLUTANT
l-Methylnaphthalene
2-nethvlnaphthalene
2-F1ethyl naphthalene
Methyl naphthal mm
Nethyl naphthal one
netnyl naphthal one
nothylnaphthalena
Hethyl naphthal one
Hethylnaphthalene
Methyl naphthal one
nothylnaphthalene
Methyl naphtha 1 mnm
Rethylnaphthal mnm
nethyl naphthal mnm
Methyl naphthal one
4-nethyl -2-«l trophenol
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS EMISSION SOURCE
90120 Scrap tin, open burning Tires In experloental
burn hut
•1574 Scrap tire, open burning Tires In experimental
burn hut
burn hut
burn hut
1321944 Scrap tire, open burning Tlree In experimental
burn hut
1321944 Scrap tire, open burning Tires In experimental
burn hut
1321944 Scrap tire, open burning Tires In experimental
burn hut
1321944 Scrap tire, opgn burning Ttrt* In experimental
burn hut
1321944 Scrap tlr«. op«l burning Urn in experimental
burn hut
1321*44 Scrap tin. open burning Tlrig In experimental
burn hut
1321944 Scrap tire, open burning Ttr« In •xpcrluntal
burn hut
1321944 Scrap tlr«, op«n burning Tiro In »/nS analyiU. Chunk condition • 1/4-1/4
XAD-2 gxtracts v/ltS analyala. Chunk condition • 1/4-1/4
XAD-2 extracts M/nS analyala. Chunk condition • 1/4-1/4
ol tin. burn rata • 2.3 kg/hr. uncontrolled
XAD-2 extracts H/I1S analyala. Chunk condition • 1/4-1/4
of tin. burn rata • 2.1 kg/hr. uncontrolled
VOST aeoplea burn rate - I.S kg/hr. ahrad condition >
2' by 2* place, uncontrolled
VOST Mevloe burn rate - 2.3 kg/nr. ehred condition •
2* by 2* place, uncontrolled
MOST eaeolee burn rate - 0.9 kg/hr. ahred condition •
2' by 2* piece, uncontrolled
VOST aieploa burn rate * 1.3 kg/hr. Hired condition •
2- by lm Piece, uncontrolled
VOST aaavlea burn rate - 1.4 kg/hr. ehred condition •
2- by 2- piece, uncontrolled
VOST aaaolea burn rate - O.I kg/hr, shred condition •
2- by 2- piece, uncontrolled
VOST eaepln burn rate - O.S kg/hr. chunk conditions •
1/4 to 1/4 of • tire, uncontrolled
VOST saoolee burn rate - 1.7 kg/hr. chunk conditions •
1/4 to 1/4 of a tire, uncontrolled
VOST aaevlee burn rate - 3.5 kg/hr. chunk conditions •
1/4 to 1/4 of a tire, uncontrolled
VOST saeoln burn rate - 1.27 kg/hr, chunk conditions •
1/4 to 1/4 of • tire, uncontrolled
VOST samples burn rate - 2.27 kg/hr, chunk conditions •
1/4 to 1/4 of • tire, uncontrolled
VOST saeoles burn rat* - 4.43 kg/hr, chunk conditions •
1/4 to 1/4 04 a tire, uncontrolled
One. test, scrubber
REFERENCE
212
212
212
212
212
212
212
212
212
212
212
212
212
212
212
212
tot
-------
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
EMISSION SOURCE
SCC CODE EMISSION FACTOR
4-l1«thy.-2-nttrophanol
11*335 4»53 Seuage *lud«*
incineration
Hultlple hearth furnace
5010050* <5.« x 10E-5 Ib/ton dry On« tttst, *crubb«r
sludge
2-H«thylprop*nc
7S2B5 2895 Carbon black manufacture
- ot 1 f urnace
Rain proce** purge vent
30100504 0.20 Ib/ton c*rbon taUck l»t«d on t«»t data
produced
Methyl atyrene
Methyl *tyr one
Molybdenum
Molybdenum
Molybdenum
Molybdenum
Honocht orodl benzof uran* .
total
Naphthalene
Naphthalene
Naphthalene
Naphtha! ene
Naphthalene
Naphthalene
Naphthalene
25013154 28*5 Acetone/phenol
manufacture from cumene
25013154 28*5 Acetone/phenol
manufacture from cumane
7439987 Uood combuatlon,
realdentlal
743*987 22* Woven fabric flnlahlng
7439987 22* Uoven fabric flnlthlng
7439987 22* Uovan fabric flnlthlng
4*53 Senate tludge
Incineration
»1203 Naphthalene production
»1201 Naphthalene production
91203 Scrap tire, open burning
•1203 Scrap tire, open burning
91203 Scrap tire, open burning
•1203 Scrap tire, open burning
91203 Scrap tire, open burning
Cumene peroxldetlon vent
Storage tank venta
Uoodttove ulthout baffle
Curing oven - reein
finlth
Heat aettlng
flni thing
Thermotol dyeing
Multiple hearth furnace
Proce** eml**ion*
Storage
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experlmmntal
burn nut
Tire* In experimental
30120202 0.0002 Ib/ton Phenol
4073* 0.004 Ib/ton phenol
4.* x 10E-4 Ib/ton mood
burned
330001 1.34 x IOt-4 Ib/ton
fabric
330001 4.1 x IOE-4 Ib/ton fabric
330001 8. a x IOE-4 Ib/ton fabric
330001 4 x 10E-5 Ib/ton fabric
5010050* 1 K lOE-t Ib/ton dry
aludge
0.478 Ib/ton naohthalene
produced
0.0454 Ib/ton produced
2.44 Ib/ton tire
1.914 Ib/ton tire
4.411 Ib/ton tire
2.180 Ib/ton tire
1.0*9 Ib/ton tire
Controlled (not ipeclfledl, baaed on sampling. 1977
data, average factor*
Controlled (unapeclfled) . baaed on teat data, 1977
data, average factor*
Uncontrolled, baled on one etudy. nonbaff led *tova
burning green pine
Uncontrolled, average of tmo teit*
Uncontrolled, baaed on teat data
Uncontrolled, average of three tette
Uncontrolled, average of three teat*
Average of tuo teat*. tcrubber
laaed on POTi *ml«ton* and 871 naphthalene
latad en data from State tile* and engineering
Judgement
IAO-2 extract* m/HS analy*!*. Mired condition • 2* by
2* Plecea, burn rate • 1.] kg/hr. uncontrolled
IAD-2 extract* m/NS analy*!*. l.l tg/hr. controlled
212
-------
Page No. 2U
0»/21/»0
POLLUTANT
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
CAS SIC
NUMBER CODE INDUSTRIAL
•1203 Scrap tire
91203 Scrap tire
91203 Scrap tire
•1203 Scrap tire
•1203 Scrap tire
•1203 Scrap tire
•1203 Scrap tire
•1203 Scrap tire
•1203 Scrap tire
•I20J Scram tire
•1203 Scrap tire
•1203 Scrap tire
•1203 Scrap tire
•1201 Halt* oil
•1201 224 Hoven fabr
PROCESS
. open burning
, open burning
, open burning
, open burning
, open burning
, open burning
, open burning
. open burning
, open burning
, open burning.
. open burning
. open burning
. open burning
coeouitlon
1C finishing
EMISSION SOURCE
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
burn hut
Tire* In mxmorlMntai
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Tire* In experimental
burn hut
Ha*t* all -fired boiler*
«1SO million Itu/h) *r
apace heater*
Curing oven - re*ln
flnl*h
SCC CODE EMISSION FACTOR
1.827 Ib/ton tire
1.436 Ib/ton tire
I.7»B Ib/ton tire
2.2* Ib/ton tire
0.4M Ib/ton tire
1.434 Ib/ton tire
2.5*0 Ib/ton tire
1.142 Ib/ton tire
3.447 Ib/ton tire
1.49 Ib/ton tire
1.03, lb/tw) tire
2.403 Ib/ton tire
1.20 Ib/ton tire
t.ll Ib/ton tire
1 O.IS lb/1000 gal oil
burned
330001 •.DO* Ib/ton fabric
NOTES
Sum of PAH analv on lie. extrat. of IAO-2 teat I filter
compont. *hred condition « 2* by 2" Piece, burn
rate- I. 7 kg/hr. controlled
compont. shred condition • 2" by 2" piece, burn
reta*2.3 kg/hr, controlled
VOST *aeple* burn rate - 1.5 kg/hr, *hrod condition •
2* by 2* piece, uncontrolled
VOST lample* burn rat* - 2.3 kg/hr, *hr*d condition •
2* by 2* Piece, uncontrolled
2- by 2- piece, uncontrolled
VOST lample* burn rate - 1.3 kg/hr, ehred condition *
2- by 2* Piece, uncontrolled
VOST eample* burn rat* - 1.4 kg/hr, ahred condition •
2" by 2' alee*, uncontrolled
VOST aample* burn rat* - O.I kg/hr. *hr*d condition •
2" by 2" olece. uncontrolled
VOST (ample* burn rate - 0.5 kg/hr, chunk condition* •
1/4 to 1/4 of a tire, uncontrolled
VOST vammlm* burn rat* - 1.7 kg/hr. chunk condition* •
1/4 to 1/4 of a tlra. uncontrolled
VOST Maple* burn rate - 3.5 kg/hr. chunk condition* •
1/4 to 1/4 of a tire, uncontrolled
VOST Maple* burn rate - 1.27 kg/hr. chunk condition* •
1/4 to 1/4 of a tire, uncontrolled
VOST Maple* burn rat* - 2.27 kg/hr, chunk condition* •
1/4 to 1/4 of a tire, uncontrolled
VOST (ample* burn rate - 4.43 kg/hr. chunk condition* *
1/4 to 1/4 of a tire, uncontrolled
Uncontrolled, band on aelMlon* data and engineering
Judgement » ******* 971 ORC
Uncontrolled, average of three t**t.
REFERENCE
212
212
212
212
919
21 of
212
212
212
212
212
212
212
212
212
SS
52
-------
P«9« No. 217
09/21/90
POLLUTANT
Mtpnthalana
N.phthalana
Naphthalana
Haphthalana
Naphthalana
N«phthalana
Naphth.lana
Naphth.lana
Naphtftalana
Naphthalana
Naphtha 1 ana
Naphtnalana
Naphthalana
Naphtha] ana
Naphthalana
Naphthalana
CAS
NUHBER
91203
91203
91203
91203
91203
91203
91203
91203
91203
91203
9120,}
91203
91203
91203
91203
91203
9120J
91203
SIC
CODE
226
226
2491
2491
2491
2491
2491
2491
2491
2491
2491
2491
2S
25
26?
21
21
21
INDUSTRIAL PROCESS
Uovan fabric flnlsntnt
Uovan fabric flnlshlns
Uood prasarvlnt
Uood prasarvlnt
Uood prassrvlnt
Wood prsssrvlnt
Uood prasarvlnt
Uood prasarvlnt
Uood prasarvlnt
Uood prasarvlnt
Uood prasarvlnt
Uood prasarvlnt
Uood coabustlon.
Industrial
Uood coabustlon.
Industrial
Papar eoatlnt
Industrial vastawatar
traataant
Industrial wastawatar
traataant
Industrial nastauatar
EHISSION SOURCE
Tantar fraaas - rasln
finish
Tharaosol dyaint
Craosota conditlonins
Craosota cool -down
Craosota traatlns
cyllndar futltlvas
Incinaration of walta
Panta traatlnt cyllndar
fualtlvas
PantachI orophanol
condttionlnf
Pantachlorophanol
cool -down
Pantachlorophanol
traatlnt - fualtlva
Tharaal (pan) avaporatlon
of craosota wastauatar
Tharaal (pan) avaporatlon
of Pantachlorophanol
wastawatar
•tlancad draft wlckas
• totar- flrad Industrial
bollar
Coatlna Una
Hair
Otl-watar saparator
Traataant tank
sec CODE enissioN FACTOR
330001 0.0034 Ib/ton fabric
330001 0.002 Ib/ton fabric
30700SOI 2.2 Ibs/hr
307005 1.06 Ibs/hr
307005 2.> n/sa3 tas 1 salad
307005 290 u«/sa3 stact tas
307005 2.4 «t/ta3 tas laakad
30700597 2.29 Ibs/hr
30700597 0.99 Ibs/hr
30700597 0.24 Ibs/hr
9
2500 at/sal tas vantad
2000 at/s«3 tas vantad
10200906 7.5 x IOE-V Ib/ton fual
(dry basts)
10200906 2.0 x IOC-7 Ib/ton fual
40201301 9.6 x 10-7 Ib/ft Papar
coatad
301 0.21 x MSS of pollutant
In wast* straaa
101 0.09 x MSS of pollutant
In wast* straaa
301 1.4 x IOE-03 x MSS of
NOTES REFERENCE
Based on one saMpling program at on* facility 10
Based on one vaapltn* progra« at on* facility 10
One ewasurewent <
Controlled «lth baenoust. average value 4
Average of 3 •easur.UMflts *
Based on one sampling progra* at on* facility 10
Based on on* sampling prograti at one facility 10
Bated on on* •aepllng progra* at en* facility 10
Average valu* *
Average valiw *
Dry Mood, on* plant* partlculate control H/Mchantcal 177
collector (cyclone), wood feed rat* 0.29 kg/a. boll.
•ff. 55.31
Based on on* saMpllng •rogra*'. §a«»led at discharge of 11
afterburner
Uncontrolled «*l««lon* 205
Uncontrolled eelsslon* 205
UncontrollMl mlgtlon* 205
pollutant In Mst« strata
-------
Pave No. 218
09/21/90
POLLUTANT
Naphthalene
Naphthalene
Haphthal ene
Naphthalene
Naphthal ene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
Naphthalene
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
91203 28 Industrial wastewater
treateant
91203 28 Industrial wastewater
treateent
91203 2B Industrial wastewater
treateent
91203 28 Industrial wastewater
treateent
treateent
91201 28 Industrial wastewater
treateent
91203 28 Industrial wastewater
treateent
91203 28 Industrial waatewater
treateent
91203 28 Industrial wastewater
treateent
91203 28 Industrial wastewater
treateent
91203 28 Industrial wastewater
treateent
91203 28*5 Acetone/phenol
eanufacture free cueane
91203 28*5 Phthallc anhydride
EMISSION SOURCE SCC CODE EMISSION FACTOR
Non-aerated blobasln 301 0.12 x eass of pollutant
In waste streae
Aerated blobasln 301 0.17 « eats of pollutant
In waste streae
In waste streae
Aerated equalization 301 0,9* x eass of pollutant
basin In waste streae
Non-aerated equalization 301 0.38 x eass of pollutant
basin In waste streae
Open trench 301 0.025 x eass of pollutant
In waste streae
Suep 301 4.7 x 10E-03 x eass of
pollutant in waste streae
Lift station 301 0.18 x eass of pollutant
In waste straae
Junction box 301 0.0*8 x eass of pollutant
In waste streae;
Manhole 301 0.0015 x eass of
Drain 301 0.011 x eass of pollutant
in wasts streae ,
Cueene peroxtdetlon vent 30120202 0.0002 Ill/too phenol
Storage tan« eeleslons 40703* 1.2 lit/ton PA. produced
NOTES
Uncontrolled eelsslons
Uncontrolled eelsslons
Uncontrolled missions
Uncontrolled eelsslons
Uncontrolled eelsslons
Uncontrolled eelsslons
Uncontrolled emissions
Uncontrolled eelsslons
Uncontrolled eelsslons
Uncontrolled eelsslons
Controlled (unspecified), based on test date. 1977
data, average factors
Uncontrolled, test data and engineering Judgeeent
REFERENCE
205
205
205
205
205
205
205
205
205
205
125
120
Naphthalene
Naphthalene
Naphthalene
91203 28*5
91201 28*9
production - naphthalene
process
Phthallc anhydride
production - naphthalene
process
Acetone/phenol
•anufacture froe cueene
Storage tank eetsslons 407 0.012 Ib/ton PA produced Controlled, test data end engineering Judgeeent
28*9 Propylene oxide
production by
chlorohydrlnatlon
Cueen* peroxldatlon vent
Xbserption
J01091J1 <0.0002 Ib
naphthalene/ton phenol
proouc
Controlled (adsorption or condensation), baeed on
Industry sources
30120501 0.1* U/ten produced Control unclear, based on ease balance and testing
-------
Pag* No. 219
0»/21/»0
POLLUTANT
Naphthalene
Naphthal *n*
Naphthalene
Naphthalene
Naphthal ene
1 ,4-Naphthoqulnone
CAS SIC
NUtlBER CODE INDUSTRIAL PROCESS
• 1203 2911 Pvtroleu* r*fln*ry
•1203 3112 Cot* production,
by-product recovery
proceu
>1203 3334 PrUary aluelnue
production
»1203 3334 PrUary aluelnue
production
• 1203 4*53 Ua*tw*t*r treatunt
130154 2I«5 Phthallc anhydrld*
EHISSION SOURCE SCC CODE EMISSION FACTOR NOTES
crackln* unit, fuvltlvM
Entlr* proc«* 303003 O.OIII4 Ib/ton cok* E*tleat*d free capacity and ut. percent naphthalene
18. B)
Soderbere potllne 303001 0.54B Ib/ton Al produced Slntl* t*lt rwort. on* plant, controlled, baohoue*
Soderbor* pot Una 303001 0.124 Ib/ton Al produced Sln*l* teat rwort. on* plant, controlled, baehouee,
eaterlal that **caped prleary control eyttee
POTU 50100701 320 Ib/ton naphthalen* In laved on «•!*. Modeling for hypoth. POTtf, repre«ent*
Influent av*r*«* POTU that treat* Industrial n»tw*t*r
(lain proc««* Inclnwator 30101* 1.38 Ib/ton PA produced Uncontrolled. t«»t eat* and *n*tn*wli>« jud«WMnt
REFERENCE
•2
n
n
•i
s»
120
1.4-Naohthooul none
production - naphthelen*
procet*
28«5 Phthallc anhydrld*
Production - naphth«l«n«
procvtl
naln proc««« tnctnerator 30101* 0.04 Ib/too PIS produced Controlled. k«»t data end endneerlne judeeeent
120
1,4-Huhthooulnoiie
1,4-Maphtho4Ulnon*
Nickel
130154 28«S Phthallc anhydride
production - naphthalene
procec*
130154 2»«! Phthallc anhydride
production • naphthalene
proceee
7440020 Coal coebuttlon
Coal coebultlon
Coal coebuetlon
Secondary Incinerator 30101* 131.2 Ib/ton PA produced Uncontrolled, teet date and enelneerlno Jud****nt
Secondary Incinerator 30101* 0.14 Ib/ton PA produced Controlled *d dry bottoei
bailor*. vtll/coeMTC/ind
il-fl Ib/IOEU Itu Controlled «lth icrubber, ba«ed on en«ln««rln*
17*0-2240 Ib/lOEIJ nu Uncontrolled. b***d on entjnewlnf Judteeent
s
5
-------
P»e No. 220
0»/21/»0
CAS SIC
NUT1BER CODE INDUSTRIAL PROCESS
EMISSION SOURCE
SCC CODE EMISSION FACTOR
7440020 Cod coebuitlon
7440020 Coil coobuitlon
7440020 Coel coobuctlon
7440020 Co«l coebuitlon
7440020 Co«l coebuetlon
7440020 Coil co.bu.tlon
7440020 Co«l coebuetlon
Coil coebuetlon
Co«l coebuitlon
7440020 Coel coebuetlon
7440020 Coil coebuttlon
7440020 Coll coebuetlon
7440020 Coel coobueUen
Anthracite coal-ilred I
pulverized dry bottoe
boilers, util'coeeerc/lnd
Anthracite coil-fired I
pulverized dry bottoe
boilers, util/coeeerc/lnd
Anthnctte coal-tired I
pulverized dry bottoe
bollen, utll/cooeorc/lnd
Anthracite coal-fired 1
pulverized yet bottoe
boiler., utll/coeeerc/lnd
Anthreclte cool-fired I
pulverized wet bottoe
boiler*, utll/coeeerc/lnd
Anthreclte coel-llred 1
pulverized vet bottoe
bollere, utll/coeeerc/lnd
Anthracite coil-tired 1
pulverized vet bottoe
bollere, utl
Anthracite coal-tired I
itoker bolleri.
utll/coeeerc/lnduetr
»0«-IHO lb/10E12 Btu Controlltd xlth rMiltlelon*, bif.d on «o«in««rint
Anthracite co>l-llred
•toker bollere,
utl l/coeeerc/lndu>tr
Anthreclte i
itoker bollere,
utl1/coeeerc/lnduecr
lituelnoue coal-tired
cyclone boiler.
utll/coeeerc/litduetr
lltuetnoue co.l-llred
cyclone boiler.
lltvelnoue coal-flreo) I
cyclone, boiler.
utII/cne.irc/lndu.tr
4B7-4IO lb/10E12 Btu Controlled ulth ESP, bleed on engineering Judqeeent 3t
«4->l lb/10E12 Itu
Controlled xlth ecrubber. bleed on enelneerlne
Judeeeent
14*0-2240 lb/10C12 Btu Uncontrolled, beeed on envlneertnf judeeeent
7ie-)i40 lb/10E12 Itu Controlled Kith eultlelone, baeed on enolneerlno
Jud
5>7-*10 Ib/lOCU Itu Controlled Kith ISP, baeed on eneineerlno Judeeeent 3*
5J-«l lb/10E12 Itu
Controlled «lth ecrubber, baeed en enilneerln
Judeeeent
1350-2240 Ib/IOEU Itu Uncontrolled, beeed on enilneerlnf Judeeeent
1 411-1140 lb/10CI2 Itu
Controlled Kith eultlelone, baeed on enolnecrlno
Judeeeent
3«7-«10 lb/IOE12 lt« Controlled «lth ISP, baeed en enilneerln* Judteeent 3*
174-12*0 Ib/lOEU Itu Uncontrolled, calculated beeed on enelneerln« Judeeeent 3e
el-454 Ib/I0tl2 Itu
Controlled Kith eultlelone, calculated baeed on
eneineerlnt Judeeeent
47-JS2 Ik/10112 Ite Controlled ulth Iff, celculeted beeod en enelneerine
-------
Page No. 221
09/21/»0
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS CIUSSION SOURCE
SCC CODE EIUSSION FACTOR
REFERENCE
Nickel
7440020 Coil coabuetlon
7440020 Coil coebuetlo
7440020 Coal coabuetlon
7440020 Coil conbuiUon
7440020 Co«l conbuotlo
7440020 Co«l co«bu>tlo
7440020 Coal coebuatlon
7440020 Coal coiebuatlon
7440020 Coal coebuetlon
7440020 Coal coebuatlon
7440020 Coal coebuatlo
7440020 Coal coebuetlon
7440020 Coal coebuatlon
lltuelnoua coal-fired I
cyclone boiler,
utll/coooerc/lnduatr
lltuelnoua coal-fired 1
pulverized dry bottoe
boiler., utll/coeeerc/lnd
lltuelnout coal-fired I
pulverized dry bottoe
bollera, utll/coeeerc/lnd
lltuelnoua coal-fired 1
pulverized dry bottoe
boiler., utll/coeeerc/lnd
•Ituelnoua coal-fired 1
pulverized dry bottoe
bollera. utll/coeeerc/lnd
lltuelnoua coal-fired I
pulverized wet bottoe
bollera, utll/coeeerc/lnd
lltuelnoua coal-fired 1
pulverized wet bottoe
bollera, utll/coeeerc/lnd
lltuelnoua coal-fired I
pulverized vet bottoe
bollera, utll/coeeerc/lnd
lltuelnoue coal-fired 1
pulverized vet bottoe
bollera. utll/coeeerc/lnd
lltuelnoue coal-fired I
apreader atoker bollera.
utll/coeeerc/tnduetr
livntnoue coal-fired 1
apreader atoker bollera,
util/coeeerc/lnduetr
lituelnoua coal-fired I
toreador stoker bet Iere,
util/coeeerc/lndustr
Lignite coal-fired 1
cyclone bollera.
utll/ceeeerc/lndu.tr
*.J-4« 1D/10E12 »lu Controlled Kith lerubber. calculated band on
•nflnooring
42S->54 lb/IOE12 Itu
1030-1290 lb/10E12 Btu Uncontrolled, calcul«t«d b«i«d on «n9in««rln9
522-454 lb/10E12 Itu Controlled Htth •ultlclonc, c«UuUt«d b»od on
onvlnoorlnfl Jud
210-152 lb/IOEI2 Itu Controlled with ESP, calculated baaed on engineering 3»
Judgeeent
37-4« lb/10EI2 Itu Controlled tilth acrubber, calculated baaed on
engineering Judgeeent
840-12*0 lb/IOE12 Itu Uncontrolled, calculated baaed on engineering judgeeent 3*
Controlled »lth eultlclone, calculated baaed on
engineering Judgeeent
228-352 I6/IOEI2 Itu Controlled uitl. ESP. calculated baaed on engineering 3.
30-4« lb/IOE12 Itu Controlled HltH acrubber, calculated baaed on
engineering Judgeeent
77S-I2VO lb/10E12 Itu Uncontrolled, calculated baaed on engineering judgeeent I*
3»I-«4 lb/10E12 Itu Controlled ultH eultlclone, calculated baaed on
engineering Judgement
211-352 lb/IC€12 Itu Controlled Mltft ESP. calculated baaed on engineering
117-1140 U/IOC12 Itu Uncontrolled, baaed on engineering Judgevent
-------
Pas« HO. 222
09/21/90
POLLUTANT
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nlck«l
Nickel
Nickel
Nickel
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS EMISSION SOURCE
7440020 Coil coobultlon Lignite coal-fired
cyclone boilers.
utll/comerc/lnduitr
cyclone boilers,
utl 1 /coiwerc/industr
7440020 Coal coebustlon Lignite coal-fired
cyclone boilers.
utl ! /coeeere/lndustr
7440020 Coal coobustlon Lttnit* coal-fired
pulverized dry bottom
boiler.
utl 1 /ccnerc/induitr
7440020 Coil coebuitlon Llenlte co»l-flred
pulverized dry bottoe
boiler.
utl 1 /cammtrctl nduitr
7440020 Co«l co«bu»tlon Llmite co«l-tlon Llenlte coal-fired
pulverized Mt bottoe
boll art.
ut 1 1 /COOMTC/I nduitr
7440020 Coal cootxieUon Llonlte coal-fired
pulverized wt botto*
bolters.
uUl/caoMKltwftntr
SCC CDD£ EHISSION FACTOR NOTES REFERENCE
1 7V-S97 lb/10E12 Btu Controlled ulth eultlclone. bated on enolMorlne 3*
Judgment
1 43-316 lb/lOE12 Btu Controlled with ESP. based on envtneerlno Judoeeent 36
1 S.t-42 Ib/10E12 llu Controlled "Ith ecrubber. ba»ed on enelneerlnt 3*
Judveeent
1 »28-IUO lb/10E12 Itu Uncontrolled, calculated baaed on enolnoertne Jud9eeent M
1 470-587 lb/IOEI2 Btu Controlled ulth eultlclone, calculated baaed on 3«
envlneerlnfl judgeeent
1 252-31* 1M1OE12 Btu Controlled Kith ESP, calculated bamed on onelneorlne 3*
Jud«e«ent
1 31-42 Ib/lOElZ itu Controlled Kith (crabber, calculated baaed on M
enilnewlne judneent
1 154-11*0 lb/10E12 Itu Uncontrolled. be«ed on engineering judgement »
1 3C2-SI7 lb/10E!2 Itu Controlled «lth eulttclong, bMod on onglMerlng M
judgeawit
1 2OS-3I4 lb/10E12 Itu Controlled »lth ttf. baled on engineering judgoeent M
I 27-42 lb/10EI2 Itu Controlled Kith gcrubber, ba«ed on engineering M
Judge***
-------
Page No. 223
0»/2U»0
POLLUTANT
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
CAS
NUMBER
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
SIC
CODE INDUSTRIAL PROCESS
Coal combustion
Coal combustion
Coal combustion
Coat combustion,
residential
Coal combustion.
residential
Coal combustion.
residential
Coal combustion.
residential
Coal combustion.
residential
Coal combustion.
residential
Coal combustion.
residential
Coal combustion.
residential
EMISSION SOURCE SCC CODE HUSSION FACTOR
Lignite coal-llred 1 4*4-1140 lb/10E12 Btu
spreader stoker boilers.
ut 1 1 /coemerc/l ndustr
Lignite coal-llred 1 352-587 lb/10E12 Btu
spreader stoker boilers,
utll/coemerc/lndustr
Lignite coal-fired 1 1B»-J14 IbMOElZ Itu
spreader stoker boilers.
utll/commerc/lndustr
Anthracite coal-fired 224 lb/10E12 Itu
boilers
Bituminous coal-fired 12* lb/10E12 Itu
boilers
Boilers fired by coal 133 16/IOEI2 Itu
from Appalachian region
Boilers fired by coal 244 lb/10E12 Btu
from interior region
•oilers fired by coal 107 lb/IOEI2 Itu
from northern plains
Boilers fired by coal *0.4 U/IOE12 Btu
from rocky mountain
region
Lignite coal-fired 114 lb/10C12 Btu
bolters
Subbltumlnous coal-fired 71. » IWIOEI2 Btu
boilers
NOTES
Uncontrolled, based on engineering Judgement
Controlled with multlclone, based on engineering
Judgement
Controlled vlth ESP. based on engineering Judgement
Uncontrolled, highly variable, calculated based on
engineering Judgeeent
Uncontrolled, highly variable, calculated based on
engineering Judgement
Uncontrolled, calculated based on engineering Judgement
Uncontrolled, calculated based on engineering Judgement
uncontrolled, calculated based on engineering Judgement
Uncontrolled, calculated based en engineering Judgement
Uncontrolled, highly variable, calculated based en
engineering Judgement
Uncontrolled, highly variable, calculated based on
engineering Judgement
REFERENCE
34
34
14
34
34
34
14
34
14
34
34
7440020
Oil combustion
Oil combustion
Oil combustion
Distillate oll-Mred
boiler.
ut11/comcerc/lndustr/resl
dentlal
Distillate oll-
-------
Page No. 224
09/21/90
CAS SIC
MUtlBER CODE INDUSTRIAL PROCESS
EMISSION SOURCE
SCC CODE EIIISSION FACTOR
Oil coobuitlon
Oil coMbuttlon
Dl.tillete oil-fired
boll.r.
util/coeeerc/indu*tr/re*i
dentlal
Realdual oil-fired
boll.r.
utll/coeeerc/lnduetr/revl
dintill
a.8 lb/10E12 Itu
12*0 Ib/10Et2 Itu
Controlled by vcrubber, ba.ed on engineering Judgement
Uncontrolled, based on engineering Judgement
Oil coibuatlon
Oil coebuetlon
Oil coobuetlon
Utita oil co.tm.Uon
Wood co.bu.tlon.
residential
7440020 V4« H.be.to. ellllng
Reddual all-find
bolUr.
utll/eo«B«rc/lndu«tr/r«*i
d.nti.l
R.tldu.l oll-«lr«d
boll.r.
utll/co»«.rc/lndu«tr/r.»l
d.ntUI
R»ldu>l o
boll.r.
utll/coM»rc/lndu«tr/r«l
d«ntt>l
W*«t« cr«nkc*«« oil
Uood.tov. ulthout biMU
mtlin* a\»t<
«42.t lb/10EI2 Itu
352.1 lb/IOEI2 Itu
SO.4 lb/10EI2 Itu
Controlled by wttlclono. b.f.d on «n«ln««rln»
Controllod by ISP. b«««d on >n«ln«rln« Jud««Mnt
Controlled by •crubber. ba*ed on engineering judgement
I 0.07 Ib Nl OKtde»/tOOO Control etetue unclear, b«ed on eource t«t>
gel uette oil
0.0034 Ib/ton vood burned Uncontrolled, b»ed on one itvidy. nonb»«led >tove
burning green vine
J05032 O.OOOOli Ib/ton tot»l Controlled by febrlc filter. b»ed en «n«lv«l« o« one
eebestos produced Bill
744O020 22i Uowen fabric finishing He«t fettlng
330001 1.24 x IOE-5 Ib/ton
Obrlc
Uncontrolled, bee*d on t..t d«t«
7440O20 22* Uoven l.brlc flnlihlng
Tenter fraee* - re»tn
llnKMng
7440020 22e Mouen fabric flnlthlng Thereoeol dyeing
110001 1.2 > 10C-4 Ib/ton fabric Uncontrelled. tverage of four teood. one Plant, participate control »/eechanlcal
lb/IOCI2 Itu collector (cyclone). Hoed feed ret* 0.2* if/i. boll.
eff. 55.31
177
s
5
-------
Pag. No. 225
0»/2I/»0
POLLUTANT
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
CAS
NUMBER
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
SIC
CODE
K
2951
2951
3241
3241
3241
3241
3241
3241
3241
3241
3241
3241
3241
33 1Z
3312
3312
INDUSTRIAL PROCESS
Wood coebustlofl.
I ndu.tr 1*1
Asphaltlc concrete
production
Asphaltlc concrete
production
Ceeent sianufaclure * dry
process
Ceeent »*nuf«ctur* - dry
Process
Ceeent •anufecture * dry
t>roc«ss
Ceeent Manufacture - dry
process
Ceeent eanufacture - dry
process
Ceeent Manufacture - dry
process
Ceeent eanufacture - wet
process
Ceeent oanufacture - wet
process
Ceeent Manufacture * wet
process
•recess
Ceeent ••nufecture - wet
process
Cok« production
Steel production
Steel Production
En I SSI ON SOURCE
Balanced draft wicke*
stoker-fired industrial
boiler
Plant stack
Plant stack
Air separator after
finish tr.ndint "111
Air separator after
initial •rlndltifl elll
Feed to finish grinding
mill
Feed to initial Winding
elll
Kiln
Raw material er.nd.nv
•ills
Clinker cooler
Clinker cooler
Clinker cooler
efter air separator
Kiln
Coke oven
Argon oxygen
decarburizatlon vessel
(stainless steel)
decarburizatlon veeeel
(.t.lnle.s steel)
SCC CODE EMISSION FACTOR
10200*0* 0.00*4 Ib/ton fuel or 55*
Ib/lOEU ItU
305002 1.48 x IOE-10 Ib/ton
concrete
305002 7.7 x IOE-10 Ib/ton
concrete
30500* < X IOC-4 Ib/ton raw
eater, feed Input
30500* 1 X IOE-* Ib/ton raw
eater, feed tnput
30500* 1 X 10E-5 Ib/ton raw
•ater. feed input
30500* 1 x IOE-5 Ib/ton raw
•ater. feed Input
30500*0* 3 X IOE-4 Ib/ton raw
•ater. feed input
30500*13 * x 1007 Ib/ton raw
•ater. feed Input
30500714 4 x IOE-* Ib/ton raw
•ater. feed Input
30500714 1 x IOE-4 Ib/ton raw
eater, fee* Input
•ater. feed Input
30500717 4 x IOE-* Ib/ton raw
eater, feed Input
3050070* 0.0002-0.002 Ib/ton raw
•ater. feed
303003 0.001* Ib/ton of coal
processed
30300**! 0.32 Ib/ton of steel
produced
30300*W 0.0*4 Ib/ton of steel
produced'
NOTES
Green wood, one plant, partlculate control w/eechanlcal
collector (cyclone), vood feed rate 0.54 kg/s. boll.
off. «I.3X
Controlled (unspecified) froe a single plant, avg. of 2
values, range Is 1.44 x IOE-10 - 1.51 x IOE-10 Ib/ton
Uncontrolled froe a single plant, avg. of 2 values,
range Is *.« x IOE-10 - a.t x IOE-10 Ib/ton
Controlled by fabric filter, based on source tests
Controlled by fabric filter, based on source tests
Controlled by fabric filter, based on source tests
Controlled by fabric filter, based on source tests
Controlled by fabric filter, baeed on source tests
Controlled by fabric filter, baeed on source tests
Controlled by fabric filter, baeed on source teets
Controlled by ESP. based en source tests
source tests
Controlled by fabric filter based on source tests
Controlled by fabric filter, based on source tests
uncontrolled, baele unclear
Uncontrolled, calculated based on source tests
Controlled with fabric filter, calculated based on
source: teete
REFERENCE
177
170
170
110
110
110
110
110
110
110
110
110
110
110
110
110
110
-------
Pag* No. 224
0»/Z1/»0
POLLUTANT
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3112 St*el production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 3312 Steel production
7440020 1312 Steel production
EMISSION SOURCE
•asic oxygen process.
fueltlves
furnace
Electric arc furnace
(alloy steel)
Electric arc furnace
(alloy steel)
Electric arc furnace
(carbon steal)
Electric arc furnace
(carbon steel)
Electric arc furnace
Electric arc furnace
(stainless steel)
Electric arc furnace
fueitive emissions (alloy
steel)
Electric arc furnace
fugitive eelsslon* (alloy
steel)
Electric arc furnace
fugitive emissions
(carbon steel)
Electric arc furnace
fugitive emissions
(carbon steel)
Electric src furnace
fugitive Missions
(stainless steel)
Electric arc furnace
fugitive emissions
(stainless steell
Open h*arth fugitive
eeisslons
SCC CODE EMISSION FACTOR
30300* 0.0001 Ib/ton of steel
produced
30300*13 0.00001B )b/ton of steel
produced
30100*04 O.O2S Ib/ton of steel
produced
30300*04 0.00003*-0. 00025 Ib/ton
steel produced
30100*01 O.OOB3 Ib/ton of steel
produced
30300*01 0.000013-0.00008* Ib/ton
steel produced
30300**! 0.3 Ib/ton of steel
produced
30300**! 0.003 Ib/ton of steel
produced
30300* 0.001* Ib/ton of steel
produced
30100* 0.00032 Ib/ton of steel
produced
30*00* 0.00054 Ib/ton of steel
produced
30JOO* 0.00011 Ib/ton of steel
produced
30300**! 0.03* Ib/ton ef steel
produced
30300*** 0.0072 Ib/ton of steel
produced
30300* O.OOOOS tb/ton of steel
produced
NOTES
Uncontrolled, calculated based on eource tests
Controlled by scrubber, calculated based on source
tests
Uncontrolled, calculated based on source tests
Controlled ulth fabric filter, calculated based on
source tests
Uncontrolled, calculated based on source tests
Controlled by fabric filter, calculated based on source
tests
Uncontrolled, calculated based on source test*
Controlled Kith fabric filter, calculated based on
source teet*
Uncontrolled, calculated based on *ourc* tests
Controlled tilth hoods end fabric filter, calculated
based on source tests
Uncontrolled, calculated bawd on source tests
Controlled vlth hoods and fabric filter, calculated
based on source tests
Uncontrolled, calculated based on source tests
Controlled ulth hoods and fabric filter, calculated
based on source tests
Uncontrslled. calculated based on source tests
REFERENCE
110
110
110
110
110
110
110
110
110
110
110
110
110
110
110
-------
on
on
on
Oil
Oil
on
OH
OH
Oil
on
OH
OH
OH
OH
Oil
Oil
rawuM
uo p»t*q p»)vt"M*3 *J*)11» >fjq»f M)fn p»noj*u* *° w*v*0*0 84«OO£0£ irtftAxo uoft.iv uon^nP0-14 l»*»S ZII£ OZOOVM
>)•») »jno« uo p»tq 'JOJIH 9|J«I»» Aq po||oj)uo3 »»J uo»/qi ZOO'O-ZOOO'O WUOOSOC ^C.*S2L ^^"»™3 »«S OZOOVH
'3.z "",!"..,".",. " ^2, *^\ — - '"'
uo pniq •I'll'-'*" "1 ••'•till »IJqt» -»! » Z HiOOSOI ^*&F ^kt " >""'3 IVZt OZOOtK
V^A *^*
>ndu| p»o> •.»}»• ^l/ .«»904d
•^••t njriM uo pntq 'rfjl Aq po||oj)uo3 "•-> uo)/qt v-301 x I MioOSOC *d$9 '• 1"««3 Ivzt OZOOVVi
*«») Mjnoa uo ponq 'JOttll 3|->q»» Aq p>||Oj)uo3 MJ uovqt »-!OI x > HiOOSOt ^ ,n»9t»nu»» )u>»3 l«£ OZOO»i
»nduj poof -j«»»» ««»30jd
•>••) »>JKO« uo pn*q 'JO)tl| 9|jq*> Aq po||>J)uo3 ntj uovqt 1-101 x • tl»OOSOt >u|pu|j« I»1J"H u»>3 Ivzc OZOOkki
>ndut po»» >jo)» • «i»30jd
•)••) OIJIMI* uo p>nq -JOMII '!-«(•» Aq po|iaj)uo3 "«J uovqi V-101 x 1 MMOSOt «!!>» Ajp . «jfH3»»nut. )»•»] tut OZOOm
>nduf f»»t *40>»o ItT* •eoaojd
)ndu| p»«| 'j»»i« 111" ttmMjt
»!•) OIJIM* uo p»nq -JOJIH 3|J<1.> Aq p.noj»uo3 «»J uovqt t-JOl x 1 MOSOC «uipu|j4 miuij a> p»«j AJP . >jn)»»nura >u.«»o uzt ozoov>i
•)•») »JM> uo pn»q 'jo^tlt 9|jqt> Aq p»|toj>uo3 x>j uovqt »-*Jt x 1 *OOSOt -»!>• Jo>»J«a». Jlv Ajp . .jn>3t>nu»« )u»»3 ivzc OZOOVVi
)ndu| pool 'j»^v« ftl* tufpuiJ* M«fut| t»aojd
«)••> oljno* uo ponq 'J«)II» >l-^t» Aq pott«J>uo3 »J l»V4t »-10t x « MOtOt •»»»» J«>tJ»d»» Jl» Ajp . •jnj3»jmj»» )uom3 t»Z£ OZOOVVi
"•Vqt 01-101 x ft - Ot-SOt x »•» «I MutJ »»J3UO> uomnpojd
'•Mit>A Z fo -»A» -»u«Id »|tu|> • «ojf pottoJtuown u>V4l 01-101 x I'L ZOOSOt »»>* »"»ld .».J3UO3 3t)) p*l|oj)uo3 uovqt 01-101 X BV'l COOfiOC ^3*>* )u*trf o>oj>uo3 9f)|*qdsu IS4Z OZOOW£
It'tt '»»• J»ltoq
•t|«l 't/H WO »»••• P*«» P04" M*<»t>A') J»»»oit» »\t ZtJOt/qt t»tJ»«"|Wl| P»Jt*-J»in3i)jtd •)»!« ou» 'peon uoojj «s •» t»»> »vqi »»00'0 MiOOZOt HH>t* >(tJP P*>»t«f -uon.nq«o5 poOfl a OZOOVM
tUON M13VJ MOttSIUl 1003 33* 13WXH NOtSSIUl (S130IM •NIXISnONt 1003 VlWnM
31$ SV3
I*"'"
.M..N
I'l'IH
1'1'IH
I"(»1N
!•»'!»
,.,>,«
......
1*1* FM
,.„,-,
,.,3,N
,.,>„
—
IHVlimN
0«/tZ/«0
szz -on Mid
-------
|»)I (0 U0)/qt SOOOO'O «OOCO£
!»>)> JO U0)/qt IIOO'O >«
ott
tune* uo p*ft*4 p«*tii«i»9 'p*uoJ)uo3un
uonanpoja |0»>s tilt OZOOVVt
!>•]! |0 uo,,ql IIOOO'O 5 Zltt OZOOVV/
Oil
*>*•> oajnoB uo po**q
l«»%f (0 uo^/qf VSOOO'O »00£0£
(|««)t uoqjtl)
T**I«0
nt aj*
•t*ot owno* uo po*iq
Oil pot*in*toa 'JOttlt a|jq*t f* *P**H Mtl" pottojtuoj loot* to uot/qt ZtOOO'O «00£OC
ott
*t«ot oajno*
!••)< to uoi/ql tlOO'O >OOtOC
poanpoJd
loot* (O uot/qt £00-0 SMOOSOE
(toot* *»iu|it«)
ZIC£ OZOOVVi
Oil
uo»/q| fO K«OOCOt
p»npojd !••>•
uo^/q| HOOOO'O-tlOOOO'O ICMOOCOt
p.jnpoj*
|»t< »o uoj/qt IBOO'O I0«00t0t
oavujnt >J» aT^t^'ia
(toot* uoqj*3>
uo|J3npojd l»«>5 Z|££
too*} ZI££ OZW*H
uo p»«tq p>tt|nl|»
poanpojd t>»9*
"01/11 SZOOO'O-itOOOO'O »0400tOC
poanpoj*'
!0>)t |0 uovqi SIO'O MWOOTOC
uon^npojd too>s ZICC OZOOkfi
|00)S Zltt OZOOtVl
toot* *o HOt/qi §10000-0 ttoOOCOC 'OU9OJ4 uoMxo :
Oil
UO P»«KJ p0^t
toot* H> «>t/qi tOOO'O MOtOC -noaoM MMXO >t*M uottanooj* toots tltt OZOO»V<
HIM
M13VJ NOISfllM M03 335
13WIOS NOUSIMJ
O330IM TVHIiWWHl 3003 KMMnN
31* SV3
0«/IZ/40
-ON o»»<
-------
P.»« No. 227
09/2I/»0
POLLUTANT
Nickel
Nickel
Nickel
Nickel
Nlck.l
Nlck«l
Nickel
Nlck.l
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
CAS
NUMBER
7*40020
7440020
7440020
7440020
7440020
744O020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
SIC
CODE
3312
3312
1112
3313
3313
333*
333*
333*
333*
333*
333*
333*
3341
3341
3341
1341
114 1
INDUSTRIAL PROCESS
Steel production
Steel production
Steel production
Ferroalloy production
Ferroalloy production
Prleary nickel ore
teelting
Prlearv nickel ore
•pelting
Prieary nickel ore
seeltlng
Prleary nickel ore
•oeltlng
Prleary nickel ore
seeltlng
Pr leery nickel ore
it.lt 1 no
Prleery nickel ore
•eel tint
Nonferrous Mtalo
production
Nonferrous eetale
production
Nonferrous oetalg
production
Nonferrous Mt»lo
production
Nonferrous ••tale
production
EMISSION SOURCE
Open hearth furnace
Argon oxygen
decarburlzation vessel
(stainless steel)
Electric arc furnace/AOD
vecvel streets coeblned
Electric ere furnace,
•e»i~sealed, ferrestlicon
Electric arc furnace,
open, f erroeenganese
Calciners
Crusher hou«e
Ore eelter/roaeter
combination
Rellnint furnace
Rotary dryer
Skip hoists
Yay bin
nelt furnace at
electricel alloy facility
Melt furnace at
nickel -cooper or
copper-nickel facility
Kelt furnace at other
nonferrous alloy facility
licit furnace at permanent
oaonet alloy facility
Helt furnace at
euporallov facility
SCC CODE EMISSION FACTOR
30300*01 O.OOOtI Id/ton of »t«.I
produced
30300* 0.38 Ibs/ton iteel
30300* 0.2S lb«/ton >teel
30300702 3.1 e
-------
Page No. 228
0«/2I/90
POLLUTANT
Nickel
Nickel
Nickel
Nickel
NIC HI
Nickel
NIC HI
Nickel
Nickel
Nickel
Nickel
Nick.l
Nickel
Nickel
Mlck«l
CAS
NUHBER
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
7440020
SIC
CODE
3341
3341
3341
3341
3341
3341
3341
3471
3*91
4911
4*11
4953
4953
4953
4953
INDUSTRIAL PROCESS
Secondary processing of
nickel-bearing scrap
nickel-bearing scrap
nickel-bearing scrap
Secondary processing of
nickel -bearing »cr*p
Secondary processing of
nickel-bearing scrap
Secondary processing of
nickel-bearing scrap
Secondary processing of
nickel -bearing scrap
Secondary processing of
nickel-bearing scrap
Nickel electro-deposition
Battery (ntckel-cadalua>
Manufacture
Cooling tow«r», utility
Cooling towers, utility
Municipal waste
combustion
Municipal waste
co*bustl0n
Municipal waste
co*bustion
nunicipal IMSU
coebustlofl
EMISSION SOURCE
Cast iron scrap Melting
furnaces
•eltlng furnaces
•citing furnaces
Iron and steel scrap
•el ting furnace
Nickel alloy steel scrap
Melting furnace
Other nickel alloy scrap
•eltinf furnace
Stainless st*el scrap
•el ting furnace
Stainless gteel scrap
••It Ing furnace
Entire process
Total plant emissions
Fresh water cooling
towers with drift loss
range of 0.002 to O.OOSt
Fresh water cooling
towers with drift loss
ranee of 0, 1 to 0,21
Incinerator burning
refuse and sludge
Incinerator burning
refuse only
Incinerator stack
Refuse derive* fuel
iftclnereter
SCC CODE EMISSION FACTOR
304010 20 Ib/ton of nickel
charged
304010 2 Ib/tofi of nickel
charged
304010 2 Ib/ton of nickel
charged
304010 0.0015 Ib/ton of Iron and
ftteel produced
304010 10 Ib/ton of nickel
charted
304010 I Ib/ton of nickel
charted
304010 10 Ib/ton of nickel
charted
304010 0.« Ib/ton of §teel
produced
4.W > IOE-7 lb/hr/ae*
304 l.l Ib/ton of nickel
proceeeed
I 0.7M Ib/tOCIZ Itu heat
Input to power plant
1 37.10 U/10E12 Itu heat
Input to power plant
501001 0.005 Ib/ton of .olid
ttaet* Incinerated
501001 0.00] Ib/ton of eolld
naste Incinerated
501001 0.002 Ib/ton Mule. Mild
«a»t«-dry wt.
501001 0.0122 Ib/ton RDF
cootanted
NOTES
Uncontrolled, baaed on enelneerine Judeeeent
Controlled) baved on entlneertnt judteeent
Controlled* based on enplneerlnt Judtepent
Controlled, baeed on eaterlal balance
Controlled, baeed on Material balance
Controlled, baeed on enttneerlnt Judteaent
Controlled, baeed on eueetionnalre purvey revulte
Valu* IP for ptrlktnt, can be ueed for platlnff,
eteaeured factor
Uncontrelled, baeed on Induetry reeponeee to
eueptlonnalre purvey
Uncontrolled, baeed on eource teetp
Uncontrolled, baeod en eourco teptp
Controlled by wet ecrubber. calculated baeed on source
teet
Controlled by wet ecrubber, calculated baeed on eource
teete
Controlled by aprav-baffle ecrubber, baled en eaterlal
balance for eedel Incinerator
1001 RDF fuel only, ftp control only, overall averaee
of eeveral source aver apes, rente It 0.00044 - 0.03*
REFEREt
110
110
110
110
110
110
1 10
110
P2
110
110
110
110
110
M
110
-------
P«»« No. 22*
0»/JI/»0
POLLUTANT
Nlck.l
Nick.l
Wlck.l
Nickel
Hlck«l
Nlck«l
Nickel
Nlck.l
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
7440020 4*5! Municipal ua»te
coebuctlon
7440020 4*53 Municipal »a«t«
coHbuptlon
7440020 4*53 Municipal «a«te
coebu*tlon
7440020 4*53 Municipal uaate
coebuption
7440020 4*53 Municipal »•!(•
coebuption
7440020 4*53 Municipal »••(•
eoebustlon
7440020 4*53 Municipal tiatt*
coBbu»tlen
7440020 4*53 Municipal M>t«
coebuption
EMISSION SOURCE SCC CODE EMISSION FACTOR
Refupe derived fuel 501001 0.005* Ib/ton RDF
Incinerator coebuited
Rafupe derived fu«J 501001 0.0052 Ib/ton RDF
Incinerator contacted
Nodular «tarved-alr 501OOI 0.00022 In/ton feed
coebuator
nodular *tarved-alr 501001 0.0030 Ib/ton <••*
coabUBter
noAil.r •xcm-tlr 501001 0.0050 tb/tan <«d
ewibuttor
Hedular «xc«i»-4tr 501001 2 x 10E-* Ib/ton Ind
eo«bu«tor
n».« burn. ut«r mil 501001 0.00034 Ib/ton fnd
Inelnarater
Lirx ••« burn rot.rv 501001 l.H » 10E-5 Ib/ton », r.no. U 1.7 x IOE-5 - O.OOM4 Ib/ton
Uncontrollad. ovorall avoraM of tavoral vourco
avora*». rani* It *.2 » IOE-5 - 0.0071 tb/ton
tSP contra! only, ant d«t« point only
Dry «orb«nt Injection aftor acid ia« and Ptl control,
on« data point only
Uncontrolled. on« data point only
Capacity > *OO tona/day. ISP control only, on* data
point only
REFERENCE
180
iao
110
i to
IK>
110
110
1*0
a«t«r I*BO
NUk.l
7440020 4*53 Municipal va»t<
coabuitlon
7440020 4*53 Municipal »«»t«
u>tlon
7440020 4W! Municipal nait<
coobuvtton
7440020 4*53 Municipal uapte
coebuetlon
7440020 4*53 Municipal MPta
coebu*tion
Laroe naps burn rotary
utorvall coatantor built
aftor 1*M
Nap* burn Matornall
coobuptor. Mall plxo now
•odol to any a*a Mdluo.
Kacp burn watorwall
coobuotor. Mall *l*o now
•odol to any a«a oadluo
Naaa burn MatoruaU
coobumtor. voall also non
•odot to any a*a o«dlu«
Ha** burn iMtorwal]
conbuator. uwll >lia notf
•odol to any a«o ••dlu*
501001 0.00017 Ib/ton fnd
501001 *.4 x IOE-5 Ib/ton »a.d
Capacity > 4OO ton*/day, opray drylnt aftor acid tap
and Ptl control, ovorall avt. of Mvoral «ourc« avo*.,
ranoe I* 0.00013 - 0.00022 Ib/ton
Capacity < «OO ton*/d*v. uncontrolled, on* data point
only
SOI 001
4.1 x tot-5 Ib/ton fnd Capacity < 4OO tonp/day. ftp control only, ovorall
avoraoo of pevoral *ourco avoraevp. ran«« la 4.4 K
10C-5 - 1.0 x 10C-S Ib/ton
0.001*2 Ib/ton food Cap. < *00 ton*/day. ppray OVylno aftor acid «ap and Ptl
control, ovorall avo. of *ovoral pourco avop.t ranto !•
2.1 x IOE-S - 0.0031 Ib/ton
I.* x JOE-* Ib/ton fnd Capacity < *OO tonp/day. dry porbont Injection after
•eld ea* and Ptl control, one dot* point only
IM
7440020 4*53 Municipal w«te
coebuption
Ra«« burn Materwall
co«bu«tor. built before
1*10
MIOOt 1.200 Ib/ton feed
ESP control enly. one data point only
7440020 4*53 Municipal mate
coebuetlon
nape burn vaterMall
coeaueter, built Mfore
IttO
(01001 0.02O Ib/ton fee4
Uncontrolled, one data point only
-------
P«oe No. 230
0»/2I/»0
POLLUTIWT
Nickel
Nickel
Nlck.l
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nickel
Nlck.l
Nickel
Nickel (II) oxide te«
Iron foundrin
Ett I SSI OH SOURCE
facility
facility
Fluldlzed bed
Fluldlzed bed
Fluldtzed-bed furnace
null! Pie hearth furnace
hJultlPle hearth
Incinerator
Multiple hearth
Incinerator
Fluldized-bed furnace
Multiple hearth furnace
nuUlple hearth furnace
Incinerator
Electric ere furnace -
•eltlne/ref tnlne
Electric ere furnace -
chart* and tw cycle
AOD veviel - awlt and
refine cycle
Electric arc furnace -
cnarte and ta* cycle
Electric arc furnace -
charee end ta» cycle
SCC CODt EMISSION FACTOR
501001 0.014 Ib/ton feed
5010050* 0.0003 tb/too of tolld
y««te tncln.rat«d
5010050* 0.15 Ib/ton of >olld
w««t* lnclnw«t.d
5010050* 0.0* Ib/ton dry tlud»«
5010050* 0.0032 Ib/ton dry «lud».
5010050* 0.003 Ib/ton of »olld
watte Incinerated
$010050* 0.15 Ib/ton of .olid
waste Incinerated
501 0.011 Ibi/ton dry eludfe
501 0.117 lot/ton dry eludfe
101 0.004 tbe/ton dry eludee
50200505 2.53 X 10C-4 Ib/ton
30IOO*Of 0-0.12 lot/ton carbon
•teel
30300«0t 0 - 0.00* Ib./ton carbon
•teel
30300* 0.4M lt»/ton eoeclalty
•teel
3O400304 0.014-0.042 Ibe/ten of
Iron produced
10400304 ». 14-0.42 lb./ton ef Iron
•reduced
NOTES
point only
Uncontrol 1 ed » one data point only
Controlled by wet •crubber, calculated baced on cource
te«t<
uncontrolled, calculated baeed on tource teete
nveraee of three te*te. ecrubber (rant* 0.0082 - O.I5*>
nveraee of 10 te«te. •crubtaer
Controlled by Met scrubber, calculated baied on tource
teate
Uncontrolled, calculated baeed on eource tnte
Uncontrolled ealHlone, alntle teet
Uncontrolled ealeelone, rente of 5 teite u»* 0.002 -
0.33 Ibe/ton
Controlled ky wet ecrubber, ranee •< * teete »»» 0.0002
- 0.0012 Ibe/ton
Uncontrolled, teet data
Uncontrolled Ml eel one
Uncontrolled nieetone
Uncontrolled eel eel one
Uncontrolled enteelone
Uncontrolled oelnlone
REFERENCE
110
110
110, 203
110
101
101
110
110
203
203
103
1*7
It!
Iff
in
tt4
It4
$
5
-------
Pa»a No. 231
09/21/90
CAS
POLLUTANT NUMBER
Nitrobenzene »«»SJ
Nitrobenzene *8*53
Nitrobenzene »B»S3
Nitrobenzene *B*53
Nitrobenzene W53
Nitrobenzene »B»S3
Nitrobanzene »B»53
Nitrobenzene »B»53
Nltrobanzena »B»S3
Nitrobenzene »8»S3
2-Mltrophenol 18755
2-Nltrophenol 18755
4-Nltrophanel 100027
4-Nltroph*nol 100027
Octachlorodl benzof urani .
total
Octachlorodl benzof wane.
total
Octachl orotf t bcnzof uren* ,
total
Octachlorodl benzof ur an*.
SIC
CODE INDUSTRIAL PROCESS EMISSION SOURCE
2* Solvent application General eai*»ioni
2B6S Nltrob«nz>n« and anlltn* Fuvitlvc Minion*
production
2B«5 Nltrob«nz«no and anlltna Ganaral ooiiitoni
production
28«5 Nltrobanzoni and anilln. Storaio
production
2l«t DUhloro.nl I ln« Sanoral nloioni
production
2849 Dlnltrobanzona production 6«n«ral ••lnlon»
28i* Nltrobonzono uia as a Fuvltlvo Million*
chaalcal Intarvadiato
2Bi9 Nltrobanzano u*a at a Canaral ••luioni
choolcal Intornadlata
2B<9 Nltrobanzona uia al a Storava
chaalcal Intarnadlata
«»S3 Ua*tayatar traataant POTU
4»53 Sayata iludia Fluldlzad-bad lurntea
Inclnaratlon
4*5! Sayan iludt* Bultlpla htartK
-------
Page No. 232
09/21/90
CAS
POLLUTWtT NW1BER
Octachl orodl benzof urans .
tot«l
Octachl or odlbmnzof urans,
total
Octachl orodl benzof urans ,
total
Octachl o** odt b*niof uranv ,
total
Dctachl orodl benzof urans.
total
Octachl or odlbanzof urans,
tot.l
Octaehlorodlbenzo-p-dloxl
ns, total
Octachl orodl benzo-p-dloxl
n«. total
Octachl orodl benzo-»-dl oxl
ns, total
Octachlorodlbmnzo-p-dloxl
ns. total
Octachlorodlbenzo-p-dloxl
ns, total
Octaclilorodlb«nzo-p-dloxl
ns, total
Octachlorodlbenzo-p-dloxl
n«. total
OctacMorodkbenlo-p-dioxl
n«. total
Octacnlorodlbenzo-e-dloxi
ns. total
Octachlorodlbenzo-p-dloxl
n>. total
l.l.J.T.I-Oentaehlorodib*.
nzofuran
SIC
CODE INDUSTRIAL PROCESS
49 Swan sludge
Incineration
49 Ulro reclamation
incineration
49 Uood combustion
combustion
4953 Municipal uaste
combustion
10* Hospital valte
Incineration
2t Pulp/paper olll, kra
-------
Page No. 233
09/21 /»0
POLLUTANT
2,3.4,7.»-Pei>tachlorodlbe
nzofuren
Pentachlorodibenzof urant,
total
Pentechler odi benzof urent,
total
Pentachl or odi benzof urent.
total
Pentachl orodl benzof urant .
total
Pentachl oredi benzof urant ,
total
Pentachl or odlbenzef urant.
total
Pentachl or odi benzof urant ,
total
Pentachl oredi benzof urant,
total
Pentachlorodibenzof urant .
total
Pentachlorodibenzof urent .
total
Pentachl oredi benzof urant ,
total
Pentachlorodibenzof urant,
total
Pentachlorodibenzof urant .
total
1 ,2,1,7.1-Pentachlorodlbe
nzo-p-dloxin
CAS SIC
NUMBER CODE
S71I7314 49S3
2«
3341
49
49
49
49
49
4953
49S3
4953
4953
4953
aoe
403217*4 4953
INDUSTRIAL PROCESS
Municipal Hatte
coebuttlon
Pulp/paper Bill, kraft
paper recovery botlert
Secondary copper .Melting
Drue and barrel furnace
lndu.tr 111 carbon
regeneration
Senaga eludee
Incineration
Uire r«clae«tlon
Incineration
Wood coebuttlon
Municipal Mete
coobuitlon
Municipal Hatte
coebuttlon
Municipal Hatte
coebuttlon
Municipal Hitte
coebu.tlon
Municipal Hatte
coebuttlon
Hotpitel natte
Incineration
Municipal H.tte
coebuttion
EMISSION SOURCE
Matt burn. Hater Halt
incinerator
Stack
Stack
Stack
Stack
Stack
Stack
Stack, lndu.tr 1.1
Hood-fired boiler
Maee burn
Matt burn, nater Hall
incinerator
Hate burn. Hater nail
inclneretor
nodular Incinerator
Refute derived fuel
Incinerator
Incinerator
Mate burn. Hater Hall
Incinerator
SCC CODE EMISSION FACTOR
5 1.14 - 10.4 noYNn3 • 121
C02
307001 Not detectable - 0.4«
ng/dlM t 31 02
304002 19.000 n./d.c. • 3> 02
5 4.2 m/dice • 31 02
0.17 H9/dtc» «, 3X 01
S 4.1 - 110 ng/dlCH t 31 02
S 22 n*/dt» * 31 O2
102009 23 ng/dtco « 31 02
S 0.423 - 11.000 ««/N«3 *
121 C02
S 33.2 - S770 nt/N.3 t 121
C02
S 2.*2 x 10C-I - S.«2 x
10E-S Ib/ton feed
S 97 - 1110 ng/N»3 • 121
C02
5 I3S - 9100 ng/H.3 • 121
C02
502O05OS 2.20 x IOE-* Ib/ton feed
S O.It - I.I ng/N.3 • I2X
coz
NOTES
n • t. 4 location., controlled Hlth an ESP
Three location, totted, detection llelt <0.1 ng/dtce t
31 02
Ettleated value fro* .tack tett retultt
Tier 4 .tack tett taopllne
Tier 4 .tack tetttno
Three location, totted, does not Include 2,3,7,1-ltoeor
Estlaated value fro* .tick tett retultt
Salt-laden Heed. Tier 4 .tack te.tlng
Developed fro« teet date, <•/ varlou. controls - MP or
Hater spray hueldlfler/dry torbent Injection
n • 9, I location., controlled Hlth en ESP
n • S, I location., controlled Hlth an ISP
Developed free teet date, ell uncontrolled
Developed free test data, *eet ESP controlled, one Hlth
ESP/cyclone
Uncontrolled, teet data
n • «. 4 locations, controlled Hlth en ESP
REFERENCE
III
115
US
IIS
US
US
US
US
117
111
111
117
117
1*7
111
Pentachlorodlbenzo-p-dlox
ln«, total
Pentechlorodl ben»-p-dlax
Ine. totel
2« Pulp/paper elll, draft
paper recovery boll ere
Stack
3341 Secondary copper .nitIne Stack
307001 Mot detectable - 0. IS Three locations totted, detection Holt <0.1 ne/dtce « IIS
*«/deai « J« 02 IS K
30400J 2100 np/d«« • II 02 (etlMted yalue free, .tack te.t reeult* IIS
-------
Page No. 234
09/21/90
CAS
POLLUTANT NUMBER
Pentachlorodlbenzo-p-dlox
lOf. total
Pentachlorodibenzo-p-dlox
in.. total
Pentachlorodibenzo-p-dlox
ini, total
Pentachlorodlbenzo-p-dlox
Ins. total
Pontachl orodl benzo-p-di ox
Ins. total
Pentachlorodlbenzo-p-dlox
Ins. total
Pentachlorodlbenzo-p-dlox
Ins. total
Pentachl orodlbanzo-p -dl ox
ln». total
Pentachlorodlbenzo-p-dlox
In*. total
Pentaehlorodlben»o-p-dlox
Ins. total
Pantachlorodibenzo-p-dlox
In*, total
Pentachloroehenol (PCP) 171*5
Pentachloroohenol (PCP) 171*5
Pantaehloroph.no! (PCP) 171*5
Pentachlorophenol (PCP) 171*5
Pentachloroph.no! (PCP) 171*5
Pai.tacMoropn.nol (PCP) I7MS
•entachloroehenol (PCP) I7MS
SIC
CODE INDUSTRIAL PROCESS
49 Drue and barrel furnace
49 Industrial carbon
regeneration
49 Sawav* >lud9«
Inclnaratlon
49 Ulr« reclamation
incineration
49 Uood co«bu«tlon
4953 Municipal yafta
coabuctton
4953 Municipal Haiti
conbuitlon
4953 Municipal yalti
coibuitlon
4953 Municipal yaitl
co«buitlon
4953 Municipal yaitl
co*«uitlon
80* Hoipltll vaitl
Inclniratlon
2491 Uood prnirvlni
Z491 Uood pr.tarvlni
2491 Uood pr.««rvlnl
2491 Uood prnirvlnt
2491 Hood priiirvtnf
2491 Uood priurvlnt
2491 Wood prmrvlnt
EftlSSIOM SOURCE
Stack
Stack
Stack
Stack
Stack, Industrial
wod-flrid bollar
Mais burn
Man burn, water wall
incinerator
Mais burn, water wall
Incinerator
Modular incinerator
Refute derived fuel
incinerator
Incinerator
Craoiote conditioning
Creosote cool -down
Craosote treetlne
cylinder fugitives
Incineration of waste
rente treatlnt cylinder
fufltlval
Pentachl orophenel
condltlonlne
Pwtachlorophenel
cool -down
SCC CODE EMISSION FACTOR NOTES
0.44 ng/dice * II 02 Tier 4 itack testing
5 Not detectable - I.I Three locations tested, detection llelt <0.1 no/dsco 1
no/die* • 31 02 31 02
102009 41 ne/dice • 31 02 felt-laden wood. Tier 4 stack testlnf
C02 water spray hueldlf ier/dry sorbent Injection
S 2.99 - 2700 ne/He3 • 121 n • 9, 4 location!, controlled with an ESP
C02
5 2.34 x lOE-l'- 1.3* x n * S, 1 locatloni. controlled wltli an Iff
10E-S Ib/tori feed
S *3 - 1540 no/Ma3 • 121 Developed fro* teet deta, all uncontrolled
C02
t 54 - 24BO ni/N»3 • 121 Developed froa teet dete, aost ESP controlled, one with
C02 ESP/cyclone
50200SOS 0.41 x IOE-* Ib/ton feed Uncontrolled, teet date
30700501 0.0009 lbi/hr lased on one eaevllnt rrovae at one facility
307005 0.0012 lbi/hr land on one sawllni proerao at one facility
107005 0.«3 e«/se3 ••• leaked One eeasurawmt
30700? Not detectable Controlled with baehoux
307005 3.« »e/»3 tas leaked Averaoe ef I omsureMnte
30700597 0.0011 Ibs/hr lased en on* iaa»llne proerae et one facility
30700597 0.0009 Ibe/nr «a»ed on one saepllno eroerae at one facility
REFERENCE
115
115
US
115
us
117
111
111
117
117
1*7
10
10
4
«
•
10
10
-------
P«»e No. 235
0»/2I/»0
POLLUTANT
Pentachlorophenol (PCP)
Pentachlorophenol (PCP)
Pentachlorophenol (PCP)
Pentachlorophenol (PCP)
Pentachlorophenol (PCP)
Pentachlorophenol (PCP)
Pentachlorophenol (PCP)
1,3-Pentadlene
1,3-Pentadlene
1 ,3-Pentadl ene
1,3-Pentadlene
1,3-Pentadiene
1,3-Pentadlene
1,3-Pentadiene
I.S-PentadlM*
1.3-Pentadlene
l,3-*«ttadt*n*
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
B7B45 24*1 Uood preserving
87845 24*1 Uood preservlnf
B7B45 24*1 Uood preservlnf
•78*5 2B7* Pentachlorophenol
production
B7845 4*53 Sewage slud*e
Incineration
87845 4*53 Sowaoe sludfe
Incineration
87B45 4*53 Uastewater treatemnt
50440* Scrap tire, open
504*0* Scrap tire, open
504*0* Scrap tire, open
504*0* Scrap tire, open
504*0* Scrap tire, open
504*0* Scrap tire, open
504*0* (crap tire, open
504*0* (cr*» tire, open
504*0* (crap tire, open
5O44O* Scrap tire, open
burnt nv
burnlnf
burnlnf
burnlnf
burnln*
burnlnf
burnlnf
burnlnf
burnlnf
burnlnf
EMISSION SOURCE
Pentecnl orophenol
treattnf - fuflltlve
Thereat (pan) evaporation
of creosote wastewater
Thermal (p«n> evaporation
of pentaehlorophenol
uastewater
General emissions
Fluldlzed-bed furnace
Hultlple hearth furnace
POTU
Tire* In experimental
burn hut
Tire* 1ft experimental
burn hut
Tlr** In experimental
burn hut
Tire* In experimental
burn hut
Tire* in experimental
burn hut
Tire* In experimental
burn hut
Tlr** In experimental
burn hut
Tires In experimental
burn hut
Tire* in experimental
burn hut
Tlr** In experimental
burn hut
SCC CODE EMISSION FACTOR
307005*7 0.72 Ibs/hr
2 ef/*m3 fa* vented
10,000 mg/sm3 fa* vented
301013 1.1 tb/ton active
Ingredient
5010050* <0.0003 Ib/ton dry sludge
5010050* <0. 00018 Ib/ton dry
•ludf*
50100701 * Ib/ton
Pentachlorophenol In
Influent
2.5* Ib/ton tire
0.707 Ib/ton tire
1.31 Ib/ton tire
2.45* Ib/ton tire
2.030 Ib/ton tire
4.** Ib/ton tire
1,1*4 Ib/ton tire
0.322 Ib/ton tire
O.041 Ib/ton tire
«.2*S Ib/ton tire
NOTES
Saved on one sampling proflram at one facility
Average value
Average value
Control unknown, ba*ed on industry
One te*t, *crubber
One te*t, *crubber
Based on eml*. modeling fop hypoth.
avera** POTU that treats industrial
VOST samples burn rate - 1. 5 If/hr,
2" by 2* piece, uncontrolled
VOST samples burn rat* - 2.3 k*/hr,
2* by 2* plmc*. uncontrolled
VOST samples burn rat* - 0.* k*/hr,
2* by 2* piece, uncontrolled
VOST (ample* burn rate - 1.3 k*/hr,
2* by 2" pl*c*. uncontrolled
VOST samples burn rat* - 1.4 kf/hr,
2* by 2* piece, uncontrolled
VOST samples burn ret* - O.I kf/hr,
2* by 2* piece, uncontrolled
VOST samples burn rat* - 0.5 kt/hr,
1/4 te !/• of • tire, uncontrolled
VOST *ae*l*« burn rat* - 1.7 kf/hr.
1/4 t* I/* of • tire, uncontrolled
VOST samples burn rate - 1.5 kt/hr,
1/4 to l/» of • tire, uncontrolled
VOST samples burn ret* - 1.27 >*/hr
1/4 to l/« *« • tire, uncontrolled
OBtlmate*
POTW, represent*
Masteweter
shred condition •
•hred condition •
•hred condition •
•hred condition •
•hred condition •
•bred condition •
chunk condition* •
chunk conditions •
chunk conditions •
, chunk condition* •
REFEREN
10
*
•
1*
101
101
5*
212
212
212
212
212
212
212
212
212
212
-------
P.g. No. 236
0»/2I/»0
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
EI1ISSION SOURCE
SCC CODE EMISSION FACTOR
I ,3-Pentadlene
Phenanthreno
Phenanthrene
Scrip tin, open burning Tire* In experimental
burn hut
Scrap tlr«, op«n burning T,r«« in •xp«rl*«nt*>l
burn hut
Scrap tlr«, op«n burning Tlr«> In •xpwlMntal
burn hut
0.0»» Ib/ton tire
0.788 Ib/ton tlr.
0.444 Ib/ton tlr.
VOST samples burn rate - 2.27 kg/hr. chunk condition! >
1/4 to 1/4 of • tiro, uncontrolled
IAD-2 extracts K/nS analysis, shred condition • 2* by
2" pieces, burn rate • 1.3 kg/hr. uncontrolled
XAD-2 extracts w/nS analysis. Chunk condition • 1/4-1/4
of tire, burn rate • 1.7 kg/hr. uncontrolled
212
212
Phonanthrene .
Phenanthrene
Scrap tire, open burning Tire* in experimental
burn hut
Scrap tire, open burning Tire* in experimental
burn hut
0.270 Ib/ton tire
O.S11 Ib/ton tire
>AD-2 extract! K/nS analysis. Chunk condition • 1/4-1/4
of tlr«. burn rat* • 2.3 k«/hr. uncontrolled
Sue of PAH analy on lie. extrat. of IAO-2 teat t filter
comeont. shred condition • 2* by 2' piece, burn
rate*1.3 kg/hr, controlled
212
Phenanthreno
Tires In experimental
burn hut
0.4*8 Ib/ton tire
Sue of PAH analy on lie extrat. of IAD-2 test t filter
coepont. shred condition • 2* by 2" piece, burn
rate*l.l kg/hr, controlled
phananthron*
Scrap tire, open burning Tires In experimental
burn hut
O.SBJ Ib/ton tire
Sum of PAH analy on 111 extrat. of IAD-2 te«t It filter
compont. shred condition • 2* by 1* piece, burn
rate-1.7 kg/hr. controlled
Phenenthrone
Scrap tire, open burning Tires in experimental
burn Hut
0.344 Ib/ton tire
Sum of PAH analy on lie extrat. of IAD-2 test * filter
compont. shred condition • 2" by 2- piece, burn
rato-2.3 kg/hr. controlled
Phenanthrone
BS01I 25 Wood combustion,
industrial
Horizontal return tube
10200*0* t.» * IX-* Ib/ton fuel
(dry basil)
Result* of (JC/rtS analysis of xad-2 resin extract
17*
Phenanthrene
85011 25 Wood combustion,
industrial
•alanced draft vlckes
•toker-flrad Industrial
boiler
I0200*0« 0.00032 Ib/ton fuel
Dry mood, one plant, partlculate control m/mochanlce!
collector (cyclone), mood feed rate 0.2* kg/s. boll.
eff. 55.31
Phenanthrene
8S01S 25 Uood combustion.
Industrial
lalanced draft ulcket
stokmr-fired Industrial
boiler
Scrap tire, open burning Tlree In experimental
burn hut
10200*0* 4.4 x IOE-S Ib/ton fuel
1.473 Ib/ton tire
Green uood. one plant, partlculate control «/mmchanlcal
collector (cyclone), uood feed rate 0.54 k*/s. boll.
eff. »I.3I
IAD-2 extract* v/ns analysis, shred condition • 2* by
2* pieces, burn rate • 1.3 kg/hr. uncontrolled
212
Scrap tire, open burning Tlras In experimental
burn hut
Scrap tire, open burning , Tires In experimental
burn hut
1.33 Ib/ton tire
1.133 Ib/ton tire
IAD-2 extracts u/rtS analysis, shred condition • 2* by
2* pieces, burn rate • I.I kg/hr. uncontrolled
IAD-2 extract* «/« analysis. Chunk condition • 1/4-1/4
of tlr*. burn rate * 1.7 kg/hr. uncontrolled
212
Scrap tire, open burning Tire* In experimental
burn hut
».3J« Ik/ton tire
IAO-2 extract* v/ns analyst*. Chunk condition > 1/4-1/4
*f tire, burn rate • 2.3 kg/hr, uncontrolled
-------
Paw No. 2J7
0*/21/»0
CAS SIC
MUHBER CODE INDUSTRIAL PROCESS
EMISSION SOURCE
SCC CODE EHISSION FACTOR
Scrap tire, open burning Tires In experimental
burn hut
0.175 Ib/ton tire
VOST aaeple* burn rate - 2.3 ke/hr, «hred condition •
2" by 2" piece, uncontrolled
Scrap tire, open burnln* Tlrea in experi*ental
burn hut
0.007 Ib/ton tire
VOST eaeple* burn rate - t.*3 k»/hr. chunk condition.
1/4 to l/< of a tire, uncontrolled
108*52 24*1 Uood prnervlne
Crvovot* trv.tlng
cylinder lu«ltlv«>
307005 0.11 »o/»»l eaa leaked One eeatureeent
108*52 24*1 Uood ereeervlno
108*52 24*1 Uood preserving
Incineration of Haste 307005 1.0 ue/sa3 ttack *..
Penta treatine cylinder 107005 0.55 eo/ie3 *ae leaked
fuiltlvea
Controlled Mith bavhouee, avaraoo value
Averaee of 3 eeasureeenta
108*52 24*1 Uood preaervlne
Th«ra.l (pan) •v.poration
of
30 ee/so3 oas vented Averaee value
Phenol
100*52 24*1 Uood pre»ervln*
of pontachloropnanol
200 *e/*e3 eaa vented Averaee value
108*52 25 Uood co.bu.tlon.
Induitrlal
Horlxontal roturn tub*
10200*0* l.t x IOE-* Ib/ton fuel Retultt of CC/nS analysts of xad-2 resin extract
(dry basis)
108*52 25 Uood co.bu.tlon,
industrial
l.l.nc.d draft vlctn
atotar-flrad Indu.trl.l
bailor
10200*0* 0.0002 Ib/ton fuel
Dry Mod, one plant, partlculate control v/Mchanlcal
collector , uood feed rate 0.2* ko/e. boll.
off. SS.JI
108*52 25 Mood co»bu»tlon,
Indu.trl.l
lalancad aVaft vlckaa
atoker-ftred Indu.trl.l
Dollar
10200*0* 2.2 x IOE-5 Ib/ton fuel Creen »ood. one Plant, partlculate control l»/oecnenl cat
collector (cyclone). anod feed rate 0.54 to/s, boll.
off. «I.3X
108*52 28 Indu.trl.l Metevate
treatoent
101
0,2* x «e> of pollutant Uncontrolled Mission*
in vaste streae
108*52 28 Indu.trl.l vutenate
treetoent
1.7 x lot-OS x eass of Uncontrolled emissions
pel It in uaste streae
Phenol
Phenol
108*52 28 Indu.trl.l vatteiiete
troatoent
10S*S2 28 Indu.trl.l ».»t«i.t<
trMtxnt
Traatoant tank
Mon-.ar.tad blgbaain
2.1 x 10C-04 x «... of
P0)]t In vaate atreae
Uncontrolled e»l*eiont
1.* x IOE-04 x «... of Uncontrolled emissions
pollt In waste streae
Phenol
108*52 21 Industrial Mtteiiater Aerated blobaslit
108*52 28 Indu.trl.l nutmat
trntnnt
l.» x 10E-OS x eass of Uncontrolled Missions
pollt In vast* streae
«.« x IOE-04 x eass of Uncontrolled emissions
poltt in Maete streae
205
108*52 28 Indu.trl.l
trMtnnt
Aerated wueilutlon
b««ln
101
V.077 x use of poll I In Uncontrolled eel salons
»aste streaei
-------
Page No. 23B
09/21/90
POLLUTANT
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
CAS
NUMBER
108*52
108*52
108*52
108952
108*52
108952
108952
108952
108952
108952
108952
108952
108952
108952
108952
108952
108*52
108952
108*52
108*52
SIC
CODE
28
2B
28
28
28
28
28
2821
2821
2821
2833
2833
2833
28*5
28*5
28*5
28**
28*9
28*9
2M*
INDUSTRIAL PROCESS
Industrial wastewater
treateent
Industrial wastawatar
treataent
Industrial wastewater
treateent
Industrial uavtewatar
treateent
Industrial wastawatar
treateent
Industrial wastewater
treateent
Industrial wastawatar
treateent
Phenolic resin production
Phenolic resin production
Phenolic resin production
Salicylic acid production
(aspirin)
Salicylic acid production
(aspirin)
Salicylic acid production
(aspirin)
Phenol production
Phenol production
Phenol production
Acetone/phenol
eonufacture froe cueene
Acetone/phenol
Manufacture froe cueene
Adlplc acid production
Adlplc acid production
EMISSION SOURCE
Non-aerated equalization
basin
Open trench
Suep
Lift station
Junction box
Manhole
Drain
Fugitive eel salons
General aeisslons
Storaee
Fueltlve eelsslons
General eolsslons
Storaee
Fueltlve eelsslone
General eeleslone
Storaee
Product transport loadlnt
vents, coeblned
Storage tank vente
contained
Fufllttve oeieelons
Generel eteleelene
SCC CODE EMISSION FACTOR
301 0.01* x eass of pollt In
waste streae
301 2.1 x 10E-05 x ea«a of
301 1.9 x 10E-04 x eass of
301 2.0 x 10E-04 x Mass of
pollt In waste streae
301 1.1 x 10E-04 x eass of
pollt In waste etrea
301 5.7 x 10E-07 x eass of
pollt In waste strea
301 4.4 x IOE-0* x eass of
pollt In waste strea
301018 0.2* Ib/ton ueed
30101805 0.7 Ib/ton used
407 0.04 Ib/ton ueed
3010*0 0.28 Ib/ton used
3010*0 0.7 Ib/ton ueed
3010*010 0.02 Ib/ton used
30120280 0.82 Ib/ton produced
30120201 3.5* Ib/ton produced
407084 0.0* Ib/ton produced
3010*151 0.22 Ib/ton phenol
produced
30109151 8.102 Ib/ton phenol
produced
30100180 0.2* Ib/ton ueed
30100101 2.* Ib/ton used
NOTES
Uncontrolled eelsslone
Uncontrolled eeisslons
Uncontrolled eelsslons
Uncontrolled eel salons
Uncontrolled eelsslone
Uncontrolled eeleslone
Uncontrolled eeleslons
Engineering Judgeeent
Engineering Judoeeent
Engineering Judeeeent
Froe engineering eatleatee
Froe engineering eetiMtoe
Froe engineering estimates
Engineering eetieatee
Engineering eetieates
Engineering estleates
Control unknown, average of two Industry estleates
Uncontrolled* overage ef a calculated value and an
Industry eetleate
Date froe alt a vlalt
late free git* vlelt
REFERENCE
205
205
205
205
205
205
205
13
13
13
13
13
13
13
13
13
If
13
13
11
s
$
-------
P«»e No. 23?
09/21/90
POLLUTANT
Phenol
Phenol
Ph.no)
Ph.nol
Phtnol
Ph.nol
Ph.nol
Ph.nol
Ph.nol
Ph.nol
Ph.nol
Ph.nol
Phenol
Ph.nol
Pfcenol
Phenol
Phenol
Phenol
Ph.nol
Phenol
Phenol
Phenol
CnS
NUMBER
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
108*52
101*52
SIC
CODE
284*
2S«»
284*
2B«»
28**
2B*»
2B<*
281*
2B«*
2B«»
2B«»
2B.»
28e»
287*
S2»*
32»«
32»«
32**
32»*
32»«
32**
32**
INDUSTRIAL PROCESS
Adi pic acid production
Bisphenol A production
Blipnenol A production
Biiphenol A production
Caprolactae production
Caprol«cta« production
Caprolactao production
Dodecvlphenal production
Dodecylphenol production
Dodecylphenol production
Nonylphenol production
Nonylphenol production
Nonvlphenol production
Pent«chlorophenol
production
Flue .tt.nu.tton yool
elan fiber production
Flaee ottenuatlon wool
glaii liber production
Flaoe attenuation wool
glail fiber production
Flaee attenuation yool
•la» fiber production
Rotary epln wool flan
fiber production
Rotary tpln wool elan
fiber production
Rotary spin HOOI elan
fiber production
Rotary »pin wool plan
fiber production
EMISSION SOURCE
Storage
Fugitive eeliilont
General eeliiioni
Storage
Fueltlve eele>lon«
General eeivmion*
Storate
Fuetttve eeieetons
General eeitelone
Storaee
Fugitive eatealone
General eniveiont
ttoraee
General eiiettont
P.- 11 product production,
curlne
R-ll product production,
curlnt
Ductbaard production,
total line
Ouctboard production.
curJne and roollnt
Ductbovd production
Heavy denelty product
.reduction
R-ll product production
•-I* product production
SCC CODE
3010010*
301152
101 15201
«07
30121080
30U1001
4070*0
301
301
407084
301
301
407084
301031
315012
315012
315012
315012
30501204
30501204
30501204
30SOI204
CnlSSlOH FACTOR
0.02 Ib/ton uied
0.24 Ib/ton u»ed
0.7 Ib/ton uied
0.04 Ib/ton uied
0.2« Ib/ton uied
l.» Ib/ton t»ed
0.02 Ib/ton uied
0.38 Ib/ton uied
!.< Ib/ton uied
0.02 Ib/ton uied
0.38 Ib/ton uied
l.« Ib/ton uied
O.O2 Ib/ton tiled
2.0 Ib/ton active
Ineredtent
0.2 Ib/ton f InUhed
product
2.7 Ib/ton flnllhed
product
*.e Ib/ton flnllhed
product
O.I Ib/ton flntehed
product
7.*8 Ib/ton flnllhed
product
1.04 Ib/ton finlihed
1.84 Ib/ton II "lined
product
I.P2 Ik/ton flnllhed
product
MOTES
Data froo lite vUlt
Froe enolneerino eltleatee
Froe enolneerlne eltleatei
Froe enelneerln* eltlaatee
Date free) lite vl.lt
Date «ro» lite vlilt
Date froe tlte vlilt
En«lneerln« Jud«eeent
Envlneerinv Judoooent
Englneerlne Judoeeent
Froe entlneerlnv eitlMtee
Froo enflineerint eltlatatee
Froe envineerlno. o«tl»Ate«
Control unknown . baled on Indultry oetlMtn
Control lod Kith a HVAT
Controlled ulth e HVAF
Controlled Kith a HVAF
Controlled vlth a HVAT
Uncontrolled, oay not represent ell oreanln in exluuit
etreao
Uncontrolled, «y not reprnent all oreanlce In exhauit
•tree*
Uncontrolled, My not repreient ell ortanlce In exhauit
•tr.ae
uncontrolled, m*r not roprwent ell ortanlce In enhauit
•treeo
REFERENCE
13
13
13
13
13
13
13
13
13
13
13
13
13
1*
173
173
173
171
»7
n
»7
•7
-------
Page No. 240
09/21/90
POLLUTANT
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
Phenol
•Kenot
CAS
NUMBER
1OB952
108952
IOB952
108952
108952
108952
108952
108952
108952
108952
108952
108952
108952
108952
108952
108952
108952
SIC
CODE
3294
3294
3294
3294
3294
3294
3294
3294
3294
3294
3294
3294
3294
3334
3334
4951
4*53
INDUSTRIAL PROCESS
fiber production
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Rotary spin wool glass
fiber production
Prloary aluelnuo)
production
Prleary elufflnuai
production
Sewage sludge
Incineration
Sewage sludge
Incineration
EMISSION SOURCE
R-14 product production.
curing and cooling
R-14 product production.
forolng
R-14 product production.
total line
R-14 product production.
curing end cooling
R-14 product production.
forolng
R-ll product production
Heavy density Insulation
production
Ductboard production
R-19 product production
R-ll product production.
forelng and curing
Cooling process
Curing process
Forolng process
Soderberg potltno
Soderbert pot line
Flgldlied-bed furnace
Multiple hearth furnace
SCC CODE Ell I SSI ON FACTOR
315012 0.2 Ib/ton finished
product
315012 0.7 Ib/ton finished
product
315012 0.9 Ib/ton finished
product
315012 0.2 Ib/ton finished
product
315012 0.7 Ib/ton finished
product
315012 0.4 Ib/ton finished
product
315012 0.7 Ib/ton finished
product
315012 3.7 Ib/ton finished
product
315012 1.8 Ib/ton finished
product
315012 l.t Ib/ton finished
product
30501204 0,011 Kg/Hg finished
product
30501205 O.IS tg/ng finished
product
30501204 1,54 kg/Kg finished
product
303001 0.291 Ib/ton Al produced
303001 0.21 Ib/ton Al produced
S0100504 <3.8 x IOE-S Ib/ton
sludge
50100504 0.0491 Ib/ton dry sludge
NOTES
Controlled with a venturi scrubber
Controlled with a venturi scrubber
Controlled with a wet scrubber
Controlled with a wet scrubber
Controlled with a wet scrubber
Controlled with a HVAF
Controlled with a Incinerator
Controlled with a wet ESP
Controlled with a wet ESP
Controlled with a wet UP
slietf facilities
Uncontrolled, overate emission factor for 4 different
el led facilities
Uncontrolled, overage Mission factor for 4 different
si led facilities
Single test report, one plant, controlled, baghouse
Single test report, on* giant, controlled, baghouse.
oat or lei that escaped prloary control systee
On* test, scrubber
On* test, scrubber
REFERENCE
173
173
173
173
173
173
173
173
173
173
173
173
173
91
91
101
101
-------
P«9« No. 241
09/21/90
POLLUTANT
Ph.nol
Phtnol
Ph«nol t
2-Ph*nvl-l-prop»nol
2-Ph*nyl-l-prop..rtol
Pho«9*n«
Pho*««nc
Pho*««n«
Phoatflww
"— ~
Pho*t«n«
Ptio»««n«
""—
Phoseene
Ptioseena
Phoaetna
Pho*«ene
CAS
NUniER
108952
108*52
1 I 23859
1123859
75445
75445
75445
75445
75445
75445
75445
75445
75445
75445
75445
75445
7S44S
SIC
CODE
4953
7*9,
28*5
28*5
2821
2821
2821
28*5
28*5
28*5
28*5
28*5
28«9
28*9
28*9
2-9
28*9
INDUSTRIAL PROCESS
Uasteuater treataent
Tank truck cleanlns
Wood co.bu.tlon,
residential
Acetone/phenol
oanufacture froe cueane
Acetone/phenol
eanuf acture froa cusene
Polycarbonate production
Polycarbonate production
Polycarbonate production
Itathylene
dl -pora-phanyl one
Isocyanate (MOD
production
Toluene dllsocyanats
production
Toluene dllsocyanat*
production
Toluene dllsocyanats
production
Toluene dtlsocvanate
production
Phoseene production
Phosaene production
Phoseene production
Phoseene production
Phoseene/dl 1 socyanate
EMISSION SOURCE
POTU
Entire process
Uoodstove or fireplace
Clsavas* section vents
(coatalned)
CuMne peroKidatton vent
Fuettlvo ealssions
Process upsets
Process vents
Process - eeneral
Fueitive Missions
Process - eeneral
Process upsets
Process vents
Fugitive eeissions
Fugitive eeissions
Process upsets
Process vents
Futitlve Mission*
SCC CODE EltlSSlON FACTOR
50100701 l.S Ib/ton phenol In
influent
4*004 0.012 Ib/truck cleaned
2,0 Ifa/ton wood burned
30120211 *.B x 10E-* Ib/ton phenol
30120202 0,0018 Ib/ton phenol
301018 0.011* Ib/ton phosoene
produced
301018 0.000* Ib/ton phossene
301018 0.0132 Ib/ton phossene
produced
101 0.0112 Ib/ton produced
30118180 0.02*4 Ib/ton Phoseene
produced
30118101 O.OI2 Ib/ton produced
10111101 0.00025 Ib/ton Phoseene
produced
10118101 O.OOIS Ib/ton phoesene
produced
0.0** Ib/ton produced
101 0.1* Ib/ton produced
0.0005 Ib/ton pneseene
produced
0.001 Ib/ton produced
301 O.OSf Ib/hr aeeratlen
NOTES
Based an Ml*, aodellno for hypoth. POTU. represents
averaoe POTU that treats Industrial usteuater
Eoission Masuraaent
Uncontrolled
Controlled (unspecified) . based on test data, 1977
data, averave factors
Controlled (not specified), based on •upline. 1977
data, average factors
Hypothetical site, upper end of ranee, loner value le
0.0001 Ib/ton Phoseene produced
Hypothe. site, value for polycarb. alone, add to value
for phos. to eet totel for phos.-polyc. plant
Derived fro* Itate air Mission files
Hypothetical site, upper end of ranee, lauer value Is
0.000* Ib/ton
Derived froe State air Mission files
Hypothetical sit*, velue for TDI produc.. add value for
Phoseene to eet total phosoone-TD! Plant
Hypothetical all*, upper and of ranee, lower value Is
0.0012 Ib/ton
Based on data froe Ma alte
Hypothetical site. Incinerator and scrubber control.
include* storte* tank*
•asetf an •eeeuraiMnta at a chMica! plant
REFERENCE
59
97
94
125
125
121
121
121
II
121
II
121
121
121
1]
121
121
14
-------
P««e No. 242
09/21/90
POLLUTANT
Phosgene
Phosgene
Phosgene
Phosphorus (yellow or
white)
Phosphorus (yellow or
white)
Phosphorus (yellow or
white)
Phosphorus (yellow or
white)
Phosphorus (yellow or
white)
Phosphorus (yellow or
white)
Phosphorus (yellow or
white)
Phosphorus (yellow or
white)
CAS SIC
NUtllER CODE INDUSTRIAL PROCESS
75445 2879 Herbicide production
75445 2879 Herbicide production
75445 2879 Herbicide production
7723140 Uood coebustlon.
residential
7723140 22* Uoven fabric finishing
7723140 22* Uoven fabric finishing
7723140 22* Uoven fabric finishing
7723140 22* Uoven fabric finishing
7723140 25 Uood coebustlon,
industrial
7723140 25 Uood coebustlon.
Industrial
7723140 25 Uood coabustlon.
Industrial
EtllSSION SOURCE
Fugitive eeisslons
Process upsets
Process vents
Uoodstove without baffle
Curing oven - resin
finish
Heat setting
Tenter fraees - resin
finishing
Theraosol dyeing
Horizontal return tube
lalanced draft wlckes
stoker-fired Industrial
boiler
lalanced draft wtckas
stoker-fired Industrial
SCC CODE EMISSION FACTOR
0.012 Ib/ton phosgene
produced
0.000* Ib/ton phosgene
produced
0.0132 Ib/ton phosgene
produced
1.4 x 10E-4 Ib/ton wood
330001 7.1 x 10E-4 Ib/ton fabric
330001 1.9 x 10C-4 Ib/ton fabric
330001 I.* x 10E-3 Ib/ton fabric
330001 3.4 x 10E-4 Ib/ton fabric
1020090* >1**.9 lb/IOE12 Itu heat
Input
1020090* «.007 Ib/ton fuel or
>4«,380 Ib/lOElZ Itu
1020090* >0.00«2 Ib/ton fuel or
>533.4 Ib/IOCIJ Itu
NOTES
3 x 10-4 Ib/ton
Hypothe. plant, value Is for herblc. alone, add to
phos. value to get value for phos.-herbtc. plant
Uncontrolled, based on on* study, nonbaffled stove
burning green pine
Uncontrolled, average of three tests
Uncontrolled, based on test data
Uncontrolled, average of four tests
Uncontrolled, average of two test*
Saeele results. 1 plant, wood flowrate • .514 kg/s,
boiler has 3-»ass design H/41va»h reinjectlon.
uncontrolled
Dry wood, one plant, partlculate control u/eechanlcal
collector (cyclone), wood feed rate 0.29 kg/*, boll.
off. Sl.n
treen wood, one plant, partlculate control w/eechanlcal
collector (cyclone), wood feed rate 0.54 kg/s. boll.
REFERENCE
121
121
121
58
52
52
52
52
17*
177
177
Phthallc anhydride
Phthallc anhydride
Pnthallc anhydride
Phthallc anhydride
15449
boiler
28*5 Phthallc anhydride Flaker/bagger
production - naphthalene
process
28*5 Phthallc anhydride Flakw/baggor
production - naphthalene
process
28*5 Phthallc anhydride neln process Incinerator
production - naphthalene
process
21*5 Phtnalle anhydride Kaln process Incinerator
production - naphthalene
process
301019 0.20 Ib/ton PA produced Uncontrolled, test data and engineering Judgeeent
10101* 0.002 Ib/ton PA produced Controlled, test data and engineering Judgeeent
301019 40.1 Ib/ton PA produced Uncontrolled, test data and engineering Judgement
301019 1.42 Ib/ton PA produced Controlled, test data and engineering Juogeeent
-------
P.«. No. 241
09/21/90
POLLUTANT
Phth.llc .nhydrlde
Phth.llc anhydride
Phth.llc .nhydrlde
Phth.llc .nhydrlde
Phth.llc .nhydrlde
Phth.llc anhydride
Phth.lic .nhydrlde
Phth.llc anhydride
Phthalic anhydride
Phthalic anhydride
Phthalic anhydride
Phthalic anhydride
Phthalic anhydride
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
B5449 28*5 Phthalic anhydride
production • naphthalene
proceee
85449 lets Phth.llc «nhydrtd«
production * n.phth.l.n.
proceaa
BS449 2B«S Phth.llc .nhydrldt
production • n.phth.lene
proceee
BS449 28*5 Phth.llc enhydrld.
production - n.phth.lene
proceee
BS449 28*5 Phth.llc .nhydrld.
production - n.phth.lene
procete
85449 28*5 Phth.llc .nhydrlde
production - n.phth.lene
proceae
BS449 26*5 Phthalic anhydride
production - xylane
proceae
•5449 2I»S Phthalic anhydride
production - xylane
proceee
BS449 2MS Phthalic anhydride
production - xylane
proceee
•5449 28*5 Phthalic anhydride
production - xyl«ne
proceee
SS449 28*5 Phthallc anhydride
production - xylane
proceee
•5449 2M5 Phthalic anhydride
production - xyltne
proceee
•5449 2MS Phthalic anhydride
production - xylene
proceee
EHISSION SOURCE SCC CODE EMISSION FACTOR NOTES
Secondary incinerator 301019 19.* Ib/ton PA produced Uncontrolled, teet data and enelneerlne Judveeent
S.cond.ry Incinerator 301019 0.2 Ib/ton PA produced Controlled (not ep.clfled), teet d.t.
-------
Page No. 244
09/21/90
CAS
NUHBER
CODE INDUSTRIAL PROCESS
En I ssi ON SOURCE
SCC CODE EMISSION FACTOR
Phthalic anhydride 85449 2B*5 Phthalic anhydride
production - xylene
process
Storaee tank Missions 407004 0.51 Ib/ton PA produced Uncontrolled, based on test data and enelnoerlne 12O
Jud
Pnthallc anhydride
85449 2865 Phthalic anhydride
production * xyl.n.
process
Transport loading 301019 0.90 Ib/ton PA produced Uncontrolled, ba.ed on test d.ta and anolnoerlne
Phthalic anhydride
B5449 2845 Phthalic anhydride
production • xylene
process
Polychlorln.t.d blph.nyl. 133*3*3
(PCI.)
Polychlorln.t.d blph.nyl. 133*3*3
(PCI.)
Polychlorln.t.d blph.nyl. 133*3*3
(PCI.)
Polychlorlnated biph.nyl. 133*3*3
Polychlorlnated blph.nyl. 133*3*3
Polychlorlnated blph.nyl. 133*3*3
(PCI.)
Polychlorlnated blph.nyl. 133*3*3
(PCI.)
Polychlorlnated blphenyls 133*3*3
(PCI.)
U..t. all coebustlon
4953 Municipal Haste
coebustlon
4953 Municipal Haste
coebustlon
4953 nunlcip.l naste
coebustlon
4953 Municipal Haste
coebustion
4953 Municipal Haste
coebustlon
4953 Municipal Haste
coobustlon
4953 Municipal Haste
coeoustlon
Polychlorlnated blphenyls 133*3*3 4953 Municipal Haste
(PCIs) coebustlon
Polychlorlnated blphenyls 133*3*3 4953 Municipal Haste
(PCI.) eoebustlon
Polychlorlnated blphenyls 133*3*3 4953 nunlcip.l Haste
(PCIs) coeoustlon
Polychlorlnated biehenvl* 133*3*3 4953 Municipal Haste
(PCIs) eoebustlen
Transport loadlne 301019 O.01 Ib/ton PA produced Controlled, test data and enelneertne Judeeeent
0.0083 lb/1000 S.I oil Uncontrolled, based on emissions data and enelnoerlne
burned judoeeent, aesuees 971 ORE
Masts oll-flred boilers 1
«150 ellllon Itu/h) or
space heaters
Exl.tlns .... burn heat 501001
recovery facility
Exl.tlns eass burn heat 501001
recovery facility
Mass burn, nonheat 501001
recovery facility
Mass burn, nonheat 501001
recovery facility
Modular fuel facility 501001
nodular inclnwator
Projected or
state-of-the-art eas
burn heat recovery
facility
Projected or
state-of-the-art eas
burn heat recovery
facility
Refuse derived fuel
Incinerator
Refuse derived fuel
Incinerator
Refuse derived fuel
Incinerator
4.2 x IOE-* Ib/ton of
Haste coebusted
2 x 10E-7 Ib/ton of Haste
coebusted
4.2 x 10E-* Ib/ton of
Haste coebusted
2 x IOE-7 Ib/ton of Haste
coebusted
1.0 x 10-* Ib/ton of
Haste coebusted
501001 * * IOE-7 Ib/ton of Haste
coebusted
Control l.d by ESP, band on .ourco t«t data
Controlled by dry alkaline scrubber • fabric fllte
•MUMS 951 control efficiency
Controlled by ESP, bated on eource t..t data
Controlled by dry alkaline scrubber t fabric fllte
assuees t5i control efficiency
Central led by ESP, ba.ed on eource te.t data
Controlled by dry alkaline ecrubber I fabric filter.
aesuoe* tSS control efficiency
501001 4.2 x IOE-7 Ib/ton of Controlled by ESP. based on source test data
501001 2 x IOE-1 Ib/ton of naste Controlled by dry alkaline ecrubber t fabric filter.
coebusted aeeueee 951 control efficiency
501001 0.0021 Ib/ton of Haste
coebusted
501001 I.I x 10E-4 Ib/ton of
Haste coebusted
MlOOl 2.* x IOE-* Ib/ton RDF
coebusted
Contralled by ESP. bated on eevce te.t date
Controlled by dry alkaline ecrubber e fabric filter.
aesuee* 951 centre! efficiency
ton RDF fuel only. ESP control only, one date point
only
III
III
III
III
III
III
-------
P««« Wo. 245
09/21/90
CAS
POLLUTANT NUMBER
Polychlorlnated biphenyls 133*3*3
>)
Polychlorlnated biphenyls 133*3*3
(PCI.)
Polychlorlnated biphenyls 133*3*3
Polychlortneted biphenyls 133*3*3
Polychlorlnated biphenyls 133*3*3
(PCI.)
Polychlorlnated biphenyls 133*3*3
Polychlorlnated
dlbenzofurans. total
Polychlorlnated
dlbenzofurans, total
Polychlorlnated
dlbenzofurans, total
Polychlorlnated
dibenzofurans, total
Polychlorlnated
dibenzofurans. total
Polychlorlnated
dibenzofurane, total
Polychlorlnated
dlbenzofurans. total
Polychlorlnated
dlbenzofurans. total
Polychlorlnated
dlfcenzofuraxs. total
SIC
CODE INDUSTRIAL PROCESS
4*53 Municipal vast*
coabustlon
4953 Municipal vasts
coebustion
4953 Municipal vasts
coebustlon
4*53 Municipal vaste
coebustlon
4*53 Municipal vasts
coebustlon
4*53 Sevage sludge
Incineration
4953 Sevage sludge
Incineration
3241 Ceesnt kilns coflrlng
vaste
3274 Llee kilns coflrlng
yastes
3274 Lies kiln* coflrlng
4* Coal and refuse-derived
fuel coebustlon
4* Hazardous vaste
Incineration
4* Hazardous vaste
Incineration
4* Hazardous vasts
incineration
4* Haste coabustlon -
Industrial
4* Haste coebustlon -
Industrial boilers
EMISSION SOURCE
Modular starved-air
coebustor
Large eass burn rotary
vatervall coebu.tor built
after 1980
Large eass burn rotary
vatoruall coabustor built
after 1980
Mass burn vatervatl
coebustor, seall size nev
eodel to any age eedlue
Mass burn vatervall
coebustor, built bsfore
!*«0
Fluldlzed-bed furnace
Multiple hearth furnace
Stack - flue gas
LlM kiln
LIM kiln - stack
Flue ges
•otto, ash
Rotary kiln - flue gas
Rotary kltn - flue gas
Stack - fly ask
Floe gas
SCC CODE EMISSION FACTOR
501001 5.0 x 10E-* Ib/ton feed
501001 2.* x IOE-S Ib/ton feed
501001 2.* x 10E-5 Ib/ton feed
501001 3.1 x 10E-5 Ib/ton feed
501001 5.4 x IOE-* Ib/ton feed
5010050* 5.5 n*/e3
NOTES
Uncontrolled, overall average of ssveral source
averages, range Is S.O x 106-7 - 1.14 x 10E-5 Ib/ton
Capacity > *OO tons/day, ESP control only, ons data
point only, detection Halt reported
Capacity > *00 tons/day, uncontrolled, one data point
only, detection Halt reported
Capacity < «OO tons/day, ESP control only, overall
average of several source averages, range 1* 1.7* x
10E-5 - *.l x 1OE-5 Ib/ton
ESP control only, overall average of several source
averages, range Is 4.2 x 10E-7 • 1.0 x IOt-5 Ib/ton
One test, scrubber, ranee over seven different PCI
One test, scrubber, renge over seven different PCR
3 loc.. lleuld vaste fuel contain, chlor. coo*..
detect. Melts range l.«-4.» n*/e3 or 1 ng/ul InJ.
1 location, baghouse dust staple, fire petrol, coke «
yeste orsanlcs. detec. tie
-------
P«ge No. 246
0«/21/»0
POLLUTANT
Polychlorlnatod
dlbenzof urans. total
Polychlorinated
dlbenzofurans. tot«l
Polychlorinated
dlbenzofurans. total
Polychlorinated
dlbenzofurans. total
Polychlorinated
dlbenzofurane. total
Polyehlorlnated
dlbonzof urans. total
Polvchlorlnatod
dtbenzofurans. total
Polychlorlnated
dlbenzofurane. total
Polvchlorlnated
dlbenzofurans. total
Polychlorlnetod
tfltaenzofurant. total
Polvchlorlnated
dlbeflzofurans. total
Polvehlorlnated
dlbenzofurane, total
Polychlorinated
dlbenzofurans. total
Polychlorlnatad
dibenzofurans. total
Polvchlortnated
dlbonzofurans. total
Polychlorlnated
dlbenzofurant, total
CAS SIC
NUMBER CODE
4*
4*
4»
4»
4*11
4*11
4*5
4*5
4»S
4*5
4*53
4*33
4»SJ
4»SJ
•0*
•04
INDUSTRIAL PROCESS
Waste combustion -
Industrial boilers
cofirini wastes
llaste oil combustion •
coflre PO-splked vaste
oil/No. « oil
Uastauater treatment -
oroanlcs rvnoval by
activated carbon
Vaitwatv troatnnt -
organic* r«»oval by
activated carbon
Coal coibuitlon, utility
Coal co-butt ion. utility
S«ua9« sludto
Incineration
Mood coabuatlon
Hood co*butlon
Municipal vaita
coMwstlon
Municipal »a«t«
coBbuttlon
Hoapttal «««ta
Incineration
HMOttat «Mt«
Incineration
EMISSION SOURCE
Fly a»h
Flue gat Iron coH«erclal
boiler
Regeneration of activated
carbon uflno fluldlzed
bed tyttee • aftrburn
Regeneration of activated
carbon utlne fluSdlzed
bad systea * recuper.
Coal-fired boiler, flue
fa*
Coal-fired boiler, fly
«th
Multiple hearth - flue
ea*
Fluldlzed bed eyiteia.
PCP-treated iwod
Incinerator. PCP-treated
KOOd
Incinerator. PCP-treated
vood
ESP catch - fly aeh
afh
(tack - fly «h
(tact - fly **h
Flue; «a*
rim ««
SCC CODE EMISSION FACTOR
102 * X 10E-4 Ib/ton
101 Not detectable
0.1* - 0.3* ne/«3
0.015 - 4.7* no/>3
101 Not detectable
101 Not detectable
S SOI - 2218 ne/e3
S 4.12 « IOE-4 Ib/ton
•
S02 0.223 - 0.7142 Ib/ton
feed
t 517 ne/.J
S Not detectable - 4.072 x
IOE-3 Ib/ton
S 440. 1 • 1212 n*/*3
S 1322 no/»I
f 1.7 x IOE-4 Ib/ton
S0200SOS 29 - 1*7 «•/•!
SOM050S » ne/e3
NOTES
One location, controls unknown
tlaate oil • 101 total feed, one location, detection
ll.lt > 0.011 - 0.10 ue/e3
With afterbur., poetehtcrln. of uaeteuater relative to
activated carbon bed, detec.ll'lt 0.00* ne/e3
Ulth afterbv., poetchlorln. of •aetevater relative to
activated carbon bed. detK.ll.lt 0.00* ne/.3
Four location*. S-day coevo*ltee. detection lleltl vary
fro* 2 x 10E-7 - 1.4 x 10E-* Ib/ton
Four location*. S-day coo»o. detection llelt* vary
fro* 2 x 10 E-7 - 1.4 « IOE-4 Ib/ton
Controlled vlth a Hater scrubber, total of three
sane lee
Fly ash eaevl*
•••ad on *t tot-seal* incineration, stack and senk* eas
saeples cooblned, n • f
Flue *as sasple
Aper. *0 sites tested, hoevloeue data elven In refer..
IIOMK- data «v be avail, fro* indlv. refer.
Four sites tested, hoeoloeue data *lven In refer..
isae«r date My be avail, fro* Indlv. references
One site tested, hosnloeue data liven In refer., Isoeer
data «ay be avail, fro* Indlv. references
One sit*, tested, hoeolovue data liven In refer., lioeer
data My be avail, fro* indlv. references
•••ad en testlns at four locations In the U.S. and
Canada
Flue eas taeel*. « • 3
REFEREI
11*
11*
11*
11*
II*
II*
11*
11*
11*
11*
11*
1U
ll«
11*
11*
It*
-------
Page No. 247
0«/21/»0
POLLUTANT
CAS
NUMBER
Polychlorlnated
dtbenzofurans. total
Polychlorlnated
dlbenzo-p-dloxlns, total
Polychlorlnated
di benzo-p-di oxlns.
Polychlorlnated
dl benzo-p-di oxi ns ,
Polychlorlnated
di benzo-p-di oxlns.
Polychlorlnated
dlbenzo-p-dloxlns.
Polychlorlnated
dl benzo-p-dl oxi ns .
Polychlorinated
di benzo-p-dl oxlns,
Polvchlorlnated
di benzo-p-dl oxlns.
Polychlorlnated
di benzo-p-dl oxins.
Polychlortneted
diben zo-p-dl oxins.
•olychlorlnated
dibenzo-p-di oxins.
Polychlorlnated
diben zo-p-dl oxins.
Polychlorlnatad
di benzo-p-dl oxlns.
Polychlorlneted
dl benzo-p-dl oxlns.
Polychlorlnated
di benzo-p-dl oxlns.
Polychlorlnated
dlbenzo-p-dloxlns.
total
total
total
total
total
total
total
total
total
total
total
total
total
total
total
SIC
CODE
eo»
3241
3274
3274
4»
4*
4*
4»
4*
4»
4*
4*
4*
4*
INDUSTRIAL PROCESS
Hospital waste
Incineration
Internal coabustlon
engine* - eoblle
Internal eoabustlon
engine* - eoblle
Internal coebu*tlon
engine* - eobile
Ceeent kiln* coflrlng
waste
Llee kilns coflring
wastes
Llee kilns coflrlni
Coal and refuse-derived
fuel coebustion
Hazardous waste
incineration
Hazardous waste
incineration
Hazardous waste
incineration
Hazardous waste
Incineration
Hazardous waste
Incineration
Hazardous waste
Incineration
Hazardous waste
incineration
Oil and coal coebustlon
Uastd coebustlon -
Industrial
EMISSION SOURCE SCC CODE EMISSION FACTOR
Incinerator 50200505 11.71 x tOE-i Ib/ton feed
Automobile emissions B x 10E-» Ib/ton
Automobile eeissions 2 x 10E-I - l.« x 10E-7
Ib/ton
Diesel truck eeissions 7.1 x 10E-7 - 1 x 10C-7
Ib/ton
Stack - flue tas 305004 Hot detectable
Llee kiln 30501s Not detectable
tin kiln - «tack 3050 U Not detectable
Flue gas 1 Not detectable
lottoe ash 50300501 0.0010B Ib/ton
Rotary kiln - flue gas 50100501 Not detectable - 45.5
ng/e3
Rotary Hlrt - five (as 50300501 1.45 x IOE-10 Ib/traln
Rotary kiln - partlculate 50100501 0.01*42 - l.»*5 Ib/ton
Rotary kiln - partlculate 50300501 2.* x IOS-S - 0.00212s
Ib/ton
Stect - fly ash 50100501 J.S x 10C-S - 0.227
ID/ton
Tar burner - parttculate 50300501 5.12 x IOC-4 - 1.144 x
IOt-3 Ib/ton
Stack - partlculate 102 1.34 x 10E-4 Ib/ton
Stack - fly ash 503 0.00142 Ib/ton
NOTES
Uncontrolled, test data
gas. tetra, hexa. hepta. octa howologues only
2 saeples scraped frow euffler. used unlead gas w/
catalytic converter, tetra/hexa/hepta/octa homol.
Saeples of scrapings froe 2 eufflers. dlesel fuel used
3 lac., lUutd waste fuel contain, chlor. cow*.,
detect. Halts range l.e-4.» ng/e3 or 1 ng/ul InJ.
I location, baghouso dust saeple, fire petrol, coke «
waste organic*, detec. lie (l-SO)xlOE-l Ib/ton
One location, stack part, saeple, fire petrol, coke «
waste organise, detec. Ilelt 0.034-2.0 ng/ej
One location, detection Halt • 0.25 ns/a-J
Use of afterburner, fuel • transformer ell w/ PC»s <
incul. fro* eluaj. s> copper wirings. 1 saemle
Two locations)
Fenta. neeta. octa COO only
One location, n • 3. both solid t lleuld waste, no
supplementary fuel used
1 location. n«4, both solid > lleuld waste, use of
suppl. fuel, hepte. hexa, octa hoeologues only
1 sites tested, homologue data given In refer.. tsomer
data eay be avail, frosi Indlv. references
One location, n • 4. Use netural gas as suppl. fuel.
hexa. hepte. octe heewloeues only
No eenta hoeolotuo Included, one location. TCDD
detection • 4 x lof-S Ib/ton
One elte tested, hoanloeue deta given In refer. . Isoeer
data eay be avail, froe Indlv. references
REFERENCE
1*7
11*
11*
11,
II*
11*
11*
II*
11*
11*
II*
II*
II*
II*
11*
11*
11*
-------
Paoe No. 249
09/21/90
POLLUTANT
Polvchlorlnated
dlbenzo-p-dloxln*.
Polychlorlnated
Polychlorlnated
Polychlorlnated
dlben*o-p-dloxln*.
Polychlorlnated
dlbenzo-p-dloxln*.
Polychlorlnated
dlb*nzo-p-dioxln«p
Polychlorlnatad
dlbenzo-p-dloxln*.
Polvchlorlnated
dlbenzo-p-dloxln*.
Polychlorlnated
dlbenzo-p-dloxln*.
Polychlorlnatad
dlbenzo-p-dloxln*.
Polychlorlnated
dlbenzo-p-dloxln*.
Polychlorlnated
dlbenzo-p-dloxln*.
Polychlorlnated
dlbenzo-p-dloxln*.
Polychlorlnated
dlbenzo-p-dloxln*.
Polychlorlnated
di benzo-p-dl oxi n* .
CAS
NUMBER
total
tot«l
total
total
total
total
total
total
total
total
total
total
total
SIC
CODE
4*
49
4»
49
49
4911
4911
495
49S
49S
49S
4953
49SJ
49SJ
INDUSTRIAL PROCESS
Ma*te co«bu*tlon -
Industrial boiler*
coflrlnf ya*ta>
Ua»te coofauvtlon -
cofirlnf Matte*
Ha*t* oil coebu*tton -
Oil/No. f oil
orfanlc* rwoval by
activated carbon
Ifaiteuatar troatawnt -
orfanlc* reeoval by
activated carbon
Ua*t*vater treatment -
orfanlc* removal by
activated carbon
Coal coebuition. utility
Coal coibuatlon. utility
Sa)va«« vludfo
inclnaratlon
Wood coa*u«tlon
Uood coibuatlon
Uood cootuition
imnlclpal «««t«
coibuttlon
nunlclpal y««ta
CfMJbuitlon
nunlclpal M fabric filter contr.. aouaxt* 951
REFERENCE
11*
119
11*
II*
II*
11*
11*
It*
11*
II*
11*
II*
IU
III
HI
-------
P.ae No. 249
0»/2I/»0
POLLUTANT
Polychlorlnatad
dlbenzo-p-dloxlnt.
Polychlorlnated
dlbenzo-p-dioxlnt.
Polychlorlnated
dl benzo-p-dloxl nt ,
Pol ychlorl Rated
di btnzo-p-dl oxl nt .
Polychlorlnated
di benzo-p-dioxl nt ,
Folychiorlnated
dl benzo-p-dl oxl nt ,
Polychlorinated
dlbtnzo-p-dtoxint.
Polychlerlneted
dlben*o-p-dloxlna.
Polychlorlnated
dlben>o-p-dloxint.
Polychlorl/ieted
dlbenzo-p-dloxlne.
Polychlarlnated
dfbenao-p-dloxine.
Polychlorlnated
dlbenze-e-dtoxlne.
PolycMorln.ted
dlbenxo-p-dioxin».
Polycnlorlneted
dibenzo-p-dloxlno.
PelyehlevliMted
dibenxo-p-dloxin».
CHS
NUMBER
total
total
total
tot.l
total
tot.l
total
tot.l
tot.l
tot.l
tot.l
tot.l
tot.l
tot.l
tot.l
SIC
CODE
4»53
4«3
4«53
4»5J
4»S3
4»SJ
4»SJ
4»SJ
4»SS
4»S3
4»53
4tS3
4W3
SO*
t04
INDUSTRIAL PROCESS
Municipal H«*t«
co«bu«tion
nuniclpal w«st<
co«bu>tlon
fluniclpal w«tc
eovbuvtion
flunlclpal H«*t«
eo0bu«tlon
nunlclpal u.*t«
covbustion
llunlclpal n»t«
CMbUBtion
flunlclpal w«»ta
eo«fau>tion
Municipal Mavta
cori>u«tlon
Hufitclpal »««t«
covbustion
nunlctpal «u«t«
covbustlofl
Hunlclp*! «.«t«
coBbuation
Municipal ».«t«
co>bue-derlvetf fuel
facility
(tact - »ly ««h
•tact - fly a«h
flue va*
flue va«
SCC CODE EMISSION FACTOR
501001 4 x 10E-« Ib/ton of a.sta
coebuftid
501001 2 x 10E-7 Ib/ton of uaite
coebuited
5 45.4 - »0« ne/e3
501001 4.2 x IOE-* Ib/ton of
waate co«bust«d
501001 4 x IOE-7 Ib/ton of ua»te
coebuited
501001 1.31 x IOE-7 Ib/ton of
uaete coebueced
501001 1 x 10E-« Ib/ton of u.«t«
coebuvted
501001 1.14 x IOE-7 Ib/ton of
Maate coebueted
501001 I x 10E-* Ib/ton of uaate
co.bo.ttd
$01001 2.4 x 10€-» Ib/ton of
>a>te CMbusted
501001 1.* x 10-7 Ib/ton of
waate coebuated
5 IS40 n«/«3
f 4.4 x IOC-4 Ik/ton
S0200S05 II - 14 n»/«3
50ZOOS05 If n«/«3
NOTES REFERENCE
Controlled by ESP, baled on tource t«.t«. eiiielone • 111
2,3,7,1-TCDO equivalent
Dry elk. ecrubber t fabric filter contr., aaeueea *5I 111
contr. efflc,, ••!«. • 2.3.7.B-TCDD enulv.
Four sltee t«»ted, hoeoloaue data vlven in refer., 114
l»o»er data «ay be avail. fro« Indiv. reference*
Controlled by ESP, baaed on tource te«t«. eelaelone • III
2.3,7,1-TCDD eeulvalent
Dry Ilk. (crubber e fabric filter contr., a«WM> •» 111
Controlled by ESP. bated on tource teata, eel.tlont • 111
Z,>,7,I-TCOO eeulvalent
Dry elk. urubber «. fabric filter contr., attune *51 11*
Controlled by ESP, bated on tource te«tt, eeileelone • III
2.3.7.1-TCDO eeulvalent
Dry alt. (crubber « fabric filter contr.. eMueei *5I 111
contr. efflc.. eelt. • 2.3.7.1-TCOD owlv.
Controlled by ISP, bated en tource tettt. eelaalont > III
I.3,7.f-TCBO eeulvalent
Dry elk. tcrubber t fabric filter contr., attuMt *5I III
contr. efflc., e*la. • 1.I.7.I-TCDD emlv.
One <le, n • 1 lit
s
5
-------
Page No. 250
0»/21/»0
CAS SIC
DUMBER CODE INDUSTRIAL PROCESS
EHISSIDN SOURCE
SCC CODE EMISSION FACTOR
Polychlorinated
dlbenxo-p-dloxlns, total
Polycyclic organic Matter
Polycyclic organic Matter
BOt Hotel til naiti
Incineration
Chain say exhausts
Chain say exhausts
Chain say
Chain say
50200505 S.30 « 10E-S Ib/ton feed Uncontrolled, test data
neasured during laboratory tests
Average of range of valuea Measured In field use (19-42
ug/>3)
114
114
Polvcvclic organic Matter
Coal coebustion
Anthracite coat -fired
hand-stoked boiler,
rclal /residential
10300103 57.3 tb/10E12 Itu heat Represente both gaseous and partlculate POn
innut
Polycyclic organic eattar
Polycyclic organic Matter
Coal coebustion
Coal coebustion
Anthracite coal-fired
•agazlne feed boiler*
rcl al /resident! at
Anthracite coal -fired
underfeed stoker.
rcl al /real dentl al
103001 ».7S lb/tonlOE12 Itu heat Saee ref. lists 21.3 pg/J for saee boiler/coal type.
Input represent* both gaseous and partlculate POM
10300102 22.2* Ib/10E12 Itu heat Saue ref. also lists «l.4 pg/J for sea* boiler/coal
input type, represents both gaseous a partlculate POrt
Polycyclic organic Matter
Polycyclic organic aatter
Polvcycllc organic eatter
Coal coebustion
Coal coobustlon
Coal coebustion
•ItuMlnou* coal-fired
hand stoked boiler.
conerclal/Industrial
lltuMlnous coal-fired
Magazine feed.
coMMerclal/resident!al
lltueineus coal-fired
underfeed stoker,
irclal/realdentlal
10300214 4,173 Ib/lOEU ttu heat Represent* both gaseous and partlculate PON
input
103002 2,»32 lb/IOE12 ttu heat Sa«a ref. also lists 352* pg/J for saee boiler/coal
input type, represent* bath gaseous a (articulate POn
1030020* 3*4.2 lb/IOE12 Itu heat iaee ref. alea list* IS01 pg/J for saee boiler/coal
input type, both represent perticulat* ft gaseous POtl
Polycyclic organic aatter
Coal coebustion
litullnoui coal -fired
underfeed etoker.
rclal/reildentlal
10300201 4,042 lb/IOCI2 Itu heat Represents both gaseous and partlculate port
input
Polycyclic organic eatter
Polycyclic organic Matter
Coal coatHiitlon
Coal coebustion
High-volatile bltuelnous
coal-fired underfeed
stoker, coMMorc/resldent
Processed lignite char
underfeed stoker.
«-clal/residential
10300101 S,«4* lb/lOEI2 Itu heat Average of * values ranging froe 3«3-S7*7 pg/J,
input represents both gaseous and partlculate Port
10300307 373.3 Ib/lOElJ Itu heat Represents bath gaseous and partlculate POM
input
Polycyclie organic Matter
Polycyclic organic Matter
Coal coobu«tlon
Coal coebustlcn.
Indue trial
Subbltiwlnou* coal -fired
underfeed stefcer.
rcl al /resldentl al
10300224 1,15* lb/IOC12 ttu heat Average of ( value* ranging fro* *07-«2J pg/J,
Input represent* both gaseous and partlculate POrt
lltuelnous coal -fired
pulverlied dry botloe,
Mater tube 'boll era
10200202 2.7t Ik/IOf 12 Itu
nultlcyclanes. represents primarily partlculate POH
-------
Pa«e No. 251
09/21/90
CAS
POLLUTANT NUflBER
Polycycllc organic Matter
Polycvcltc organic Matter
Polycycllc organic Matter
Polvcyclle organic Matter
Polvcycllc organic natter
Polycycllc organic natter
Polycyclic organic Matter
Polycycllc organic natter
Polycyclic organic Matter
Polycycllc organic Matter
Polycycltc organic natter
Polycycltc organic aattcr
Polycycllc organic Matter
Polycycltc organic Matter
Polycycllc organic utter
SIC
CODE INDUSTRIAL PROCESS
Coal combustion.
Industrial
industrial
Coal co»buBtion.
Industrial
Coal coebustlon,
Industrial
Coal combustion.
Industrial
Coal combustion.
Industrial
Natural gas co*bustion
Natural gas coebustl on
Natural gas coMbustlon
Natural gas combustion
Natural gas eoMbustion
Oil coMbustlon
Oil coobustion
Oil coebustlon
Oil coMbustlon
Oil coMbustlon.
coMMMrcial
EMISSION SOURCE
lituelnou* co«i-«ir«d
pulvwizad wt potto*
bollars
Dry botto*.
horllontally-«lr«d,
pulverized bituefnous
coal
Hass-flred overfeed
stoker. bltuMlnous coal
Spreader stoker
Underfeed stoker
Uatertube. putverlied
bltuelnous coal
Double shell boilers,
ho«e heating
Firetube boiler, process
heater
Hot air furnace, hoee
heating
Scotch Marine, hospital
heating
Hall space hetter, tioee
heating
Cast Iron sectional
boilers, distillate oil
Distillate natertiibe
boilers
Hot air furnace.
distillate Ml
Scotch earlne boiler*.
distillate ell
Scotch Marine boiler*.
residual oil
SCC CODE EMISSION FACTOR
10200201 «.49 lb/lOE12 Itu
10200205 32.*2 Ib/lOf 12 Itu
10200204 3.014 lb/IOE12 Itu
1020020* 194.4 !b/IOE12 Itu
10200202 47.94 Ib/10EI2 Itu
1.113 lb/10C12 Itu heat
Input
10200401 0.449 lb/10EI2 Itu heat
Input
0.745 lb/IOE12 Itu heat
Input
10200401 43. J Ib/IOElZ Itu heat
Input
43.77 Ib/10€l2 Itu heat
Input
10300301 34. 1 Ib/10EI2 Itu
10J0050I 0.271 lb/10E12 Itu heat
Input
IOS00501 0.124 lb/10E!2 Itu
I0300S01 41.04 lk/10CI2 Itu
10300401 2.203 lb/IOE12 It* heet
input
NOTES
Cyclones/ESP, represents both gaseous and partlculate
PON
•
Uncontrolled, represent* both gaseous and particulat*
Pon
Nuttlclones. coal type not given, represents Mostly
partlculate POfl
Uncontrolled, coal type not given, represent* Mostly
•articulate POfl
ESP, represents both gaseous and particulate POtl
Represent* prlMarlly partjculate PON. uncontrolled
Represent* prlMarlly partlculate PON, uncontrolled
•.•presents prlMarlly partlculate POfl. uncontrolled
*epre**nt« prlearlly partlculate POfl. uncontrolled
Represent* prloerlly particulat* POU. uncontrolled
Uncontrolled. ho*e heating application
Uncontrolled
Uncontrolled, •*** reference also lists
-------
Page No. 252
0»/21/»0
CAS
POLLUTANT NUMBER
Polycycllc organic eatter
Polycyclic organic eatter
Potycyclic organic eatter
Polycycllc organic eatter
Polycvcllc organic Batter
Polycycltc organic Batter
Polycyclic organic eatter
Polycycllc organic oatter
Polycycllc organic eatter
Polycycltc organic eatter
Polycycllc organic eatter
Polycyclic organic oatter
Polycycllc organic eatter
Polycycllc organic eatter
SIC
CODE INDUSTRIAL PROCESS
Oil coebustion,
industrial
Oil coebustlon
Industrial
Oil coebustlon, utility
Oil coebustlon, utility
Oil coebustlon, utility
Open burning
Open burning
Open burning
Wood coebustlon
Uood coobustlon
Uood coebustlon
Uood coebustlon,
Indultrlal
Uood coebustlon.
Industrial
Uood coebustlon,
industrial
Uood coebustlon,
Industrial
EMISSION SOURCE
Stoae atoelzed vatertube.
rasldual oil
Uatertubo, residual oil
Face-fired, residual oil
Tangential -fired.
residual oil
UaU-flred. residual oil
Autoeoblle body burning
Autoeoblle tiro burning
Grass, leaves, branches
Laaf burning
nuniclpal refuse opon
burning
Industrial stick burner
boiler, yhlte oak and
elxod logs, Ind/coeoerc
Industrial /coeeerclal hot
yator boiler, harduood
chips
Industrial /coeeerclal
spreader stoker , bark
Fluldlled bed, green bark
Horizontal return tube
boiler, green ash
Horizontal return tube,
dry hardyaod
Horizontal return tube.
dry hardnood
SCC CODE EMISSION FACTOR
10200401 5.33 lb/iOE12 Itu heat
Input
10200401 1.4* lb/10E12 Itu heat
Input
10100401 0.8SB lb/10E12 Itu haat
input
10100404 5.7* lb/10EI2 Itu heat
Input
10100401 *.04 lb/10E12 Itu heat
Input
50300203 0.22 Ib/ton easts
50300203 0.41 Ib/ton yaste
50300201 0.005 - 0.0114 Ib/ton
yasto
50300201 0.02 - 0.044 Ib/ton
leaves
50300202 0.001 - 0.00*4 Ib/ton
yaste
10200*03 0.15* Ib/ton yaod burned
10200*01 0.0031 Ib/ton dry fuel
burned
10200*01 0.032 Ib/lOtlJ Itu haat
Input
10200*03 0.0023 Ib/ton dry yood
burned
10200*03 0.004* Ib/ton dry yood
burned
10200*01 1.4 x IOC-4 Ib/ton dry
yood burnod
10200*01 0.0014 Ib/ton dry Mod
NOTES
Uncontrollod, represents eostly partlculato POtl
Uncontrollod. represents both gaseous and particulate
POtl
Uncontrolled, represents both gaseous and particulato
POM
Cyclone controls, represents both gaseoue and
particulate POn
Uncontrolled, eve. of 4 value* ranging froe 0.4S-12.3
pg/J. represents gaseous t partlculato POM
lasod on concontratlon eeasured In seok* pluoo
lased on concontratlon eeasured In seoke pluee
lased on concentration oeasurod In seok* pluoe
lased on lab tests
lased en concentration eoasured In seoke slues
Uncontrollod. avo. of 3 values ranging 0.013-0.174
Ib/ton, represent* both gasoou* t partlculato POH
Hultlclono, represents both gaseous and particulate POtl
Cyclones, represents both gaseous and particulato POn
nulttcyclon*. represents both gaseous and partlculato
POtl. average of 3 (0.0014 - 0.00311 Ib/ton)
Uncontrolled, represent* both gaseou* and partlcul*t*
POM. overage of 3 valve*
-------
Page No.
0»/2l/»0
POLLUTANT
Polycyclic
Polycyclic
Polycyclic
Polycyclic
Polycyclic
Potycyclic
Polycyclic
Polycyclic
Polycvclie
Polycyclic
Polycvclie
Polycvclie
Polycyclic
Polycyclic
Polycyclic
Polycyclic
25J
orfanlc
orfanlc
orvanjc
orfanlc
orfanic
orf an! c
oryanic
orfanlc
orfanlc
orfanlc
orfanlc
orftnic
orfanic
orfanlc
orfanlc
orfanlc
CAS
NUMBER
etttar
•attar
•attar
eattar
•attar
•attar
•attar
eattar
eattar
eattar
eattar
eattar
•attar
•attar
•attar
•attar
•attar
SIC
CODE INDUSTRIAL PROCESS
Uood coabustlon.
industrial
Uood coebustlon ,
Industrial
Uood coabustlon,
industrial
Uood coebustlon.
Industrial
Uood coabustlon,
residential
Uood coobustlon.
residential
Uood coebustlon.
residential
Uood coabustlon.
residential
Uood coabuatlon.
residential
Uood coebustlon.
residential
Vood coebustlon.
raaldentlal
Uood coabustlon,
residential
Uood combustion,
residential
Uood combust Ion,
residential
Uood coebustlon,
residential
Uood coebustlon.
residential
Uood combust Ion.
raaldentlal
EMISSION SOURCE
Horizontal return tube,
ereen ptna/sawdust/bark
Underload stoker , dry
hardwood
Uatertube, dry oat
Watertube. fraan sawdust
•allied catalytic
woodstove
•allied Moodstove
Fireplace
Fireplace
Fluldlzad bed lurnace.
Pine wood chips
Fluldlzed bad lurnace.
Pine wood chips
Nonballled catalytic
woodstove
Nonballlad catalytic
woodstove
Nonballlad woodstove
feall airtifht
woodstoves, birch voed
Small airtifht
Moedstove*. birch Mood
Small alrtleht
Moodstove*. spruce wood
teall alrtlaht
Moodstove*. fmruce Mood
SCC CODE EMISSION FACTOR
10200*03 0.00128
burned
Ib/ton dry wood
10200905 O.OOtO* Ib/ton dry wood
burned
1020090] 0.0044
burned
10200*03 0.001*4
burnad
0.32*4
Ib/ton
Ib/tw
Ib/ton
dry
l dry
luel
0.533* Ib/ton lual
0.0*5 Ib/ton lual
3.1 x IOE-5 Ib/ton
burned
0.303*
O.*074
0.0*44
0.4034
0.3*22
0.04U
burned
0.0402
burned
0.0052
burned
0.0*4*
burned
Ib/ton
Ib/ton
Ik/tan
Ib/ton
Ib/ton
Ib/ton
Ib/ton
Ib/ton
Ib/ton
luel
luel
luel
lual
lual
dry
dry
dry
dry
wood
wood
burnad
burnad
burned
. lual
burnad
burned
burned
burnad
burnad
luel
luel
fuel
luel
NOTES
uncontrolled, repreaants easaous t partlculata POtl,
rel. also Hits 0.0084* lor saee botler/lual
nultlcyclone, represents both eassous and
POM. avarafa ol O.O045* - 0.00**4 Ib/ton
partlculate
nulticlone. represents both fasaous and particulata PON
(averafa ol 0.00228. 0.004*4 Ib/ton)
nulticlone, represents both fasaous and partlculate
PON, averafa ol 0.00172, 0.00151 Ib/ton
Uncontrolled, represents both fasaous and
POH. but all Mere lound in faseou* phaae
Uncontrolled, repreaents both easeou* and
aelsslons, averaee ol 2 values
Uncontrolled, represents both faaeous and
PON. avarafe ol 3 values
Uncontrolled, represents only partlculate
ol 3 value*
partlculate
p articulate
partlculata
POH, averaee
laahouse. raprasants both easeeus and partlculate POtl.
avarafe ol 2 valuea
Uncontrolled, represents both faaeou* and
PON. avarafe of 2 values
Uncontrolled, represent* both faaeou* and
POH. but all Mare lound In easaous phase
Uncontrolled, repreaents both faeoous and
POM. but all Mare lound in oasaoue phase
Uncontrolled, represents both oaaeoua and
POM. avarafe ol 4 values
Noreal hifh-teeeerature burnlnf conditloni
eniaslon teat*
Starved air condition*, based on aelsslon
particulata
partlculate
partlculate
partlculate
i. based on
tests
Normal hlfh-teeeeratura burnlnf condltlona, based en
emission test*
Noreal Mfh-temperature burnlnf conditloni
emission test*
i, based on
REFEREN
114
114
114
114
114
114
114
114
114
114
114
114
114
S7
57
87
87
-------
Pa«e No. 254
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
EMISSION SOURCE
SCC CODE EMISSION FACTOR
Polycycllc organic Bitter
Polycyclic organic natter
Polycyclle organic eatter
Polycycllc organic •attar
Polycvclic organic Batter
Polycycllc organic natter
Polycycllc organic Matter
Polycyclle organic Batter
Polycyclle organic Matter
Polycvclic organic Batter
Polycycllc organic natter
Polycyclic organic aatter
Polycvclic organic Batter
Polycyclic organic Batter
Polycycllc organic »atter
Polycycllc organic Batter
Polycyclic organic Batter
Polycyclic organic eatter
0133
0133
0051
0851
0651
0051
oosi
0851
1311
20(1
28*5
2951
2*51
2951
2*51
1*51
2*52
Hood cOBbustlon,
residential
8agasse coebustlon
Vagasse COBbustlon
Control led/prescrl bed
burning
Controlled/prescribed
burning
Control 1 ed/prescr 1 bed
burning
Control led/prescribed
burning
Control led/prescrl bed
burnlna
Control 1 ed/prescr 1 bed
burning
Oil shale retorting
Carbon black eanufacture
Asphalt (hot B!X)
production
Asphalt (hot elx)
production
Asphalt (hot oix)
production
Asphalt (hot Blxl
production
Asphalt (not Blx)
production
Asphalt rooflne eaterlal
production
uoodstove Mith secondary
COBbustlon
Industrial boilers
Industrial boilers
lacking fire, 0.1 Ib/ft2
lacking fire. 0.31 Ib/ft2
lacking fire. 0.4* Ib/ft2
Heading fire, O.I Ib/ft2
Heading fire. 0.31 Ib/ft2
Heading fire, 0.4* Ib/ft2
Modified In situ retort
Product recovery baghouse
on Bain process vent
dryer and elxer
Drue B!X plant
Drue «lx plant
OTUB nix plant
Drue win plant
Asphalt bloving still
0.14*4 Ib/ton fuel burned
10201101 17*. 7 lb/10EI2 Itu heat
Input
10201101 **.* lb/10E12 Itu heat
Input
27.94 Ib/ton TSP eeltted
12.51 Ib/ton tSP eeltted
8.17 Ib/ton TSP eeltted
I.7S Ib/ton TSP eeltted
0.8 Ib/ton TSP eelttad
0.78 Ib/ton TSP oeltted
0.0071 Ib/hr
30100403 0 007 Ib/ton charcoal
produced
30100504 0.0038 Ib/ton carbon
black produced
30500201 3 *4 x IOE-S Ib/ton
asphalt produced
30500205 7.18 x IOE-5 Ib/ton
asphalt produced
30500205 3.38 x IOE-S Ib/ton
asphalt produced
3O500205 4.42 x IOE-5 Ib/ton
asphalt produced
30500205 t.T x IOE-S Ib/ton
asphalt produced
IO5OOI01 0.0304 Ib/ton asphalt
MOM
Uncontrolled, represents both gaseous and partlculate
POH, but all were found In gaseous phase
2 boilers each w/ eultlcyclone vented to 1 coeeon
Average of 2 (17.2-4i.9l. eultlcyclone. represents both
easeou* and pertlculate POn.
Lab tests of burning pine needles
Lab test* of burning pine needle*
Lab tests of burnin* pine needles
Lab tests of burning pine needles
Lab tests of burnin* pine needles
Lab tests of burning Pine needles
eased en effeae: concentration and flow rate
Uncontrolled, overage of S tests
Uncontrolled, average of 3 test*, both aaseoue and
partlculate POft
Cyclone and wet scrubber, virgin feed Baterlal
Knock out box, using recycled feed
Knock out box end venturl scrubber, using recycled feed
Knock out box
Knock out box and venturl scrubber
Uncontrolled
114
114
114
114
114
114
114
114
114
114
114
114
114
114
114
114
114
114
-------
Page No. 255
09/21/90
CAS
POLLUTANT NUMBER
Polvcvclie organic patter
Polvcvclic org»nic natter
Polvcvclic organic natter
Polvcvclic organic natter
Polvcvclic organic natter
Polvcvclic organic matter
Polvcvclic organic natter
Polvcvclle organic natter
SIC
CODE
2*52
2952
2952
2952
2952
2952
2952
2952
33
3312
INDUSTRIAL PROCESS
production
A*ph*lt roofing natcrlal
production
Asphalt roofing notarial
production
Asphalt roofing naterlal
production
production
Asphalt roofing natirlal
production
Asphalt roofing material
production
Asphalt roofing BateMal
production
Ferroalloy production
Coke production.
en i ssi OH SOURCE sec CODE
Asphalt blowing still 30500101
Asphalt bloving still 30500101
Asphalt blowing .till 30500101
Asphalt blowing (till 30500101
Saturator 30500103
Saturetor 30500103
Saturator and »phalt 30500103
storage tank*
Electric arc furnace. 30300*05
sealed, elllcosanganese
•v-product rKoviry, tar 30300315
EMISSION FACTOR
• .• x 10E-S Ib/tofi
aapiialt blown
4.2 x 10E-« Ib/ton
asphalt blown
1.1* X IOE-5 Ib/ton
atphalt blown
O.OO»i Ib/ton awhalt
blown
4 2 x 10E~4 Ib/ton
produced
l.n x 10E-4 Ib/ton
produced
».« x 10E-4 )b/ton
produced
0.042 Ib/ton produetd
00.0022 ib/rtn-hr •n*r«y
con«UM«d by furnace
0.0082 Ib/ton coal fad to
NOTES REFERENCE
Afterburner 114
FUM Incinerator 114
Process heater furnace 114
Stack baffles, represents participate rotl 114
Uncontrolled 114
ESP controlled '14
Uncontrolled 114
High velocity air filter 114
Hl«h pressure drop, net scrubber represents faseous and 114
partlculate POn
Uncontrolled, represents both faseous and partlculate 114
Polvcvclic organic «att«r
Polvcyclic organic *att*r
Polvcvclic organic •attw
Polycyclic organic flatter
Polycyeltc org«nic »att«r
bv-product recovery
procecs
3312 Coke production.
by-product recovery
procec*
3312 Coke production.
by-product recovery
process
3312 Coke productien,
by-product recovery
process
3312 Coke production.
byproduct recovery
process
3312 Coke production,
by-product recovery
process
processing * decanter
•v-product recovery, tar
protesting * devatering
and •tor***
•y-product recovery, tar
processjng - distillation
product storage
Slot oven coir 1 fig * cole*
quenching
Slot oven loking - coke
quenching
30300315 * x 10C-4 Ib/ton coal fed Uncontrolled, represents both gaseous and Partlculata
to coking oven POfl
30300315 2.2 x IOC-5 tb/ton coal Uncontrolled, represents both gaseous and parttculate
fed to coking ov PWt
30300304 0.0037 Ib/ton coal Clean vater euencfi
charged
30300304 1.22* Ib/ton coal charged Cont*«inaiad water used for euanch
Slot oven coking - door 3O30030* SS24 ng/ltaS
leaks
Uncontrolled, average of 4 test rung
-------
Page No. 256
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
EHISSION SOURCE
SCC CODE EMISSION FACTOR
Polycycllc organic .tatter
Polycycllc organic Matter
Polycyclic organic Matter
Polycycllc organic Matter
Polycycllc organic Matter
Pol ycycl tc organic Matter
Polycycl ic organic Matter
Polycyclic organic Matter
Polycyclic organic Matter
Polycycllc organic Matter
Polycyclic organic Matter
Polycyclic organic Matter
Polycyclic organic Matter
Polycyclic organic Matter
3312 Coke production. Slot oven coking - door
by-product recovery leak*
process
3312 Coke production. Slot oven coking - door
by-product recovery leak*
process
3313 Ferroalloy production Electric arc furnace,
sealed, ferroaanganese
3313 Ferroalloy production Electric arc furnace,
seei -teal ed , f errosl 1 i con
3334 Primary aluelnue SMeltlng Mode paste process -
•Ixer
Pitch Miter
trlqusttlng
3334 Primary alualnu* SMeltlng Horizontal Soderberg pot
roe* - pot gas scrubber
3334 Primary aluM.nue smiting Vertical Soderberg pot
TOM - pot •** dry
scrubber
3334 Primary aluelnu* smiting Vertical Soderberg pot
reoM * scrubber for
ventilation air
3341 Secondary lead suiting Secondary satelter
49.1 Coal combustion, utility aUtuMnou* coal Hired
cyclone utility boiler
4*11 Coal coabustlon. utility f HUM! nous coal -fired
cyclone utility boiler
4911 Coal coatoistlon. utility fltualnous coal -fired
30300308 125* ng/N«3 Uet ESP
3030030B 1.4 x 10E-7 Ib/ton coal Uet ESP
charged
30300701 0.343 Ib/Mw-hr energy uncontrolled, represents gaseous and partlculate POM
consumed by furnace
consu-Md by furnace particulate POH
303001 575 »g/M3 Uncontrolled
3O3001 2752 •g/«3 Uncontrolled
303001 9.2 ng/n3 Uncontrolled
30300102 2.04 Ib/ton Al
30300103 0.002 Ib/ton Al
30300103 0.08 Ib/ton Al
30400403 1107 ng/N»3 Controlled, device not specified, average of 4 tests,
shelter processing batteries
10100203 2.040 Ib/tOCU Itu heat CSP. represent* both **seous and partlculate POH
input
10100203 U.2 Ib/IOElZ Itu heat Uet scrubber, represents both partlculate end eateous
input POn
10100202 t.« lb/IOCI2 Itu Uet gcrubOvr. represents both gaseous end partlculate
114
114
114
114
114
114
114
114
114
114
114
114
114
114
Polycycllc organic Matter
pulverized dry bottoej
boilers
4*11 Coal coMbustlon, utility lltuMlnous coal-fired
pulverliod dry bottoe
boilers
10100201 II.* Ib/lOCli Itu
nultlclone/ltP, represents bath gaseous and partlculate 114,
-------
Page No. 257
0»/21/»0
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
EMISSION SOURCE
SCC CODE EMISSION FACTOR
REFERENCE
Polycycllc organic oatt*r
4*11 Coal co.bu.tlon, utility
(Itu.Ioou. coal-fir**
pulvor!z*d ugt botto«
bolUrf
10100201 IB.I 10/IOE12 Itu ESP, repreMnt* both ****ou* Mid »artlc particulate ran 114
Itu
10100202 0.»»! - l.«2 Ib/lOElZ Itu nultleleni/fS*. reprefent* mtly •articulate POD 114
He*t Input
10100205 0.125 - 0.4*3 lb/10E12 nultlclone, co«l type not reported, represent* Mo*tly 114
Itu heat Input partlcuUte POH
1010022* O.«t5 lb/IOE12 Itu heat ESC controlled, repreient* both partlculate and «a*eou* 114
input POH
Polycycllc organic Matter
Polycycllc organic Matter
Polycyclle organic Matter
Polycycllc ori*nic Matter
Polycycllc organic eatter
4*11 Coal co.bu.tlon, utility
4»S3 nunlclpal na*te
coabuvtion
4WJ nunlclpal M*t*
coftbuvtion
4«SJ nunlclMl w>t<
coftbuctlon
4tS3 ftunlcl.al iu»t«
coobuitton
vertically fired boiler*.
pulverized *ubbitUMinou*
Hultlpl* chaober
reciprocating atoker
grate Incinerator
nultlple chaMber.
reclprocetlng ptoter
grate
nultlple ehubor.
reciprocating atoker
«ret«
nultlple ch
reciprocating Itoker
grete
10100201 t.4* lb/10E12 Itu heat ISP controlled, represent* both particulate and ganou*
Input PON
50100101 o.2« x 10E-4 Ib/ton va*te Uncontrolled, repre**nt* prlBVlly particulate POtl
burned
50100101 1.24 x IOE-S Ib/ton ua*te Uet acrlibber, represent* particulate POH
burned
90100101 1.1 x IOE-* Ib/ton «a*te ESI*, repreunt* particulate PON
burned
MlOOtOl ' 0.012* lb/to« «a*te ISP. reprnenta both eaaeou* end particulate I
feuriMd
-------
Page No. 259
CAS SIC
NUMBER CODE INDUSTRIAL PROCESS
EMISSION SOURCE
SCC CODE EHISSION FACTOR
Polvcyclic organic Matter
4*53 Municipal waste
coebustlon
Hultlple chaeber,
traveling grate
incinerator
50100101 1.01 x 10E-5 Ib/ton waste Settling charter Is control device, represents
burned prlearlly partlculate POM
Polvcyclic organic ••ttsr
Polycycllc organic Batter
4*53 nunlclpal waste
coMbustlon
Rocking bar grate
4*53 Solid waste Incineration. nultlple chenber with
coeeercial auxllllary gas burner
50100101 3.44 X 10E-5 Ib/ton waste wet scrubber and ESP, represents both gaseous and
burned partlculate Poll
50100101 0.044 Ib/ton waste burned Uncontrolled, represents partlculate PON
114
Polvcyclic organic Matter
Polvcyclic organic Matter
4*53 Solid wast* incineration. Single chaeber
coMoercial Incinerator
4*53 Uastewater treetMont
50100102 0.00417 Ib/ton xaste
burned
Uncontrolled, represents partlculate Poll
50100701 0-l**l Ib/ton of PON In Depends on coop., based on eels. Model, for hypoth.
Influent POTU, repr. eve. POTU treat. Indue, wastewater
Polycycllc organic natter
5032 Asphalt distribution/us. Entire process
0.0001 Ib/ton asphalt
applied
1 essueed te be O.II of THC
PolydlMothyl slloxane *014004 224 Uoven fabric finishing Tenter fraees - resin
finish
744OO*7 25 Uood co*bustlon.
Industrial
Horizontal return tube
330001 0.001* Ib/ton fabric Uncontrolled, one test
10200*04 554 lb/10E12 Itu heat
Input
taeplg results. 1 plant, wood flovrate • .514 kg/s,
boiler has 3-pass design w/flyaeh relnjectlon,
uncontrolled
174
PotassiuM
1.2-Propadlene
Propane
Propanol
Prop I onal dehyde
74400*7 25 Uood coMbustlon,
industrial
74400*7 25 Uood coebustlon.
Industrial
4434*0 214* Acetic anhydride
production
74*14 214* Acrylonltrlle production
- SOH10 process
lalanced draft wlckes
stoker-fired industrial
boiler
•alanced draft wlckes
stoker-fired Industrial
boiler
Reaction by-product gas
Absorb" "«'
74914 21*5 Carbon black Manufacture lain procogg purge vent
- oil furnace
74*84 104 Hospital waste
Incineration
71231 2145 Acetone/Phenol
Mnuf acture fro* cuoene
Uood co«bu»tlon.
residential
Cuoene eeronldatlOT vent
10200*0* 0.0132 Ib/ton fuel or
>I5I lb/lOE12 Itu
10200*04 0.021 Ib/ton fuel or
>2.551 lb/10E12 ttu
30113302 3.1 Ib/ton acetic
anhydride produced
30125404 121.4 Ib/ton
acrylonltrlle produced
30100504 0.44 Ib/ton carbon black
produced
31S02O <0.024 Ib/ton feed
30120202 0.022 Ib/ton phenol
0,1 Ib/ton mod
Dry wood, one plant, partlculate control w/oechanlcal 177
collector (cyclone), wood feed rate 0.2* kg/e. boll.
eff. SS.3I
Creen mod. one plant, partlculate control v/Mchenlcal 177
collector (cyclone), wood feed rate 0.54 kg/i, boll.
eff. 41.31
lased on data fro* three plants 152
Uncontrolled, based on data fro* plants end EPA studies 14*
tesed on test deta
Uncontrolled, test data
Controlled
-------
PMO Mo. 2S?
CAS sic
Nuneep. CODE INDUSTRIAL PROCESS
EMISSION SOURCE
SCC CODE EMISSION FACTOR
Propyl benzene
Propyl benzene
Propyl benzene
Propyl benzene
Propyl benzene
Propyl benzene
Propyl benzene
Propyl benxene
Propyl benzene
Propyl benzene
Propyl benxene
Propyl bensene
Propyl benxene
Propyl one
Propylene
Propylene
Propylene
103*51 Scrap tiro, open burning
103*51 Scrap tire, open burning
103*51 Scrap tiro, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
103*51 Scrap tire, open burning
115071 2821 Polyvlnyl chloride
production
' 115071 28*5 Cueene production
115071 28*t Acrylic acid production
115071 2I*» Acrylonltrlle production
Tires in experleental
burn hut
Tires in experioental
burn hut
Tires in experloental
burn hut
Tires In experloental
burn hut
Tires In experloental
burn hut
Tires In experloental
burn hut
Tires In experleental
burn hut
Tires In experloental
burn hut
Tires In experloental
burn hut
Tires In experloental
burn hut
Tires In oxpertoental
burn hut
Tiros In experloental
burn hut
Tires In experloentol
burn hut
Suspension process,
entire plant
Entire procoss
Entire procoss
Absorber
0.3*9 Ib/ton tire
0.502 Ib/ton tire
O.I2B Ib/ton tire
0.041 Ib/ton tire
O.l*» Ib/ton tire
0.11* Ib/ton tire
0.148 Ib/ton tire
0.425 Ib/ton tire
0.«»» Ib/ton tire
0.070 Ib/ton tire
0.044 Ib/ton tire
0.010 Ib/ton tire
0.00* Ib/ton tire
30101801 1.4 x IOE-4 Ib/ton PVC
30115*01 0.14 Ib/ton cuoene
30111221 O.I Ib/ton acrylic acid
produced
3012540* 1.2 Ib/ton acrylonl trllo
»AO-2 extracts u/KS analysis, shred condition • 2' by
2* pieces, burn rate • I.I ke/hr, uncontrolled
XAD-2 extracts u/HS analysis, shred condition > 2* by
2" pieces, burn rate • 1.1 kg/hr. uncontrolled
VOST saoples burn rate - I.S kg/hr. shred condition •
2* by 2* Piece, uncontrolled
VOST saoples burn rate - 2.3 kg/hr. shred condition •
I' by 2* Piece, uncontrolled
VOST saswlet burn rat* - 0.* kg/hr. shred condition •
2" by 2* Piece, uncontrolled
VOST saoples burn rate - 1.3 kg/hr. shred condition •
2- by 2' Piece, uncontrolled
VOST saoples burn rate - 1.4 kg/hr. shred condition •
2* by 2* Piece, uncontrolled
VOST saooles burn rate - O.I kg/hr. shred condition •
2* by 2* Hole, uncontrolled
VOST sasvles burn rate - O.S kg/hr, chunk conditions •
1/4 to I/* of a tiro, uncontrolled
VOST saeples burn rote - 1.7 kg/hr. chunk conditions •
1/4 to l/« of a tire, uncontrolled
VOST saeoles burn rato - 1.27 kg/hr, chunk condition* •
1/4 to l/« of a tire, uncontrolled
VOST •••Pies burn rate - 2.27 kg/hr, chunk conditions •
1/4 to I/* of o tire, uncontrolled
VOST saeples burn rate - «.«> kg/hr. chunk condition* •
1/4 to l/« of a tiro, uncontrolled
iased on a oodel plant, l»7f data. I.S x lOCi Ib
capacity* control status not certain
Controlled, engineering Judeeeent. based on ratio of
propane eolsslone
|