Toluene And Benzoic Acid Production r5c68

LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF TOLUENE

Final Report

Prepared for: Dennis Beauregard Emission Inventory Branch Technical Division Office of Air Quality Planning and Standards U.S. Environmental Protection Agency Research Triangle Park, North Carolina 27711

Prepared by: TRC Environmental Corporation 100 Europa Drive, Suite 150 Chapel Hill, North Carolina 27514

September 1993

EPA Contract No. 68-D9-0173 Work Assignment No. 3/316

DISCLAIMER

This report was furnished to the U.S. Environmental Protection Agency by TRC Environmental Corporation, 100 Europa Drive, Chapel Hill, North Carolina, 27514, in partial fulfillment of Contract No. 68-D9-0173, Work Assignment No. 3/316. This document has been reviewed by the Office of Air Quality Planning and Standards and has been approved for publication. The opinions, findings, and conclusions expressed are those of the authors and not necessarily those of the U.S. Environmental Protection Agency. Mention of company or product name is not to be considered as an endorsement by the U.S. Environmental Protection Agency.

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TABLE OF CONTENTS Section

Page

DISCLAIMER . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ii LIST OF FIGURES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . vi LIST OF TABLES . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . viii 1.0

PURPOSE OF DOCUMENT . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1-1 1.1 Reference for Section 1.0 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1-5

2.0

OVERVIEW OF DOCUMENT CONTENTS . . . . . . . . . . . . . . . . . . . . . . . . . . . 2-1 2.1 References for Section 2.0 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2-5

3.0

BACKGROUND . . . . . . . . . . . . . . . 3.1 Nature of Pollutant . . . . . . . . . 3.2 Overview of Production and Use 3.3 References for Section 3.0 . . . .

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3-1 3-1 3-4 3-7

4.0

EMISSIONS FROM TOLUENE PRODUCTION . . . . . . . . . 4.1 Toluene Production from Petroleum Fractions . . . . . . . . 4.1.1 Hydrotreating . . . . . . . . . . . . . . . . . . . . . . . . . . 4.1.2 Catalytic Reforming . . . . . . . . . . . . . . . . . . . . . 4.1.3 Secondary Hydrogenation (for Pyrolysis Gasoline) 4.1.4 Toluene Recovery . . . . . . . . . . . . . . . . . . . . . . 4.1.5 Emissions . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4.2 Toluene Production from Coal . . . . . . . . . . . . . . . . . . 4.2.1 Process Descriptions . . . . . . . . . . . . . . . . . . . . . 4.2.2 Emissions . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4.3 Toluene Production from Styrene . . . . . . . . . . . . . . . . 4.3.1 Process Description . . . . . . . . . . . . . . . . . . . . . 4.3.2 Emissions . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4.4 References for Section 4.0 . . . . . . . . . . . . . . . . . . . . . .

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4-1 4-5 4-5 4-7 4-10 4-10 4-14 4-18 4-20 4-21 4-21 4-22 4-22 4-25

5.0

EMISSIONS FROM MAJOR USES OF 5.1 Benzene Production . . . . . . . . . . 5.1.1 Process Description . . . . . 5.1.2 Emissions . . . . . . . . . . . . 5.2 Toluene Diisocyanate Production . 5.2.1 Process Description . . . . . 5.2.2 Emissions . . . . . . . . . . . . 5.3 Trinitrotoluene Production . . . . . 5.3.1 Process Description . . . . . 5.3.2 Emissions . . . . . . . . . . . .

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5-1 5-1 5-2 5-5 5-6 5-8 5-9 5-11 5-11 5-13

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TOLUENE ......... ......... ......... ......... ......... ......... ......... ......... .........

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TABLE OF CONTENTS (Continued) Section 5.4

Benzoic Acid Production . . 5.4.1 Process Description . 5.4.2 Emissions . . . . . . . . 5.5 Benzyl Chloride Production 5.5.1 Process Description . 5.5.2 Emissions . . . . . . . . 5.6 Other Toluene Derivatives . 5.7 Paint and Ink Manufacturing 5.7.1 Process Description . 5.7.2 Emissions . . . . . . . . 5.8 Solvent Cleaning Operations 5.8.1 Process Description . 5.8.2 Emissions . . . . . . . . 5.9 Other Solvent Uses . . . . . . 5.10 References for Section 5.0 . 6.0

7.0

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EMISSIONS FROM THE USE OF TOLUENE-CONTAINING MATERIALS 6.1 Surface Coating Operations . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6.1.1 Process Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6.1.2 Emissions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6.2 Printing and Publishing . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6.2.1 Process Description . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6.2.2 Emissions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6.3 Gasoline and Automotive Emissions . . . . . . . . . . . . . . . . . . . . . . . . . 6.4 Gasoline Marketing . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6.4.1 Toluene Emissions from Loading Marine Vessels . . . . . . . . . . . 6.4.2 Toluene Emissions from Bulk Gasoline Plants, Bulk Gasoline Terminals and Service Stations . . . . . . . . . . . . . . . . . . . . . . . . 6.4.3 Control Technology for Gasoline Transfer . . . . . . . . . . . . . . . . . 6.4.4 Control Technology for Gasoline Storage . . . . . . . . . . . . . . . . . 6.4.5 Control Technology for Vehicle Refueling Emissions . . . . . . . . . 6.5 Other Sources of Residual Toluene Emissions . . . . . . . . . . . . . . . . . . . 6.6 References for Section 6.0 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

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TO PRODUCTION ............... ............... ............... ............... ...............

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BY-PRODUCT EMISSIONS: PROCESSES UNRELATED OR USE OF TOLUENE . . . . . . . . . . . . . . . . . . . . . . . . 7.1 Coal Combustion . . . . . . . . . . . . . . . . . . . . . . . . . . 7.2 Hazardous and Solid Waste Incineration . . . . . . . . . . 7.3 Wastewater Treatment Processes . . . . . . . . . . . . . . . 7.4 References for Section 7.0 . . . . . . . . . . . . . . . . . . .

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5-14 5-15 5-16 5-16 5-17 5-17 5-18 5-19 5-24 5-26 5-28 5-28 5-29 5-30 5-32 . . . . . . .

6-1 6-1 6-2 6-2 6-5 6-6 6-8 6-11 6-12 6-15 6-17 6-22 6-26 6-26 6-28 6-30

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7-1 7-1 7-3 7-4 7-7

TABLE OF CONTENTS (Continued) Section 8.0

Page

AMBIENT AIR AND STATIONARY SOURCE TEST PROCEDURES 8.1 EPA Method TO-1 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.2 EPA Method TO-2 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.3 EPA Method TO-3 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.4 EPA Method TO-14 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.5 EPA Method 0030 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.6 EPA Method 5040 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.7 EPA Reference Method 18 . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.8 EPA Method 0010 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.9 EPA Method 8270 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.10 NIOSH Method 1501 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.11 References for Section 8.0 . . . . . . . . . . . . . . . . . . . . . . . . . . . .

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8-1 8-2 8-2 8-5 8-8 8-8 8-10 8-12 8-16 8-16 8-18 8-20

APPENDIX A

POTENTIAL SOURCE CATEGORIES OF TOLUENE EMISSIONS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . A-1

APPENDIX B

LISTS OF PAINT, INK, AND PRINTING FACILITIES WITH ANNUAL SALES GREATER THAN $1 MILLION . . . . . . . . . . . . . . B-1

APPENDIX C

TOLUENE SOURCE CATEGORIES IN SURFACE COATING OPERATIONS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . C-1

APPENDIX D

SUMMARY OF EMISSION FACTORS LISTED IN THIS DOCUMENT . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . D-1

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LIST OF FIGURES Number

Page

3-1

Chemical Use Tree for Toluene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3-6

4-1

Process Flow Diagram for Hydrotreating . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4-6

4-2

Typical Reforming Unit . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4-8

4-3

Generalized Toluene Recovery Process Flow Diagram . . . . . . . . . . . . . . . . . . 4-12

4-4

Process Flow Diagram for Styrene Production by Ethylbenzene Dehydrogenation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4-23

5-1

Process Flow Diagram of a Toluene Dealkylation Unit . . . . . . . . . . . . . . . . . . 5-4

5-2

Basic Operations That May Be Used in Toluene Diisocyanate Production . . . . 5-10

5-3

TNT Production . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5-12

5-4

Usage of Toluene in the Paint and Coatings Industry . . . . . . . . . . . . . . . . . . . 5-20

5-5

Flow Diagram of the Paint and Ink Manufacturing Process . . . . . . . . . . . . . . 5-25

6-1

Flow Diagram of a Surface Coating Operation . . . . . . . . . . . . . . . . . . . . . . . . 6-3

6-2

The Gasoline Marketing Distribution System in the United States . . . . . . . . . . 6-14

6-3

Bulk Plant Vapor Balance System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6-24

6-4

Service Station Vapor Balance System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6-25

8-1

EPA Method TO-1 Sampling System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8-3

8-2

Tenax® Cartridge Design . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8-4

8-3

Carbon Molecular Sieve Trap (CMS) Construction . . . . . . . . . . . . . . . . . . . . . 8-6

8-4

Automated Sampling and Analysis System for Cryogenic Trapping . . . . . . . . . . 8-7

8-5

Canister Sampling System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8-9

8-6

Schematic of Volatile Organic Sampling Train (VOST) . . . . . . . . . . . . . . . . . 8-11

8-7

Schematic Diagram of Trap Desorption/Analysis System . . . . . . . . . . . . . . . . 8-13 vi

LIST OF FIGURES (Continued) Number

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8-8

Direct Interface Sampling System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8-14

8-9

Integrated Bag Sampling Train . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8-15

8-10

Modified Method 5 Sampling Train . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8-17

8-11

Method 1501 Sampling System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8-19

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LIST OF TABLES Number

Page

3-1

Chemical Identification of Toluene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3-2

3-2

Physical and Chemical Properties of Toluene . . . . . . . . . . . . . . . . . . . . . . . . . 3-3

4-1

Toluene Production Locations and Capacities . . . . . . . . . . . . . . . . . . . . . . . . . 4-2

4-2

Estimated Domestic U.S. Supply and Demand of Toluene . . . . . . . . . . . . . . . . 4-4

4-3

World-Wide Toluene Production . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4-5

4-4

Catalytic Reforming Processes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4-9

4-5

Pyrolysis Gasoline Hydrogenation Processes . . . . . . . . . . . . . . . . . . . . . . . . . 4-11

4-6

Emission Factors for Toluene Production from Petroleum Fractions . . . . . . . . 4-15

4-7

Average Emission Factors for Fugitive Equipment Leak Emissions . . . . . . . . . 4-17

4-8

Control Techniques and Efficiencies Applicable to Equipment Leak Emissions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4-19

4-9

Emission Factors for Toluene Production from Coal . . . . . . . . . . . . . . . . . . . 4-21

4-10

Emission Factors for Toluene Production from Styrene Production . . . . . . . . . 4-24

5-1

Benzene Producers Using Toluene Feedstock . . . . . . . . . . . . . . . . . . . . . . . . . 5-3

5-2

Toluene Diisocyanate Production Locations and Capacities . . . . . . . . . . . . . . . 5-7

5-3

Benzoic Acid Production Locations and Capacities . . . . . . . . . . . . . . . . . . . . 5-14

5-4

Estimated Consumption of Toluene Derivatives in Paints and Coatings . . . . . . 5-21

5-5

Estimated Consumption of Solvents in Paints and Coatings, By Market . . . . . . 5-22

5-6

Emissions from Miscellaneous Sources of Toluene . . . . . . . . . . . . . . . . . . . . 5-31

6-1

Gravure Association of America Industry Survey Results . . . . . . . . . . . . . . . . 6-10

6-2

Emission Factors from Gasoline Use . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6-12

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LIST OF TABLES (Continued) Number

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6-3

Uncontrolled Volatile Organic Compound and Toluene Emissions from Loading Gasoline in Marine Vessels . . . . . . . . . . . . . . . . . . . . . . . . . . 6-16

6-4

Toluene Emission Factors for Gasoline Loading and Bulk Terminals and Bulk Plants . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6-18

6-5

Toluene Emission Factors for Storage Losses at a Typical Gasoline Bulk Terminal . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6-20

6-6

Uncontrolled Gasoline Vapor and Toluene Emission from a Typical Bulk Plant . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6-21

6-7

Uncontrolled Gasoline Vapor and Toluene Emissions from a Typical Service Station . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 6-23

6-8

Residual Emissions from Miscellaneous Sources of Toluene . . . . . . . . . . . . . . 6-29

7-1

Toluene Emissions from Combustible Coal Refuse Material . . . . . . . . . . . . . . . 7-3

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EXECUTIVE SUMMARY

Emissions of toluene into the atmosphere are of special significance because of the Clean Air Act Amendments of 1990. These amendments mandate that toluene emissions be subject to standards that allow for the maximum degree of reduction of emissions and that, by 1995, a list of source categories be established that s for no less than 90 percent of toluene emissions. This document is designed to assist groups interested in inventorying air emissions of toluene by providing a compilation of available information on sources and emissions of this substance.

Toluene is a man-made aromatic hydrocarbon produced mostly from petroleum. In the U.S., the Virgin Islands and Puerto Rico, toluene is produced by 21 companies at 30 plants. Most toluene produced is derived from petroleum fractions. In 1991, 3,104,000 megagrams (944 million gallons) of toluene were recovered. Growth in demand is expected to be very modest over the next few years.

Toluene is used as a cleaning solvent in the coating, printing and leather industry and in the manufacturing of paints and coatings, inks, adhesives, resins, and pharmaceuticals. It is also used as an intermediate in the production of benzene and toluene diisocyanate, and for gasoline blending.

At the time of publication of this document, estimates of nationwide emissions of toluene were not available.

Updates to this document will attempt to incorporate any nationwide

emission estimates subsequently developed.

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SECTION 1.0 PURPOSE OF DOCUMENT

The Environmental Protection Agency (EPA) and State and local air pollution control agencies are becoming increasingly aware of the presence of substances in the ambient air that may be toxic at certain concentrations. This awareness, in turn, has led to attempts to identify source/receptor relationships for these substances and to develop control programs to regulate emissions. Unfortunately, very little information is available on the ambient air concentrations of these substances or on the sources that may be discharging them to the atmosphere.

To assist groups interested in inventorying air emissions of various potentially toxic substances, EPA is preparing a series of documents such as this that compiles available information on sources and emissions of these substances. Prior documents in the series are listed below:

Substance

EPA Publication Number

Acrylonitrile Carbon Tetrachloride Chloroform Ethylene Dichloride Formaldehyde (Revised) Nickel Chromium Manganese Phosgene Epichlorohydrin Vinylidene Chloride Ethylene Oxide Chlorobenzenes Polychlorinated Biphenyls (PCBs) Polycyclic Organic Matter (POM) Benzene Organic Liquid Storage Tanks Coal and Oil Combustion Sources Municipal Waste Combustors Perchloroethylene and Trichloroethylene 1,3-Butadiene Chromium (supplement)

EPA-450/4-84-007a EPA-450/4-84-007b EPA-450/4-84-007c EPA-450/4-84-007d EPA-450/2-91-012 EPA-450/4-84-007f EPA-450/4-84-007g EPA-450/4-84-007h EPA-450/4-84-007i EPA-450/4-84-007j EPA-450/4-84-007k EPA-450/4-84-007l EPA-450/4-84-007m EPA-450/4-84-007n EPA-450/4-84-007p EPA-450/4-84-007q EPA-450/4-88-004 EPA-450/2-89-001 EPA-450/2-89-006 EPA-450/2-90-013 EPA-450/2-89-021 EPA-450/2-89-002

1-1

Substance

EPA Publication Number

Sewage Sludge Styrene Methylene Chloride

EPA-450/2-90-009 EPA-450/4-91-029 EPA-454/R-93-006

This document deals specifically with toluene. Its intended audience includes Federal, State, and local air pollution personnel and others who are interested in locating potential emitters of toluene, and making gross estimates of air emissions therefrom.

Because of the limited amounts of data available on potential sources of toluene emissions, and since the process configurations, control equipment, and operating procedures of many sources will not be the same as those described here, this document is best used as a primer to inform air pollution personnel about (1) the types of sources that may emit toluene, (2) process variations and release points that may be expected within these sources, and (3) available emissions information indicating the potential for toluene to be released into the air from each operation.

The reader is strongly cautioned against using the emissions information contained in this document to try to develop an exact assessment of emissions from any particular facility. Because insufficient data are available to develop statistical estimates of the accuracy of these emission factors, no estimate can be made of the error that could result when these factors are used to calculate emissions from any given facility. It is possible, in some extreme cases, that order-of-magnitude differences could result between actual and calculated emissions, depending on differences in source configurations, control equipment, and operating practices. Thus, in situations where an accurate assessment of toluene emissions is necessary, source-specific information should be obtained to confirm the existence of particular emitting operations, the types and effectiveness of control measures, and the impact of operating practices. A source test and in some cases a material balance should be considered as the best means to determine air emissions directly from an operation.

1-2

Another potential source of emissions data for toluene is the Toxic Chemical Release Inventory (TRI) form required by Section 313 of Title III of the Superfund Amendments and Reauthorization Act of 1986 (SARA 313).1 SARA 313 requires owners and operators of certain facilities that manufacture, import, process, or otherwise use certain toxic chemicals to report annually their releases of these chemicals to any environmental media. As part of SARA 313, EPA provides public access to the annual emissions data. The TRI data include general facility information, chemical information, and emissions data. Air emissions data are reported as total facility release estimates, broken out into fugitive and point components. No individual process or stack data are provided to EPA. The TRI requires the use of available stack monitoring or measurement of emissions to comply with SARA 313. If monitoring data are unavailable, emissions are to be quantified based on best estimates of releases to the environment.

The reader is cautioned that the TRI will not likely provide facility, emissions, and chemical release data sufficient for conducting detailed exposure modeling and risk assessment. Accidental releases are also ed for in the TRI, but are not included in inventories of toxicair pollutants. In many cases, the TRI data are based on annual estimates of emissions (e.g., on emission factors, material balances, engineering judgement). Although the TRI database was consulted during the development of this report, it should be referred to as an additional information source to locate potential emitters of toluene, and to make preliminary estimates of air emissions from these facilities.

To obtain an exact assessment of air emissions from

processes at a specific facility, source tests or in some cases detailed material balance calculations should be conducted, and detailed plant site information should be compiled.

Each L&E document, as standard procedure, is sent to government, industry, and environmental groups wherever EPA is aware of expertise.

These groups are given the

opportunity to review the document, comment, and provide additional data where applicable. Where necessary, the documents are then revised to incorporate these comments. Although these documents have undergone extensive review, there may still be shortcomings.

Comments

subsequent to publication are welcome and will be addressed based on available time and resources. In addition, any information is welcome on process descriptions, operating parameters,

1-3

control measures, and emissions information that would enable EPA to improve the contents of this document. Comments and information may be sent to the following address:

Chief, Emission Factor and Methodologies Section Emission Inventory Branch, (MD-14) U.S. Environmental Protection Agency Research Triangle Park, NC 27711

1-4

1.1

REFERENCE FOR SECTION 1.0

1.

Toxic Chemical Release Reporting: Community Right-To-Know. 52 FR 21152. June 4, 1987.

1-5

SECTION 2.0 OVERVIEW OF DOCUMENT CONTENTS

The purpose of this document is to assist Federal, State and local air pollution agencies and others who are interested in locating potential air emitters of toluene and making gross estimates of air emissions therefrom. Because of the limited background data available, the information summarized in this document does not and should not be assumed to represent the source configuration or emissions associated with any particular facility.

This section provides an overview of the contents of this document. It briefly outlines the nature, extent, and format of the material presented in the remaining sections of this report.

Section 3.0 of this document briefly summarizes the physical and chemical characteristics of toluene, and provides an overview of its production and use. This background section may be useful to someone who needs to develop a general perspective on the nature of this substance and how it is manufactured and consumed.

Section 4.0 of this document focuses on major production source categories that may discharge air emissions containing toluene. Section 5.0 discusses the uses of toluene as industrial feedstocks and major solvent uses, particularly degreasing and coating operations. Section 6.0 addresses emissions as a result of releases from toluene-containing products after manufacture. Section 7.0 describes emissions sources from the manufacture of products other than toluene, or as a by-product of processes (e.g., burning of fuel oil). Example process descriptions and flow diagrams are provided in addition to available emission factor estimates for each major industrial source category described in Sections 4.0, 5.0, 6.0, and 7.0. Individual companies involved with either the production or use of toluene are reported throughout the document. Information reported is extracted primarily from trade publications.

Section 8.0 of this document summarizes available procedures for source sampling and analysis of toluene. The summaries provide an overview of applicable sampling and analytical

2-1

procedures, citing references for those interested in conducting source tests. Although a NIOSH procedure is provided, no EPA endorsement of this method is given or implied.

Appendix A identifies potential source categories of toluene emissions by Standard Industrial Classification (SIC) code and associated description. These potential source categories do not necessarily denote significant sources of toluene emissions. The readers interested in cross referencing SICs with Source Classification Codes (SCCs) and associated descriptions should consult the Crosswalk/Air Toxic Emission Factor Database Management System, Version 1.2 (October 1991) and/or the Volatile Organic Compound (VOC)/Particulate Matter (PM) Speciation Database Management System, Version 1.4 (October 1991).1,2 Appendix B lists paint and ink manufacturing facilities and printing facilities with sales greater than $1,000,000. Appendix C contains a listing of some of the surface coating operations using toluene-containing coatings. Appendix D summarizes, in table format, all the emission factors listed in this document.

Each emission factor listed in Sections 3.0 through 7.0 has been assigned an emission factor grade based on the criteria for asg data quality and emission factor ratings as required in the document Technical Procedures for Developing AP-42 Emission Factors and Preparing AP-42 Sections. These criteria for rating test data used to develop emission factors are presented below.3 The data used to develop emission factors are rated as follows: A -

Tests performed by a sound methodology and reported in enough detail for adequate validation. These tests are not necessarily EPA reference test methods, although such reference methods are certainly to be used as a guide.

B -

Tests that are performed by a generally sound methodology but lack enough detail for adequate validation.

C -

Tests that are based on a nonvalidated or draft methodology or that lack a significant amount of background data.

D -

Tests that are based on a generally unacceptable method but may provide an order-of-magnitude value for the source.

Because of the almost impossible task of asg a meaningful confidence limit to industry-specific variables (e.g., sample size vs. sample population, industry and facility 2-2

variability, method of measurement), the use of a statistical confidence interval for an emission factor is not practical. Therefore, some subjective quality rating is necessary.

The following

emission factor quality ratings are applied to the emission factor tables.

A - Excellent. The emission factor was developed only from A-rated test data taken from many randomly chosen facilities in the industry population. The source category* is specific enough to minimize variability within the source category population. B - Above average. The emission factor was developed only from A-rated test data from a reasonable number of facilities. Although no specific bias is evident, it is not clear if the facilities tested represent a random sample of the industries. As in the A rating, the source category is specific enough to minimize variability within the source category population. C - Average. The emission factor was developed only from A- and B-rated test data from a reasonable number of facilities. Although no specific bias is evident, it is not clear if the facilities tested represent a random sample of the industry. As in the A rating, the source category is specific enough to minimize variability within the source category population. D - Below average. The emission factor was developed only from A- and B-rated test data from a small number of facilities, and there may be reason to suspect that these facilities do not represent a random sample of the industry. There also may be evidence of variability within the source category population. Limitations on the use of the emission factor are footnoted in the emission factor table. E - Poor. The emission factor was developed from C- and D-rated test data, and there may be reason to suspect that the facilities tested do not represent a random sample of the industry. There also may be evidence of variability within the source category population. Limitations on the use of these factors are always footnoted. U - Unrated or Unratable. The emission factor was developed from suspect data with no ing documentation to accurately apply an A through E rating. A "U" rating may be applied in the following circumstances:4 -

a gross mass balance estimation QA/QC deficiencies found with C- and D-rated test data gross engineering judgement technology transfer

*Source category: A category in the emission factor table for which an emission factor has been calculated; generally a single process.

2-3

This document does not contain any discussion of health or other environmental effects of toluene. It does include a discussion of ambient air monitoring techniques; however, these ambient air monitoring methods may require modifications for stack sampling and may affect data quality.

EPA recently acquired air toxics emissions information from the California Air Resources Board (CARB) as part of the California Rule AB-2588. The AB-2588 regulations allow for facilities to perform pooled source testing. The tests may be used to derive emission factors for all sources of the same type. Several of the pooled source test reports contain information on toluene emissions; however, the reports were unavailable when this document was prepared.5

Information from the Toluene section of the SRI Chemical Economics Handbook was also unavailable. This source is believed to contain the most recent production information and would be useful in confirming toluene facilities, capacities, and production processes.

2-4

2.1

REFERENCES FOR SECTION 2.0

1.

U.S. Environmental Protection Agency. Crosswalk/Air Toxic Emission Factor Database Management System, Version 1.2. Office of Air Quality Planning and Standards. Research Triangle Park, NC. October 1991.

2.

U.S. Environmental Protection Agency. Volatile Organic Compound (VOC)/Particulate Matter (PM) Speciation Database Management System, Version 1.4. Office of Air Quality Planning and Standards. Research Triangle Park, NC. October 1991.

3.

U.S. Environmental Protection Agency. Technical Procedures for Developing AP-42 Emission Factors and Preparing AP-42 Sections, Draft Document. Office of Air Quality Planning and Standards. Research Triangle Park, NC. March 1992.

4.

Group discussion meeting on applying "U" rating to emission factors. Anne Pope, EIB; Robin Baker Jones, Midwest Research Institute; Garry Brooks, Radian Corporation; and Theresa Moody, TRC Environmental Corporation.

5.

Memorandum from Theresa K. Moody and Candace R. Blackley, Radian Corporation, to Anne Pope, EIB, Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, "Evaluating California Air Toxics Emissions Data for Air Toxics Compounds," February 28, 1992.

2-5

SECTION 3.0 BACKGROUND

3.1

NATURE OF POLLUTANT

Toluene is a man-made aromatic hydrocarbon produced mostly from petroleum. This chemical intermediate is the predominant feedstock in benzene production and a key octaneboosting component for gasoline blending. Toluene is also used as a raw material in the production of other chemicals (e.g., toluene diisocyanate and benzoic acid) and as a solvent in paints and coatings, inks, adhesives, and pharmaceuticals.1

Toluene’s molecular formula is C6H5CH3; its molecular structure is represented as:

Table 3-1 summarizes the chemical identification information for toluene, and Table 3-2 presents toluene’s chemical and physical properties. This colorless liquid is volatile, flammable, and explosive in air. Toluene will react with airborne hydroxyl radicals (OH-), atomic oxygen (O), ozone (O3), and peroxy radicals (RO2) where R is an alkyl or aryl group to form a variety of oxidation products. Toluene is not corrosive and will not react with dilute acids or bases. Purified toluene (nitration grade) normally contains less than 0.01 percent benzene, while the industrial grade may contain up to 25 percent benzene.2

Toluene is released in the environment from several man-made sources, including the following:2 •

inadvertent sources (65 percent), such as emissions from motor vehicles and aircraft exhaust, losses during gasoline marketing activities, chemical spills, and cigarette smoke

TABLE 3-1.

CHEMICAL IDENTIFICATION OF TOLUENE Chemical name

Toluene

Synonyms

Methylbenzene; toluol; phenylmethane; methacide; methylbenzol

Molecular formula

C6H5CH3

Identification numbers:a CAS Registry NIOSH RTECS EPA Hazardous Waste OHM/TADS DOT/UN/NA NCI STCC a

108-88-3 XS 5250000 U220 7216928 UN 1294; Toluene (Toluol) C07272 49 093 05; Toluene

CAS (Chemical Abstract Services); NIOSH (National Institute of Occupational Safety and Health); RTECS (Registry of Toxic Effects of Chemical Substances); EPA (Environmental Protection Agency); OHM/TADS (Oil and Hazardous Materials/Technical Assistance Data System); DOT/UN/NA (Department of Transportation/United Nations/North America); NCI (National Cancer Institute); STCC (Standard Transport Commodity Code)

Source: References 3-5

3-2

TABLE 3-2.

PHYSICAL AND CHEMICAL PROPERTIES OF TOLUENE Property

Value

Molecular weight (grams) Melting point Boiling point (760 mm Hg)

92.14 -95 to -94.5°C (-139 to -138.1°F) 110.63°C (231.13°F)

Density, g/cm3 at 25°C (77°F) at 20°C (68°F)

0.8623 0.8667

Physical state (ambient conditions) Color Odor

Liquid Clear Benzene-like

Odor threshold: Range

0.17 ppm 0.17 - 40 ppm

Solubility: Water at 20°C (68°F)

Very slightly soluble (0.05 g/100 mL)

Organic solvents

Miscible with absolute alcohol, ether, and chloroform Soluble in acetone

Partition coefficients: Log10 octanol/water

2.69 (at 20°C or 68°F)

Vapor pressure at 20°C (68°F) at 30°C (86°F) at 40°C (104°F)

21.9 mm Hg (2.92 kPa) 36.7 mm Hg (4.89 kPa) 59.3 mm Hg (7.91 kPa)

Auto ignition temperature Flashpointa

480°C (896°F) 4.4°C (40°F) (C.C.) 16°C (60.8°F) (O.C.)

Conversion factors (Vapor weight to volume)

1 ppm = 3.824 mg/m3 (at 20°C)

a

C.C. (closed cup); O.C. (open cup)

Source: References 3-5

3-3

•

processes in which toluene is used (33 percent)

•

toluene production (2 percent)

It is estimated that 86 percent of the toluene produced is eventually released into the biosphere (primarily the troposphere), where its lifetime ranges from 4 days (at high-altitudes during the summer) to several months (at low-altitudes during the winter). The average toluene half-life resulting from atmospheric oxidation is estimated to be 12.8 hours.2

Toluene released to water may be removed by activated sludge degradation, biodegradation, and/or volatilization. The expected evaporative half-life of toluene in water is approximately five hours in water one meter in depth (3.28 feet).2

3.2

OVERVIEW OF PRODUCTION AND USE

The total annual capacity of toluene manufacturing facilities in the United States, the Virgin Islands, and Puerto Rico was 5,344,000 megagrams (1,625 million gallons) in 1989.6 The majority of toluene (99.5 percent) is produced from petroleum fractions. Catalytic reformates, produced by catalytic reforming, for approximately 94.5 percent of the production capacity feedstocks. Pyrolysis gasolines, another petroleum feedstock, for an additional five percent of feedstock materials. Coke-oven light oil comprises the remaining 0.5 percent of production capacity. In 1989, 21 companies produced toluene at 30 manufacturing sites.1,6

Toluene is manufactured for use as an intermediate in the production of benzene (50 percent) and toluene diisocyanate (9 percent), for gasoline blending (34 percent), for solvents (5 percent), and for the production of miscellaneous chemicals (2 percent).1 As a solvent, toluene is used in paints and coatings, inks, adhesives, resins, pharmaceuticals, and other formulated products requiring a solvent carrier. Toluene is also used as a cleaning solvent in surface coating, printing, and the leather industry. In addition to benzene and toluene diisocyanate, toluene derivatives include benzoic acid, benzyl chloride, trinitrotoluene, vinyl toluene, toluenesulfonic acid, benzaldehyde, and toluenesulfonyl chloride.1,3 Figure 3-1 illustrates some

3-4

of the end uses of toluene. These uses are discussed in detail in Sections 5.0 and 6.0. A list of all potential toluene emission sources organized according to SIC code and associated description is presented in Appendix A.

It is important to note that these source categories do not

necessarily denote significant sources of toluene emissions, but only that these sources have the potential to emit toluene.

3-5

3.3


1.

Toluene Chemical Product Synopsis, Mannsville Chemical Products Corp., Asbury Park, NJ. March 1990.

2.

International Programme on Chemical Safety. Environmental Health Criteria 52: Toluene. World Health Organization. Geneva. 1985.

3.

Kirk-Othmer Encyclopedia of Chemical Technology. 3rd edition. Toluene. Volume 23. John Wiley and Sons. New York, NY. pp. 246-273. 1983.

4.

Environmental Protection Service, Environment Canada. Environmental and Technical Information for Problem Spills: Toluene. Technical Services Branch. Beauregard Press Limited, Minister of Supply and Services Canada. 1984.

5.

Sax, Irving N. and Richard J. Lewis, Sr., Dangerous Properties of Industrial Materials. Seventh Edition. Volume III. Van Nostrand Reinhold. New York, NY. p. 3287. 1989.

6.

SRI International Directory of Chemical Manufacturers. Chemical Economics Handbook. Menlo Park, CA. 1991.

3-7

SECTION 4.0 EMISSIONS FROM TOLUENE PRODUCTION

Toluene production and the associated air emissions are described in this section. Process flow diagrams are included as appropriate, with specific streams or vents in the figures labeled to correspond with the discussion in the text. Emission factors for the production processes are presented when available, and associated control technologies are described. If a particular facility is being included in an inventory, the reader should the specific facility to the nature of the processes used, production volume, and controls that are in place before applying any of the emission factors presented in this document.

Toluene is currently produced by 21 companies at 30 plants in the United States, the Virgin Islands, and Puerto Rico. The production locations and capacities are presented in Table 4-1.1 In 1991, 3,104,000 megagrams (944 million gallons) of toluene were recovered compared with a 1989 total annual capacity of approximately 5,344,000 megagrams (1,625 million gallons).1,2 In 1989 eight facilities, representing seven companies, had annual capacities exceeding 55 million gallons. Collectively, Amoco, Exxon, BP, Sun, Amerada Hess, Phillips, Mobil, and Chevron ed for 72 percent of the total toluene capacity in the United States, the Virgin Islands, and Puerto Rico. The capacities listed in Table 4-1 are approximations, as most aromatics operations have some flexibility in the amount of toluene they recover. Table 4-1 also identifies the feedstock (e.g., catalytic reformate (reformate), coke-oven light oil, or pyrolysis gasoline) from which toluene is recovered.1

Although the domestic extraction and distillation capacity for toluene exceeds 4,932 millions of kilograms (1.5 billion gallons), the projected domestic demand for 1992 is only 2,795 millions of kilograms (850 million gallons) with growth expected to be very modest over the next few years.2 No growth or slight growth in toluene demand is anticipated because of the trend to remove aromatics from gasoline blending in favor of adding oxygenated octane enhancers.

If significant amounts of toluene are removed from the gasoline pool, toluene

surpluses will occur possibly resulting in lower prices and industry-wide containment difficulties. Use of toluene in most solvent and chemical applications has also slowed. Using toluene to 4-1

TABLE 4-1.

TOLUENE PRODUCTION LOCATIONS AND CAPACITIES

Facility

Location

1989 Capacity Millions of Kilograms (Millions of Gallons)

Feedstock

Amerada Hess Corporation

St. Croix, WI

460

(140) Reformate

American Petrofina Incorporated

Port Arthur, TX

170

(52) Reformate

Amoco Corporation

Texas City, TX

806

(245) Reformate

Ashland Oil, Inc.

Catlettsburg, KY

79 26

Atlantic Richfield Company

Channelview, TX

105

(24) Reformate (8) Coke-oven light oil

Houston, TX

99

(32) Pyrolysis gasoline (30) Reformate

BP America, Inc. (Sohio)

Alliance, LA Lima, OH

197 329

(60) Reformate (100) Reformate

Champlin Petroleum Co.

Corpus Christi, TX

99

(30) Reformate

Chevron Corporation

Philadelphia, PA Port Arthur, TX

79 92 39

(24) Reformate (28) Reformate (12) Pyrolysis gasoline

Dow Chemical U.S.A.

Freeport, TX

13

(4) Pyrolysis gasoline

Exxon Corporation

Baytown, TX

605

(184) Reformate

Kerr-McGee Corporation

Corpus Christi, TX

135

(41) Reformate

Koch Industries, Inc.

Corpus Christi, TX

247

(75) Reformate

Mobil Corporation

Beaumont, TX

148 16

Chalmette, LA

109

(45) Reformate (5) Pyrolysis gasoline (33) Reformate

Occidental Petroleum Corp.

Chocolate Bayou, TX (continued) 4-2

82

(25) Pyrolysis gasoline

TABLE 4-1.

TOLUENE PRODUCTION LOCATIONS AND CAPACITIES

Facility

Location

1989 Capacity Millions of Kilograms (Millions of Gallons)

Feedstock

Phillips Petroleum Company

Sweeny, TX Guayama, PR

95 243


Salomon Inc.

Houston, TX

46

(14) Reformate

Shell Oil Company

Deer Park, TX

164

(50) Reformate

Sun Company, Inc.

Marcus Hook, PA Toledo, OH Tulsa, OK

158 233 76

(48) Reformate (71) Reformate (23) Reformate

Texaco, Inc.

Delaware City, DE El Dorado, KS

135 36


Unocal Corporation

Beaumont, TX Lemont, IL

95 62


USX Corporation (Marathon)

Texas City, TX

66

(20) Reformate

Source: Reference 1 NOTE: This listing is subject to change as market conditions change, facility ownership changes, plants are closed down, etc. The reader should the existence of particular facilities by consulting current listings and/or the plants themselves. The level of toluene emissions from any given facility is a function of variables such as capacity, throughput and control measures, and should be determined through direct s with plant personnel. These operating plants and locations were current as of January 1989.

produce benzene via hydrodealkylation is one exception, as benzene demand is expected to grow at approximately three percent per year.3 Table 4-2 shows historical and projected figures for domestic toluene capacity, production, imports, exports and demand. Similarly, other countries anticipate a slow growth or decline in toluene production. Table 4-3 shows historical production in other industrialized nations.

4-3

TABLE 4-2.

ESTIMATED DOMESTIC U.S. SUPPLY AND DEMAND OF TOLUENE Millions of Kilograms (Millions of Pounds) By Year 1985

1986

1987

1988

1989

320 (705) .45 (1) 320 (705)

340 (749E) -- -340 (749)

439 (967) -- -439 (967)

397 (874) -- -397 (874)

365 (804E) -365 (804)

N/A

N/A

Imports

71 (157)

63 (138)

43 (95)

56 (123)

40 (87)

N/A

N/A

Exports

13 (28)

12 (27)

62 (136)

35 (76)

49 (108)

N/A

N/A

Demand

379 (834)

391 (860E)

421 (926)

419 (921)

356 (783)

364

Production Petroleum Coke Total

1990

(800)

1992

386

(850)

Since 1982 the United States International Trade Commission (USITC) has not reported toluene production by coke-oven operators. Coke-oven output has been insignificant since 1986. Sales data for toluene produced by petroleum refiners include only high-purity (98 to 100 percent) toluene. It is assumed that all indicated output is high purity. E - Estimated figure (Mannsville Chemical Products Corp.)3 N/A - Not available Source: Reference 3

Most of the toluene produced annually is derived from petroleum fractions. However, the concentration of light aromatics [e.g., benzene, toluene, and xylene (BTX)] in petroleum rarely exceeds one percent. Through processing, petroleum, specifically crude oil, can be converted to BTX streams. Several petroleum fractions are used in aromatic conversion processing. The fraction most important to the toluene production process is "straight-run light naphtha" which includes all of the crude oil components heavier than pentanes and up to a final boiling point between 105°C and 170°C (221° to 338°F).4 It is from this stream that the majority of toluene is produced by catalytic reforming via hydrotreating. A second refinery stream, also used as a feedstock in toluene production, is the naphtha that results from the pyrolysis or "steam cracking" (e.g., hydrocracking) of heavier distillate fractions. Although the primary goal of cracking naphtha is to manufacture ethylene and propylene, secondary reactions also produce considerable 4-4

TABLE 4-3.

WORLD-WIDE TOLUENE PRODUCTION Millions of Kilograms (Millions of Pounds) By Year

Country

1988

1989

47

(104)

34

a,b

605

(1,330)

538

Italyb

218

(480)

Japan

1,019 417

Canada

1990

(74)

%Change 1990-91

1991

34

(74)

(1,184)

418

(919)

460

(1,013)

10

152

(338)

192

(423)

165

(363)

-14

(2,242)

1,075

(2,365)

1,078

(2,372)

1,119

(2,462)

(917)

397

(873)

425

(935)

364

(801)

---

4 -14

a

Data are for the former West only. Data for 1991 are Chemical & Engineering News estimates based on nine months reporting. N/A - Not available b

Source: Reference 2

amounts of "pyrolysis gasoline" rich in aromatics.3-5 Additional toluene production methods include separation from coal tars and recovery as a by-product from styrene manufacture.3,5

4.1

TOLUENE PRODUCTION FROM PETROLEUM FRACTIONS

4.1.1

Hydrotreating

Hydrotreating, schematically illustrated in Figure 4-1, is the process by which the quality of liquid hydrocarbon streams is improved by subjecting them to mild or severe conditions of hydrogen pressure in the presence of a catalyst. Both pyrolysis gasolines and straight-run light naphthas (e.g., catalytic reformer feeds) undergo hydrotreating prior to subsequent processing and toluene recovery. The liquid petroleum feed is preheated (Step 1), heated in a furnace (Step 2), and combined with recycled hydrogen gas. The combined feed is ed through a reactor containing a catalyst bed where the hydrogenation reaction takes place (Step 3).6 Upon leaving the reactor, the stream is cooled and moved to a separator vessel where recycle or net hydrogen is removed (Step 4). The liquid then moves to a stabilizer or stripper which removes hydrogen, hydrogen sulfide, ammonia, water, organic compounds of arsenic and palladium, and light 4-5

hydrocarbons dissolved in the separator liquid (Step 5). The stripped, hydrotreated fraction is then routed to the next processing step, either catalytic reforming or secondary hydrogenation.7

4.1.2 Catalytic Reforming

Catalytic reformate is the major source of toluene, ing for approximately 87 percent of the toluene produced domestically and approximately 94.5 percent of the production capacity feedstocks.1,5 Catalytic reforming involves the catalytic dehydrogenation of straight-run light naphtha in the presence of hydrogen (which reduces coke formation) to yield a mixture of aromatic hydrocarbons (e.g., benzene, toluene, and the xylenes).4,5

The catalytic reforming

process is illustrated in Figure 4-2.

Prior to reforming, the light naphtha, containing the three primary toluene synthesis compounds dimethylcyclopentane, methylcyclohexane, and ethylcyclopentane, is hydrotreated to remove compounds that would act as catalyst poisons in the reforming step.4,6

The

hydrotreated naphtha is fed to the reformer unit containing the following components:4,7 •

reactors which contain fixed bed catalysts

•

heaters to bring the naphtha and recycle gas to reaction temperature and to supply heats of reaction

•

a product cooling system and a gas-liquid separator

•

a hydrogen-gas recycle system

•

a stabilizer to separate light hydrocarbons dissolved in the receiver liquid

The naphtha is combined with recycled hydrogen (Step 1), preheated (Step 2), heated to the reaction temperature in a fired heater (Step 3), and then transferred to a series of catalystcontaining reactors (Step 4).4 Because the reaction is endothermic, a series of three or four reactors with inter-stage reheat furnaces may be necessary to achieve the required conversion. The reactors normally contain increasing amounts of catalyst in each stage.4-6

4-7

The effluent from the last reactor is cooled and transferred to a receiving unit (e.g., the flash drum) where the hydrogen is separated from the liquid reformate (Step 5). The hydrogen gases are compressed and recycled to the reactors while the reformate is moved to a stabilizer fractionator (Step 6).

The fractionator removes C4 and lighter hydrocarbons to produce a

stabilized reformate. The stabilized reformate is used as a feedstock in the toluene recovery process (described in Section 4.1.4).4,7

Most of the facilities that produce toluene by catalytic reforming have proprietary processes. Table 4-4 lists the process licensor and the process name. The primary differences between these processes involve solving reforming process problems such as catalyst regeneration. The processes also differ in the methods used to extract aromatics depending on the type and purity of the product desired.4 TABLE 4-4.

CATALYTIC REFORMING PROCESSES Licensor

Name of Process

Chevron Research Co.

Rheniforming

Engelhard Industries

Magnaforming

Exxon Research Engineering

Powerforming

Houdry Division, Air Products

Houdriforming

Institut Francais du Petrole

Aromizing Catalytic Reforming

Standard Oil Co. (Indiana)

Ultraforming

UOP Process Division

Platforming

Source: Reference 4

4-9

4.1.3 Secondary Hydrogenation (for Pyrolysis Gasoline)

Pyrolysis gasoline, a by-product of ethylene and propylene manufacture, s for nine percent of domestic toluene production and five percent of production capacity feedstock materials.1,5 Because pyrolysis gasoline contains reactive compounds (e.g., diolefins and styrenes) which will polymerize if subjected to reactor conditions severe enough to saturate olefins and remove sulfur compounds, it must undergo an initial hydrogenation step described in Section 4.1.1 to reduce the reactives to olefins prior to storage or further processing. The resulting product can be used as a high octane gasoline blending component or treated further for aromatic (e.g. benzene, toluene, and xylenes) extraction.4

Following initial hydrogenation, the pyrolysis gasoline (containing 21 percent toluene) normally undergoes second stage hydrogenation in which olefins are saturated, organic sulfur forms hydrogen sulfide, combined nitrogen is converted to ammonia, and oxygenated compounds are reduced to hydrocarbons and water. After these parallel reactions have been completed, the gases and liquid are separated. The liquid (containing 38 percent toluene) is then stripped of gaseous impurities, such as hydrogen sulfide, and remaining light hydrocarbons before being transferred to toluene recovery units.4,7

Most of the world’s facilities that produce toluene from pyrolysis gasoline have proprietary hydrotreating processes. The primary differences between these processes involve operating parameters such as temperature, pressure, catalyst composition, and reactor geometry. Table 4-5 lists the process licensor and the process name.4

4.1.4 Toluene Recovery

The hydrotreated and/or catalytically reformed streams are rich in aromatics such as toluene, benzene, and the xylenes, as well as nonaromatics of similar boiling points. Therefore, the most appropriate procedures for separating toluene (and other aromatics) from other process streams are extractive distillation and liquid-liquid extraction.4,6 Liquid-liquid extraction is the most commonly used extraction method.5 If only one aromatic (e.g., benzene, toluene, or xylene) 4-10

TABLE 4-5.

PYROLYSIS GASOLINE HYDROGENATION PROCESSES Licensor

Name of Process

British Petroleum (BP)

BP Selective Hydrogenation Process

C-E Lummus

DPG Hydrotreating

Engelhard Industries

HPN Process

Houdry Division, Air Products

HPG Process

Institut Francais du Petrole

IFP Selective Hydrogenation Process

Lurgi GmbH/Bayer AG

Bayer Selective Diolefin Hydrogenation Lurgi Olefin Hydrogenation and Desulphurisation

UOP Process Division

LT Unibon Process

Source: Reference 4

is to be recovered in pure form, extractive distillation is preferred as the capital and operating expenses are less than those associated with liquid-liquid extraction.4 Figure 4-3 shows a process flow diagram for toluene recovery. The diagram includes prefractionation, extraction/ distillation, and benzene/toluene fractionation.

Liquid-liquid extraction methods are the most commonly used processes to recover toluene.

Two compounds commonly used in liquid-liquid extraction are sulfolane and

tetraethylene glycol. The sulfolane process was developed by Shell and is licensed by Universal Oil Products (UOP). Union Carbide developed and licensed the tetraethylene glycol method. These two processes have replaced the Udex process which used diethylene glycol as the extractant.5

Another commonly used liquid-liquid extraction method is dimethylsulfoxide

(DMSO) extraction, commercialized by the Institut Francais du Petrole. This process is different from the other processes in that aromatics are extracted twice, the first time using dimethylsulfoxide (DMSO) and the second time using a light hydrocarbon.4 4-11

The hydrotreated and/or catalytically reformed streams (crude BTX) are normally prefractionated prior to the recovery of toluene by liquid-liquid extraction to reduce the throughput of the extraction step. The crude BTX stream is first depentanized (Step 1) to remove the majority of components lighter than benzene (e.g., C5 and lower compounds) and then distilled (Step 2) to remove components heavier than o-xylene. The C5 compounds are removed for gasoline blending, while the xylenes fraction is processed for xylene recovery.

The

benzene/toluene fraction is fed to a cut column where the top portion is separated and moved to the extraction unit (Step 3). The bottoms are removed and further refined. Nonaromatics (the raffinate phase) leave through the top of the extractor while a mixture of aromatics, solvent and light nonaromatics leave through the bottom. The raffinate is sent to a water wash for removal of solvent. The aromatics/solvent and light nonaromatics stream is transferred from the extractor either directly to a stripper or to an extractive distillation column where nonaromatics are removed to be used later. The stripper removes solvent leaving an aromatic stream rich in toluene. (If only a stripper is used, then it acts as both an extractive distillation column and a solvent stripper, thereby reducing capital expenditures but requiring the facility to install a water washer to further reduce solvent content).4

Extractive distillation methods are preferred when only one aromatic (e.g., benzene, toluene, or xylene) is to be recovered in pure form. Extractive distillation methods separate components by introducing a solvent to a mixture. The solvent suppresses the relative vapor pressure of some components compared to other components in the mixture allowing the desired component to be extracted.4

The end result of the extractive distillation process description is very similar to that of the liquid-liquid extraction process. The crude BTX stream and the extractive solvent are fed to an extractive distillation column where nonaromatics (the raffinate) are separated (Step 3). The aromatic/solvent stream is transferred to a stripper which removes the solvent leaving the aromatic.

Some of the solvents commonly used in extractive distillation units are

dimethylformamide, n-formylmorpholine, m-methylpyrrolidone, and sulfolane.4

4-13

After a toluene-rich aromatic stream has been extracted from crude BTX by either liquidliquid extraction or extractive distillation, it can be further processed by conventional distillation to produce pure benzene and toluene. The benzene/toluene fraction is often moved through a clay treatment tower prior to further distillation to remove any trace olefins (Step 4). Benzene is removed from the top of the first distillation column (Step 5) while the distillation bottoms are fed to the toluene column. The purified toluene (99.8 percent) is taken from the top of the second distillation column (Step 6).4

4.1.5 Emissions

Most air emissions associated with toluene production from petroleum fractions arise from loading operations, toluene storage, and equipment leaks. Process vents may also contribute to air emissions. Toluene emissions from other sources, such as waste treatment and disposal facilities are discussed in Section 7.0.

Process Emissions-Figure 4-3 shows that during toluene production, process vent discharges (A) of toluene occur primarily from the vacuum column vents, the reactor process vents, and the reactor process recovery vent. The hydrogen separation vent is only used during startup, shutdown, and during recovery section outages.9,10 The vacuum column vents remove air that leaks into the column, as well as light hydrocarbons and hydrogen that form during dehydrogenation, noncombustibles dissolved in the column feed, and any entrained aromatics. The majority of toluene emissions occur at the benzene and toluene columns in the distillation train.

Other sources of process emissions from toluene production are less likely because of the need to operate most processes under a vacuum and because of the heating value of the gases. The available emission estimates for toluene production are given in Table 4-6.

Little

information was found on specific emission controls. Several types of recovery devices are used in the Synthetic Organic Chemical Manufacturing Industry (SOCMI) to recover hazardous air pollutants including toluene. These control methods include condensers, absorbers, adsorbers,

4-14

and incinerators. Recovery devices are used to recover products or by-products for sale or reuse.9,10

TABLE 4-6.

EMISSION FACTORS FOR TOLUENE PRODUCTION FROM PETROLEUM FRACTIONS Emission Source

Emission Factor

Quality Ratinge

Storage tank working losses, Toluene recoverya

0.66 lb/1000 gallon (0.079 kg/1000 liter) throughput

U

Storage tank breathing losses, Toluene recoverya


U

Toluene recovery, General process emissionsb

1.7 x 10-4lb/lb toluene produced

U

Toluene recovery, Storageb


U

Toluene recovery from catalytic formate, cracking unitb


U

Fugitives from petroleum refining with cracking and reformingb,c

21 lb toluene/ton (10.5 g/kg) total hydrocarbon

U

Fugitives from petroleum refining without cracking and reformingb,d

21 lb toluene/ton (10.5 g/kg) total hydrocarbon

U

a

Reference 12 Reference 14, 15. c Assumes fugitives are 1.05 percent toluene. d Assumes fugitives are 0.105 percent toluene. e Based on engineering judgement. b

Storage Emissions-Other possible sources of toluene emissions are storage tank losses (B) and handling losses (C) that occur during product loading into drums, tank trucks, tank cars, barges, or ships. Storage tank losses including working losses that occur while filling the tank, and breathing 4-15

losses due to expansion from temperature changes. The calculations to determine emissions from storage tanks are complex and require a knowledge of a number of factors which are plant specific. Equations for storage tank emissions are given in the U.S. Environmental Protection Agency’s report titled Estimating Air Toxics Emissions from Organic Liquid Storage Tanks (EPA450/4-88-004).11 In the absence of specific data on the storage tank, two emission factors were identified in the literature.12 Both emission factors are shown in Table 4-6. No information was available regarding the use of floating roof tanks or any other control techniques on storage tanks.

Equipment Leak Emissions-Emissions occur from process equipment components whenever the liquid or gas streams leak from the equipment. Equipment leaks can occur from the following components: pump seals, process valves, compressor seals and safety relief valves, flanges, open-ended lines, and sampling connections. Emission estimates can be calculated in the five ways described in the EPA publication Protocols for Generating Unit-Specific Emission Estimates for VOC and VHAP (EPA-450/3-88-010).13 The methods differ in complexity; however, the more complex, the more accurate the emission estimate.

The simplest method requires that the number of each component type be known. Furthermore, for each component, the toluene content of the stream and the time the component is in service is needed. This information is then multiplied by the EPA’s average emission factors for the Synthetic Organic Chemical Manufacturing Industries (SOCMI) shown in Table 4-7. This method should only be used if no other data are available, as it may result in an overestimation of actual equipment leak emissions. For each component, estimated emissions are:13 No. of equipment components

X

Weight % toluene in the stream

X

Componentspecific emission factor

X

No. hrs/yr in toluene service

More complex methodologies may be used to obtain more accurate equipment leak emission estimates.

However, these methodologies require that some level of emission

measurements (leak concentrations) be made for the facility’s process equipment components. These methodologies are briefly described here, and the reader is referred to the EPA Protocols 4-16

TABLE 4-7.

AVERAGE EMISSION FACTORS FOR FUGITIVE EQUIPMENT LEAK EMISSIONS

Service

Emission Factor (kg/hr/source)

Valves

Gas Light Liquid Heavy Liquid

0.0056 0.0071 0.00023

0.0123 0.0157 0.00051

U

Pump Seals

Light Liquid Heavy Liquid

0.0494 0.0214

0.1089 0.0472

U

Compressor Seals

Gas/Vapor

0.228

0.5027

U

Pressure Relief Seals

Gas/Vapor

0.104

0.2293

U

Equipment

Emission Factor (lb/hr/source)

Quality Ratinga

Flanges

All

0.00083

0.0018

U

Open-Ended Lines

All

0.0017

0.0037

U

Sampling Connections

All

0.0150

0.0331

U

a

Based on engineering judgement. Source: Reference 13

document or Fugitive Emission Sources of Organic Compounds--Additional Information on Emissions, Emission Reductions, and Costs for calculation details.13,14

The first method, the leak/no leak approach, is based on a determination of the number of leaking and nonleaking components. A leaking component is defined by a measured or estimated leak concentration greater than or equal to 10,000 ppmv.13 Once the number of leaking/nonleaking equipment components have been determined, the fugitive equipment leak emissions are estimated using the appropriate emission factors and the equation identified previously for the average emission factor method.

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The second method differentiates fugitive equipment leak emissions into three leak concentration ranges: 0 - 1,000 ppmv; 1,000 - 10,000 ppmv; and greater than 10,000 ppmv. The number of components falling into a particular range is then multiplied by the component-specific emission factor for that range. The component-specific emission factors can be found in EPA’s Protocols document.13

The third method uses screening data in correlation equations derived by EPA. Correlation equations are only available for flanges, pump seals, and valves in light-liquid and gas service. Finally, the fourth complex method gives each facility an option to develop its own correlation equations, but requires more rigorous testing, bagging, and analysis of equipment leaks to determine mass emission rates.14

Although no specific information on emissions controls used by the industry was identified, equipment components in toluene service typically have some type of control. Generally, control of fugitive emissions requires the use of low-emission or emissionless process equipment, an inspection and maintenance program, and routine replacement of chronic leaking components. Typical controls for equipment leaks are listed in Table 4-8.14 In addition, other leakless process equipment is available such as leakless valves and sealless pumps.

4.2 TOLUENE PRODUCTION FROM COAL

Toluene can also be recovered from coal products, although coal is no longer an important source of toluene. When coal is carbonized (e.g., heated in the absence of air) in coke ovens or horizontal retorts, it produces coke residue and volatile matter consisting of gas, tar, and water. Both the coal tar and the coal gas contain small amounts of toluene which can be separated through extraction processes. The coal gas is normally scrubbed with an oil of coal tar or an oil of petroleum origin. These oils absorb the hydrocarbons entrained in the coal gas. The oil can then be distilled and the aromatics recovered as crude benzene.4,6

Crude benzene can be refined either by acid washing or hydrorefining. Hydrorefining is the more commonly used method.

The two methods of hydrorefining are the Lurgi 4-18

TABLE 4-8.

CONTROL TECHNIQUES AND EFFICIENCIES APPLICABLE TO EQUIPMENT LEAK EMISSIONS Equipment Component (Emission Source) Pump Seals Packed and mechanical

Double mechanicalc Compressors Flanges Valves Gas

Liquid

Pressure Relief Devices Gas Sample Connections Open-ended Lines

Control Technique Seal area enclosure vented to a combustion device Monthly LDARb Quarterly LDAR Semiannual LDAR Annual LDAR N/Ad Vent degassing reservoir to combustion device None available Monthly LDAR Quarterly LDAR Semiannual LDAR Annual LDAR Monthly LDAR Quarterly LDAR Semiannual LDAR Annual LDAR Monthly LDAR Quarterly LDAR Rupture Disk Closed-purge sampling Caps on open ends

a b c

Percent Reduction 100a 61 32 0 0 -100a 0 73 64 50 24 59 44 22 0 50 44 100 100 100

Combustion devices approach 100 percent control efficiency. LDAR (Leak detection and repair program). Assumes the seal barrier fluid is maintained at a pressure above the pump stuffing box pressure and the system is equipped with a sensor that detects failure of the seal and/or barrier fluid system. d N/A (Not applicable). There are no VOC emissions from this component. Source: Reference 14

4-19

Hydrorefining® process and the Houdry Litol Hydrorefining® process.4 Many of the process steps described in the next two paragraphs are the same as those encountered in the previous section, Toluene Production from Petroleum Fractions. The reader should refer to Section 4.1 for further detail.

4.2.1 Process Descriptions Crude benzene, in the Lurgi Hydrorefining® process, is preheated, vaporized and ed through a reactor where hydrodesulfurization, saturation of hydrocarbons, and reduction of oxygen- and nitrogen-containing compounds occurs.

The reactor products are cooled and

condensed with the condensed hydrocarbon stream undergoing stripping of hydrogen sulfide. The clean hydrotreated stream, the raffinate, is fed to an extractive distillation unit where a toluene mixture is separated from nonaromatics also in the raffinate. The toluene mixture then es to a recovery column where high purity toluene is recovered.4 In the Houdry Litol Hydrorefining® process, the crude benzene is first prefractioned as described previously in Section 4.1.4 Toluene Recovery. The prefractionated distillate, containing approximately 17 percent by weight toluene, is mixed with hot hydrogen gas and vaporized. The stream es to a reactor where olefins are saturated and hydrogen sulfide and butane are produced. The resulting process stream moves to the Lithol reactor where desulfurization, hydrocracking and dealkylation take place. The reactions in the Lithol reactor are exothermic and must be moderated by heat exchangers. After leaving the Lithol reactor, the stream moves to a flash drum where aromatic hydrocarbons are separated, condensed, and forwarded to a stabilizer, a clay tower, and then the benzene tower. The final fractionation takes place in the toluene tower which yields pure toluene.4

Several new methods have been developed by which toluene can be produced from coal. Many of these new processes come from the liquification of coal and are still in the developmental stages. One process, the South African Coal, Oil, and Gas Corporation (SASOL) operation has proven commercially feasible in South Africa. These processes, if successful, could

4-20

lead to coal refineries that manufacture many of the products currently available from petroleum refineries.4

4.2.2 Emissions

No information was located in the literature that discussed process emission sources from toluene production from coal feedstocks. Emissions are expected to be similar to those occurring from petroleum feedstocks where the equipment in use is the same. An overall emission factor for coke manufacture is shown in Table 4-9.

TABLE 4-9.

EMISSION FACTORS FOR TOLUENE PRODUCTION FROM COAL Emission Source Coke manufacture, Coke oven

Emission Factor

Quality Ratinga

2.4 x 10-4lb/lb coke produced

U

a

Based on engineering judgement. Source: Reference 14.

4.3 TOLUENE PRODUCTION FROM STYRENE

Toluene is a by-product in the production of styrene from ethylbenzene by dehydrogenation. Small amounts of toluene are also produced as a styrene by-product via the isothermal production process. However, because the isothermal method is not currently used in the United States and emissions of toluene are minimal from this process, it will not be discussed in this document. Additional information on the isothermal process can be found in Locating and Estimating Air Emissions from Sources of Styrene (EPA-450/4-91-029).8

4-21

4.3.1 Process Description

In the dehydrogenation process shown in Figure 4-4, purified ethylbenzene is preheated in a heat exchanger (Step 1), and the resultant vapor is mixed continuously with steam at 710°C (1310°F) in the dehydrogenation reactor (Step 2) that contains one of several catalysts. The reaction product exits through the heat exchanger and is further cooled in a condenser (Step 3) where water and crude styrene vapors are condensed. The hydrogen-rich process gas is recovered (Step 4) and used as a fuel and the process water is purified in a stripper (Step 5) and recycled to the boiler. The remaining crude liquid styrene goes to a storage tank (Step 6). The liquid consists of styrene (37 percent), ethlybenzene (61 percent), toluene (1 percent), benzene (0.7 percent), and tars (0.3 percent). Benzene and toluene are removed from the crude styrene in the benzene/toluene column (Step 7). They are then typically separated by distillation (Step 8). The toluene is normally sold, while the benzene is returned to the ethylbenzene production section or sold. In some facilities, an ethylbenzene/benzene/toluene stream is separated from the crude styrene initially (at step 6) and processed separately.

4.3.2 Emissions

Emission factors for the production of toluene from styrene production are shown in Table 4-10. These emission factors were based on engineering judgement, and are therefore given ratings of "U."

The emission factor for styrene purification came from engineering

calculations at one facility, while the two factors for production process and production fugitive emissions were based on typical composition and design information from two emission sources.14

4-22

TABLE 4-10.

EMISSION FACTORS FOR TOLUENE PRODUCTION FROM STYRENE PRODUCTION Emission Source

Emission Factor

Quality Ratingc

Styrene production process emissionsa

3.04 lb/ton (1.52 g/kg) styrene produced

U

Styrene purification process emissions, Styrene productiona

2.34 lb/ton (1.17 g/kg) styrene produced

U

Styrene production fugitive emissionsa

22,840 lb (10,358 kg)/process unit, annually

U

Storage Tank working lossesb


U

Storage Tank breathing lossesb


U

a

Reference 14 Reference 12 c Based on engineering judgement. b

4-24

4.4 REFERENCES FOR SECTION 4.0 1.

SRI International. Chemical Economics Handbook. Menlo Park, CA. 1991.

2.

Facts and Figures. Chemical & Engineering News 70(26). pp 35-39, 66-75. 1992.

3.

Toluene Chemical Product Synopsis. Mannsville Chemical Products Corp. Asbury Park, NJ, March 1990.

4.

Hancock, E.G., ed., Toluene, the Xylenes and their Industrial Derivatives. Elsevier Scientific Publishing Company. New York, NY. 1982.

5.

Kirk-Othmer Encyclopedia of Chemical Technology. 3rd edition. Toluene. Volume 23. John Wiley and Sons. New York, NY. pp. 246-273. 1983.

6.

Faith, Keyes, and Clark’s Industrial Chemicals. Fourth Edition. 1975.

7.

Considine, Douglas M., ed., Chemical and Process Technology Encyclopedia. McGrawHill, Inc. pp. 603-606, 975-979, 1104-1106. 1974.

8.

U.S. Environmental Protection Agency. Locating and Estimating Air Emissions from Sources of Styrene, Interim Report, EPA-450/3-90-020. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1991.

9.

U.S. Environmental Protection Agency. Locating and Estimating Air Emissions from Sources of Benzene, EPA-450/4-84-007q. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1988.

10.

U.S. Environmental Protection Agency. Reactor Processes in Synthetic Organic Chemical Manufacturing Industry - Background Information for Proposed Standard, EPA-450/3-90016a. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1990.

11.

U.S. Environmental Protection Agency. Estimating Air Toxics Emissions from Organic Liquid Storage Tanks, EPA-450/4-88-004. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1988.

12.

U.S. Environmental Protection Agency. Criteria Pollutant Emission Factors for the 1985 NAPAP Emissions Inventory, EPA-600/7-87-015. Air and Energy Engineering Research Laboratory. Research Triangle Park, NC 27711. 1987.

13.

U.S. Environmental Protection Agency. Protocols for Generating Unit-Specific Emission Estimates for Equipment Leaks of VOC and VHAP, EPA-450/3-88-010. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1988.

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14.

U.S. Environmental Protection Agency. Fugitive Emission Sources of Organic Compounds--Additional Information on Emissions, Emission Reductions, and Costs. EPA-450/3-82-010. Office of Air Quality Planning and Standards. Research Triangle Park, NC. April 1982.

15.

U.S. Environmental Protection Agency. Toxic Air Pollutant Emission Factors - A Compilation for Selected Air Toxic Compounds and Sources, EPA-450/2-88-006a. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1988.

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SECTION 5.0 EMISSIONS FROM MAJOR USES OF TOLUENE

This section discusses emissions from major industrial processes that use toluene as a solvent or feedstock.

The processes described are the production of benzene, toluene

diisocyanate (TDI), trinitrotoluene (TNT), benzoic acid, and benzyl chloride. In addition, product and process descriptions are provided for uses of toluene in solvent applications, such as paint and ink manufacturing and solvent cleaning operations. The application of toluene containing paints, coatings, and inks will be discussed in Section 6.0. Process flow diagrams are included as appropriate, with specific streams or vents in the figures labeled to correspond with the discussion in the text.

Emissions of toluene are expected from all facilities involved in the previously mentioned operations.

However, insufficient information is available to develop emission factors for

fugitives or process emission sources. Available information is provided in each subsection. The reader is encouraged to the Toxic Chemical Release Inventory (TRI) and specific production facilities for information on toluene emissions and control technologies. It should be noted, however, that TRI emission estimates may be based upon engineering estimates, may include accidental releases, and, therefore, may not be reliable.

Residual emissions from toluene-containing materials are discussed separately in Section 6.0.

Toluene emissions resulting as a by-product of another process (by-product

emissions) are discussed in Section 7.0.

5.1

BENZENE PRODUCTION

Benzene can be produced from catalytic reformate, pyrolysis gasoline, coke-oven light oil, or from toluene by hydrodealkylation (HDA) and disproportionation. Benzene production directly from toluene s for approximately 25 percent of the total benzene produced.1 Major derivatives of benzene, ing for 98 percent of benzene end uses, include ethylbenzene (for styrene), cumene (for phenol), cyclohexane, nitrobenzene (for aniline), chlorobenzene, and 5-1

alkylbenzenes (for detergents).2 In addition, approximately two percent of the benzene produced is used as a solvent or feedstock in the following industries and products: laboratories, metal degreasing, pharmaceuticals manufacture, alcohols production, textiles, and miscellaneous small volume chemicals.2,3

Thirteen companies at eighteen facilities currently produce benzene by toluene hydrodealkylation or disproportionation. These facilities and their 1989 production capacities are listed in Table 5-1.1 The manufacture of benzene s for 50 percent of toluene end use.4


Benzene may be produced from toluene through HDA or disproportionation. Hydrodealkylation of toluene can be accomplished through thermal or catalytic processes. The total dealkylation capacity is almost evenly distributed between the two methods. As shown in Figure 5-1, pure toluene (92 to 99 percent), or toluene (85 to 90 percent) mixed with other aromatics or paraffins is heated to 730°C (1,346°F) at a specified pressure (Step 1) and is charged to the reactor (Step 2) in the presence of excess hydrogen.1,3 Toluene reacts with the hydrogen, either by thermal initiation or with a dealkylation catalyst, to yield benzene and methane. The benzene may be separated from the methane in a low pressure separator (Step 3) by flashing off the methane-containing gas. The product is then stabilized (Step 4) and benzene is recovered by distillation (Step 5). Benzene is sent to storage (Step 6). Unreacted toluene and some heavy by-products are recycled (Step 7). Approximately 70 to 85 percent conversion of toluene to benzene is accomplished per through the system, and the ultimate yield is 95 percent of the theoretical yield.3 Many facilities that produce benzene from petroleum sources also have the ability to produce benzene from toluene via HDA. The HDA process is reported to be economically feasible when low-cost hydrogen is available and when benzene is valued at approximately 30 cents per gallon more than toluene.1,2

5-2

TABLE 5-1.

BENZENE PRODUCERS USING TOLUENE FEEDSTOCK

Facility

Location

1989 Capacity millons of kilograms (millions of gallons)

Amerada Hess Corporation

St. Croix, VI

American Petrofina Incorporated

Port Arthur, TX

109 (33)

Disproportionation

Arochem International

Penuelas, PR

115 (35)

HDA

BP America, Inc. (Sohio)

Alliance, LA Lima, OH

155 (47) 263 (80)

HDA HDA

Chevron Corporation

Philadelphia, PA Port Arthur, TX

46 (14) 164 (50)

HDA HDA

Coastal Refining and Marketing

Corpus Christi, TX

53 (16)

HDA

Dow Chemical U.S.A.

Freeport, TX Plaquemine, LA

82 (25) 395 (120)

HDA HDA

Hoechst Celanese

Bayport, TX

49 (15)

HDA

Koch Industries, Inc.

Corpus Christi, TX

197 (60)

HDA

Lyondell Petrochemical Co. Houston, TX

N/A

Production Method

49 (15)

Disproportionation

Disproportionation

Occidental Petroleum Corp. Chocolate Bayou,TX Corpus Christi, TX

132 (40) 99 (30)

HDA HDA

Phillips Puerto Rico Core Inc.

Guayama, PR

161 (49)

HDA

Sun Company, Inc.

Marcus Hook, PA Tulsa, OK

Source: Reference 1 N/A = Not Available HDA = hydrodealkylation

5-3

36 (11) 66 (20)

Disproportionation HDA

Toluene disproportionation, or transalkylation, catalytically converts two molecules of toluene to one molecule each of benzene and xylenes, as indicated by the reaction:5

The transalkylation process is similar to that of toluene HDA but occurs under less severe conditions (e.g., the transalkylation process operates at lower temperatures and consumes less hydrogen). Toluene is heated, combined with hydrogen, and sent to the reactor. The reacted material is moved to a separator for removal of off-gases. The product is stabilized and moved through clay towers. Benzene, toluene, and xylenes are recovered by distillation and unreacted toluene is recycled.2,3 Toluene disproportionation is used when the desired product is xylene. If benzene is the only product required, then HDA is a more economical and feasible process.1

5.1.2 Emissions

Facilities manufacturing benzene emit toluene from process equipment vents, open process equipment, equipment leaks, storage tank vents, secondary sources, and transfer and handling operations. No specific emissions data for any of these sources are available; however, it has been estimated that 5.0 x 10-5 pounds of toluene are emitted for every pound of toluene used in the benzene manufacturing process.6

5-5

Process equipment sources include heaters, reactors, separation tanks, stabilization columns, distillation columns, and the toluene recovery system.

The emissions will vary

according to the type of process used (e.g., HDA or disproportionation) and the percentage of toluene in the raw material feed stream.

To control process vent emissions, the process streams can be routed to a flare or blowdown tank. Recovered toluene emissions from the distillation column are recycled with the reactor feed stream. Where feasible, open equipment may be enclosed.

Sources of fugitive emissions and emission estimation procedures are discussed in Section 4.0. Also included in Section 4.0 is a table of emission control options and efficiencies.

A significant source of toluene air emissions occurs from toluene transfer during the loading and unloading of trucks, tank cars, and barges and the filling of toluene storage tanks. Losses of toluene from storage tanks may also occur due to normal tank working and breathing losses. Toluene emissions from storage tanks are discussed in Section 4.1.5 under the topics of Storage and Fugitives.

5.2

TOLUENE DIISOCYANATE PRODUCTION

Toluene diisocyanate (TDI) is produced by a reaction sequence in which toluene is dinitrated to form dinitrotoluene. Dinitrotoluene is hydrogenated to form 2,4-diaminotoluene which is treated with phosgene to yield two isomers of toluene diisocyanate 2,4-TDI and 2,6-TDI. Commercial toluene diisocyanates are available in three isomer ratios.

The majority of

commercially used TDI is a mixture of 80 parts of the 2,4-TDI isomer and 20 parts of the 2,6TDI isomer. A 65:35 mixture of the 2,4- and 2,6-TDI isomers is also available, as is pure TDI (greater than 99.5 percent 2,4-TDI).5,7 Either nitration-grade toluene or highly refined toluene (99.95+ percent) is used as the basic feedstock by most TDI manufacturers.8

Toluene diisocyanates are industrial intermediates used in the production of polyurethane foams, paints, varnishes, elastomers, and coatings. Rigid polyurethane foams, ing for 5-6

about five percent of TDI demand, are used as insulation in refrigeration equipment.9 Flexible polyurethane foams, used in furniture cushioning, transportation (e.g., automotive seating), bedding, packaging, and carpet underlay, for approximately 90 percent of the use of toluene diisocyanates.7 Little or no growth in production of TDI is expected for several reasons. Methyl diphenyl diisocyanate (MDI) is replacing TDI in many polyurethane foam applications. TDI can react violently with compounds containing an active hydrogen atom.7

Toluene diisocyanate is currently produced by five companies at six facilities in three States.

These facilities and their 1990 production capacities are listed in Table 5-2.9

Manufacture of toluene diisocyanates s for nine percent of toluene end use.4 TABLE 5-2.

TOLUENE DIISOCYANATE PRODUCTION LOCATIONS AND CAPACITIES

Facility

Location

1990 Capacity Millions of Kilograms (Millions of Pounds)

BASF Corp.

Geismar, LA

73

(160)

Dow Chemical

Freeport, TX

63

(140)

ICI Americas

Geismar, LA

32

(70)

Mobay

New Martinsville, WV

45

(100)

Mobay

Baytown, TX

61

(135)

Olin

Lake Charles, LA

88

(195)

Source: Reference 9

5-7

Figure 5-2 illustrates the basic operations that may be used in toluene diisocyanate production. The first step in the manufacture of TDI is the nitration of toluene (Step 1). Nitration grade toluene is reacted with nitric acid to form DNT. The reaction takes place at 65° to 80°C (149° to 176°F) in a well-agitated reactor equipped with cooling coils using sulfuric acid (60 to 70 percent) as the catalyzing agent.10 The spent sulfuric acid is separated from the DNT reaction mixture, concentrated in a direct evaporator, and recycled to the nitration reactor (Step 2).8

The DNT is washed in a wash tank (Step 3) and then reacted with hydrogen in catalytic reduction reactors (Step 4), using precious metal, nickel, or carbon catalysts, to form crude TDA. The hydrogenation of DNT normally occurs in an inert diluent (e.g., an alcohol) to avoid explosion hazards and to control the heat resulting from the exothermic process. The crude TDA is purified by filtration and distillation (Step 5).8,10

TDA is reacted with phosgene in a solvent, usually o-dichlorobenzene or mono-chlorobenzene to form crude TDI and hydrogen chloride (HCl) (Step 6). Phosgene is condensed out of the HCl by-product and recycled to the reactor. Crude TDI is sent to a distillation column for the removal of residual phosgene (Step 7). After a series of distillation and condensation steps, the phosgene (from the crude TDI) is recycled to the phosgenation reactor. The crude TDI still contains some of the chlorobenzene solvent in which it was reacted. This mixture (TDI and solvent) is transferred to a vacuum distillation column where the solvent is recovered and recycled (Step 8). The remaining crude TDI is vaporized by vacuum flash distillation to separate TDI from any polymeric isocyanates that may have formed (Step 9). The TDI is then condensed and sent to a vacuum distillation column from which purified TDI is removed (Step 10). The purified TDI stream undergoes a final condensation step before being transferred to product storage (Step 11).8,10

5.2.2 Emissions

Typical emission sources at TDI manufacturing facilities include process equipment vents, open process equipment, equipment leaks, storage tank vents, secondary sources, and transfer and 5-9

handling operations. No specific emissions data for any of these sources are available; however, it has been estimated that 7.7 x 10-4 pounds of toluene are emitted for every pound of toluene used in TDI manufacturing. An additional 1.9 x 10-4 pounds of toluene are released from fugitive sources per pound of toluene used.6

Process equipment sources include nitration reactors, evaporators, the DNT wash tank, TDA reactors, filtration units, stabilization columns, and the condensation and distillation units. The emissions will vary according to degree of agitation of the reactors and the level of control on the equipment.

5.3

TRINITROTOLUENE PRODUCTION

At one time, the production of trinitrotoluene (TNT) for explosives was the major end use of toluene.

Although TNT is no longer a primary toluene derivative, it is still a modern

explosive used mainly for military purposes, but also with commercial applications.

TNT

provides low manufacturing cost, excellent chemical and thermal stability, and favorable physical properties to allow usage as a bursting-charge in shells, bombs, and grenades and as an ingredient in binary explosives, metallized explosives, propellant compositions and commercial blasting explosives.10

Once manufactured by private companies, TNT is now produced by government facilities. It is not likely that private manufacture of TNT will resume as less expensive, competitive industrial explosives are now available.11 5.3.1 Process Description8,10

The production of TNT can be accomplished in two or three stage processes and in batch or continuous fashion. The chemical process is the same for both the continuous and batch methods. Figure 5-3 illustrates the TNT manufacturing process. TNT is normally produced by the nitration of toluene in three distinct mononitration stages each consisting of the addition of one nitro (NO2) group into the aromatic ring. The first nitro group can be introduced easily, but 5-11

the second and third nitration steps require reaction forcing conditions using various mixtures of nitric and sulfuric acids in water. Increasing amounts of sulfuric acid (and decreasing amounts of nitric acid) are used with each successive mononitration step.

The mixed acids and the toluene are fed into a series of cooled, agitated reactors (Step 1). The sulfuric acid catalyzes the reaction producing 97 to 98 percent mononitrotoluene, approximately 0.2 percent DNT, 1 percent unreacted toluene, and some nitrocresols.10 Once the reaction has gone to completion, the spent acid and the mononitrotoluene separate into two phases (Step 2). The mononitrotoluene is purified by a water wash followed by an alkali wash and a second water wash (Step 3). The spent acid (primarily sulfuric acid) is concentrated in a direct evaporator using gases from a natural gas burner, recycled to the nitration reactor, and mixed with additional virgin acids to provide nitration acids of the desired strength.

The crude mononitrotoluene is topped to remove unconverted toluene (Step 4) and then separated by fractional distillation into a 2-nitrotoluene (2-NT) stream and a distillation residue which can be further distilled and crystallized (Step 5) to recover the 3- and 4-NT isomers. (End uses for these isomers are discussed in Section 5.6.) The basic nitration process is repeated two additional times to produce DNT and then TNT.

5.3.2 Emissions

Typical emission sources at TNT manufacturing facilities include process equipment vents, open process equipment, equipment leaks, storage tank vents, secondary sources, and transfer and handling operations. No emissions data for any of these sources were available during the preparation of this document.

Process equipment sources include nitration reactors, separation columns, wash tanks, evaporators, filtration units, and distillation units. The emissions will vary according to the type of process used (e.g., two or three stage operations or batch or continuous processing) and the strength of the nitration acid mixture.

5-13

5.4 BENZOIC ACID PRODUCTION

Benzoic acid is manufactured from toluene by continuous liquid-phase oxidation. Approximately 52 percent of the benzoic acid produced from toluene is converted to phenol by the only U.S. phenol producer, Kalama Chemical. Phenol, in turn, is used to manufacture phenolic resin for use in adhesives in plywood, binders for insulation, and laminating agents. Other end uses for benzoic acid include plasticizers (20 percent), sodium and potassium benzoate (12 percent), benzoyl chloride (6 percent), alkyd resins (3 percent), and butyl benzoate (2 percent). Miscellaneous uses for the remaining five percent of benzoic acid end uses. Sodium and potassium benzoate, benzoic acid salts, are used mainly as food and beverage preservatives in the United States. European countries and Japan use sodium benzoate as a corrosion inhibitor in antifreeze.13

Benzoic acid is currently produced by three companies. These facilities and their 1990 production capacities are listed in Table 5-3.13 TABLE 5-3.

BENZOIC ACID PRODUCTION LOCATIONS AND CAPACITIES

Facility

Location

Kalama Chemical

Kalama, WA

Pfizer

Terre Haute, IN

Velsicol

Chattanooga, TN

Source: Reference 13

5-14

1990 Capacity Millions of Kilograms (Millions of Pounds) 63 4.5 29

(140) (10) (65)


Benzoic acid is manufactured from toluene in the presence of cobalt catalysts by continuous liquid-phase oxidation according to the following reaction:1

Approximately 0.87 pounds of toluene are required per pound of benzoic acid produced, with a 40 percent toluene conversion per .12

Although many of the process details are proprietary, the basic reaction mechanisms are presented. Toluene, the catalyst, and air (the source of oxygen) are fed continuously into a reactor maintained at 150° to 250°C (300° to 480°F) and at a pressure of 5 to 50 atm.11 The temperature and the catalyst concentration determine the reaction rate. The reaction is complete when 40 percent of the toluene has been oxidized to yield crude benzoic acid.11 The reactor effluent moves from the oxidation reactor to an atmospheric stripping column heated by a circulating hot oil reboiler. The unreacted toluene and other intermediates/by-products [e.g., benzaldehyde (one to two percent) and benzyl benzoate (ten percent)] boiling below benzoic acid are removed from the column and recycled.10 Crude benzoic acid is extracted from the column using water and moved to a small finishing column where pure benzoic acid is removed overhead. The finishing column bottoms are returned to the stripping column.

Vent gases from the oxidation reactor are cooled by exchange with incoming air, then with cooling water, and finally, by ammonia refrigeration. The vent gases are then expanded and vented to the atmosphere through a carbon scrubber. Much of the toluene in the vent gases is recovered for recycle through the cooling process. 5-15

5.4.2 Emissions

Typical emission sources at benzoic acid manufacturing facilities include process equipment vents, open process equipment, equipment leaks, storage tank vents, secondary sources, and transfer and handling operations. No specific emissions data for any of these sources are available; however it has been estimated that 1 x 10-3 pounds of toluene are emitted for every pound of toluene used in benzoic acid manufacturing. An additional 1 x 10-4 pounds of toluene are released from fugitive sources.6

Process equipment sources include reactors, stripping columns, wash tanks, and distillation units. The emissions will vary according to the type of process used (process details are proprietary) and the temperature of the oxidation reactor.

5.5 BENZYL CHLORIDE PRODUCTION

Benzyl chloride is produced commercially by the direct chlorination of boiling toluene. Two facilities in the United States produce benzyl chloride. As of January 1, 1990, Monsanto in Bridgeport, New Jersey, had a capacity of approximately 45 million kilograms (100 million pounds). Akzo Chemical in Edison, New Jersey operated a facility with an 11 million kilogram (25 million pound) capacity. The primary end use of benzyl chloride (69 percent) is as an intermediate in the production of butyl benzyl phthalate which is a plasticizer for vinyl flooring and polyvinyl acetate emulsion adhesives used in packaging. Sixteen percent of benzyl chloride is used in the production of quaternary ammonium compounds (quats). Quats are used in sanitizers, disinfectants, deodorants, fungicides and algicides applied in food production, dairies, bottling plants, restaurants, swimming pools, and industrial water treatment bactericides. Other uses of benzyl chloride include the production of benzyl alcohol, benzyl acetate, butyl benzoate, and benzyl salicylate. Some of the end products of these chemicals are perfumes, cosmetics, and flavorings.15 The annual growth rate of benzyl chloride in the Unites States is expected to increase by no more than 1.0 percent from 1988 to 1993.1

5-16


Benzyl chloride is produced by the direct chlorination of boiling toluene according to the following reaction:1

Toluene is heated to 65° to 100°C (150° to 212°F) and chlorinated in the dark (or in an alternate process by photochlorination) until the mixture increases in weight by 37.5 percent.1,14 The reaction mixture is agitated with a mild alkali and then distilled.

Benzal chloride and

benzotrichloride are by-products of the chlorination reaction and occur in ratios with benzyl chloride of 1:0.1:10.14 Excess toluene is recovered and recycled to the chlorinator while the resulting hydrogen chloride gas is absorbed in water forming muriatic acid. For every pound of benzyl chloride produced, 0.8 pounds of toluene are consumed.1

5.5.2 Emissions

Typical emission sources at benzyl chloride manufacturing facilities include process equipment vents, open process equipment, equipment leaks, storage tank vents, secondary sources, and transfer and handling operations. No specific emissions data for any of these sources are available; however, it has been estimated that 5.5 x 10-4 pounds of toluene are emitted for every pound of toluene used in benzyl chloride production. An additional 1.5 x 10-4 pounds of toluene are released from fugitive sources.6

Process equipment sources include heaters, chlorination reactors, and wash tanks. The emissions will vary according to the type of process used (e.g., dark chlorination or photochlorination).

5-17

5.6 OTHER TOLUENE DERIVATIVES

Other toluene derivatives include mono- and dinitrotoluene, vinyl toluene, benzaldehyde, toluenesulfonyl chloride, chlorotoluenes, and toluenesulfonic acid. End uses for these chemicals are discussed below.5,10

The mono- and dinitrotoluene isomers can be hydrogenated to amines and then used as dye intermediates. The 3-nitrotoluene isomer is used in the production of red-violet dyes for polyester fibers, while 4-nitrotoluene is used in fluorescent brightening agents for cellulosic materials.10

Benzaldehyde is a by-product of toluene in the manufacture of benzoic acid. The primary use of benzaldehyde is as a chemical intermediate in the production of specialty chemicals used for food flavoring, pharmaceuticals, herbicides, and dyestuffs.

The production of vinyl toluene is accomplished by reacting ethylene and pure toluene in the presence of aluminum chloride and hydrogen chloride. Dow Chemical currently holds several patents for this manufacturing process. Vinyl toluene is used in unsaturated polyester and alkyd resins and as a co-polymer with butadiene. The end uses of these chemicals are normally paints, adhesives, and printing inks.5,10

Toluene can be sulfonated with sulfuric acid or sulfur trioxide to form toluene sulfonic acids. Sulfonation with chlorosulfonic acids yields toluene sulfonyl chloride. The largest use of mixed toluene sulfonic acids is in the production of cresols. One of the isomers of toluene sulfonic acid, p-toluene sulfonic acid (PTSA), is used in the production of resins, dyes, adhesives, antidiabetic drugs, and as an additive in electroplating baths. Toluene sulfonyl chlorides are used in disinfectants and in the manufacture of saccharin.5,10

Mono-, di-, and trichlorotoluenes are prepared by the ring-chlorination of toluene. Toluene is reacted with elemental chlorine in the presence of catalysts such as chlorides of iron, aluminum, tin, titanium, and zirconium to yield ortho- and para-chlorotoluene. These isomers 5-18

are used as solvents and in paint and rubber stripping formulations and dye carrier formulations. Other eventual end uses include dyestuffs, pharmaceuticals, and preservatives.5,10

5.7 PAINT AND INK MANUFACTURING

Toluene is one of the solvents used as a raw material in the manufacture of paints and inks. In 1989, toluene ed for 15 percent of the 1,977 kilograms (4,358 million pounds) of solvent consumed in paints and coatings.15 Consumption in paints and coatings s for approximately 45 percent of total toluene solvent sales. A breakdown of the consumption of toluene and its derivatives as they are used in paints and coatings is given in Table 5-4. Figure 5-4 is a flow diagram indicating the uses of toluene in the paint and coatings industry.15 Section 6.0 discusses the application of toluene containing paints (surface coating) and inks (printing).

Paints and inks are made by blending pigments, solvents, resins (or binders), oils (for some inks), and other additives. The fluid component of the paint or ink, made of binders (oils and/or resins) and solvents, is called the vehicle. Vehicles transfer the pigment/binder mixture to a surface in a thin, uniform film and normally play no role in film formation. (In the case of reactive diluents and two- and three-component coatings, the vehicle becomes part of the coating film.) When a paint or ink is deposited on a substrate, the vehicle solvent(s) should evaporate completely. Toluene is only one of the vehicle solvents used by paint and ink manufacturers.16 Total toluene consumption in paints and coatings has increased since 1980. One explanation for this increased consumption is that toluene is priced lower than other commonly used solvents like ketones and esters.15

In 1987, Paint and Allied Products facilities were composed of 1,123 companies operating 1,426 plants, two-thirds of which were located in ten states. The 1987 Census of Manufactures shows that the 504 ink manufacturing facilities in the United States are owned by 224 companies in nineteen States and the District of Columbia. Ward’s Business Directory lists 364 paint and allied products facilities in SIC 2851 with 1990 sales greater than $1,000,000.17 Ward’s also lists

5-19

TABLE 5-4.

ESTIMATED CONSUMPTION OF TOLUENE DERIVATIVES IN PAINTS AND COATINGS, 1988 Millions of Kilograms (Millions of Pounds)

Derivative

Derivative Production from Toluene

Solvent Toluene Diisocyanate

--

--

Toluene Consumption

Derivative Consumed in Paints and Coatings

Toluene Equivalents for Paints and Coatings

636

(1,400)

287

(635)

287

(635)

329

(725)

227

(500)

9

(20)

6

(14)

Benzyl Chloride

29

(63)

23

(50)

1

(2)

1

(2)

Benzoic Acid

91

(200)

76

(168)

3

(7)

3

(6)

278

(612)

16

(35)

11

(25)

1,241

(2,730)

310

(682)

Othera Total Toluene

--

--

a Includes TNT, vinyl toluene, cresols, benzaldehyde, toluene sulfonic acids, toluene sulfonates, benzotin chloride, toluene diamine (other than the amount consumed for TDI), nitrotoluenes, chlorotoluenes, p-tert-butyl benzoic acid, toluene sulfonyl chloride, and as a denaturant. Excludes fuel use and benzene/xylenes production. Source: Reference 15

56 ink manufacturing facilities in SIC 2893 with 1990 sales greater than $1,000,000. These lists are provided in Appendix B, Table B-1 and Table B-2.

One method used to categorize the products of the paint manufacturing industry is by enduse (e.g., markets served). The use categories are architectural coatings, product coatings for original equipment manufacturers (OEM), and special purpose coatings. A summary of toluene consumption in the paint use divisions by use category and subcategory is found in Table 5-5. No toluene was consumed in architectural coatings in 1988 or 1989. Toluene is commonly used in OEM product coatings such as those for wood furniture and fixtures, containers and closures, automotive finishes, and machinery and equipment.15

5-21

TABLE 5-5.

ESTIMATED CONSUMPTION OF SOLVENTS IN PAINTS AND COATINGS, BY MARKET Total Solvents Millions of Kilograms (Millions of Pounds) Product Finishes Wood Furniture and Finishes

1988

Total Toluene Millions of Kilograms (Millions of Pounds)

1989

1988

1989

127

(280)

123

(270)

33.7

(74.1)

32.5

(71.5)

3

(7)

3

(6)

0.4

(0.8)

0.3

(0.6)

Metal Furniture and Fixtures

39

(85)

39

(85)

3.8

(8.3)

3.8

(8.3)

Containers and Closures

86

(189)

87

(191)

10.4

(22.8)

10.4

(22.9)

Sheet, Strip and Coil

32

(71)

32

(71)

2.6

(5.8)

2.6

(5.8)

Major Appliances

19

(41)

19

(41)

1.5

(3.3)

1.5

(3.3)

Other Appliances

10

(23)

10

(23)

1.2

(2.7)

1.2

(2.7)

Automotive

--

--

--

--

--

--

--

--

Topcoat

28

(61)

28

(61)

4.5

(10.0)

4.5

(10.0)

Primer

16

(35)

16

(35)

2.5

(5.6)

2.5

(5.6)

Underbody Components and Parts

16

(35)

16

(35)

2.0

(4.5)

2.0

(4.5)

16

(35)

15

(33)

1.8

(3.9)

1.7

(3.7)

Railroad

4

(8)

3

(7)

0.9

(2.0)

0.8

(1.7)

Other Transportation

6

(13)

6

(13)

1.1

(2.4)

1.1

(2.4)

Machinery and Equipment

70

(155)

72

(159)

7.9

(17.3)

8.0

(17.7)

Electrical Insulation

27

(59)

27

(59)

--

--

--

--

Paper, Foil, and Film

18

(40)

18

(40)

2.6

(5.8)

2.6

(5.8)

116

(255)

116

(256)

11.4

(25.0)

11.4

(25.0)

633

(1,392)

635

(1,398)

87.7

Wood Flat Stock

Trucks and Buses

Other Product Finishes PRODUCT-OEM TOTAL

(continued)

5-22

(193)

87.3

(192)

TABLE 5-5.

ESTIMATED CONSUMPTION OF SOLVENTS IN PAINTS AND COATINGS, BY MARKET (Continued) Total Solvent Millions of Kilograms (Millions of Pounds) Special Purpose Coatings Maintenance Marine

1988 54

Total Toluene Millions of Kilograms (Millions of Pounds)

1989 (118)

59

1988 (121)

1989

10.5

(23.1)

10.9

(23.9)

--

--

--

--

--

--

--

--

1

(3)

1

(2)

--

--

--

--

15

(33)

15

(33)

2.0

(4.4)

2.0

(4.4)

Auto Refinishing

74

(162)

74

(162)

9.5

(21.0)

9.5

(21.0)

Traffic Paints

59

(130)

59

(130)

28.3

(62.3)

28.3

(62.3)

Aerosol

42

(93)

42

(93)

6.2

(13.7)

6.2

(13.7)

Other

53

(117)

54

(118)

5.5

(12.1)

5.5

(12.2)

TOTAL SPECIAL PURPOSE

298

(656)

300

(659)

62.0

(136.6)

TOTAL THINNER AND MISC.

488

(1,073)

764

(1,982)

138.6

(305)

141.4 (311)

1,975

(4,345)

1,977

(4,349)

288.6

(635)

290.0 (640)

Pleasure Commercial and Maintenance

TOTAL PAINTS AND COATINGS

Note: Totals may not add due to rounding. Source: Reference 15

5-23

62.4 (137.5)

No specific information was available relating the amount of toluene consumed in inks. However, toluene (and other organic solvents) are most often used in inks that employ a solvent carrier such as flexographic and rotogravure inks. The other two primary ink classifications, letterpress, and lithographic and offset inks, are of an oil or paste base.16


Paint and ink facilities use similar manufacturing processes to produce their respective products in batch scale production fashion. Most small plants (e.g., facilities employing less than 20 people) produce paint in 40 to 2,000 liter (10 to 500 gallon) batches, while larger facilities produce paint in 800 to 11,000 liter (200 to 3,000 gallon) batches with stock items made in 40,000 liter (10,000 gallon) runs. Inks are produced in batches ranging from 4 liters to over 4,000 liters (1 to 1000 gallons).15

In most cases, manufacturing facilities purchase raw materials (e.g., pigments, solvents, resins, and other additives) and then formulate, or blend, a finished product. Normally, no chemical reactions take place during the process. Batch process production of paint and ink involves four major steps:

•

preassembly and premix

•

pigment grinding/milling

•

product finishing/blending

•

product filling/packaging

The manufacturing process is summarized in Figure 5-5.16

The first step in the manufacturing process is preassembly and premix. In this step, the liquid raw materials (e.g., resins, solvents, oils, alcohols, and/or water) are "assembled" and mixed in containers to form a viscous material to which pigments are added. The premix stage results in the formation of an intermediate product which is referred to as the base or mill base.

5-24

With further processing, this base with high pigment concentration may become any one of a variety of specific end products.16

The incorporation of the pigment into the paint or ink vehicle to yield a fine particle dispersion is referred to as pigment grinding or milling. The goal of pigment grinding is to achieve fine, uniformly-ground, smooth, round pigment particles which are permanently separated from other pigment particles. The degree to which this is realized determines the coating effectiveness and permanency of the paint or ink. Some of the more commonly used types of dispersion (milling) equipment are roller mills, ball and pebble mills, attritors, sand mills, bead and shot mills, high-speed stone and colloid mills, high-speed disk dispersers, impingement mills, and horizontal media mills.16

Final product specifications are achieved in the product finishing step which consists of three intermediate stages: thinning, tinting and blending. Material letdown, or thinning, is the process by which a completed mill base dispersion is let down or reduced with solvent and/or binder to give a coating which is designed to provide a durable, serviceable film that is easily applied to the substrate. Tinting is the process of adjusting the color of completed mill base dispersions. Various combinations of pigments, solvents, resins, and pastes are added to the material to meet the color requirements. Blending is the process of incorporating the additions into the material in order to meet the desired product specifications.16

The final step in paint and ink manufacturing is product filling operations. After the material has been blended, it is transferred from the blend tanks into containers for product shipment. The transfer step normally involves product filtration.16

5.7.2 Emissions

The primary factors affecting the emission of toluene are the types of solvents and resins used in the manufacturing process, the temperature at which these compounds are mixed, and the methods and materials used during cleanup operations.16

5-26

Toluene is released from several types of equipment and handling operations throughout the paint and ink manufacturing process and during cleanup operations. During the preassembly and premix stage, emissions may come from equipment such as mix tanks or drums while resins are being thinned and materials are being added. Toluene emissions also occur during the pigment grinding step when materials are added to the dispersion equipment. The emissions that occur during the product finishing step are mainly a result of material additions during the thinning and tinting stages. Toluene emissions from product filling operations occur during material transfer and free-fall into the receiving container. Another emission source is product filtering. As product flows through a filtering device, it is often exposed to the air, resulting in releases of the incorporated toluene. Toluene emissions during filling operations result from product free-fall and material splashing. Fugitive emissions also result from flanges, valves, and pumps used to transfer material from equipment for one manufacturing stage to equipment for the next stage.16 Emissions occurring during the manufacturing stages may be reduced by using equipment and process modifications such as tank lids or closed-system milling equipment.

In addition to emissions from process operations, toluene is also released from a variety of cleaning operations following the manufacture of solvent based products. In many facilities, manufacturing equipment is cleaned manually (with solvents, brushes, and /or rags) on the production floor on an as-needed basis. The standard method of cleaning grinding equipment involves emptying the mill of product and then adding solvent to the vessel to capture remaining product residue. Emissions occur during cleaning solvent addition and removal as well as during the cleaning process.16 Emissions from cleaning equipment may be reduced by using rubber wipers, high-pressure spray heads, or automatic tub washers.16

There is little emission factor information available for the manufacture of paints and inks. Estimates range from process solvent losses of one to two percent under well controlled conditions to much higher percentages. The process solvent losses vary significantly from facility to facility, and therefore those emissions should be evaluated on a case-by-case basis. Many paint and ink manufacturing facilities calculate total plant VOC emissions based on raw material consumption rather than calculating emissions from processes or equipment by an alternative

5-27

method.

Total emissions therefore reflect solvent losses during manufacturing, cleaning

operations, and storage.16

5.8 SOLVENT CLEANING OPERATIONS

Surface cleaning or degreasing operations include solvent cleaning or conditioning of metal surfaces and parts, fabricated plastics, electronic and electrical components and other nonporous substrates. These cleaning processes are designed to remove foreign materials, such as grease, waxes, and moisture in preparation for further treatment such as painting, electroplating, galvanizing, anodizing or applying conversion coatings.

The three categories of solvent cleaning operations are cold cleaning, open-top vapor degreasing, and conveyorized degreasing which can employ either cold cleaning or vapor degreasing as its major cleaning process. When toluene is used, it is typically in cold cleaning operations.


Cold cleaning is a batch process operation in which solvents are applied at room temperature or slightly above room temperature, but always below the solvent’s boiling point. The mechanical or industrial parts or tools to be cleaned are placed in a basket inside the cold cleaner and immersed in the solvent. Parts too large for immersion may be sprayed or brushed. The solvent tank is often agitated to enhance its cleaning action. After cleaning, the parts are removed from the tank and allowed to dry.

Cold cleaners are usually the simplest and least expensive of the three types of solvent cleaners. The two basic types of cold cleaners are maintenance cold cleaners and manufacturing cold cleaners.18 Maintenance cold cleaners are normally simpler, less expensive, and smaller than manufacturing cold cleaners.

They are used primarily for automotive and general plant

maintenance cleaning. Manufacturing cold cleaners are larger, more specialized cleaners which perform a higher quality of cleaning than maintenance cleaners.19 Cold cleaners may incorporate 5-28

covers and freeboards to limit the evaporative loss of solvents. Freeboard is the distance between the solvent level and the top edge of the unit.18

5.8.2 Emissions

Cold cleaning can result in both direct and indirect atmospheric emissions of toluene. Cold cleaners are estimated to result in the largest total emissions of the three types of solvent cleaners, primarily due to the large numbers of these units and the high degree of evaporative losses. Emissions from cold cleaners can occur through bath evaporation, solvent carry-out, solvent agitation, waste solvent evaporation, and spray evaporation. These typical sources of emissions from cold cleaners are discussed below.19,20

Bath evaporation from cold cleaners is simply evaporation from an uncovered solvent tank. This form of solvent loss can be reduced by covering the tank with a lid, increasing the freeboard height of the tank over the level of the solvent, and decreasing the amount of ventilation over an uncovered tank. Of these options, covering an open tank with a lid will usually render bath evaporation insignificant. Bath evaporation s for approximately 20 percent of the total organic emissions from cold cleaners.18 Solvent carry-out emissions are due to evaporation of the solvent residue from the part that was cleaned. Several factors regulate the amount of emissions from carry-out sources. Porous or absorbent materials (cloth, leather, wood) absorb the solvent and keep it retained for extended periods of time. The size of the load to be cleaned must be manageable in order to keep the solvent from splashing out of the degreasing unit. Proper drainage racks or shelves need to be employed to provide a place where the parts can dry off. It is recommended that all cold cleaned parts dry for a minimum of 15 seconds while in the drainage facility.19,20

Emissions from the agitation of the solvent depends on use of the cover, agitation system adjustments, and volatility of the solvent. If the cover is kept closed, then usually emissions from agitation are kept low; however, when the tank is left open, emissions due to agitation of the solvent increase dramatically. Poor adjustment of the agitation system, especially the air flow, may lead to increased emissions. 5-29

Waste solvent evaporation is the largest source of atmospheric emissions from cold cleaners, ing for between 50 and 75 percent of the total organic emissions.18 The degree of evaporation depends on the size of the cold cleaner, the frequency of disposal, and the method(s) of disposal. If the cold cleaning removes large amounts of contaminants, or the parts require a high degree of cleanliness, then the solvent will need replacement more often and emissions will generally be greater. Disposal methods also influence the degree of evaporation from the waste solvent. Some acceptable methods include proper incineration, distillation, and chemical landfilling, and emissions from these methods will vary depending on environmental and operational factors. Some disposal methods will result in total release of the waste solvent into the atmosphere. These methods include flushing the waste solvent into sewers or bodies of water, spreading the waste solvent for dust control, land-farming, and landfilling where the solvent can easily leach into the soil or evaporate into the air.

Evaporative emissions from spraying the solvent over the part to be cleaned vary depending on the pressure of the spray, the fineness of the spray, and the tendency of the solvent to splash and overspray out of the tank. Evaporation is also increased when the spray is used continuously and when the solvents are highly volatile. Generally, however, emissions from spray evaporation can be prevented through careful operation and equipment design.19,20

5.9

OTHER SOLVENT USES

In addition to the previously discussed solvent end uses, toluene is used either alone or as a component of a multi-solvent system, in adhesives, rubbers, photographic film, agricultural sprays, and other chemical derivatives.

Available emission factors for some of these

miscellaneous uses are included in Table 5-6.

5-30

TABLE 5-6.

EMISSIONS FROM MISCELLANEOUS SOURCES OF TOLUENE Process Neoprene Manufacture

Emission Factor

Quality Rating

Blend Tank

0.05 g/kg neoprene

E

Solution Makeup Tank

0.04 g/kg neoprene

E

Batch Polykettle

0.018 g/kg neoprene

E

Stripper

0.019 g/kg neoprene

E

Wash Belts

0.015 g/kg neoprene

E

2.0 g/kg neoprene

E

Potential Source

Dryer Exhaust Source: Reference 21

5-31

5.10


1.

SRI International. Chemical Economics Handbook. Menlo Park, CA. 1991.

2.

Benzene Chemical Product Synopsis, Mannsville Chemical Products Corp., Asbury Park, NJ. March 1992.

3.

U.S. Environmental Protection Agency. Locating and Estimating Air Emissions from Sources of Benzene, EPA-450/4-84-007q. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1988.

4.

Toluene Chemical Product Synopsis, Mannsville Chemical Products Corp., Asbury Park, NJ. March 1990.

5.

Kirk-Othmer Encyclopedia of Chemical Technology, 3rd edition. Toluene. Volume 23. John Wiley and Sons. New York, NY. pp. 246-273. 1983.

6.

U.S. Environmental Protection Agency. Air Pollutant Emission Factors - A Compilation for Selected Air Toxic Compounds and Sources, EPA-450/2-88-006a. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1988.

7.

International Programme on Chemical Safety. Environmental Health Criteria 75: Toluene Diisocyanates. World Health Organization. Geneva. 1987.

8.

U.S. Environmental Protection Agency. Organic Chemical Manufacturing. Volume 7: Selected Processes, Report 4: Toluene Diisocyanate, EPA-450/3-80-028b. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1980.

9.

Toluene Diisocyanate Chemical Product Synopsis, Mannsville Chemical Products Corp., Asbury Park, NJ. October 1990.

10.

Hancock, E.G., ed., Toluene, the Xylenes and their Industrial Derivatives. Elsevier Scientific Publishing Company. New York, NY. 1982.

11.

Lowenheim, Fredrick A. and Moran, Marguerite K., Faith, Keyes, and Clark’s Industrial Chemicals. Fourth Edition. 1975.

12.

U.S. Environmental Protection Agency. Compilation of Air Pollution Emission Factors. AP-42, Fourth Edition and Supplements. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1985.

13.

Benzoic Acid Chemical Product Synopsis, Mannsville Chemical Products Corp., Asbury Park, NJ. March 1990.

14.

Benzyl Chloride Chemical Product Synopsis, Mannsville Chemical Products Corp., Asbury Park, NJ. January 1990. 5-32

15.

SRI International. U.S. Paint Industry Database. Prepared for the National Paint and Coatings Association. Washington D.C. 1990.

16.

U.S. Environmental Protection Agency. Control of VOC Emissions from Ink and Paint Manufacturing Processes, EPA-450/3-92-013. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1991.

17.

Gale Research, Inc. Ward’s Business Directory of U.S. Private and Public Companies1991, Volume 4. Detroit, MI. 1991.

18.

U.S. Environmental Protection Agency. Organic Solvent Cleaners - Background Information on Proposed Standards, EPA-450/2-78-045a. 1979.

19.

U.S. Environmental Protection Agency. Control of Volatile Organic Emissions from Solvent Metal Cleaning, EPA-450/2-77-022. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1977.

20.

U.S. Environmental Protection Agency. Alternative Control Technology Document Halogenated Solvent Cleaners, EPA-450/3-89-030. Office of Air Quality Planning and Standards. Research Triangle Park, NC. August 1989.

21.

U.S. Environmental Protection Agency. Source Assessment: Polychloroprene, State of the Art, EPA-600/2-77-1070. Industrial Environmental Research Laboratory. Cincinnati, OH. 1977.

5-33

SECTION 6.0 EMISSIONS FROM THE USE OF TOLUENE-CONTAINING MATERIALS

As discussed in Section 3.0, toluene is present in many materials, including paints and coatings, inks, adhesives, resins, pharmaceuticals, gasoline and other formulated products using a solvent carrier. This section examines residual emissions from the use of toluene-containing materials. Toluene may be emitted when toluene-containing products such as paint, ink and gasoline release small amounts over time. Such releases are described in this section as residual emissions.

The production descriptions and emissions data presented in this section represent the most common and relevant processes and products. Because of toluene’s widespread use, all processes cannot be included in this document.

6.1

SURFACE COATING OPERATIONS

Surface coating operations involve the application of paint, varnish, lacquer or primer for decorative, functional, or protective purposes. In 1989, 290 million kilograms (640 million pounds) of toluene were consumed in paints and coatings.1 Consumption of toluene in specific end-use markets was presented in Section 5.7, Table 5-5. Appendix C contains a listing of some of the surface coating source categories in which toluene is used. Appendix C also indicates associated SIC codes, potential toluene emission points, and emissions reduction opportunities. References are provided for additional information.

The general application methods for surface coating operations are discussed below. Because surface coating is a very broad category, detailed process descriptions and process flow diagrams for each category are not included in this document; however, the reader is encouraged to review the references mentioned at the end of this section and in Appendix C.

6-1

6.1.1

Process Description

Industrial surface coating operations use several different methods to apply coatings to substrates. Some of the more commonly used techniques include spraying, dipping, rolling, flow coating, knife coating, and brushing. In addition to the application of coatings to substrates, many surface coating operations also include surface preparation steps (e.g., cleaning and degreasing), drying and curing stages. Spraying operations are normally performed in a spray booth using one of the following spray application methods: air atomization, airless atomization, air-assisted airless, high-volume, low-pressure (HVLP), and electrostatic methods. Dip coating involves briefly immersing the substrate in a tank containing a bath of paint. The object is slowly removed from the tank allowing excess paint to drain back into the tank. Roller coating is used to apply coatings and inks to flat surfaces. A typical roller coating machine contains three or more power driven rollers, one of which is partially immersed in the coating material. The paint is transferred to a second, parallel roller by direct . The sheet to be coated is run between the second and third rollers, and is coated by transfer of paint from the second roller. Flow coating is used on articles which cannot be dipped due to their buoyancy, such as fuel oil tanks, gas cylinders, or pressure bottles. In this operation the coating material is fed through overhead nozzles which causes the paint to flow in a steady stream over the article to be coated. Excess paint is allowed to drain from the coated object and is then recycled. Knife coating is used primarily to coat paper or fabric webs. The adjustable blade or "knife" distributes a liquid coating evenly over a moving surface.

6.1.2

Emissions2,3

Figure 6-1 is a generic schematic flow diagram of a surface coating operation. Process operations, auxiliary facilities, and emission points are illustrated. Note that this is a generic figure and may differ significantly from any specific coating operation. The operations shown include degreasing, surface coating, and drying and curing.

Auxiliary facilities include

degreasing solvent storage, and surface coating storage and blending. Industrial categories, specific operations and emission points resulting in expected toluene emissions from surface coating operations are presented in Appendix A and in Appendix C. 6-2

Streams 1, 2, 3, 4 depict the flow of products through the plant. Stream 1 represents the input of uncoated products to the surface coating system. Stream 2 represents the flow of degreased or scoured products to the surface coating operation. The type of surface coating operation used will depend upon the product-type coated, coating requirements, and the method of application. Stream 3 represents the product flow to the drying and curing operation. Stream 4 represents the flow of coated finished products from the surface coating section of a manufacturing plant.

Streams 5 through 10 represent the flow of degreasing solvent through the surface coating section of a manufacturing plant. Streams 5 and 6 depict the flow of solvent into the plant and to the degreasing unit. Streams 7 and 8 represent the flow of solvent vapors from the degreasing unit through the fume handling system. Uncontrolled and controlled emissions are represented by streams 9 and 10, respectively.

Streams 11 through 21 represent the flow of surface coating raw materials through the plant. Streams 11, 12, 13, and 14 represent the flow of solvent, pigment, resin, and additives to the surface coating blending tank. Stream 15 is the flow of coating to the surface coating unit. For those operations that use spray painting, stream 16 is the flow of compressed air. Streams 18 and 19 represent the flow of solvent and resin from the surface coating unit through the fume handling equipment. Uncontrolled and controlled emissions are depicted by streams 20 and 21. Potential release sources are identified in Appendix C.

In Figure 6-1, streams 22 through 25 represent the flow of gases (e.g., fuel, steam or electrically heated air) to the drying and curing operation. Drying and curing operations occur in flash-off areas and curing ovens. Flash-off areas are the places between application areas, or between an application area and an oven, in which solvent is allowed to volatilize from the coated piece. Ovens are used between some coating steps to cure the coating prior to the next step in the finishing sequence.

Streams 24 and 25 represent uncontrolled and controlled

emissions. No emission factor data were found in the literature.

6-4

Facilities with surface coating operations may purchase and apply ready-to-use coatings, or they may dilute their purchased coatings to decrease the coating viscosity and improve performance and ease of application. Toluene is used in solvent based coating formulations either as part of the coating vehicle or as a thinner. If a coating formulation is to be diluted inhouse, several factors (e.g., temperature, humidity, and type of coating) can determine the required dilution ratio. Consequently, the amount of toluene used may vary.2,4-6 Emissions from the mixing and blending of surface coatings are discussed in Section 5.7.2.

Toluene may also be used in clean-up operations. Clean-up solvent is used to clean application equipment, piping, spray booths, coating storage and distribution equipment, and to strip cured coatings from wood parts or machinery.1

One method of reducing toluene emissions from surface coating operations is to modify the surface coating formulation. Conventional coatings normally contain at least 70 percent by volume solvent (either one solvent or a mixture of solvents) to permit easy handling and application. Minimizing or eliminating the use of these solvents in surface coating formulations is the most effective way to reduce VOC emissions. Alternatives to these conventional coatings include water-based coatings, high-solids coatings, powder coatings, and radiation curable coatings.2

Large surface coating facilities may use add-on control devices to capture and control solvent emissions. Some commonly used capture devices include covers, vents, hoods, and partial or total enclosures. Adsorbers, condensers and incinerators, with control efficiencies of 95 to 98 percent, are the most common control devices used in surface coating operations.2,4,5

6.2 PRINTING AND PUBLISHING

The printing and publishing industry encomes publishing, commercial printing, and trade services.7 The trade services group includes typesetting, photoengraving, electrotyping and stereotyping, and platemaking services.

The trade services group is not examined in this

document because data on solvent use and emissions from these services are not available. Ink 6-5

consumption in these groups has been apportioned to the four printing processes according to the type of ink consumed (e.g., gravure ink consumption assigned to gravure printing). Process descriptions, however, will only be provided for the commercial printing processes. Attention is given to the gravure and flexographic processes as end uses of toluene. Toluene emissions from off-set lithography processes have not been measured and are thought to be minimal. The reader is encouraged to explore toluene consumption and emissions in all facilities reporting under the SIC code 27 as solvent use is an inherent aspect of the operations in printing and publishing facilities.

The publishing and printing groups are concentrated in four States, California, New York, Pennsylvania, and Illinois. The majority of establishments are small facilities that employ between 1 and 20 people.7,8 Appendix B, Table B-3 presents the companies in the printing and publishing SIC codes grossing $1,000,000 or greater in annual sales.9


The production of a printed product consists of five steps. First, the artwork and/or copy (text) is developed. Next, a printing plate is made. The plate is then tested in the press adjustment step. The actual printing of the product is the second to the last step in the printing process, and the main source of toluene emissions. The final step is cutting and finishing10

Printing ink composition varies among printing methods as well as among jobs using the same printing press and method. Printing inks in general can be described as heat-set or nonheatset. Heatset inks require the application of heat to drive off the ink solvent and set the ink to the substrate. Non-heatset inks dry by oxidation or adsorption to the substrate and do not require heat. Other, less common, ink types include radiation and thermally cured inks. All evaporative inks consist of three basic components: pigments, binders, and solvents.2 Printing processes using heatset inks that dry through evaporation of the solvent are the major concern for VOC (including toluene) emissions. Only the gravure and flexography printing processes are described here because specific emissions of toluene were not identified from the other printing methods. 6-6

Gravure Printing Process Description-The configuration of the image surface makes the gravure process unique. The printing cylinder is etched or engraved, creating tiny cells which comprise the image surface. The depth of each cell may vary and regulates the quantity of ink received by the substrate. The average rotogravure press has eight printing units, each printing one color. The paper position, speed, and tension through the printing unit is regulated by a series of rollers. A substrate dryer, equipped with heated air jets to evaporate the solvent from the substrate and set the ink, is located at the top of each printing unit.

The dryer air is exhausted from the unit by a

recirculation fan. The fan directs a portion of the solvent laden air to a control device, such as a carbon adsorption system. The remaining portion of the air flow is recirculated over a steam heating coil and back through the dryer.11

Each printing unit has a self-contained inking system. The ink system consists of an ink fountain, a circulation pump, and a mix tank. Solvent, and occasionally extenders or varnishes, are added to the ink concentrate in the mix tank.

Additional ink, solvent, varnishes, and

extenders are automatically added to the mix tank. The additions are monitored by level and viscosity control devices.11

A low viscosity ink is required for the gravure printing process. Raw ink concentrate generally contains 50 percent solvent by volume. The two most commonly used solvents in gravure printing and inks are toluene and a xylene-toluene-lactol spirit mixture (naphtha). Lactol Spirit is a petroleum solvent component of naphtha used in mixture to hasten evaporation. Toluene is known to produce a higher quality product and dissolves the ink resins well. However, toluene has a limited supply and is more expensive than naphtha. The ink concentrate is diluted at press side with additional solvent at a volume ratio of approximately 1:1. Since solvent is also added automatically to the inking system to replace evaporative losses, the resultant ink mixture may contain as much as 80 percent solvent by volume and 20 percent by volume ink and varnish solids.11

6-7

Flexographic Printing Process Description-Flexographic printing is used to print flexible packaging, milk cartons, gift wraps, folding cartons, paperboard, paper cups and plates, and labels, tapes, and envelopes. The majority of flexographic printing is done with a web-fed substrate.2

Solvent-based flexographic inks typically consist of alcohols, glycols, esters, hydrocarbons, and ethers. These inks may contain as much as 75 percent solvent by volume. Water-based and steam-set inks are also used in flexographic printing. Water-based inks contain approximately 25 percent by volume solvents.12 About 15 percent of all flexographic inks used are water-based.13 Steam-set inks use glycol solvents but do not contribute significantly to air emissions.14

6.2.2 Emissions

Gravure Printing Emission Points-Emissions from the rotogravure press occur from the ink fountain, the press, the dryer, and the chill rolls.2 The dryer vent is the most typical point of control. The other emission sources are considered fugitive. Emissions are influenced by press and job variables, solvent concentration in the ink, and solvent added as make-up during printing. Approximately 2.5 percent to 7 percent of the solvents used are retained in the printed product. The remaining solvents are reclaimed for reuse, recycled, and sold back to suppliers, or lost as fugitive emissions.11,15,16 Typical ink formulations contain approximately 50 percent to 85 percent solvents by volume. Water based inks, used in packaging and product printing, contain approximately 5 percent to 30 percent solvents by volume and for 30 percent to 40 percent of all inks used. Water-based inks for approximately 15 percent of all inks used in all gravure printing processes.13,17

Although specific emission estimates of toluene are not available, ink and solvent consumption numbers have been published and are reported below. Additionally, VOC emission factors and rates are available. A local survey may provide the needed information on the percentage of toluene used relative to total solvent consumption. Toluene emissions may then 6-8

be estimated by multiplying the percentage of toluene by the ink consumption rate and solvent content of the ink.

The Gravure Association of America (GAA) conducted a survey of their hip which reported solvent purchased, reused, and recovered in the various segments of the industry during 1987.18 Table 6-1 presents a summary of these statistics for publication, folding cartons, flexible packaging, and product gravure printing. The GAA hip reported a total of 41.4 million pounds of virgin solvent purchased, 246.2 million pounds of solvent recovered, and 179.3 million pounds of solvent reused. More solvent is recovered than bought due to solvent recovery from ink formulations. The portion of solvent that is recovered but not reused is sold back to the manufacturers, lost as fugitive emissions, or destroyed by incineration. Projected to the entire gravure industry, these figures total 622.3 million pounds of solvent purchased or reused, and 606.7 million pounds of solvent recovered.

The GAA projected total gravure

publication plants’ solvent consumption and fate based upon the percentage (by sales) of this segment responding to the survey.18 EPA projected solvent consumption and fate for the folding carton and flexible packaging segments based upon the same principle. The estimated ratio of solvent recovered to ink consumed for the publication segment of the industry was 73 percent.18

Carbon adsorption and incineration systems have traditionally been employed to control VOC emissions from the gravure printing process. The package printing sector has also achieved significant VOC reduction through the use of water-based printing inks.

Rotogravure package printing plants may use water-based inks. The use of water-based inks may contribute to an overall VOC reduction of 65 to 75 percent, if the solvent content of the inks is maintained below 25 percent by volume.12

One recent study has demonstrated that capture and control systems have been successfully applied to gravure printing presses that achieve greater than 90 percent overall VOC control.19 The average VOC control efficiency at these facilities ranged from 94 to 99.5 percent.

6-9

TABLE 6-1.

GRAVURE ASSOCIATION OF AMERICA INDUSTRY SURVEY RESULTS MILLIONS OF KILOGRAMS (MILLIONS OF POUNDS) Projected Gravure Industry Estimates

Reported Results

Printing Process

Solvents Purchased

Solvents Recovered

Solvents Reused

Solvents Purchased or Reused

Publication Plants

1

(2.2)

101.3

(222.9)

73.8

(162.3)

182.3

Folding Cartons

2.9

(6.4)

0.7

(1.6)

0.7

(1.6)

22.2

Flexible Packaging

7.2

(15.9)

2.8

(6.2)

1.9

(4.1)

78.4

Product Gravure

7.7

(16.9)

7.0

(15.5)

5.1

(11.3)

--

(401)

Solvents Recovered

247.1

(543.6)

(48.8)

4.4

(9.7)

(172.5)

24.3

(53.4)

--

--

--

aSurvey results scaled up to make projections for industry segments. Source: Reference 18

The facilities included in the study used total enclosure capture systems and one of the following add-on destruction devices: •

Catalytic Incineration

•

Regenerative Incineration

•

Thermal Incineration

•

Carbon Adsorption

The Environmental Protection Agency (EPA) has developed and published standard criteria for the design and operation of permanent total enclosure (PTE) systems. The PTE criteria have been published in the following sources: •

Guidelines for Developing a State Protocol for the Measurement of Capture Efficiency. Environmental Protection Agency. Policy Statement. April 16, 1990.

•

Polymeric Coating of ing Substrates - Background Information for Promulgated Standards (EPA-450/3-85-022b)20

•

Magnetic Tape Manufacturing Industry - Background Information for Promulgated Standards (EPA-450/3-85-029b)21

6-10

Capture efficiency may be estimated at 100 percent if all the EPA PTE criteria are met.19

Flexographic Printing Emission Points-Sources of emissions from flexographic printing operations are similar to the sources encountered from gravure operations. Emission control strategies are also similar. Incineration and carbon adsorption emission control techniques are available for use in the flexographic printing process. However, it is often difficult to install effective hooding and ducting devices on the presses. Therefore, overall control efficiencies approximate only 60 percent.12 Alternative emission control techniques include the use of water-based inks and microwave driers.14

Recent studies have indicated that flexographic printing presses controlled by catalytic and regenerative incineration may achieve a 95 percent overall VOC reduction efficiency.13,22 A metal oxide catalyst is used on flexographic printing presses to avoid poisoning by chlorinated solvents.22

6.3 GASOLINE AND AUTOMOTIVE EMISSIONS

Aromatic hydrocarbons including toluene are added to gasoline to raise the octane rating, thereby suppressing engine knock, increasing power, and providing smoother running engines. Toluene and other hazardous components may then be emitted in automotive exhaust. One study estimates the global release rate of toluene from automobile exhaust to be in the range of 3 to 8 metric tons (6,600 to 17,600 pounds) per year.23 Automotive emissions have been related to photochemical smog and ozone formation for many years. Atmospheric models recently became sophisticated enough to accommodate compositional variations.24

One recent study involving automotive emissions used 46 vehicles to provide detailed composition of organic emissions under various driving conditions.24 Another study used a mobile TAGA 6000 EM tandem mass spectrometer system to obtain time resolved data for selected aromatic compounds.25 Both of these studies present possible protocols to perform tests that would better characterize emissions and eventually estimate emissions of various VOC

6-11

species, including toluene.

However, the information presented in these studies was not

sufficiently comprehensive for emission factor development.

Table 6-2 lists the existing emission factors for toluene as a result of gasoline use. These emission factors were based on engineering estimates and are therefore given a quality rating of "U."

TABLE 6-2.

EMISSION FACTORS FROM GASOLINE USE Quality Ratinga

Emission Source

Emission Factor

Evaporation from automobile fuel tank

2.22 x 10-5 lb/vehicle mile traveled (1.0 x 10-2 g/vehicle mile traveled)

U

Automobile exhaust

8.46 x 10-4 lb/vehicle mile traveled (3.8 x 10-1 g/vehicle mile traveled)

U

a

Based on engineering judgement. Source: Reference 26

6.4 GASOLINE MARKETING

Gasoline storage and distribution activities represent potential sources of toluene emissions. The toluene content of whole gasoline ranges from less than 1 to almost 16 percent ( gasoline) by weight, but typical concentrations are around 15 percent by weight.27 Therefore, total hydrocarbon emissions resulting from storage tanks, material transfer, and vehicle fueling include emissions of toluene. This section describes sources of toluene emissions from gasoline marketing operations. Because the sources of these emissions are so widespread, individual locations are not identified in this section. Instead, emission factors are presented, along with a general discussion of the sources of these emissions. The discussion is taken from Reference 28.

6-12

The transportation and marketing of petroleum liquids involve many distinct operations, each of which represents a potential source of toluene evaporative losses. Crude petroleum products are transported from production operations to a refinery by pipelines, water carriers (e.g., barges), tank trucks, and rail tank cars.

The refined products are conveyed to fuel

marketing terminals and petrochemical industries by these same modes. From fuel marketing terminals, the fuels are delivered by tank trucks to service stations, commercial s and local bulk storage plants.29

As shown in Figure 6-2, typical components of gasoline marketing include refinery storage, gasoline terminals, gasoline bulk plants, service stations, and ground transportation. The gasoline terminals and gasoline bulk plants are large facilities for the wholesale marketing of gasoline, kerosene, and fuel oil. They receive these petroleum products from refineries or other terminals, mostly by pipeline, tanker, or barge, and store the products in large tanks. The primary function of marine and pipeline terminals is to distribute products to other terminals. Tank truck loading terminals distribute products by tank trucks to bulk plants, retail outlets or final consumers. The typical bulk gasoline terminals have a daily throughput of 950,000 liters (250,000 gallons) of gasoline.28

Service stations receive gasoline by tank truck from terminals or bulk plants or directly from refineries, and usually store the gasoline in underground tanks. Gasoline service stations are establishments primarily selling gasoline and automotive lubricants.

Gasoline is by far the largest volume petroleum product marketed in the U.S., with a nationwide consumption of 419 billion liters (111 billion gallons) in 1991.30 There are presently an estimated 1,700 bulk terminals storing gasoline in the U.S.31 About half of these terminals receive products from refineries by pipeline, and half receive products by ship or barge delivery. Most of the terminals (66 percent) are located along the east coast and in the Midwest. The remainder are dispersed throughout the country, with locations largely determined by population patterns.

6-13

Evaporative emissions from the transportation and marketing of petroleum liquids may be separated, by storage equipment and mode of transportation used, into four categories. •

Rail tank cars, tank trucks and marine vessels: loading, transit and ballasting losses

•

Service stations: bulk fuel drop losses and underground tank breathing losses

•

Motor vehicle tanks: refueling losses

•

Large storage tanks: breathing, working and standing storage losses The emission factors presented in the following discussions were derived from

References 2, 28 and 32.

A recent EPA memorandum describing speciated motor vehicle

emissions identified diurnal, base gasoline evaporative organic emissions as consisting of 10.6 percent toluene. This reference defined a base gasoline (i.e., an industry average summer fuel) as having 32 percent aromatics.32 Diurnal losses occur over a 24-hour period due to normal temperature changes. Although these losses refer to emissions from vehicles when the vehicle is stationary for an extended period with the engine switched off, the diurnal losses also approach the mechanisms that occur during the loading, unloading, and storage of gasoline.33 To calculate an emission factor for toluene, the 10.6 (0.106) percent toluene factor was applied to the VOC emission factors for evaporative emissions presented in EPA documents.2,28,32

6.4.1

Toluene Emissions From Loading Marine Vessels

Volatile organic compounds (VOC) can be emitted as crude oil and refinery products (gasoline, distillate oil, etc.) and are loaded and transported by marine tankers and barges. Loading losses are the primary source of evaporative emissions from marine vessel operations.28 These emissions occur as vapors in "empty" cargo tanks are expelled into the atmosphere as liquid is added to the cargo tank. The vapors may be composed of residual material left in the "empty" cargo tank and/or the material being added to the tank. Therefore, the exact composition of the vapors emitted during the loading process is difficult to determine.

Assuming an average toluene/VOC ratio of 0.106 (Reference 32), emission factors for toluene from marine vessel loading were calculated and are given in Table 6-3. Factors are

6-15

TABLE 6-3.

UNCONTROLLED VOLATILE ORGANIC COMPOUND AND TOLUENE EMISSIONS FROM LOADING GASOLINE IN MARINE VESSELS

Emission Source Ship/Ocean Barge:d Uncleaned; volatile previous cargo Ballasted; volatile previous cargo Cleaned; volatile previous cargo Gas-freed; volatile previous cargo Any condition; nonvolatile previous cargo Typical situation; any cargo Barge:d Uncleaned; volatile previous cargo Gas-freed; any cargo Typical situation; any cargo

Volatile Organic Compound Emission Factor (mg/L Transferred)a

Toluene Emission Factor (mg/L Transferred)b

Quality Ratingc

315

33.4

U

205

21.7

U

180

19.1

U

85

9.0

U

85

9.0

U

215

22.8

U

465

49.3

U

245 410

25.9 43.5

U U

a

Factors are for nonmethane-nonethane VOC emissions. Based on an average toluene/VOC ratio of 0.106 (Reference 32). c Based on engineering judgement. d Ocean barge is a vessel with tank compartment depth of 40 feet; barge is a vessel with compartment depth of 10-12 feet. Source: References 2 and 32 b

6-16

available for crude oil, distillate oil, and other fuels.2,28 However, reliable estimates of the toluene content of these fuels were not found. Therefore, it was not possible to provide toluene emission factors for marine vessel loading of fuels other than gasoline.

6.4.2

Toluene Emissions from Bulk Gasoline Plants, Bulk Gasoline Terminals and Service Stations

Each operation in which gasoline is transferred or stored is a potential source of toluene emissions. At bulk terminals and bulk plants, loading and unloading gasoline and storing gasoline are sources of toluene emissions. The gasoline that is stored in above ground tanks is pumped through loading racks that measure the amount of product. The loading racks consist of pumps, meters, and piping to transfer the gasoline or other liquid petroleum products. Loading of gasoline into tank trucks can be accomplished by one of three methods: splash, top submerged, or bottom loading. In splash loading, gasoline is introduced into the tank truck directly through a compartment located on the top of the truck.28 Top submerged loading is done by attaching a downspout to the fill pipe so that gasoline is added to the tank truck near the bottom of the tank. Bottom loading is the loading of product into the truck tank from the bottom. Because emissions occur when the product being loaded displaces vapors in the tank being filled, top submerged loading and bottom loading reduce the amount of material (including toluene) that is emitted.28

Vapor balancing systems, consisting of a pipeline between the vapor spaces of the truck and the storage tanks, are closed systems. These systems allow the transfer of vapor displaced by liquid in the storage tank into the transfer truck as gasoline is put into the storage tank.28 Table 6-4 lists emission factors for gasoline vapor and toluene from gasoline loading racks at bulk terminals and bulk plants.

The gasoline vapor emission factors were taken from

Reference 28. The toluene factors were obtained by multiplying the gasoline vapor factor by the average toluene content of the vapor (0.106 percent).32

A typical bulk terminal may have four or five above ground storage tanks with capacities ranging from 1,500-15,000 m3.

28

Most tanks in gasoline service have an external floating roof 6-17

TABLE 6-4.

TOLUENE EMISSION FACTORS FOR GASOLINE LOADING AT BULK TERMINALS AND BULK PLANTS Gasoline Vapor Emission Factora mg/L

Toluene Emission Factorb mg/L

Quality Ratingc

1430

151.6

U

Submergedd

590

62.5

U

Balance Service

980

103.9

U

Loading Method Splash

a

From Reference 28. Gasoline factors represent emissions of nonmethane-nonethane VOC. Factors are expressed as mg gasoline vapor per liter gasoline transferred. b Based on an average toluene/VOC ratio of 0.106 (Reference 32). c Based on engineering judgement. d Submerged loading is either top or bottom submerged. Source: References 28 and 32

to prevent the loss of product through evaporation and working losses. Fixed-roof tanks, still used in some areas to store gasoline, use pressure-vacuum vents to control breathing losses. Some tanks may use vapor balancing or processing equipment to control working losses. A breather valve (pressure-vacuum valve), which is commonly installed on many fixed-roof tanks, allows the tank to operate at a slight internal pressure or vacuum.

The major types of emissions from fixed-roof tanks are breathing and working losses. Breathing loss is the expulsion of vapor from a tank vapor space that has expanded or contracted because of daily changes in temperature and barometric pressure. The emissions occur in the absence of any liquid level change in the tank. Combined filling and emptying losses are called "working losses." Emptying losses occur when the air that is drawn into the tank during liquid removal saturates with hydrocarbon vapor and expands, thus exceeding the fixed capacity of the vapor space and overflowing through the pressure vacuum valve.28

6-18

A typical external floating-roof tank consists of a cylindrical steel shell equipped with a deck or roof that floats on the surface of the stored liquid, rising and falling with the liquid level. The liquid surface is completely covered by the floating roof except in the small annular space between the roof and the shell. A seal attached to the roof touches the tank wall (except for small gaps in some cases) and covers the remaining area. The seal slides against the tank wall as the roof is raised or lowered. The floating roof and the seal system serve to reduce the evaporative loss of the stored liquid.28

An internal floating-roof tank has both a permanently affixed roof and a roof that floats inside the tank on the liquid surface ( roof), or ed on pontoons several inches above the liquid surface (non roof). The internal floating-roof rises and falls with the liquid level, and helps to restrict the evaporation of organic liquids.28

Losses from floating-roof tanks include standing-storage losses and withdrawal losses. Standing-storage losses, which result from causes other than a change in the liquid level, constitute the major source of emissions from external floating-roof tanks. The largest potential source of these losses is an improper fit between the seal and the tank shell (seal losses). As a result, some liquid surface is exposed to the atmosphere. Air flowing over the tank creates pressure differentials around the floating roof. Air flows into the annular vapor space on the leeward side and an air-vapor mixture flows out on the windward side.28

Withdrawal loss is another source of emissions from floating-roof tanks. When liquid is withdrawn from a tank, the floating roof is lowered and a wet portion of the tank wall is exposed. Withdrawal loss is the vaporization of liquid from the wet tank wall.28

Table 6-5 presents emission factors for toluene from storage tanks at a typical bulk terminal. The emission factors were based on EPA (Reference 28) factors and the average weight fraction of toluene in the vapor of 0.106.32

The two basic types of gasoline loading into tank trucks at bulk plants are the same as those used at terminals. The first is the splash filling method, which usually results in high levels 6-19

TABLE 6-5.

TOLUENE EMISSION FACTORS FOR STORAGE LOSSES AT A TYPICAL GASOLINE BULK TERMINAL Gasoline Vapor Emissions Factor (Mg/yr/Tank)

Toluene Emission Factor Mg/yr/Tanka

Quality Ratingb

Working Loss

34.2

3.6

U

Breathing Loss

8.8

0.9

U

Working Loss

e

e

U

Storage Loss

9.6

1.0

U

Storage Method Fixed Roofc

External Floating Roof

d

a

Terminal with 950,000 liters/day (250,000 gallons/day) with four storage tanks for gasoline. b Based on engineering judgement. c Typical fixed-roof tank based upon capacity of 2,680 m3 (16,750 barrels). d Typical floating-roof tank based upon capacity of 5,760 m3 (36,000 barrels). e Emission factor = 9.89 x 10-7 Q) Mg/yr, where Q is the throughput through the tanks in barrels (References 28 and 32). Source: References 28 and 32.

of vapor generation and loss. The second method is submerged filling with either a submerged fill pipe or bottom filling, which significantly reduces liquid turbulence and vapor-liquid resulting in much lower emissions. Table 6-6 shows the uncontrolled emission factors for toluene from a typical bulk plant.

Gasoline tank trucks have been demonstrated to be major sources of vapor leakage. Some vapors may leak uncontrolled to the atmosphere from dome cover assemblies, pressure-vacuum (P-V) vents, and vapor collection piping and vents. Other sources of vapor leakage on tank trucks that occur less frequently include tank shell flaws, liquid and vapor transfer hoses, improperly installed or loosened overfill protection sensors, and vapor couplers. Since terminal 6-20

TABLE 6-6.

UNCONTROLLED GASOLINE VAPOR AND TOLUENE EMISSION FROM A TYPICAL BULK PLANT

Emission Source

a

Gasoline Vapor Emission Factor mg/L


Quality Ratingc

Storage Tanks - Fixed Roof Breathing Loss

600

63.6

U

1150

121.9

U

460

48.8

U

1430

151.6

U

Submerged Loading

590

62.5

U

Submerged Loading (Balance Service)

980

103.9

U

Filling Loss Draining Loss Gasoline Loading Racks Splash Loading

a

Typical bulk plant with a gasoline throughput of 19,000 liters/day (5,000 gallons/day). Based on gasoline emission factor and toluene/vapor ratio of 0.106 (Reference 32). c Based on engineering judgement. Source: References 28 and 32 b

controls are usually found in areas where trucks are required to collect vapors after delivery of product to bulk plants or service stations (balance service), the gasoline vapor emission factor associated with uncontrolled truck leakage was assumed to be 30 percent of the balance service truck loading factor (960 mg/liter x 0.30 = 288 mg/liter).28 Thus, the emission factor for toluene emissions from uncontrolled truck leakage is 30.5 mg/liter, based on a toluene/vapor ratio of 0.106.32

The discussion on service station operations is divided into two areas: the filling of the underground storage tank (Stage I) and automobile refueling (Stage II). Although terminals and bulk plants also have two distinct operations (tank filling and truck loading), the filling of the underground tank at the service station ends the wholesale gasoline marketing chain. The 6-21

automobile refueling operations interact directly with the public and control of these operations can be performed by putting control equipment on either the service station or the automobile.28

Toluene Emission from Service Stations-Normally, gasoline is delivered to service stations in large tank trucks from bulk terminals or smaller trucks from bulk plants. Emissions are generated when hydrocarbon vapors in the underground storage tank are displaced to the atmosphere by the gasoline being loaded into the tank. As with other loading losses, the quantity of the service station tank loading loss depends on several variables, including the quantity of liquid transferred, size and length of the fill pipe, the method of filling, the tank configuration and gasoline temperature, vapor pressure, and composition. A second source of emissions from service station tankage is underground tank breathing. Breathing losses occur daily and are attributed to temperature changes, barometric pressure changes, and gasoline evaporation.28

In addition to service station tank loading losses, vehicle refueling operations are considered to be a major source of emissions. Vehicle refueling emissions are attributable to vapor displaced from the automobile tank by dispensed gasoline and to spillage. The major factors affecting the quantity of emissions are gasoline temperature, auto tank temperature, gasoline Reid vapor pressure (RVP), and dispensing rates. Table 6-7 lists the uncontrolled emissions from a typical gasoline service station. The gasoline vapor emission factors presented in Table 6-7 are from EPA documents.28

6.4.3

Control Technology for Gasoline Transfer

At bulk terminals and bulk plants, toluene emissions from gasoline transfer may be controlled by a vapor processing system in conjunction with a vapor collection system.28 Figure 6-3 shows a Stage I control vapor balance system at a bulk plant. These systems collect and recover gasoline vapors from empty, returning tank trucks as they are filled with gasoline from storage tanks.28

6-22

TABLE 6-7.

UNCONTROLLED GASOLINE VAPOR AND TOLUENE EMISSIONS FROM A TYPICAL SERVICE STATION

Emission Source

a

Gasoline Vapor Emission Factor mg/L


Quality Ratingc

Underground Storage Tanks Tank Filling Losses -

Submerged Fill

-

Splash Fill

-

Balanced Submerged Filling

Breathing Losses

880

93.3

U

1380

146.3

U

40

4.2

U

120

12.7

U

1320

139.9

U

132

13.9

U

84

8.9

U

Automobile Refueling Displacement Losses -

Uncontrolled

-

Controlled

Spillage a

Typical service station has a gasoline throughput of 190,000 liters/month (50,000 gallons/month). b Based on gasoline vapor emission factor and toluene/vapor ratio of 0.106 (Reference 32). c Based on engineering judgement. Source: References 28 and 32

6-23

At service stations, vapor balance systems contain the gasoline vapors within the station’s underground storage tanks for transfer to empty gasoline tank trucks returning to the bulk terminal or bulk plant. Figure 6-4 shows a diagram of a service station vapor balance system.

6.4.4

Control Technology For Gasoline Storage

The control technologies for controlling toluene emissions from gasoline storage involve upgrading the type of storage tank used or addition of a vapor control system. For fixed-roof tanks, emissions are most readily controlled by installation of internal floating roofs.28 An internal floating roof reduces the area of exposed liquid surface on the tank and, therefore, decreases evaporative loss. Installing an internal floating-roof in a fixed-roof tank can reduce total emissions by 68.5 to 97.8 percent.28

For external floating-roof tanks, no control measures have been identified for controlling withdrawal losses and emissions.28 These emissions are functions of the turnover rate of the tank and the characteristics of the tank shell. Rim seal losses in external floating-roof tanks depend on the type of seal. Liquid-mounted seals are more effective than vapor-mounted seals in reducing rim seal losses.28 Metallic shoe seals are more effective than vapor-mounted seals but less effective than liquid mounted seals.28

6.4.5

Control Technology For Vehicle Refueling Emissions

Vehicle refueling emissions are attributable to vapor displaced from the automobile tank by dispensed gasoline and to spillage. The quantity of displaced vapors is dependent on gasoline temperature, vehicle tank size and temperature, fuel level, gasoline RVP, and dispensing rates.28

The two basic refueling vapor control alternatives are control systems on service station equipment (Stage II controls), and control systems on vehicles (onboard controls). Onboard controls are basically limited to the carbon canister.

6-26

There are currently three types of Stage II systems in limited use in the United States: the vapor balance, the hybrid, and the vacuum assist systems. In the vapor balance system, gasoline vapor in the automobile fuel tank is displaced by the incoming liquid gasoline and is prevented from escaping to the atmosphere at the fillneck/nozzle interface by a flexible rubber "boot." This boot is fitted over the standard nozzle and is attached to a hose similar to the liquid hose. The hose is connected to piping which vents to the underground tank. An exchange is made (vapor for liquid) as the liquid displaces vapor to the underground storage tank. The underground storage tank assists this transaction by drawing in a volume of vapor equal to the volume of liquid removed.28

The vacuum assist system differs from the balance system in that a "blower" (a vacuum pump) is used to provide an extra pull at the nozzle/fillneck interface. Assist systems can recover vapors effectively without a tight seal at the nozzle/fillpipe interface because only a close fit is necessary. A slight vacuum is maintained at the nozzle/fillneck interface allowing air to be drawn into the system and not allowing the vapors to escape. Because of this assist, the interface "boot" need not be as tight fitting as with balance systems. Further, the vast majority of assist nozzles do not require interlock mechanisms. Assist systems generally have vapor age valves located in the vapor age somewhere other than in the nozzles, resulting in a nozzle which is less bulky and cumbersome than nozzles employed by vapor balance systems.28

The hybrid system borrows from the concepts of both the balance and vacuum assist systems. It is designed to enhance vapor recovery at the nozzle/fillneck interface by vacuum, while keeping the vacuum low enough so that a minimum level of excess vapor/air is returned to the underground storage tank.

With the hybrid system, a small amount of the liquid gasoline (less than 10 percent) pumped from the storage tank is routed (before metering) to a restricting nozzle called an aspirator. As the gasoline goes through this restricting nozzle, a small vacuum is generated. This vacuum is used to draw vapors into the rubber boot at the interface. Because the vacuum is so small, very little excess air, if any, is drawn into the boot, hose, and underground storage tank, and thus there is no need for a secondary processor, such as the vacuum assist’s incinerator.28 6-27

Onboard vapor control systems consist of carbon canisters installed on the vehicle to control refueling emissions. The carbon canister system adsorbs, on activated carbon, the vapors which are displaced from the vehicle fuel tank by the incoming gasoline. Such a system first adsorbs the emissions released during refueling and subsequently purges these vapors from the carbon to the engine carburetor when it is operating. This system is essentially an expansion of the present evaporative emissions control system used in all new cars to minimize breathing losses from the fuel tank and to control carburetor evaporative emissions. However, unlike the present system, a refueling vapor recovery system will require a tight seal at the nozzle/fillneck interface during refueling operations to ensure vapors flow into the carbon canister and are not lost to the atmosphere.28

6.5

OTHER SOURCES OF RESIDUAL TOLUENE EMISSIONS

Toluene can be emitted during the use of toluene-containing materials in manufacturing another product. Emissions from some of these miscellaneous sources are presented in Table 6-8.

6-28

TABLE 6-8.

RESIDUAL EMISSIONS FROM MISCELLANEOUS SOURCES OF TOLUENE Concentration in Air

Emission Rate

Quality Rating

N/A

0.061 µg/m2/hour

E

Mineral wool used as thermal insulationb

13-90 µg/m3

N/A

D

Building materials (particle board, plywood, sealing agents, wallpaper, floor coverings, paint foam, and concrete)c

39.7 µg/m3

N/A

D

Clear acrylic latex caulk with siliconed

Detected

N/A

Ug

Synthetic rubber adhesive (for walls and ceilings)e

N/A

0.59 µg/g/hour

E

Synthetic rubber adhesive (for vinyl carpet)e

N/A

62 µg/g/hour

E

N/A

2.4-2.6 µg/g/hour

E

detected detected detected

N/A N/A N/A

Ug Ug Ug

Source Particle board with carpeta

Unspecified polymer adhesive (for subflooring)e Building materialsf vinyl cove molding telephone cable urethane insulant N/A - Not available a - Reference 34 b - Reference 35 c - Reference 36 d - Reference 37

e - Reference 38 f - Reference 39 g - Not enough available information to apply a rating

6-29

6.6


1.

SRI International. U.S. Paint Industry Database. Prepared for the National Paint and Coatings Association. Washington D.C. 1990.

2.

U.S. Environmental Protection Agency. Compilation of Air Pollutant Emission Factors. AP-42, fourth edition and supplements. Research Triangle Park, NC. 1985.

3.

U.S. Environmental Protection Agency. Source Assessment: Prioritization of Air Pollution from Industrial Surface Operations, EPA-650/2-75-019a. Research Triangle Park, NC. 1975.

4.

Bridgewater, A.V. and C.J. Mumford, Water Recycling and Pollution Control Handbook. Van Nostrand Reinhold Company. 1979.

5.

Godish, Thad, Air Quality. Director of the Indoor Air Quality Research Laboratory. 1985.

6.

U.S. Environmental Protection Agency. VOC Pollution Prevention Options for the Surface Coating Industry. Research Triangle Park, NC. 1991.

7.

1987 Census of Manufacturers. U.S. Department of Commerce, Bureau of Census.

8.

The NAPL Printer’s Almanac. The Printing Economic Research Center. Association of Printers and Lithographers. Teaneck, New Jersey. 1990.

9.

Gale Research Inc., Ward’s Business Directory of U.S. Private and Public Companies1991. Volume 4. Detroit, MI. 1991.

10.

U.S. Environmental Protection Agency. Guides to Pollution Prevention: The Commercial Printing Industry, EPA/625/7-90/008. Office of Research and Development. Washington, DC. August 1990.

11.

U.S. Environmental Protection Agency. Publication Rotogravure Printing - Background Information for Proposed Standards, EPA-450/3-80-031a. Office of Air Quality Planning and Standards. Research Triangle Park, NC. October 1980.

12.

U.S. Environmental Protection Agency. Control of Volatile Organic Emissions from Existing Stationary Sources. Volume VIII: Graphic Arts Rotogravure and Flexograph, EPA-450/2-78-033. Office of Air Quality Planning and Standards. Research Triangle Park, NC. December 1978.

13.

North Carolina Department of Natural Resources and Community Development. Companion Document for the Conference on Waste Reduction for Industrial Air Toxics Emissions. Pollution Prevention Pays Program. Greensboro, NC. April 24, 1989.

6-30

National

14.

Office of Toxic Substances. Carpenter, Ben H. and Garland K. Hilliard. U.S. Environmental Protection Agency, Overview of Printing Process and Chemicals Used. Conference Proceedings: Environmental Aspects of Chemical Use in Printing Operations. Volume 1: King of Prussia, PA. Washington, DC. September 1975.

15.

Neal, Barry and Robert H. Oppenheimer. "Environmental Regulations and Compliance in the Gravure Industry," Tappi Journal. p. 121. July 1989.

16.

Burt, Richard, Radian Corporation. NSPS for VOC Emissions from Publication Rotogravure Printing Industry. National Air Pollution Control Techniques Advisory Committee Meeting Minutes. December 12-13, 1979.

17.

U.S. Environmental Protection Agency. Control of Volatile Organic Emissions from Existing Stationary Sources. Volume III: Graphic Arts - Rotogravure and Flexography, EPA-450/2-78-033. Emission Standards Engineering Division, Chemical and Petroleum Branch. Research Triangle Park, NC.

18.

Profile Survey of the U.S. Gravure Industry. Gravure Association of America, New York, NY. 1989.

19.

U.S. Environmental Protection Agency. Best Demonstrated Control Technology for Graphic Arts. EPA-450/3-91-008. Office of Air Quality Planning and Standards. Research Triangle Park, NC. February 1991.

20.

U.S. Environmental Protection Agency. Polymeric Coating of ing Substrates-Background Information for Promulgated Standards, Final EIS, EPA-450/3-85-022b. Office of Air Quality Planning and Standards. Research Triangle Park, NC. April 1989.

21.

U.S. Environmental Protection Agency. Magnetic Tape Manufacturing Industry-Background Information for Promulgated Standards, Final EIS, EPA-450/3-85-029b. Office of Air Quality Planning and Standards. Research Triangle Park, NC. July 1988.

22.

Michael Kosusko and Carlos M. Nunez. Air Waste Management Association. Destruction of Volatile Organic Compounds Using Catalytic Oxidation. Volume 2. pp. 254-259. February 1990.

23.

Isaksen, Ivar S. A., et al, "Model Analysis of the Measured Concentration of Organic Gases in the Norwegian Arctic," Journal of Atmospheric Chemistry. 3(1):3-27. 1985.

24.

Sigsby, Jr., John E., Tejada, Silvestre, and Roy, William, "Volatile Organic Compound Emissions from 46 In-Use enger Cars," Environmental Science Technology. 21(5): 466-475. 1987.

6-31

25.

Mo, S.H., Gibbs, R.E., Hill, B.J., Johnson, R.E., Webster, W.J., and Whitby, R.A. Relationships Among Time-Resolved Roadside Measurements of Benzene, Toluene, Xylene and Carbon Monoxide. Presented at the 80th Annual Meeting of APCA. New York, NY. June 21-26, 1987.

26.

U.S. Environmental Protection Agency. Toxic Air Pollutant Emission Factors - A Compilation for Selected Air Toxic Compounds and Sources, EPA-450/2-88-006a. Office of Air Quality Planning and Standards. Research Triangle Park, NC. 1988.

27.

Bartok, William and Sarofim, Adel F., ed., Fossil Fuel Combustion: A Source Book. John Wiley & Sons, Inc. New York, NY. 1991.

28.

U.S. Environmental Protection Agency. Evaluation of Air Pollution Regulatory Strategies for Gasoline Marketing Industry. EPA-450/3-84-012a. Washington, DC. 1984.

29.

U.S. Environmental Protection Agency. Development of VOC Compliance Monitoring and Enforcement Strategies: The Wholesale Gasoline Marketing Chain - Volume II, EPA-340/1-80-01-013a. Office of Air Quality Planning and Standards. Research Triangle Park, NC. July 1980.

30.

Energy Information istration. DOE/EIA=0340(91)/1.

31.

Telecon. George Woodall, TRC Environmental Corporation to Bonnie Ayotte of the Computer Petroleum Company, St. Paul, MN. September 22, 1992.

32.

Memorandum from Chris Lindhjem, et al, U.S. Environmental Protection Agency to Record, U.S. Environmental Protection Agency, "Speciation for SAI Runs," April 14, 1992.

33.

Owen, Keith and Coley, Trevor, Automotive Fuels Handbook. Society of Automotive Engineers, Inc. Warrendale, PA. 1990.

34.

Colombo, A., et al, "Chamber Testing of Organic Emissions from Building and Furnishing Materials," The Science of the Total Environment. 91: 237-249. 1990.

35.

van der Wal, Jan F., et al, "Thermal Insulation as a Source of Air Pollution," Environment International. 15: 409-412. 1989.

36.

Molhave, Lars, "Indoor Air Pollution due to Organic Gases and Vapors of Solvents in Building Materials," Environment International. 8(1-6): 117-127. 1982.

37.

Tichenor, Bruce A., Jackson, Merrill D., and Merrill, Raymond G., "Measurement of Organic Emissions from Indoor Materials - Small Chamber Studies," Proceedings of the 1986 EPA/APCA Symposium on Measurement of Toxic Air Pollutants.

Petroleum Supply Annual 1991, Volume 1.

6-32

38.

Girman, J.R., et al, "Emissions of Volatile Organic Compounds from Adhesives with Indoor Applications," Environment International. 12(1-4): 317-321. 1986.

39.

Sheldon, Linda S., et al, "Volatile Organic Emissions from Building Materials," Presented at the 79th Annual Meeting of the Air Pollution Control Association. Minneapolis, MN. June 22-27, 1986.

6-33

SECTION 7.0 BY-PRODUCT EMISSIONS: PROCESSES UNRELATED TO PRODUCTION OR USE OF TOLUENE

Toluene and other pollutants can be emitted to the atmosphere as the result of product manufacturing or from the burning of fossil fuels. Processes that release toluene as by-product emissions are described in this section. These processes include coal combustion, hazardous and solid waste incineration, and wastewater treatment processes. Data pertaining to emissions from fossil fuel combustion in boilers and heaters were unavailable and therefore are not included in this section.

7.1

COAL COMBUSTION

Two coal combustion studies are briefly described in this section. analyzed samples collected from a gasifier.

The first study

The second coal combustion study analyzed

emissions from a burning coal refuse pile.1,2

A coal combustion study was performed to collect data on the chemical composition of fugitive aerosol emissions at a pilot-scale gasifier using lignite coal. Sampling was conducted at the Grand Forks Energy Technology Center gasifier, Grand Forks, North Dakota. From the gas chromatography (GC) and gas chromatography/mass spectrometry (GC/MS) analyses that were performed, it was determined that toluene existed at the gasifier. However, no data were reported.1

Another air monitoring study was performed on a burning coal refuse (gob) pile in Oak Hill, West Virginia. The West Virginia Air Pollution Control Commission requested assistance from EPA to perform a study of the heavy metal and organic chemical emissions from a burning gob pile.

Carbon monoxide emissions are expected from these burning gob piles, while

emissions of other compounds such as toluene are suspected. Under the direction of EPA, GCA/Technology Division performed a study on the types and quantities of emissions from the gob pile.2 7-1

The gob pile studied was similar to many of the hundred known to exist in coal mining areas in the country. This coal waste pile was created as the result of a nearby deep mining operation.

The emissions have been generated for decades as a result of the spontaneous

combustion of low grade, yet combustible coal refuse material.2

Red dog, the solid matrix remaining after the combustible fractions are burned out of the coal waste is a popular fill and highway construction material. The two major results of mining red dog are increased gaseous emissions and an increased fugitive particulate emission rate due to the excavation and loading of the red dog into trucks. The slow natural combustion process presents a difficult situation for effective pollution control. Due to cost and the large amount of material involved, emission control of such a large area source is usually restrictive, although not impossible.2

GCA’s investigative study was a two-phase approach in order to maximize the quality of results. The first phase was a preliminary assessment, followed by a more comprehensive quantitative emissions program. The preliminary assessment assisted in identifying pollutants present in the gob pile emissions and their approximate concentrations. The second phase of the investigation began with the siting of GCA’s Mobile Laboratory and the startup of the analytical instrumentation. In addition, two meteorological monitoring stations were erected and calibrated, one at approximately 10 feet elevation directly at the test area and one slightly downwind at approximately 200 feet in elevation above the test area to measure overall regional wind conditions.2

Samples were collected at the centerpoint of each of 24 equal area grids. All samples were collected from within 10-inch diameter ductwork positioned over the sample point to minimize dilution, mixing, and variable wind conditions.

After all sample analyses were

completed, a calculation was performed to convert measured concentrations (ppm, ppb, µg/m3) to average emission rates (lb/hr) for each parameter. An extrapolation of the average emission rate from the sampled area to that of the total pile was then performed. Also, due to the large range of values for most parameters, a standard error calculation was used to describe the

7-2

variability of each compound specific average rate. Table 7-1 lists the emission rate and the emission factor for toluene resulting from this study.2

TABLE 7-1.

TOLUENE EMISSIONS FROM COMBUSTIBLE COAL REFUSE MATERIAL Parameter

Total Emission Rate

Emission Factor

Toluene

4.3 + 3.6 kg/hr (9.4 + 8.0 lb/hr)

4.1 x 10-5 kg/hr/m3 (2.5 x 10-6 lb/hr/ft3) of burning refuse material

Quality Rating D

Source: Reference 2.

In summary, the investigative study resulted in calculated emission rates and emission factors for various parameters. This study concludes that the possibility of downwind exposure to toxic and suspected toxic airborne contaminants from the burning coal refuse pile exists.2

7.2

HAZARDOUS AND SOLID WASTE INCINERATION

The majority of atmospheric emissions of pollutants from the various hazardous and solid waste disposal methods comes from incineration.

In addition to particulate matter, other

pollutants, such as volatile organic compounds (including toluene) and carbon monoxide are frequently emitted as a result of incomplete combustion of the waste due to improper combustor design or poor operating conditions.

Several methods are used to incinerate municipal waste. These include mass burn excess air combustion, starved air or modular combustion, and refuse-derived fuel combustion. Approximately 70 percent of the total municipal solid waste is incinerated in mass burn units. More information on the methods of municipal waste combustion can be found in the document, Characterization of the Municipal Waste Combustion Industry.3 Similarly, hazardous waste can

7-3

be incinerated by several methods including thermal, catalytic and regenerative incineration. Toluene emission factors from incineration sources were not found.

Open-air burning presents a particularly unique source of atmospheric emissions of pollutants. This method of solid waste incineration allows for exposure to many variables including wind, ambient temperatures, and other environmental parameters such as rain and humidity, degree of compactness of the refuse, and composition and moisture of the refuse. In general, lower temperatures are achieved in open-air burning than in closed combustion. Therefore, this allows for increased emissions of particulate matter, carbon monoxide, and volatile organic compounds (including toluene) with decreased emissions of nitrogen oxides. Other important regulating factors for open-air burning are fuel loading (how much refuse material is burned per unit of land area) and arrangement of the refuse (in rows, piles, or spread out).4 Although specific toluene emission factors are unavailable, data indicate that emissions of volatile organic compounds from non-agricultural materials are approximately 25 percent methane, 8 percent other saturates, 18 percent olefins, and 42 percent other compounds (oxygenates, acetylene, and aromatics, including toluene).4

7.3

WASTEWATER TREATMENT PROCESSES

Atmospheric emissions of volatile organic compounds such as toluene can occur at any wastewater treatment process where the wastewater comes into with the surrounding ambient air. An estimated 5 million kilograms (11 million pounds) of toluene are discharged to the environment annually as a constituent in wastewater.5 A study conducted at two Chicago-area wastewater treatment facilities estimated that approximately 94 percent of the toluene in the influent waters biodegraded in activated sludge systems while only 3 percent volatilized. However, if all of the influent toluene at the two facilities were to volatilize, it would for nearly 29,000 kilograms (64,000 pounds) per year.6 Another study conducted in California estimated total air emissions of toluene from statewide municipal wastewater treatment plants to be approximately 250,000 kilograms (550,000 pounds per year).7

7-4

The majority of air emissions from wastewater treatment facilities usually comes from the initial physical processes (e.g., screening, sedimentation, floatation, and filtration) due to both a higher pollutant concentration in the influent and a greater surface area caused by turbulence and mixing. Other sources of emissions include equalization and aeration basins and clarifiers. Because of the many factors that may affect emissions of volatile organics, including toluene, from wastewater treatment processes, calculating actual emissions estimates must be performed on a chemical-by-chemical, process-by-process basis. Several models have been developed that estimate emissions from wastewater treatment processes. A brief description of some appropriate models are presented below; however, further information should be consulted in the appropriate reference(s).

The SIMS model (Surface Impoundment Modeling System), developed by the Control Technology Center of the U.S. Environmental Protection Agency, is a personal computer-based software program designed to estimate atmospheric emissions from surface impoundments and wastewater collection devices.8,9 The Tsivoglou and Neal Reaeration model can be used with the SIMS model to estimate VOC emissions from the devices that comprise the headworks of a POTW (since the SIMS model does not for emissions from these devices or for adsorption onto solids).10

Several inherent problems exist with using these models. First, the VOC concentrations in the wastewater are highly variable among the influent, effluent, and sludge partitions: therefore, a single emission estimate would be highly questionable. Second, the estimates are usually based on constant behavior of relatively pure compounds, so mixing and variable chemical concentrations would render the emission factors less useful. Finally, these estimates are generally on the conservative side, and actual emissions will often tend to be higher than the estimates.

A major process resulting in the emission of wastewater pollutants is the separation of the lighter organic phase from the main body of wastewater and the heavier inorganic solid phase. A top organic layer consisting of many volatile organic and oil-based compounds is formed and exposed to ambient air. Factors affecting volatilization of organic compounds from the top 7-5

organic layer include characteristics of the wastewater and oil layers, the ambient wind speed, design characteristics of the wastewater treatment operation, the concentration of pollutants in the wastewater, detention time in the treatment system, and partition coefficients of the pollutants. EPA has published several guidance documents and reports regarding emissions from wastewater treatment systems which are referenced here.7,8

7-6

7.4


1.

Joseph R. Stetter, Richard D. Flotard, and Elizabeth Gebert. Environmental Monitoring and Assessment in International Journal, Characterization of Airborne Particles at a High-BTU Coal-Gasification Pilot Plant. 1(4). 1982.

2.

Seely, Douglas E. and Engle, Ronald J. Investigative Air Monitoring Study at a Burning Coal Refuse Pile in Oak Hill, West Virginia. Presented at the 77th Annual Meeting of APCA. San Francisco, CA. June 24-29, 1984.

3.

Radian Corporation. Characterization of the Municipal Waste Combustion Industry, Appendix A. Research Triangle Park, NC. October 1986.

4.

Gerstle, R.W., and D. A. Kemnitz. "Atmospheric Emissions from Open Burning," Journal of Air Pollution Control Association. 12:324-327. May 1967.

5.

U.S. Environmental Protection Agency. Development Document for Effluent Limitations Guidelines and Standards for the Plastics Molding and Forming Point Source Category, EPA-450/1-84-069b. Effluent Guidelines Division. Washington DC. 1984.

6.

Rittman, Bruce E. and Namkung, Eun. "Estimating Volatile Organic Compound Emissions from Publicly Owned Treatment Works," Journal of The Water Pollution Control Federation, 59(7):670-678. July 1987.

7.

Corsi, Richard L. "Emissions of Volatile and Potentially Toxic Organic Compounds from Municipal Wastewater Treatment Plants." Presented at the 80th Annual Meeting of APCA. New York, NY. June 21-26, 1987.

8.

U.S. Environmental Protection Agency. Guidance Services, Control of Volatile Organic Compound Emissions from Industrial Wastewater, Volume I, Preliminary Draft. Office of Air Quality Planning and Standards. Research Triangle Park, NC. April 1989.

9.

U.S. Environmental Protection Agency. Surface Impoundment Modeling System (SIMS) Version 2.0 ’s Manual, EPA-450/4-90-019a. Control Technology Center. Research Triangle Park, NC. 1990.

10.

Tsivoglou, E.C., and L.A. Neal. "Tracer Measurement of Reaeration, III. Predicting the Reaeration Capacity of Inland Streams," Journal of Water Pollution Control Federation. 48(12):2669. 1976.

7-7

SECTION 8.0 AMBIENT AIR AND STATIONARY SOURCE TEST PROCEDURES

Toluene emissions can be measured from ambient air and stationary sources utilizing the test methods presented below. If applied to stack sampling, the ambient air monitoring methods may require adaptation or modification. If ambient air methodology is applied to stationary source testing, appropriate precautions must be taken to ensure that the capacity of the methodology is not exceeded so that results will be quantitative. Ambient methods which require the use of sorbents are susceptible to sorbent saturation if high concentration levels exist. If this happens, breakthrough will occur, and quantitative analysis is not possible.

•

EPA Method TO-1: Determination of Volatile Organic Compounds in Ambient Air Using Tenax® Adsorption and Gas Chromatography/Mass Spectrometry (GC/MS)

•

EPA Method TO-2: Determination of Volatile Organic Compounds in Ambient Air by Carbon Molecular Sieve Adsorption and Gas Chromatography/Mass Spectrometry (GC/MS)

•

EPA Method TO-3: Determination of Volatile Organic Compounds in Ambient Air Using Cryogenic Preconcentration Techniques and Gas Chromatography with Flame Ionization and Electron Capture Detection

•

EPA Method TO-14: Determination of Volatile Organic Compounds (VOCs) in Ambient Air Using SUMMA® ivated Canister Sampling and Gas Chromatographic (GC) Analysis

•

EPA Method 0030: Volatile Organic Sampling Train (VOST) with EPA Method 5040: Analysis of Sorbent Cartridges from VOST

•

EPA Reference Method 18: Measurement of Gaseous Organic Compound Emissions by Gas Chromatography

•

EPA Method 0010: Modified Method 5 Sampling Train with EPA Method 8270: Gas Chromatography/Mass Spectrometry for Semi-volatile Organics: Capillary Column Technique

•

NIOSH Method 1501: Aromatic Hydrocarbons

8-1

The following subsections briefly describe the recommended sampling and analytical methods for determining toluene emissions.

8.1

EPA METHOD TO-11

Ambient air concentrations of toluene can be measured using EPA Method TO-1 from the Compendium of Methods for the Determination of Toxic Organic Compounds in Ambient Air. This method is used to collect and determine volatile nonpolar organics (aromatic hydrocarbons, chlorinated hydrocarbons) that can be captured on Tenax® and determined by thermal desorption techniques. The compounds determined by this method have boiling points in the range of 80° to 200°C (180° to 390°F).

Figure 8-1 presents a schematic of the sampling system and Figure 8-2 presents a schematic of typical Tenax® cartridge designs.

Ambient air is drawn through the cartridge which contains approximately 1-2 grams (0.035 to 0.07 ounces) of Tenax®. Toluene is trapped on the Tenax® cartridge which is then capped and sent to the laboratory for analysis utilizing purge-and-trap gas chromatography/mass spectrometry (GC/MS) according to the procedures specified in EPA Method 5040 (see Section 8.6). The recommended GC column is a 50 meter capillary, type SE-30 with an internal diameter of 0.3 mm.

The exact run time, flow rate and volume sampled varies from source to source depending on the expected concentrations and the required detection limit. Typically, 10 to 20 L (0.3 to 0.7 ft3) of ambient air are sampled. Analysis should be conducted within 14 days of sample collection.

8.2

EPA METHOD TO-21

Ambient air concentrations of toluene can be measured using EPA Method TO-2 from the Compendium of Methods for the Determination of Toxic Organic Compounds in Ambient Air. 8-2

Compounds which can be determined using this method are nonpolar and highly volatile organics that can be captured on carbon molecular sieve (CMS) and determined by thermal desorption techniques. The compounds to be determined by this method have boiling points in the range of -15° to 120°C (5° to 250°F). Toluene can be determined using this method.

In summary, ambient air is drawn through a cartridge containing approximately 0.4 grams (0.01 ounces) of CMS adsorbent. Toluene is captured on the adsorbent while major inorganic compounds through. The sample is then capped and sent to the laboratory for analysis. Prior to analysis, the CMS cartridge is purged with 2 or 3 L (0.07 to 0.1 ft3) of pure dry air to remove any moisture. The cartridge is then heated to 350° to 400°C (660° to 750°F) under a helium purge, and the desorbed toluene is collected in a specially designed cryogenic trap. The collected toluene is then flash evaporated onto a capillary column (SE-30) and quantified using a GC/MS system.

The exact run time, flow rate and volume sampled varies from source to source depending on the expected concentration and the required detection limit. Typically, Method TO-2 is used when ambient air concentrations are expected to be high. CMS has the ability to adsorb large quantities of organics before breakthrough occurs.

Figure 8-1 is representative of both Methods TO-1 and TO-2 sampling systems. Figure 8-3 illustrates a CMS trap.

8.3

EPA METHOD TO-31

Ambient air concentrations of toluene can be measured directly at the source using EPA Method TO-3 from the Compendium Methods for the Determination of Toxic Organic Compounds in Ambient Air. This method is designed for the determination of highly volatile nonpolar organic compounds having boiling points in the range of -10° to 200°C (14° to 390°F). Figure 8-4 presents a schematic of a typical on-line GC sampling system using cryogenic trapping. 8-5

The ambient air sample is collected in the cryogenic trap using a vacuum pump equipped with a mass flow controller. The GC oven is then chilled to a subambient temperature. The sample valve is then switched and the sample is carried onto the cooled GC column. Simultaneously, the cryogenic trap is heated to assist in the sample transfer process. The GC column is then heated to the desired temperature and the eluting peaks are identified and quantified using a flame ionization detector (FID).

8.4

EPA METHOD TO-141

Ambient air concentrations of toluene can also be measured using EPA Method TO-14 from the Compendium of Methods for the Determination of Toxic Organic Compounds in Ambient Air. This method is based on collection of a whole air sample in SUMMA® ivated stainless steel canisters and is used to determine semi-volatile and volatile organic compounds. The compounds are separated by gas chromatography and measured by mass-selective detector or multidetector techniques such as FID, electron capture detection (ECD), and photoionization detection (PID). The recommended column for Method TO-14 is an HP OV-1 capillary with 0.32mm I.D. x 0.88 µm cross-linked methyl silicone coating or equivalent. Samples should be analyzed within 14 days of collection.

This method is applicable to specific semi-volatiles and volatile organic compounds that have been tested and determined to be stable when stored in pressurized and subatmospheric pressure canisters. Toluene can be successfully measured at the parts per billion by volume (ppbv) level using this method.

Figure 8-5 presents a diagram of the canister sampling system.

8.5

EPA METHOD 00302

The volatile organic sampling train (VOST) from SW-846, (third edition) is designed for the collection of volatile organic compounds from the stack gas effluents of hazardous waste 8-8

incinerators. The VOST method was designed to collect volatile organics with boiling points in the range of 30° to 100°C (86° to 212°F). Many compounds with boiling points above 100°C (212°F) may also be effectively collected using this method. Toluene concentrations can be measured using this method. Figure 8-6 presents a schematic of the principle components of the VOST. In most cases, 20 L (0.7 ft3) of effluent stack gas are sampled at an approximate flow rate of 1 L/minute (0.04 ft3/min) using a glass-lined heated probe. The gas stream is cooled to 20°C (68°F) by age through a water-cooled condenser and the volatile organics are collected on a pair of sorbent resin traps. Liquid condensate is collected in the impinger located between the two resin traps. The first resin trap contains about 1.6 g (0.06 ounce) Tenax® and the second trap contains about 1 g (0.04 ounce) each of Tenax® and petroleum-based charcoal. The Tenax® cartridges are then thermally desorbed and analyzed by purge-and-trap GC/MS along with the condensate catch as specified in EPA Method 5040. Analysis should be conducted within 14 days of sample collection.

8.6

EPA METHOD 50402

Principal organic hazardous constituents (POHCs) are collected on Tenax® and Tenax®/charcoal sorbent cartridges using a VOST, EPA Method 0030. The contents of the sorbent cartridges are spiked with an internal standard and thermally desorbed for 10 minutes at 80°C (176°F) with organic-free nitrogen or helium gas [at a flow rate of 40 mL/min (2.4 in3)], bubbled through 5 mL (0.3 in3) of organic-free water, and trapped on an analytical adsorbent trap. After the 10 minute desorption, the analytical adsorbent trap is rapidly heated to 180°C (356°F), with the carrier gas flow reversed so that the effluent flow from the analytical trap is directed into the GC/MS.

The volatile POHCs are separated by temperature-programmed gas

chromatography and detected by low resolution mass spectrometry. The concentrations of the volatile POHCs are calculated using the internal standard technique.

8-10

EPA Methods 5030 and 8240 may be referenced for specific requirements for the thermal desorption unit, purge-and-trap unit, and GC/MS system. A diagram of the analytical system is presented in Figure 8-7. The Tenax® cartridges should be analyzed within 14 days of collection. The desired detection limit of this method is 0.1 ng/L (20 ng per Tenax® cartridge).

8.7

EPA REFERENCE METHOD 183

EPA Reference Method 18 from 40 CFR Part 60, Appendix A, can be utilized for the sampling and analysis of approximately 90 percent of the total gaseous organics emitted from industrial sources. It does not include techniques to identify and measure trace amounts of organic compounds, such as those found in room air and from fugitive sources.

Toluene

emissions can be measured from stationary sources using this method. Method 18 can be conducted using either the direct interface method (on-line GC with FID) or by the collection of an integrated Tedlar® or Mylar® bag with subsequent analysis by GC/FID.

The direct interface method draws a sample of the exhaust gas through a heated sample line directly into a heated sample loop and onto the column of the GC fitted with an FID. Figure 8-8 presents a diagram of the principle components of the direct interface sampling system.

Using the bag in drum technique as presented in Figure 8-9, a sample of the exhaust gas is drawn into a Tedlar® or Mylar® bag. The bag is placed inside a rigid leakproof container and evacuated. The bag is then connected by a Teflon® sample line to a sampling probe located at the center of the stack. The sample is drawn into the bag by pumping air out of the rigid container. The sample is then analyzed on-site or back at the laboratory by GC/FID. The stability of toluene in a Tedlar® or Mylar® bag is currently unknown. Therefore, it is recommended that the analysis be conducted as soon as possible.

8-12

8.8

EPA METHOD 00102

EPA Method 0010 (Modified Method 5 Sampling Train) is used to determine the destruction and removal efficiency of semi-volatile principal organic hazardous constituents (POHCs) from incineration systems.

This method may be used for determining toluene

emissions.

Gaseous and particulate pollutants are withdrawn isokinetically from an emission source and collected in a multicomponent sampling train. Figure 8-10 presents a schematic of the sampling system. Principal components of the train include a high-efficiency glass- or quartz® fiber filter and a packed bed of porous polymeric adsorbent resin (typically XAD-2 or polyurethane foam for PCBs). The filter is used to collect organic-laden particulate materials and the porous polymeric resin to adsorb semi-volatile organic species (compounds with a boiling point above 100°C (212°F)). Comprehensive chemical analyses, using a variety of applicable analytical methodologies, are conducted to determine the identity and concentration of the organic materials.

8.9

EPA METHOD 82702

EPA Method 8270 is used to determine the concentration of semi-volatile organic compounds in extracts prepared from all types of solid waste matrices, soils, and ground water. It is also applicable to an extract from sorbent media in conjunction with Method 0010. Direct injection of a sample may be used in limited applications.

Method 8270 can be used to quantify most neutral, acidic, and basic organic compounds that are soluble in methylene chloride and capable of being eluted without derivatization as sharp peaks from a gas chromatographic fused-silica capillary column coated with a slightly polar silicone.

Toluene is within the boiling point range and may be determined using this

methodology.

8-16

The practical quantitation limit for Method 8270 is approximately 50 µg/mL of extract. The entire sorbent module with filter is typically extracted and concentrated to 1 mL (0.03 in3) (a final volume of 5 mL (0.2 in3)is used to avoid loss of volatile compounds), and this final extract volume represents the entire volume of gas sampled.

8.10

NIOSH METHOD 15014

Ambient air and exhaust gas concentrations of toluene can also be measured using NIOSH Method 1501. The levels of detection for NIOSH methods are usually much higher than the other procedures discussed. NIOSH methods are designed for worker exposure studies that are usually conducted over an 8 hour period.

Ambient air or exhaust gas samples are collected on a solid sorbent tube containing coconut shell charcoal with 100 mg on the front-half portion and 50 mg on the back-half. Two to 8 L (0.07 to 0.3 ft3) of air are collected, depending on the expected concentrations, using a vacuum pump set at an approximate flow rate of 0.2 L/minute (0.007 ft3/minute).

The

breakthrough volume for toluene is 12 L (0.4 ft3).

The samples are then capped, sent to the laboratory, desorbed with carbon disulfide (CS2) and analyzed by GC/FID. The column specified in NIOSH Method 1501 is a 3.0m x 2mm glass or stainless steel with 10 percent OV-275 on 100/200 mesh Chromosorb W-AW or equivalent. The stability of the sorbent sample is currently unknown, therefore analysis should be conducted as soon as possible.

Figure 8-11 presents a schematic of the sampling system.

8-18

8.11


1.

U.S. Environmental Protection Agency. Compendium of Methods for the Determination of Toxic Organic Compounds in Ambient Air. EPA/600/4-89/017. June 1988.

2.

U.S. Environmental Protection Agency. Test Methods for Evaluating Solid Waste, Third Edition, Report No. SW-846. Office of Solid Waste and Emergency Response. Washington, DC. November 1986.

3.

40 CFR, Part 60, Appendix A, Method 18: Measurement of Gaseous Organic Compounds by Gas Chromatography. pp 823 through 852.

4.

NIOSH Manual of Analytical Methods, Third Edition, Volume 1 and 2. February 1984.

8-20

APPENDIX A POTENTIAL SOURCE CATEGORIES OF TOLUENE EMISSIONS

A-1

TABLE A-1.

POTENTIAL SOURCE CATEGORIES OF TOLUENE EMISSIONS (continued) SIC Code

Source Description

1011

Iron ores: taconite iron ore processing

1099

Metal ores, NEC: aluminum ore (bauxite)

1300

Oil and gas extraction fuel fired process heaters

1311

Oil and gas production: crude oil production

1321

Natural gas liquids

1382

Oil and gas exploration services

1400

Nonmetallic minerals, except fuels (mining operations)

1442

Mineral products: sand and gravel

1475

Mineral products: phosphate rock

1499

Mineral products: salt mining

1611

Highway and street construction

1629

Heavy construction, nec

1781

Water well drilling

1791

Structural steel erection

1799

Special trade contractors, nec

2000

Food and agriculture fuel fired equipment: process heaters

2011

Meat packing plants

2013

Sausages and other prepared meats

2015

Food and kindred products: poultry slaughtering and processing

2023

Dry, condensed, evaporated products

2026

Fluid milk

2032

Organic solvent surface coating: can coating

2033

Canned fruits and vegetables

2034

Dehydrated fruits, vegetables, soups

2037

Frozen fruits and vegetables (continued) A-2

TABLE A-1.


Source Description

2043

Cereal breakfast foods

2044

Rice milling

2046

Wet corn milling

2047

Dog and cat food

2048

Prepared feeds, nec

2051

Bread, cake, and related products

2052

Cookies and crackers

2064

Candy & other confectionery products

2076

Vegetable oil mills, nec

2077

Animal and marine fats and oils

2079

Edible fats and oils, nec

2082

Malt beverages

2084

Wines, brandy, and brandy spirits

2085

Distilled and blended liquors

2086

Bottled and canned soft drinks

2087

Flavoring extracts and syrups, nec

2091

Canned and cured fish and seafoods

2099

Food preparations, nec

2111

Cigarettes

2121

Cigars

2200

Organic solvent - textile manufacturing: knit fabric scouring

2211

Broadwoven fabric mills, cotton

2221

Broadwoven fabric mills, manmade

2231

Broadwoven fabric mills, wool

2241

Narrow fabric mills (continued) A-3

TABLE A-1.


Source Description

2257

Weft knit fabric mills

2261

Finishing plants, cotton

2262

Finishing plants, manmade

2269

Finishing plants, nec

2281

Yarn spinning mills

2282

Throwing and winding mills

2284

Thread mills

2295

Coated fabrics, not rubberized

2296

Tire cord and fabrics

2297

Nonwoven fabrics

2298

Cordage and twine

2299

Textile goods, nec

2321

Men’s and boys’ shirts

2326

Men’s and boys’ work clothing

2341

Women’s and children’s underwear

2353

Hats, caps, and millinery

2369

Girls’ and children’s outerwear, nec

2381

Fabric dress and work gloves

2385

Waterproof outerwear

2387

Apparel belts

2389

Apparel and accessories, nec

2392

House furnishings, nec

2394

Canvas and related products

2396

Automotive and apparel trimmings

2399

Fabricated textile products, nec (continued) A-4

TABLE A-1.


Source Description

2421

Sawmills and planing mills, general

2426

Hardwood dimension & flooring mills

2429

Special product sawmills, nec

2431

Millwork

2434

Wood kitchen cabinets

2435

Hardwood veneer and plywood

2436

Softwood veneer and plywood

2439

Structural wood , nec

2449

Wood containers, nec

2451

Mobile homes

2452

Prefabricated wood buildings

2491

Wood preserving

2493

Lumber and wood products: reconstituted wood products

2499

Wood products, nec

2511

Wood household furniture

2512

Upholstered household furniture

2514

Metal household furniture

2515

Mattresses and bedsprings

2517

Wood TV and radio cabinets

2519

Household furniture, nec

2521

Wood office furniture

2522

Office furniture, except wood

2531

Public building & related furniture

2541

Wood partitions and fixtures

2542

Partitions and fixtures, except wood (continued) A-5

TABLE A-1.


Source Description

2585

Refrigeration and heating equipment

2591

Drapery hardware & blinds & shades

2599

Furniture and fixtures, nec

2611

Pulp mills

2621

Paper mills

2631

Paperboard mills

2652

Setup paperboard boxes

2653

Corrugated and solid fiber boxes

2655

Fiber cans, drums & similar products

2656

Sanitary food containers

2657

Paper and allied products: folding paperboard boxes

2670

Paper and allied products: miscellaneous converted paper products

2670

Organic solvent surface coating: paper coating

2671

Paper coated & laminated, packaging

2672

Paper coated and laminated, nec

2673

Bags: plastics, laminated, & coated

2674

Bags: uncoated paper & multiwall

2675

Paper and allied products: die-cut paper and board

2676

Sanitary paper products

2677

Envelopes

2679

Paper and allied products: converted paper products

2711

Newspapers

2721

Periodicals

2731

Book publishing

2732

Book printing (continued) A-6

TABLE A-1.


Source Description

2741

Miscellaneous publishing

2751

Printing/publishing: printing process

2752

Commercial printing, lithographic

2754

Commercial printing, gravure

2759

Printing and publishing: commercial printing, nec

2761

Manifold business forms

2771

Greeting cards

2782

Blankbooks and looseleaf binders

2789

Bookbinding and related work

2791

Typesetting

2796

Printing and publishing: platemaking services

2800

Chemicals and allied products

2812

Alkalies and chlorine

2813

Industrial gases

2816

Inorganic pigments

2819

Industrial inorganic chemicals, nec

2821

Plastics materials and resins

2822

Synthetic rubber

2823

Cellulosic manmade fibers

2824

Organic fibers, noncellulosic

2833

Medicinals and botanicals

2834

Pharmaceutical preparations

2835

Diagnostic substances

2836

Biological products exc. diagnostic

2841

Soap and other detergents (continued) A-7

TABLE A-1.


Source Description

2842

Polishes and sanitation goods

2843

Surface active agents

2844

Toilet preparations

2851

Paints and allied products

2861

Gum and wood chemicals

2865

Cyclic crudes and intermediates

2869

Industrial organic chemicals, nec

2873

Nitrogenous fertilizers

2874

Phosphatic fertilizers

2879

Agricultural chemicals, nec

2891

Adhesives and sealants

2892

Explosives

2893

Printing ink

2895

Carbon black

2899

Chemical preparations, nec

2900

Petroleum and coal products petroleum industry

2911

Petroleum refining

2922

Petroleum Industry: Lube Oil Refining

2951

Asphalt paving mixtures and blocks

2952

Asphalt felts and coatings

2992

Lubricating oils and greases

2999

Petroleum industry - petroleum refining: sludge converter

3011

Tires and inner tubes

3021

Rubber and plastics footwear

3052

Rubber and plastics products: rubber and plastics hose and belting (continued) A-8

TABLE A-1.


Source Description

3053

Gaskets, packing and sealing devices

3061

Mechanical rubber goods

3069

Fabricated rubber products, nec

3079

Organic solvent: surface coating of plastic parts

3080

Rubber and plastics products: miscellaneous plastics products, nec

3081

Uned plastics film & sheet

3082

Uned plastics profile shapes

3083

Laminated plastics plate & sheet

3086

Plastics foam products

3087

Custom compound purchased resins

3088

Plastics plumbing fixtures

3089

Plastics products, nec

3111

Leather tanning and finishing

3131

Footwear cut stock

3142

House slippers

3143

Men’s footwear, except athletic

3144

Women’s footwear, except athletic

3149

Footwear, except rubber, nec

3172

Personal leather goods, nec

3199

Leather goods, nec

3211

Flat glass

3221

Glass containers

3229

Pressed and blown glass, nec

3231

Products of purchased glass

3241

Cement, hydraulic (continued) A-9

TABLE A-1.


Source Description

3251

Mineral products: brick manufacturing

3253

Ceramic wall and floor tile

3255

Mineral products: castable refractory

3261

Vitreous plumbing fixtures

3263

Semivitreous table & kitchenware

3264

Porcelain electrical supplies

3271

Concrete block and brick

3272

Concrete products, nec

3274

Lime

3275

Mineral products: gypsum manufacturing

3291

Abrasive products

3292

Asbestos products

3295

Minerals, ground or treated

3296

Mineral wool

3297

Nonclay refractories

3299

Nonmetallic mineral products, nec

3300

Secondary metals: misc. casting and fabricating

3312

Blast furnaces and steel mills

3313

Electrometallurgical products

3315

Steel wire and related products

3316

Cold finishing of steel shapes

3317

Steel pipe and tubes

3320

Primary metal industries, iron and steel foundries

3321

Primary metal industries: gray and ductile iron foundries (gray iron)

3324

Steel investment foundries (continued) A-10

TABLE A-1.


Source Description

3325

Steel foundries, nec

3331

Primary copper

3334

Primary aluminum

3339

Primary metal industries: primary nonferrous metals, nec (lead production)

3341

Secondary nonferrous metals

3351

Copper rolling and drawing

3353

Aluminum sheet, plate, and foil

3354

Aluminum extruded products

3355

Aluminum rolling and drawing, nec

3357

Nonferrous wiredrawing & insulating

3360

Primary metal industries: nonferrous foundries (castings)

3363

Aluminum die-castings

3364

Nonferrous die-casting exc. aluminum

3365

Aluminum foundries

3366

Copper foundries

3369

Nonferrous foundries, nec

3398

Metal heat treating

3399

Primary metal products, nec

3400

Fabricated metal products: iron and steel general processes

3411

Metal cans

3412

Metal barrels, drums, and pails

3421

Cutlery

3423

Hand and edge tools, nec

3425

Saw blades and handsaws

3429

Hardware, nec (continued) A-11

TABLE A-1.


Source Description

3431

Fabricated metal products: porcelain enamel/ceramic glaze spraying

3432

Plumbing fixture fittings and trim

3433

Heating equipment, except electric

3441

Fabricated structural metal

3442

Metal doors, sash, and trim

3443

Fabricated plate work (boiler shops)

3444

Sheet metalwork

3446

Architectural metal work

3448

Prefabricated metal buildings

3449

Miscellaneous metal work

3451

Screw machine products

3452

Bolts, nuts, rivets, and washers

3462

Iron and steel forgings

3463

Nonferrous forgings

3465

Automotive stampings

3466

Crowns and closures

3469

Metal stampings, nec

3471

Plating and polishing

3479

Metal coating and allied services

3482

Small arms ammunition

3483

Ammunition, exc. for small arms, nec

3484

Small arms

3489

Ordnance and accessories, nec

3491

Industrial valves

3492

Fluid power valves & hose fittings (continued) A-12

TABLE A-1.


Source Description

3493

Steel springs, except wire

3494

Valves and pipe fittings, nec

3496

Misc. fabricated wire products

3497

Metal foil and leaf

3498

Fabricated pipe and fittings

3499

Fabricated metal products, nec

3511

Turbines and turbine generator sets

3519

Internal combustion engines, nec

3523

Farm machinery and equipment

3524

Lawn and garden equipment

3531

Construction machinery

3532

Mining machinery

3533

Oil and gas field machinery

3534

Elevators and moving stairways

3535

Conveyors and conveying equipment

3536

Hoists, cranes, and monorails

3537

Industrial trucks and tractors

3541

Machine tools, metal cutting types

3542

Machine tools, metal forming types

3543

Industrial patterns

3544

Special dies, tools, jigs & fixtures

3545

Machine tool accessories

3546

Power-driven hand tools

3548

Welding apparatus (continued)

A-13

TABLE A-1.


Source Description

3549

Metalworking machinery, nec

3552

Textile machinery

3553

Woodworking machinery

3554

Paper industries machinery

3555

Printing trades machinery

3556

Food products machinery

3559

Special industry machinery, nec

3561

Pumps and pumping equipment

3562

Ball and roller bearings

3563

Air and gas compressors

3564

Blowers and fans

3565

Packaging machinery

3566

Speed changers, drives, and gears

3567

Industrial furnaces and ovens

3569

General industrial machinery, nec

3571

Electronic computers

3572

Computer storage devices

3575

Computer terminals

3577

Computer peripheral equipment, nec

3578

Calculating and ing equipment

3579

Office machines, nec

3581

Automatic vending machines

3582

Commercial laundry equipment

3585

Refrigeration and heating equipment

3586

Measuring and dispensing pumps (continued) A-14

TABLE A-1.


Source Description

3589

Service industry machinery, nec

3592

Carburetors, pistons, rings, valves

3593

Fluid power cylinders & actuators

3594

Fluid power pumps and motors

3599

Industrial machinery, nec

3612

Transformers, except electronic

3613

Switch gear and switchboard apparatus

3621

Motors and generators

3624

Carbon and graphite products

3625

Electronic equipment: relays and industrial controls

3629

Electrical industrial apparatus, nec

3631

Household cooking equipment

3632

Household refrigerators and freezers

3633

Household laundry equipment

3634

Electric housewares and fans

3635

Household vacuum cleaners

3639

Household appliances, nec

3641

Electric lamps

3643

Current-carrying wiring devices

3644

Noncurrent-carrying wiring devices

3645

Residential lighting fixtures

3646

Commercial lighting fixtures

3647

Vehicular lighting equipment

3648

Lighting equipment, nec

3651

Household audio and video equipment (continued) A-15

TABLE A-1.


Source Description

3652

Prerecorded records and tapes

3661

Telephone and telegraph apparatus

3663

Radio & TV communications equipment

3669

Communications equipment, nec

3671

Electron tubes

3672

Printed circuit boards

3674

Semiconductors and related devices

3675

Electronic capacitors

3676

Electronic resistors

3679

Electronic components, nec

3691

Storage batteries

3692

Primary batteries, dry and wet

3694

Engine electrical equipment

3695

Magnetic and optical recording media

3699

Electrical equipment & supplies, nec

3711

Motor vehicles and car bodies

3713

Truck and bus bodies

3714

Motor vehicle parts and accessories

3715

Truck trailers

3716

Motor homes

3721

Aircraft

3724

Aircraft engines and engine parts

3728

Aircraft parts and equipment, nec

3731

Ship building and repairing

3732

Boat building and repairing (continued) A-16

TABLE A-1.


Source Description

3743

Railroad equipment

3751

Motorcycles, bicycles, and parts

3761

Guided missiles and space vehicles

3764

Space propulsion units and parts

3769

Space vehicle equipment, nec

3792

Travel trailers and campers

3795

Tanks and tank components

3799

Transportation equipment, nec

3812

Search and navigation equipment

3820

Instruments/related products - measuring/controlling devices:

3821

Laboratory apparatus and furniture

3822

Environmental controls

3823

Process control instruments

3824

Fluid meters and counting devices

3825

Instruments to measure electricity

3826

Analytical instruments

3827

Optical instruments and lenses

3829

Measuring & controlling devices, nec

3840

Instruments and related products - medical instruments and supplies: x-ray

3841

Surgical and medical instruments

3842

Surgical appliances and supplies

3843

Dental equipment and supplies

3844

X-ray apparatus and tubes

3845

Electromedical equipment

3851

Ophthalmic goods (continued) A-17

TABLE A-1.


Source Description

3861

Photographic equipment and supplies

3873

Watches, clocks, watchcases & parts

3900

Miscellaneous manufacturing industries: process heaters

3911

Jewelry, precious metal

3914

Silverware and plated ware

3915

Jewelers’ materials & lapidary work

3931

Musical instruments

3942

Dolls and stuffed toys

3944

Games, toys, and children’s vehicles

3949

Sporting and athletic goods, nec

3951

Pens and mechanical pencils

3952

Lead pencils and art goods

3953

Marking devices

3955

Carbon paper and inked ribbons

3961

Costume jewelry

3965

Miscellaneous manufacturing industries: fasteners, buttons, needles, and pins

3991

Brooms and brushes

3993

Signs and advertising specialties

3995

Burial caskets

3996

Hard surface floor coverings, nec

3999

Manufacturing industries, nec

4111

Local and suburban transit

4131

Intercity & rural bus transportation

4173

Bus terminal and service facilities

4212

Local trucking, without storage (continued) A-18

TABLE A-1.


Source Description

4215

Courier services, except by air

4226

Special warehousing and storage, nec

4231

Trucking terminal facilities

4491

Water transportation: marine cargo handling

4499

Water transportation services, nec

4510

Air transportation: scheduled air transportation

4512

Air transportation, scheduled

4612

Crude petroleum pipelines

4741

Rental of railroad cars

4785

Inspection & fixed facilities

4789

Transportation services, nec

4900

Solid waste disposal - commercial/institutional: landfill dump

4911

Anthracite coal

4922

Natural gas transmission

4923

Gas transmission and distribution

4925

Gas production and/or distribution

4941

Water supply

4952

Sewerage systems

4953

Refuse systems

4961

Steam and air-conditioning supply

5013

Motor vehicle supplies and new parts

5021

Furniture

5031

Lumber, plywood, and millwork

5040

Wholesale trade (durable goods): professional equipment and supplies (continued)

A-19

TABLE A-1.


Source Description

5044

Office equipment

5045

Computers, peripherals & software

5046

Commercial equipment, nec

5063

Electrical apparatus and equipment

5078

Refrigeration equipment and supplies

5084

Industrial machinery and equipment

5085

Industrial supplies

5092

Toys and hobby goods and supplies

5093

Scrap and waste materials

5113

Industrial & personal service paper

5130

Apparel, Piece Goods, and Notions

5169

Chemicals & allied products, nec

5171

Petroleum bulk stations & terminals

5172

Petroleum products, nec

5182

Wine and distilled beverages

5191

Farm supplies

5194

Tobacco and tobacco products

5198

Paints, varnishes, and supplies

5211

Lumber and other building materials

5231

Paint, glass, and wallpaper stores

5511

New and used car dealers

5541

Gasoline service stations

5551

Boat dealers

5599

Automotive dealers, nec

5712

Furniture stores (continued) A-20

TABLE A-1.


Source Description

5984

Liquefied petroleum gas dealers

5999

Miscellaneous retail stores, nec

6141

Personal credit institutions

6512

Nonresidential building operators

6513

Apartment building operators

6514

Dwelling operators, exc. apartments

7215

Coin-operated laundries and cleaning

7216

Drycleaning plants, except rug

7218

Industrial launderers

7359

Equipment rental & leasing, nec

7372

Prepackaged software

7378

Computer maintenance & repair

7389

Business services, nec

7514

enger car rental

7515

enger car leasing

7532

Top & body repair & paint shops

7534

Tire retreading and repair shops

7538

General automotive repair shops

7539

Automotive repair shops, nec

7540

Auto repair, services, and parking: automotive services, except repair

7600

Miscellaneous repair services: electrical equipment

7629

Electrical repair shops, nec

7641

Reupholstery and furniture repair

7694

Armature rewinding shops

7699

Repair services, nec (continued) A-21

TABLE A-1.


Source Description

8062

General medical & surgical hospitals

8211

Elementary and secondary schools

8244

Business and secretarial schools

8249

Vocational schools, nec

8331

Job training and related services

8412

Museums and art galleries

8711

Engineering services

8731

Engineering and management services: commercial physical research

8732

Commercial nonphysical research

8734

Testing laboratories

8740

Engineering and management services: management and public relations

8999

Services, nec

9199

General government, nec

9223

Correctional institutions

9224

Solid waste disposal - government: fire fighting

9511

Air, water, & solid waste management

9711

National security

9999

Nonclassifiable establishments

NEC = Not elsewhere classified. Sources: Toxic Chemical Release Inventory (TRI), 1987-1990. On-line access through the databases. National Library of Medicine, Bethesda, MD. Crosswalk/Air Toxic Emission Factor Database Management System (XATEF), Version 1.2. U.S. Environmental Protection Agency, Office of Air Quality Planning and Standards, Research Triangle Park, NC. October 1991. Volatile Organic Compound (VOC) Particulate Matter (PM) Speciation Database Management System, Version 1.4. U.S. Environmental Protection Agency, Office of Air Quality Planning and Standards, Research Triangle Park, NC. October 1991. A-22

APPENDIX B

LISTS OF PAINT, INK, AND PRINTING FACILITIES WITH ANNUAL SALES GREATER THAN $1 MILLION

B-1

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name Aervoe-Pacific Co. Inc. AExcel Corp. Agri-Blend Inc. Akron Paint & Varnish Inc. Akzo Coatings Inc. Reliance Universal Inc. Akzo Coatings Inc. Akzo Resins & Vehicles Akzo Coatings Inc. Allentown Paint Manufacturing Co. Also Indus Inc. Morton Paint Co. Ameritone Paint Corp. Ameron Inc. Enmar Finishes Div. Ameron Inc. Ameron Protective Coatings Div. Amsterdam Color Works Inc. Aspen Paints Atlas Coating Corp. Automotive Finishes Inc. Baker Sealants & Coating Barrett Varnish Co. Bee Chem Co. Behr Process Corp. Benjamin Moore & Co. Bennette Paint Manufacturing Co. Best Bros Paint Manufacturing Co. Beverly Manufacturing Co. (Los Angeles) Birk Paint Manufacturing Inc. Blue Ridge Talc Co. Inc. Brewer Chem Corp. Brod-Dugan Co. Bruning Paint Co. Burkes Paint Co. Inc. Buten Paint & Wallpaper Cabot Stains Cal Western Paint Corp. Calbar Inc. California Products Corp. Carbit Paint Co.

Address

Sales in $ Millions

PO Box 485, Gardnerville NV 89410 7373 Production Dr, Mentor OH 44060 PO Box 957, Rowlett TX 75088 1390 Firestone Parkway, Akron OH 44301 1930 Bishop Ln, Louisville KY 40218 21625 Oak St, Matteson IL 60443 1600 Watterson Towers, Louisville KY 40218 PO Box 597, Allentown PA 18105 Box 6208, Canton OH 44706 PO Box 190, Long Beach CA 90801 PO Box 9610, Little Rock AR 72219 201 N Berry St, Brea CA 92621

11 20 1* 4* 300 13 550* 4 3 40 15 112

1546 Stillwell Ave, Bronx NY 10461 1128 SW Spokane St, Seattle WA 98134 820 E 140th St, Bronx NY 10454 6430 Wyoming Ave, Dearborn MI 48126 234 Suydam Ave, Jersey City NJ 07304 1532 S 50th Ct, Cicero IL 60650 2700 E 170th St, Lansing IL 60438 PO Box 1287, Santa Ana CA 92702 51 Chestnut Ridge Rd., Montvale NJ 07645 PO Box 9088, Hampton VA 23670 PO Box 2056, Sinking Spr PA 19608 9118 S Main St, Los Angeles CA 90003 230 Kearny Ave, Jersey City NJ 07305 PO Box 39, Henry VA 24102 PO Box 48, Honolulu HI 96810 2145 Schuetz Rd, St. Louis MO 63146 601 S Haven, Baltimore, MD 21224 727 S 27th St, Washougal WA 98671 5000 Ridge Ave, Philadelphia PA 19128 100 Hale St, Newburyport MA 01950 11748 Slauson Ave, Santa Fe Spr CA 90670 2626 N Martha St, Philadelphia PA 19125 PO Box 569, Cambridge MA 02139 927 W Blackhawk St, Chicago IL 60622

7 4 7* 4 5 3 66 33* 370* 5 1 2 2 9 50 15 30 3 40 30 5 4 32 5

(continued)

B-2

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name Carboline Co. Cardinal Color Co. Cardinal Indus Finish Inc. Century Chem Co. Certified Coating Products CF Jameson & Co. Inc. Charles A Crosbie Labs Inc. Chemical Technology Labs Inc. Chemical Coating Corp. Ciba-Geigy Corp. Drakenfeld Colors Clement Coverall Inc. CM Athey Paint Co. Coatings & Chems Corp. Colonial Refining & Chem Co. Columbia Paint Corp. Columbia Paint Co. Colwell Gen Inc. Commercial Chem Co. Inc. Con-Lux Coatings Inc. Cook & Dunn Paint Corp. Pure All Paint Coatings Co. Cook & Dunn Paint Corp. Cook & Dunn Paint Corp. Adelphi Coating Cook Paint & Varnish Co. Coronado Paint Co. Inc. Cosan Chem Corp. Cotter & Co. Gen Paint & Chem Co. Courtlaulds Coatings USA Inc. Cowman & Campbell Inc. Crest Chem Indus Ltd. Crosby Coatings Inc. CWC Indus Inc. Dalys Inc. Dampney Co. Inc. Daniel Products Co. Davis Paint Co.

Address

Sales in $ Millions

350 Hanley Indus Ct, St. Louis MO 63144 50-56 1st St, Paterson NJ 07524 1329 Potrero Ave, South El Mon CA 91733 5 Lawrence St, Bloomfield NJ 07003 2414 S Connor Ave, Los Angeles CA 90040 PO Box 197, Bradford MA 01835 PO Box 3497, Van Nuys CA 91407 12150 S Alameda St, Lynwood CA 90262 7300 Crider Ave, Pico Rivera CA 90660 PO Box 519, Washington PA 15301 PO Box 557, Camden NJ 08101 1809 Bayard St, Baltimore MD 21230 3067 N Elston Ave, Chicago IL 60618 20575 Ctr Ridge Rd, Cleveland OH 44116 PO Box 2888, Huntington WV 25728 PO Box 4569, Spokane WA 99202 PO Box 329, Fort Wayne IN 46801 PO Box 2126, Santa Ana CA 92707 PO Box 847, Edison NJ 08818 700 Gotham Ave, Carlstadt NJ 07072

65 7 18 5 1 1 1 3 3 28 4 6 5 3 5 17 20 4 25 8*

700 Gotham Parkway, Carlstadt NJ 07072 700 Gotham Parkway, Carlstadt NJ 07072

20 3

PO Box 419389, Kansas City MO 64141 PO Box 308, Edgewater FL 32032 400 14th St, Carlstadt NJ 07072 201 Jandus Rd., Cary IL 60013 PO Box 1439, Louisville, KY 40201 PO Box 70328, Seattle WA 98107 PO Box 333, Connersville IN 47331 PO Box 85, New Lenox IL 60451 PO Box 1038, Chico CA 95927 2686 Lisbon Rd, Cleveland OH 44104 3525 Stone Way N, Seattle WA 98103 85 Paris St, Everett MA 02149 400 Claremont Ave, Jersey City NJ 07304 1311 Iron St, Kansas City MO 64116

100 28 10* 120 160* 3 5 1* 6 5 5 4 20 13

(continued)

B-3

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name Davlin Paint Co. Inc. DC Franche & Co. De Boom Paint Co. Dean & Barry Co. Decratrend Paints Deft Inc. Del Paint Corp. Delrac Manufacturers of Bisonite Products Co. Inc. DeSoto Inc. Devoe & Raynolds Co. Dexter Corp. Dexter Specialty Coatings Div. Diamond Products Co. Inc. DJ Simpson Co. Dover Sales Co. Inc. Duncan Enterprises Dunn Edwards Corp. Dupli-Color Products Co. Duralac Inc. Duron Inc. Dye Specialties Inc. Egyptian Lacquer Manufacturing Ellis & Everard (US Holdings) Inc. Prillaman Chem Corp. Elpaco Coatings Corp. Emco Finishing Products Inc. Empire State Varnish Co. Environmental Coatings Inc. Epoca Co. Epoxy Coatings Co. Evans Paint Inc. Everseal Manufacturing Co. Inc. Fabrionics Inc. Farboil Co. Farwest Paint Manufacturing Co. Inc. Federated Paint Manufacturing Co. Ferro Corp. Coatings Div.

Address 700 Allston Way, Berkely CA 94702 1401 W Wabansia Ave, Chicago IL 60622 645 Texas St, San Francisco CA 94107 296 Marconi Blvd, Columbus OH 43215 251 Mason Way, City of Indu CA 91746 17451 Von Karman Ave, Irvine CA 92714 3105 E Reno St, Oklahoma City OK 73117 PO Box 764, Tonawanda NY 14151

Sales in $ Millions 3* 3 5 15 17 15 4 3*

PO Box 5030, Des Plaines IL 60017 PO Box 7600, Louisville KY 40207 1 E Water St, Waukegan IL 60085

408 120* 80

709 S 3rd Ave, Marshalltown IA 50158 PO Box 2265, South San Francisco CA 94080 PO Box 2479, Berkeley CA 94702 PO Box 7827, Fresno CA 93747 PO Box 30389, Los Angeles CA 90039 1601 Nicholas Blvd, Elk Grove Vi IL 60007 84 Lister Ave. Newark NJ 07105 10406 Tucker St, Beltsville MD 20705 PO Box 1447, Secaucus NJ 07096 PO Box 4449, Lafayette IN 47903 PO Box 4024, Martinsville VA 24112

18* 5 3* 30 150* 50 4 150 8 10 96*

PO Box 447, Elkhart IN 46515 470 Cresent St, Jamestown NY 14701 38 Varick St, Brooklyn NY 11222 6450 Hanna Lake SE, Caledonia MI 49316 5 Lawrence St, Bloomfield NJ 07003 PO Box 1035, Union City CA 94587 PO Box 4098, Roanoke VA 24015 475 Broad Ave, Ridgefield NJ 07657 Route 130 S, Camargo IL 61919 8200 Fischer Rd, Baltimore MD 21222 PO Box 68726, Tukwila WA 98168 1882 S Normal St, Chicago IL 60616 PO Box 6550, Cleveland OH 44101 (continued)

B-4

8 2 5 5 1 1 4* 12 13 11 3 8* 73*

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name

Address

Fiber-Resin Corp. PO Box 4187, Burbank CA 91503 Fine Line Paint Corp. 12234 Los Nietos Rd, Santa Fe Spr CA 90670 Finishes Unlimited Inc. PO Box 69, Sugar Grove IL 60554 Finnaren & Haley Inc. 2320 Haverford Rd, Ardmore PA 19003 Flecto Co. Inc. PO Box 12955, Oakland CA 94608 Frank W Dunne Co. 1007 41st St, Oakland CA 94608 Frazee Indus Inc. PO Box 2471, San Diego CA 92112 Fredericks-Hansen Paint PO Box 5638, San Bernardino CA 92408 Fuller O’Brien Corp. 450 E Grand Ave, South San Francisco CA 94080 Gilbert Spruance Co. Richmond St & Tioga St, Philadelphia PA 19134 Given Paint Manufacturing Co. Inc. 111 N Piedras St, El Paso TX 79905 GJ Nikolas & Co. Inc. 2810 Washington Blvd, Bellwood IL 60104 Glidden Co. Eastern Region PO Box 15049, Reading PA 19612 Glidden Co. Southwest Region PO Box 566, Carrollton TX 75011 Glidden Co. Resin Div. 1065 Glidden St NW, Atlanta GA 30318 Gloss-Flo Corp. 135 Jackson St, Brooklyn NY 11211 Glyptal Inc. 305 Eastern Ave, Chelsea MA 02150 Gordon Bartels Co. 2600 Harrison Ave, Rockford IL 61108 Graham Paint & Varnish Co. 4800 S Richmond St, Chicago IL 60632 Grow Group Inc. US Paint Div. 831 S 21st St, St. Louis MO 63103 Grow Group Inc. Natl Aerosol Products Co. 2193 E 14th St, Los Angeles CA 90021 Grow Group Inc. 200 Park Ave, New York NY 10166 Guardsman Products Inc. 3033 Orchard Vista Dr, Grand Rapids MI 49501 Guardsman Chems Inc. 13535 Monster Rd, Seattle WA 98178 H Behlen & Brother Inc. Route 30 N Perth Rd, Amsterdam NY 12010 Hancock Paint & Varnish 109 Accord Dr, Norwell MA 02061 Hanna Chem Coatings Inc. PO Box 147, Columbus OH 43216 Harco Chem Coatings Inc. 208 DuPont St, Brooklyn NY 11222 Harrison Paint Corp. PO Box 8470, Canton OH 44711 Hartin Paint & Filler PO Box 116, Carlstadt NJ 07072 Hempel Coatings USA 201 Route 17 N, Rutherford NJ 07070 Hentzen Coatings Inc. 6937 W Mill Rd, Milwaukee WI 53218 Heresite Protective Coatings Inc. Hoboken Paint Co. Inc. Hoffers Inc. Hy-Klas Paints Inc. Hydrosol Inc.

PO Box 250, Manitowoc WI 54221 40 Indus Rd, Lodi NJ 07644 PO Box 777, Wausau WI 54401 1401 S 12th St, Louisville KY 40210 8407 S 77th Ave, Bridgeview IL 60455 (continued)

B-5

Sales in $ Millions 10 5 3 25* 20 7 100 12 140 10 7* 2 140 59 30 4 5 7 10* 30* 5 413 190 6 10 10 25 6 20 3 15 12 15 17 47 6 30

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name ICI Americas Inc. ICI Paints Illinois Bronze Paint Co. Indurall Coatings Inc. Industrial Coatings Intl. Insilco Corp. Sinclair Paint Co. International Paint Co. USA Inc. International Paint Co. USA Inc. Southwest Div. International Coatings Co. Irathane Syss Inc. IVC Indus Coatings Inc. J Landau & Co. Inc. James B Day & Co. James Bute Co. Jasco Chem Corp. John L Armitage & Co. Johnson Paints Inc. Jones Blair Co. Gilman Paint & Wallcovering Div. Kalcor Coatings Co. Kaufman Products Inc. Keeler & Long Inc. Kelly-Moore Paint Co. Inc. Hurst Div. Kelly-Moore Paint Co. King Fiber Glass Corp. Fiber Resin Supply Div. Komac Paint Inc. Kop-Coat Co. Inc. Kop-Coat Co. Inc. Pettit Paint Co. Kurfees Coatings Inc. Kwal-Howells Inc. L & H Paint Products Inc. Lasting Paints Inc. Lenmar Inc. Lilly Chem Products Inc. Lilly Industrial Coatings Inc. Lily Co. Inc. Linear Dynamics Inc.

Address 925 Euclid Ave, Cleveland OH 44115 300 E Main St, Lake Zurich IL 60047 PO Box 2371, Birmingham AL 35201 7030 Quad Ave, Baltimore MD 21237 6100 S Garfield Ave, Los Angeles CA 90040 6001 Antoine, Houston TX 77091 PO Box 920762, Houston TX 77292 13929 E 166th St, Cerritos CA 90701 PO Box 276, Hibbing MN 55746 PO Box 18163, Indianapolis IN 46218 PO Box 135, Carlstadt NJ 07072 Day Ln, Carpentersville IL 60110 PO Box 1819, Houston TX 77251 PO Drawer J, Mountain View CA 94040 1259 Route 46 E, Parsippany NJ 07054 PO Box 061319, Fort Myers FL 33906 PO Box 1257, Chattanooga TN 37401

Sales in $ Millions 843 25 8 14* 100* 50 18 5 8* 9 4 8 3* 7 8* 9 38

37721 Stevens, Willoughby OH 44094 1326 N Bentalov St, Baltimore MD 21216 PO Box 460, Watertown CT 06795 301 W Hurst Blvd, Hurst TX 76053 987 Commercial St, San Carlos CA 94070 366 W Nickerson St, Seattle WA 98119

6 1* 10 15 230* 2

1201 Osage St, Denver CO 80204 480 Frelinghuysen Ave, Newark NJ 07114 36 Pine St, Rockaway NJ 07866 201 E Market St, Louisville KY 40202 PO Box 39-R, Denver CO 80239 PO Box 7311, San Francisco CA 94120 PO Box 4428, Baltimore MD 21223 150 S Calverton Rd, Baltimore MD 21223 PO Box 188, Templeton MA 01468 733 S West St, Indianapolis, IN 46225 PO Box 2358, High Point NC 27261 400 Lanidex Plz, Parsippany NJ 07054

10 15 11 16 23 4 6 13 11 212 30 30

(continued)

B-6

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name Lyle Van Patten Co. Inc. MA Bruder & Sons Inc. Maas & Waldstein Co. MAB Paints Inc. Magruder Color Co. Inc. Radiant Color Div. Major Paint Co. Mansfield Paint Co. Inc. Martec Inc. Martin-Senour Co. Mautz Paint Co. McCormick Paint Works Co. McWhorter-McCloskey Inc. Mercury Paint Co. Inc. Mid-States Paint Co. Midwest Lacquer Manufacturing Co. Midwest Paint Manufacturing Co. Millmaster Onyx Group Inc. MantroseHae Co. Mobile Paint Manufacturing Co. Mohawk Finishing Products Moline Paint Manufacturing Co. Moling Paint Manufacturing Monarch Paint Co. Morton Intl Inc. Norris Paint/TMT Muralo Co. Inc. Muralo Co. Inc. Olympic Paint & Chem Co. N Siperstein Inc. National Paint Co. Inc. National Lacquer & Paint Co. Nelson Tech Coatings Inc. New York Bronze Powder Co. Inc. Niles Chem Paint Co. Norton & Son Inc. Nu-Brite Chem Co. Inc. Kyanize Paints O’Brien Corp. O’Brien Corp. Powder Coatings Div. O’Brien Corp. Southeast Region

Address

Sales in $ Millions

321 W 135th St, Los Angeles CA 90061 PO Box 600, Broomall PA 19008 2121 McCarter Highway, Newark NJ 07104 630 N 3rd St, Terre Haute IN 47808 PO Box 4019, Richmond CA 94804 4300 W 190th St, Torrance CA 90509 169 W Longview Ave, Mansfield OH 44905 760 Aloha St, Seattle WA 98109 101 Prospect Ave, Cleveland OH 44115 PO Box 7068, Madison WI 53707 2355 Lewis Ave, Rockville, MD 20851 5501 E Slauson Ave, Los Angeles CA 90040 14300 Schaefer Highway, Detroit MI 48227 9315 Watson Indus Park, St. Louis MO 63126 9353 Seymour Ave, Schiller Par IL 60176 2313 W River Rd N, Minneapolis MN 55411 500 Post Rd E, Westport CT 06880

3 140* 15 32 30 65 2 3 44* 19 18* 5 18 3 5 2 15

4775 Hamilton Blvd, Theodore AL 36582 Route 30 N, Amsterdam NY 12010 5400 23rd Ave, Moline IL 61265 5400 23rd Ave, Moline IL 61265 PO Box 55604, Houston TX 77255 PO Box 2023, Salem OR 97308 PO Box 455, Bayonne NJ 07002 5928 S Garfield Ave, Los Angeles CA 90040

45 35* 17 125 29* 5 42 2*

415 Montgomery St, Jersey City NJ 07302 3441 E 14th St, Los Angeles CA 90023 7415 S Green St, Chicago IL 60621 2147 N Tyler Ave, South El Mon CA 91733 519 Dowd Ave, Elizabeth NJ 07201 PO Box 307, Niles MI 49120 148 E 5th St, Bayonne NJ 07002 2nd & Boston St, Everett MA 02149 450 E Grand Ave, South San Francisco CA 94080 5300 Sunrise Rd, Houston TX 77021 PO Box 864, Brunswick GA 31521

40 3 2 2 30 16* 15* 20 150* 40 11*

(continued)

B-7

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name

Address

Sales in $ Millions

Old Quaker Paint Co. Orelite Chem Coatings Pacific Coast Lacquer Co. Inc. Palmer Paint Products Inc. Pan Chem Corp. Paragon Paint & Varnish Corp. Parker Paint Manufacturing Co. Parks Corp. Parks Paint & Varnish Co. Inc. onno Paints Pave-Mark Corp. PavePrep Corp. Penn Color Inc. Pentagon Chem & Paint Co. Perfection Paint & Color Co. Performance Coatings Inc. Perry & Derrick Co. Pervo Paint Co. PFI Incorporated-Paints for Industry Pierce & Stevens Corp. Plasti-Kote Co. Inc. Plasticolors Inc. Plextone Corp. of America PMC Inc. Gen Plastics Div. Ponderosa Paint Manufacturing Co. Inc. Porter Paint Co. Potter Paint Co. Inc. PPG Indus Architectual Finishes Inc. PPG Indus Inc. Automotive Products Group Pratt & Lambert Inc. Pratt & Lambert Inc. Western Div. Premier Coatings Inc. Preservative Paint Co. Inc. Pro-Line Paint Manufacturing Co. Inc. Proctor Paint & Varnish Progress Paint Manufacturing Co. Pruett-Schaffer Chem Co.

2209 S Main St, Santa Ana CA 92707 62 Woolsey St, Irvington NJ 07111 3150 E Pico Blvd, Los Angeles CA 90023 PO Box 1058, Troy MI 48099 1 Washington Ave, Hawthorne NJ 07506 5-49 46th Ave, Long Island NY 11101 PO Box 11047, Tacoma WA 98411 PO Box 5, Somerset MA 02726 660 Tonnelle Ave, Jersey City NJ 07307 500 Broadway, Watervliet NY 12189 PO Box 94108, Atlanta GA 30318 141 Central Ave, Westfield NJ 07090 400 Old Dublin Pike, Doylestown PA 18901 24 Woodward Ave, Ridgewood NY 11385 715 E Maryland St, Indianapolis IN 46202 PO Box 1569, Ukiah CA 95482 2510 Highland Ave, Cincinnati OH 45212 6624 Stanford Ave, Los Angeles CA 90001 921 Santa Fe Springs Rd, Santa Fe Spr CA 90670 710 Ohio St, Buffalo NY 14203 PO Box 708, Medina OH 44258 2600 Michigan Ave, Ashtabula OH 44004 2141 McCarter Highway, Newark NJ 07104 55-T La Ave, Bloomfield NJ 07003 PO Box 5466, Boise ID 83705 PO Box 1439, Louisville KY 40201 PO Box 265, Cambridge Ci IN 47327 2233 112th Ave NE, Bellevue WA 98004 PO Box 3510, Troy MI 48007 75 Tonawanda St, Buffalo NY 14207 PO Box 668, Marysville CA 95901 2250 Arthur Ave, Elk Grove Vi IL 60007 5410 Airport Way S, Seattle WA 98108 2646 Main St, San Diego CA 92113 38 Wells Ave, Yonkers NY 10701 PO Box 33188, Louisville KY 40232 PO Box 4350, Pittsburgh PA 15204

31 4 3 7 5 14* 26 20 3* 10 20 14* 40 16* 6* 3 15 13 2 50 50 17 3 4 10 121 2* 110* 20* 246 10 20 13 7* 20 10 4

(continued)

B-8

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name Pyrolac Corp. Quality Coatings Inc. Raffi & Swanson Inc. Randolph Products Co. Red Spot Paint Varnish Co. Red Spot Westland Inc. Red Spot Paint Varnish Co. Reliable Coatings Inc. Republic Clear Thru Corp. Republic Powdered Metals Inc. Riley Bros Inc. River Valley Coatings Inc. Riverside Labs Inc. RJ McGlennon Co. Inc. Roymal Inc. RPM Inc. Rudd Co. Inc. Rust-Oleum Corp. Rutland Fire Clay Co. Sampson Paint Manufacturing Co. Sampson Coatings Inc. Sandstrom Products Co. Saxon Paint & Home Care Centers Inc. Dreeblan Paint Co. Schalk Chems Inc. Scott Paint Corp. Seagrave Coatings Corp. Clover Leaf Paint & Varnish Seaside Inc. Seibert-Oxidermo Inc. SEM Products Inc. Sentry Paint Technologies Inc. Seymour of Sycamore Inc. Sheboygan Paint Co. Sheffield Bronze Paint Corp. Sherwin-Williams Co. Sherwin-Williams Co. Automotive Div. Sherwin-Williams Co. Consumer Div.

Address 55 Schoon Ave, Hawthorne NJ 07506 1700 N State, Chandler IN 47610 100 Eames St, Wilmington MA 01887 Park Place E, Carlstadt NJ 07072 550 S Edwin St, Westland MI 48185 PO Box 418, Evansville IN 47703 13108 Euless St, Euless TX 76040 211 63rd St, Brooklyn NY 11220 PO Box 777, Median OH 44258 860 Washington Ave, Burlington IA 52601 PO Box 580, Aurora IL 60507 411 Union St, Geneva IL 60134 198 Utah St, San Francisco CA 94103 Route 103, Newport NH 03773 PO Box 777, Medina OH 44258 1630 15th Ave W, Seattle WA 98119 11 Hawthorne Parkway, Vernon Hills IL 60061 PO Box 340, Rutland VT 05702 1900 Ellen Rd, Richmond VA 23224 PO Box 6625, Richmond VA 23230 218 S High, Port Byron IL 61275 3729 W 49th St, Chicago IL 60632 2400 Vauxhall Rd, Union NJ 07083 5940 Palmer Blvd, Sarasota FL 34232 320 Paterson Plank Rd, Carlstadt NJ 07072 PO Box 2809, Long Beach CA 90801 6455 Strong Ave, Detroit MI 48211 120 Sem Ln, Belmont CA 94002 237 Mill St, Darby PA 19023 917 Crosby Ave, Sycamore IL 60178 PO Box 417, Sheboygan WI 53082 17814 S. Waterloo Rd, Cleveland OH 44119 101 Prospect Ave NW, Cleveland OH 44115 101 Prospect Ave NW, Cleveland OH 44115 101 Prospect Ave NW, Cleveland OH 44115 (continued)

B-9

Sales in $ Millions 4* 2 15 9 15 56 14* 6 15 3 2* 3* 3 4 380 10 89 2 42 9 7 15* 7 16* 14* 3 11 7 10 10 12 3 2,124 160 170*

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name Sherwin-Williams Co. Oakland Sherwin-Williams Co. Chem Coatings Div. Sigma Coatings Co. Smiland Paint Co. Snyder Bros Co. Southern Coatings Inc. Southwestern Petroleum Corp. Spatz Paints Inc. Specialty Coating & Chem Spectra-Tone Paint Corp. Spraylat Corp. Los Angeles Stanchem Inc. Standard Detroit Paint Co. Standard T Chem Co. Inc. Star Finishing Products Inc. Star Bronze Co. STD Coating Corp. Steelcote Manufacturing Corp. Sterling Twelve Star Paint Sterling-Clark-Lurton Stevens Paint Corp. Stonhard Inc. Strathmore Products Inc. Sullivan Coatings Inc. Sunnyside Corp Superior Varnish & Drier Co. Superior Sealants Inc. Supro Corp. Technical Coatings Laboratory Inc. Technical Coatings Inc. Technical Coatings Co. Tenax Finishing Products Tera Lite Inc. Testor Corp. Thompson & Formby Inc. Ti-Kromatic Paints Inc. Tnemec Co. Inc.

Address 1450 Sherwin Ave, Oakland CA 94608 11541 S Champlain Ave, Chicago IL 60628 PO Box 816, Harvey LA 70059 620 Lamar St, Los Angeles CA 90031 PO Box 760, Toccoa GA 30577 PO Box 160, Sumter SC 29151 PO Box 961005, Fort Worth TX 76161 1439 Hanley Industrial Ct, St. Louis MO 63144 7360 Varna Ave, North Hollywood CA 91605 9635 Klingerman St, South El Mon CA 91733 3465 S La Cienega, Los Angeles CA 90016 401 Berlin St, East Berlin CT 06023 8225 Lyndon Ave, Detroit MI 48238 290 E Joe Orr Rd, Chicago Heights IL 60411 360 Shore Dr, Hinsdale IL 60521 PO Box 2206, Alliance OH 44601 461 Broad Ave, Ridgefield NJ 07657 3418 Gratiot St, St. Louis MO 63103 PO Box 791, Little Rock AR 72203 184 Commercial St, Malden MA 02148 38 Wells Ave, Yonkers NY 10701 PO Box 308, Maple Shade NJ 08052 1970 W Fayette St, Syracuse NY 13204 410 N Hart St, Chicago IL 60622 225 Carpenter Ave, Wheeling IL 60090 PO Box 1310, Merchantville NJ 08109 1135 Sylvan SW, Atlanta GA 30310 2650 Pomona Blvd, Pomona CA 91768 PO Box 565, Avon CT 06001 PO Box 3337, Austin TX 78764 1000 Walsh Ave, Santa Clara CA 95050 390 Adams St, Newark NJ 07114 1631 S 10th St, San Jose Ca 95112 620 Buckbee St, Rockford IL 61106 825 Crossover Ln, Memphis TN 38117 2492 Doswell Ave, St. Paul MN 55108 PO Box 411749, Kansas City MO 64141 (continued)

B-10

Sales in $ Millions 32* 250 15 10 7 40 26 5 3 7 5 10 8 14* 15 11 3 4 15 9 15 62 6 2* 14 7* 11* 4 6 8 6 6* 3 43* 44* 3 50

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name Touraine Paints Inc. Tower Paint Manufacturing Trail Chem Corp. Triangle Coatings Inc. United Paint & Chem Corp. United Coatings Inc. United Paint Co. United Gilsonite Labs Universal Paint Corp. Universal Chems & Coatings Inc. Universe Paint Co. Valspar Corp. MCI Quality Coatings Valspar Corp. Colony Paints Div. Valspar Corp. Valspar Corp. Masury Paint Co. Vanex Color Inc. VJ Dolan & Co. Inc. Vogel Paint & Wax Inc. Marwin Paints Inc. Vogel Paint & Wax Inc. Voplex Corp. Allerton Chem Div. Waterlox Chem & Coatings Corp. Watson-Standard Co. Jordan Paint Manufacturing Co. Watson-Standard Co. Wattyl Group Precision Paint Group WC Richards Co. Inc. Welco Manufacturing Co. Inc. Wellborn Paint Manufacturing Co. Western Automotive Finishes Westfield Coatings Corp. Westinghouse Elec Corp. Insulating Materials Div. Whittaker Corp. Whittaker Decatur Coatings William Zinsser & Co. Wiltech Corp. Wisconsin Protective Coatings Corp. WM Barr & Co. Inc. Yenkin Majestic Paint Corp.

Address

Sales in $ Millions

1760 Revere Beach Parkway, Everett MA 02149 620 W 27th St, Hialeah FL 33010 9904 Gidley St, El Monte CA 91731 1930 Fairway Dr, San Leandro CA 94577 24671 Telegraph Rd, Southfield MI 48034 2850 Festival Dr, Kankakee IL 60901 404 E Mallory, Memphis TN 38109 PO Box 70, Scranton PA 18501 PO Box 1218, La Puente CA 91749 1975 Fox Ln, Elgin IL 60123 PO Box 668, Marysville CA 95901 6110 Gunn Highway, Tampa FL 33625 PO Box 418037, Kansas City MO 64141 1101 S 3rd St, Minneapolis MN 55415 1401 Severn St, Baltimore MD 21230 1700 Shawnee St, Mount Vernon IL 62864 1830 N Laramie Ave, Chicago IL 60639 2100 N 2nd St, Minneapolis MN 55411 Industrial Air Park Rd., Orange City IA 51041 763 Linden Ave, Rochester NY 14625 9808 Meech Ave, Cleveland OH 44105 7250 Franklin St, Forest Park IL 60130

17 10 4 5 11* 65 25 22* 20 10 3* 12 15 527 8 4 5 8* 100 1 4 4

PO Box 11250, Pittsburgh PA 15238 5275 Peachtree, Atlanta GA 30341 3555 W 123rd St, Blue Island IL 60406 1225 Ozark St, North Kansas MO 64116 215 Rossmoor Rd SW, Albuquerque NM 87102 1450 Ave R, Grand Prairi TX 75050 PO Box 815, Westfiled MA 01086 Route 993, Manor PA 15665

29* 15 15* 10 15 17* 7 15

PO Box 2238, Decatur AL 35602 31 Belmont Dr, Somerset NJ 08873 PO Box 517, Longview WA 98632 PO Box 216, Green Bay WI 54305 PO Box 1879, Memphis TN 38113 PO Box 369004, Columbus OH 43236

12* 16 2 10 95 80

(continued)

B-11

TABLE B-1.

PAINT AND ALLIED PRODUCTS FACILITIES (SIC 2851) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name Zehrung Corp Zolatone Process Inc. ZPC Indus Coatings Inc. Zynolyte Products Co.

Address 3273 Casitas Ave, Los Angeles CA 90039 3411 E 15th St, Los Angeles CA 90023 120 E Minereal St, Milwaukee WI 53204 PO Box 6244, Carson CA 90749

Sales in $ Millions 2* 6 2 25

* Indicates an estimated financial figure. Source: Gale Research, Inc. Ward’s Business Directory of U.S. Private and Public Companies-1991, Volume 4. Detroit, MI. 1991.

B-12

TABLE B-2.

PRINTING INK MANUFACTURING FACILITIES (SIC 2893) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name

Address

Sales in $ Millions

Acme Printing Ink Co. Packaging Inc. Corp. 5001 S Mason Ave, Chicago IL 60638

100

Acme Printing Ink Co.

165 Bond St, Elk Grove Vi IL 60007

140*

AJ Daw Printing Ink Co.

3559 S Greenwood Ave, Los Angeles CA 90040

13

American Inks & Coatings Corp.

PO Box 803, Valley Forge PA 19482

15

Autoroll Machine Corp.

11 River St, Middleton MA 01949

12

BASF Corp. Coatings & Colorants Div.

1255 Broad St, Clifton NJ 07015

Bomark Inc.

601 S 6th Ave, City of Indu CA 91746

Borden Inc. Coatings & Graphics Group

630 Glendale - Milford, Cincinnati OH 45215

17*

Braden Sutphin Ink Co.

3650 E 93rd St, Cleveland OH 44105

25

Celia Corp.

320 Union St, Sparta MI 49345

15

Central Ink & Chem

1100 N Harvester Rd, West Chicago IL 60185

Colonial Printing Ink Corp

180 E Union Ave, East Rutherford NJ 07073

17

Converters Ink Co.

1301 S Park Ave, Linden NJ 07036

16*

Croda Inks Corp.

7777 N Merrimac, Niles IL 60648

32*

Custom Chem Corp.

30 Paul Kohner Pl, Elmwood Park NJ 07407

40

Del Val Ink & Color Co. Inc.

1301 Taylors Ln, Riverton NJ 08077

5

Excello Color & Chem

1446 W Kinzie St, Chicago IL 60622

84*

Flint Ink Corp.

25111 Glendale Ave, Detroit MI 48234

Flint Ink Corp. Capitol Printing Ink

806 Channing Pl NE, Washington DC 20018

23

Flint Ink Corp.

1404 4th St, Berkeley CA 94710

30*

Gans Ink & Supply Co. Inc.

1441 Boyd St, Los Angeles CA 90033

18

Gotham Ink & Color Co. Inc.

5-19 47th Ave, Long Island NY 11101

4

Graphic Color Corp.

750 Arthur Ave, Elk Grove Vi IL 60007

18

Handschy Ink & Chems Inc.

120 25th Ave, Bellwood IL 60104

30

Ink Masters Inc.

2842 S 17th Ave, Broadview IL 60153

105* 3

9

235

3

James River Corp. of Virginia CZ Inks Div. 4150 Carr Ln, St. Louis MO 63119

28

JM Huber Corp. Carbon Div.

9300 Needlepoint Rd, Baytown TX 77521

18*

Kerley Ink Engineers Inc.

2839 19th Ave, Broadview IL 60153

Kohl & Madden Printing Ink Corp.

222 Bridge Plz Sq, Hackensack NJ 07601

Lakeland Laboratory Inc. Alfa Ink Div.

655 Washington Ave, Carlstadt NJ 07072

2*

Lakeland Laboratory Inc.

655 Washington Ave, Carlstadt NJ 07072

3

Lawter Intl Inc.

990 Skokie Blvd, Northbrook IL 60062

Merit Printing Inc. Co.

1451 S Lorena St, Los Angeles CA 90023 (continued)

B-13

4* 45

136 4*

TABLE B-2.

PRINTING INK MANUFACTURING FACILITIES (SIC 2893) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Name

Address

Sales in $ Millions

Midland Color Co.

651 Bonnie Ln, Elk Grove Vi IL 60007

85

Miller-Cooper Co.

1601 Prospect Ave, Kansas City MO 64127

Morrison Printing Ink Co.

4801 W 160th St, Cleveland OH 44135

14*

Naz-Dar Co.

1087 N Northbranch St, Chicago IL 60622

15*

Nor-Cote Intl Inc.

PO Box 668, Crawfordsville IN 47933

North American Printing Ink

1524 David Rd, Elgin IL 60123

Northern Printing Ink Corp.

8360 10th Ave N, Minneapolis MN 55427

Polypore Inc.

4601 S 3rd Ave, Tucson AZ 85714

Polytex Color & Chem

820 E 140th St, Bronx NY 10454

PPG Indus Inc. PPG Ink Products Co.

1835 Airport Exchange Blvd, Covington KY 41018

Rexart Chem Corp.

1183 Westside Ave, Jersey City NJ 07306

6*

Ron Ink Co. Inc.

61 Halstead St, Rochester NY 14610

7

Sia Indus of America Inc.

8000 Research Way, Springfield VA 22153

Sinclair & Valentine LP

2520 Pilot Knob Rd, St. Paul MN 55120

Sun Chem Corp.

PO Box 1302, Fort Lee NJ 07024

Sun Chem Corp. Gen. Printing Ink Div.

135 W Lake St, Northlake IL 60164

410*

Superior Printing Ink Co. Inc.

70 Bethune St, New York NY 10014

50

United States Printing Ink Corp. Leber Ink Div.

PO Box 88700, Seattle WA 98138

United States Printing Ink Corp.

343 Murray Hill Pkwy, East Rutherford NJ 07073

65

Van Son Holland Corp. of America

92 Union St, Mineola NY 11501

42

Vivitone Inc.

110 E 27th St, Paterson NJ 07514

8

Walter W Lawrence

9715 Alpaca St, South El Mon CA 91733

1

Wikoff Color Corp.

PO Box W, Fort Mill SC 29715

6

5 14 8 10 3 15

25 186 1,100

6

45*

*Indicates an estimated financial figure. Source: Gale Research, Inc. Ward’s Business Directory of U.S. Private and Public Companies-1991, Volume 4. Detroit, MI. 1991.

B-14

TABLE B-3.

PRINTING AND PUBLISHING FACILITIES (SIC 27) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Company

Location

Sales in $ Millions

(SIC 2711) Newspapers Advance Publications Inc.

Staten Island, NY

2,200*

d Publications Inc.

Boston, MA

542

Chicago Tribune Co.

Chicago, IL

500

Cox Enterprises Inc.

Atlanta, GA

1,970

Dow Jones & Co. Inc.

Washington, DC

1,444

EW Scripps Co.

Wilmington, DE

1,266

Freedom Newspapers Inc.

Irvine, CA

Gannett Co. Inc.

Arlington, VA

3,518

Hearst Corp.

New York, NY

1,900*

Ingersoll Publications Co.

Princeton, NJ

1,010*

Knight-Ridder Inc.

Miami, FL

2,268

Media Gen Inc.

Richmond, VA

606

New York Times Co.

New York, NY

1,769

News America Publishing Inc.

New York, NY

3,000

Thomson Newspapers Corp.

Des Plaines, IL

Times Mirro Co.

Los Angeles, CA

3,475

Tribune Co.

Chicago, IL

2,455

500

550*

(SIC 2721) Periodicals ABC Publishing

New York, NY

310*

Billboard Publications Inc.

New York, NY

100

BPI Communications Inc.

New York, NY

105

Cahners Publishing Co. New York Magazine Div.

New York, NY

102

Chilton Co.

Radnor, PA

150

CMP Publications Inc.

Manhasset, NY

187*

Conde Nast Publications Inc.

New York, NY

280*

(continued)

B-15

TABLE B-3.


Location

Sales in $ Millions

Crain Communicating Inc.

Chicago, IL

145

Diamonds Communications Inc.

New York, NY

470*

Edgell Communications Inc.

Cleveland, OH

205

Forbes Inc.

New York, NY

200

International Data Group Inc.

Framingham, MA

500

Meredith Corp.

Des Moines, IA

792

Meredith Corp. Ladies’ Home Journal

New York, NY

100

National Enquirer Inc.

Lantana, FL

180

National Geographic Soc.

Washington, DC

425

Newsweek Inc.

New York, NY

256

Official Airline Guides Inc.

Oak Brook, IL

130*

Penthouse Intl. Ltd.

New York, NY

160*

Penton Publishing Inc.

Cleveland, OH

151

Peterson Publishing Co.

Los Angeles, CA

140*

Playboy Enterprises Inc.

Chicago, IL

160

Reader’s Digest Assn. Inc.

Pleasantville, NY

Reed Publishing (USA) Inc. Cahners Publishing Co.

Newton, MA

430

Reed Publishing (USA) Inc.

Newton, MA

600

Rodale Press Inc.

Emmaus, PA

150*

Scholastic Inc.

New York, NY

250*

Simon & Shuster Inc. Bur of Bus Practice

Waterford, CT

100*

Standard & Poor’s Corp.

New York, NY

260*

Thompson Corp. Thompson Bus. Info.

Stamford, CT

160*

Time Inc. Magazine Co.

New York, NY

1,500*

Times Mirror Magazines Inc.

New York, NY

470*

(continued)

B-16

1,832

TABLE B-3.


Location

Sales in $ Millions

Trader Publications Inc.

Clearwater, FL

270*

US News & World Report Inc.

New York, NY

140*

Warren Gorham & Lamont Inc.

New York, NY

130

Whittle Communications Inc.

Knoxville, TN

210*

Ziff Communications Co.

New York, NY

340*

Ziff Communications Co. Zif-Davis Publishing Co.

New York, NY

160*

Addison-Wesley Publishing Co.

Reading, MA

120*

Bantam Doubleday Dell Publishing Group Inc.

New York, NY

180*

David C. Cook Publishing Co.

Elgin, IL

100

Encyclopedia Britannica Inc.

Chicago, IL

624

Field Publications

Middletown, CT

100*

Grolier Inc.

Danbury, CT

440*

Harcourt Brace Jovanovich Inc.

Orlando, FL

Harper Collins Publishers Inc.

New York, NY

450

Houghton Mifflin Co.

Boston, MA

370

Insilco Corp.

Midland, TX

450*

John Wiley & Sons Inc.

New York, NY

282

Lawyers Co-Operative Publishing Co. Inc.

Rochester, NY

150*

Macmillan Inc.

New York, NY

950*

Macmillan Inc. Info Svcs & Instruction

New York, NY

416

MacMillan Intl. Inc.

New York, NY

146*

Macmillan-McGraw-Hill School Publishing Co. School Div.

New York, NY

200

(SIC 2731) Book Publishing

(continued)

B-17

1,341

TABLE B-3.


Location

Sales in $ Millions

Macmillian-McGraw-Hill School Publishing Co.

Lake Forest, IL

390*

McGraw-Hill Inc. McGraw-Hill Intl Book Group

New York, NY

115

Mosby Year Book Inc.

St. Louis, MO

150

Prentice Hall Inc.

New York, NY

970*

Putnam Publishing Group, Inc.

New York, NY

100

Rand McNally & Co.

Skokie, IL

430*

Random House, Inc.

New York, NY

325

RR Donnelley & Sons Co. Willard Div.

Willard, OH

150

Simon & Schuster Inc.

New York, NY

1,320

South-Western Publishing Co.

Cincinnati, OH

112

Sunday School Bd of the Southern Baptist Convention

Nashville, TN

172

Time-Life Books Inc.

Alexandria, VA

350

West Publishing Co.

St. Paul, MN

450*

Western Publishing Group Inc.

Racine, WI

480

World Book Inc.

Chicago, IL

330*

Zondervan Corp.

Grand Rapids, MI

100*

Arcata Graphics Co. Arcata Graphics Book Group

Kingsport, TN

170*

Banta Corp.

Menasha, WI

568

Bertelsmann Printing & Mfg. Corp.

Berryville, VA

220*

Brown Printing Co. (Waseca Minnesota)

Waseca, MN

363

Great Lakes Color Printing Corp.

Brentwood, TN

210*

Harper & Row Publishers

New York, NY

450

(SIC 2732) Book Printing

(continued)

B-18

TABLE B-3.


Location

Jostens Inc. Printing & Publishing Div.

Minneapolis, MN

RR Donnelley & Sons Co.

Chicago, IL

Sales in $ Millions 121 3,122

(SIC 2741) Misc Publishing Commerce Clearing House Inc.

Riverwoods, IL

678

Donnelley Directory

New York, NY

1,300*

GTE Telephone Operations Inc. GTE Directories Corp.

Dallas-Fort, TX

360*

McGraw-Hill Info. Svcs. Co.

New York, NY

668

NYNEX Info Resources Co.

Middleton, MA

800

RL Polk & Co.

Detroit, MI

280

Simplicity Holdings, Inc.

New York, NY

110*

Simplicity Pattern Co.

New York, NY

101

Southwestern Bell Yellow Pages Inc.

St. Louis, MO

240*

Southwestern Bell Publications Inc.

St. Louis, MO

280*

U.S. West Direct (U.S. West Marketing Resources Group Inc.)

Aurora, CO

160*

Wonderland Music Co. Inc.

Burbank, CA

200*

American Signature Graphics Foote & Davies Div.

Atlanta, GA

195

American Bank Stationary Co.

Baltimore, MD

110*

Avery Intl Corp. Avery Label Co.

Azusa, CA

110*

Graphic Controls Corp.

Buffalo, NY

140

Graphisphere Corp.

Des Plaines, IL

110

HS Crocker Co. Inc.

South San Francisco, CA

140*

Judd’s Inc.

Washington, DC

114

NMG Inc.

Los Angeles, CA

105

(SIC 2752) Commercial Printing-Lithographic

(continued)

B-19

TABLE B-3.


Location

Sales in $ Millions

Perry Printing Corp.

Waterloo, WI

175

Quebecor Printing (USA) Inc.

St. Paul, MN

770

Queens Group Inc.

Long Island, NY

100

Ringler America Inc.

Itasca, IL

700

RR Donnelley & Sons Co. Mattoon Mfg. Div.

Mattoon, IL

110*

RR Donnelley & Sons Co. Lancaster Mfg. Div.

Lancaster, PA

190*

Shea Communications Co.

Louisville, KY

120

Taylor Corp.

Mankato, MN

540*

Treasure Chest Advertising Co. Inc.

Glendora, CA

550*

Valassis Inserts Inc.

Livonia, MI

400*

World Color Press Inc.

Effingham, IL

650

All-State Legal Supply Co.

Cranford, NJ

43

Arcata Graphics Co.

Baltimore, MD

Beck Co. (Langhorne Pennsylvania)

W, Langhorne, PA

10

Clark Printing Co. Inc.

North Kansas, MO

14*

ColorArt Inc.

St. Louis, MO

30

Dennison Mfg. Co. IPC Dennison Co.

Rogersville, TN

60

Dinagraphics Inc.

Cincinnati, OH

20

Golden Belt Mfg. Co.

Durham, NC

70

Graphic Ctr. Cos. Inc. Blake Printery

St. San Luis Obi, CA

11

International Label Co.

Clarksville, TN

30

JW Fergusson & Sons

Richmond, VA

34

Maxwell Communications Corp. Atglen

Atglen, PA

50*

McCleery-Cumming Co.

Washington, IA

22

(SIC 2754) Commercial Printing-Gravure

(continued)

B-20

500*

TABLE B-3.


Location

Sales in $ Millions

Meredith-Burda Corp.

Des Moines, IA

500

Perry Printing Corp. Norway Div.

Norway, MI

25*

Printing House Inc. (Quincy Florida)

Quincy, FL

24

Ringier America Inc. Corinth Div.

Corinth, MS

80

Sheridan Press

Hanover, PA

15

Southern Gravure Svc. Inc.

Louisville, KY

58*

Stevens Graphics Inc.

Atlanta, GA

Technographic Inc. Decotone

Lexington, SC

30

World Color Press Inc. Salem Gravure Div.

Salem, IL

80

150

(SIC 2759) Commercial Printing Nec Alden Press Inc.

Elk Grove Village, IL

170*

Avery Intl. Corp. Soabar Products Group

Philadelphia, PA

100*

Bowne & Co. Inc.

New York, NY

190

Curtis 1000 Inc.

Atlanta, GA

160*

Data Documents Inc. (Omaha)

Omaha, NE

200

Deluxe Corp.

St. Paul, MN

1,316

Duplex Products Inc.

Sycamore, IL

327

Graphic Indus. Inc.

Atlanta, GA

310

John H. Harland Co.

Atlanta, GA

345

Maxwell Commun Corp.

St. Paul, MN

720*

Meehan-Tooker Inc.

East Rutherford, NJ

110

Quad Graphics Inc.

Pewaukee, WI

380

RR Donnelley & Sons Co. Warsaw Mfg. Div.

Warsaw, IN

160*

Webcraft Technologies Inc.

North Brunswick, NJ

220*

Williamhouse-Regency Inc.

New York, NY

230

(continued)

B-21

TABLE B-3.

PRINTING AND PUBLISHING FACILITIES (SIC 27) WITH ANNUAL SALES GREATER THAN $1 MILLION (continued) Company World Color Press Inc. Spartan Printing Co.

Location

Sales in $ Millions

Sparta, IL

100*

Allied Paper Inc. Allied-Energy Syss Inc.

Dayton, OH

130*

American Bus Products Inc.

Atlanta, GA

387

Arnold Corp.

Dayton, OH

200

CST Group Inc.

Wheeling, IL

110

Ennis Bus. Forms Inc.

Ennis, TX

130

McGregor Printing Corp.

Washington, DC

125

Moore Corp. Ltd. Moore Bus. Forms & Syss. Div.

Glenview, IL

New England Bus. Svc. Inc.

Groton, MA

226

Office Electronic Inc.

Itasca, IL

105

Standard Co.

Dayton, OH

709

Uarco Inc.

Barrington, IL

520*

Vanier Graphics Corp. (American Bus. Products Inc.)

Santee, CA

133

Wallace Computer Svcs. Inc.

Hillside, IL

429

(SIC 2761) Manifold Business Forms

1,675

(SIC 2771) Greeting Cards American Greetings Corp.

Cleveland, OH

1,309

American Greetings Corp. Seasonal Div.

Oscoola, AR

110

Current Inc. (Colorado Springs Colorado)

Colorado Springs, CO

160

Gibson Greetings Inc.

Cincinnati, OH

463

Hallmark Cards Inc.

Kansas City, MO

Hallmark Cards Inc. Topeka Products

Topeka, KS

2,500 120*

NEC = Not elsewhere classified * Indicates an estimated financial figure Source: Gale Research, Inc. Ward’s Business Directory of U.S. Private and Public Companies-1991, Volume 4. Detroit, MI. 1991.

B-22

APPENDIX C TOLUENE SOURCE CATEGORIES IN SURFACE COATING OPERATIONS

C-1

TABLE C-1.

TOLUENE SOURCE CATEGORIES IN SURFACE COATING OPERATIONSa (continued) Emissions reduction by process/product modification

Additional References

[1] Application area [2] Flashoff area [3] Oven areas [4] Coating mixing [5] Coating and solvent storage [6] Equipment cleanup [7] All solvent used and not recovered or destroyed may be considered potential emission sources

[1] [2] [3] [4] [5]

Thermal incineration Catalytic incineration Carbon adsorbers Waterborne coatings High solids materials

7,8

3546, 3621, 3643, 3351, 3357

[1] Coating application (low emissions) [2] Exhaust oven (high emissions) [3] Coating mixing [4] Coating and solvent storage [5] Equipment cleanup [6] All solvent used and not recovered or destroyed can be considered potential emission sources

[1] [2] [3] [4] [5]

Thermal incineration Catalytic incineration Ultraviolet cure coatings Waterborne coatings Powder coatings

9

3711-16

[1] Cleaning pretreatment [2] Application area [3] Flashoff area [4] Oven areas [5] Coating mixing [6] Coating and solvent storage [7] Equipment cleanup [8] All solvent used and not recovered or destroyed can be considered potential emission sources

[1] [2] [3] [4] [5]

Thermal incineration Catalytic incineration Carbon adsorber Waterborne coatings Powder coatings

10,11,12

General Source Category

Associated SIC(s)

Emission Point Sources

Large Appliances

3585,36313639,3651

Magnet Wire

Automobiles and Light Duty Trucks. (Locomotives and heavyduty trucks, hopper car and tank interiors, and paint and drum interiors are covered under metal products.)

(continued)

TABLE C-1.



[1] Coating area [2] Flashoff area: two piece and exterior base coating, interior spray coating, sheet basecoating (interior), sheet basecoating (exterior), side seam spray coating, end sealing compound, lithography, over varnish [3] Oven areas [4] Coating mixing [5] Coating and solvent storage [6] Equipment cleanup [7] All solvent used and not recovered or destroyed can be considered potential emission sources

[1] Thermal incineration [2] Catalytic incineration [3] Waterborne coatings for two piece cans [4] High solids coatings [5] Powder coating-side seam coating of uncemented three piece cans [6] Carbon adsorption-low temperature processes [7] Ultraviolet cure coatings

10,13,14

3444, 3449, 3353, 3354, 3479

[1] Application area [2] Flashoff area: prime coating, finish coating, [3] Exhaust oven area [4] Quench area [5] Fugitive emissions [6] Solvent mixing [7] Solvent storage [8] Equipment cleanup [9] All solvent used and not recovered or destroyed can be considered potential emission sources

[1] Thermal incineration [2] Catalytic incineration [3] Waterborne coatings

10,15,16

2621, 2631, 265253, 2656, 2657, 2671-72, 2675, 2676, 2678-79

[1] Application area [2] Oven areas [3] Coating mixing [4] Coating and solvent storage [5] Equipment cleanup [6] All solvent used and not recovered or destroyed can be considered potential emission sources

[1] [2] [3] [4]

10


Associated SIC(s)


Can Two-piece

3411-12

Metal Coils

Paper and Paperboard

Three-piece

(continued)

Carbon adsorber Thermal incinerator Catalytic incinerator Condensers

TABLE C-1.



[1] Adhesive application [2] Drying oven exhaust [3] Solvent mixing [4] Solvent storage [5] All solvent used and not recovered or destroyed can be considered potential emission sources

[1] Thermal incineration [2] Carbon adsorption

17,18

2426-29, 2434, 452, 2511-12, 2515, 2517, 2519, 2521, 2531, 2541, 3995

[1] Application area [2] Flashoff coating operations [3] Oven areas [4] Coating mixing [5] Coating and solvent storage [6] Equipment cleanup [7] All solvent used and not recovered or destroyed can be considered potential emission sources

[1] [2] [3] [4]

19

Flatwood Products

2435-36, 2491-99

[1] Application area [2] Flashoff area: Filler, sealer, basecoat, topcoat, inks [3] Oven areas [4] Coating mix [5] Coating and solvent storage [6] Equipment cleanup [7] All solvent used and not recovered or destroyed can be considered potential emission sources

[1] Waterborne coatings specially in filler and basecoat [2] Ultraviolet cure coatings [3] Afterburners [4] Carbon adsorption

11,20

Misc. Metal Parts and Products

2514, 2522, 2542, 2599, 3412-99, 3511-69, 3581-82, 3586-99

[1] Application area [2] Flashoff area: flow coating, dip coating or spray application [3] Oven areas [4] Coating mixing [5] Coating and solvent storage [6] Equipment cleanup [7] All solvent used and not recovered can be considered potential emission sources

[1] [2] [3] [4] [5] [6]

21,22,23,24


Associated SIC(s)


Adhesives and Sealants

2891

Wood Products

(continued)

Waterborne coatings Carbon adsorption Thermal incineration Catalytic incineration

Thermal incinerator Catalytic incinerator Carbon adsorbers Waterborne coatings Powder coatings High solids coating

TABLE C-1.

TOLUENE SOURCE CATEGORIES IN SURFACE COATING OPERATIONSa (continued)

a

Emissions reduction by process/product modification


[1] Coating application [2] Flashoff area: flow coating, dip coating or spray application [3] Coating mixing [4] Coating and solvent storage [5] Equipment cleanup [6] All solvent used and not recovered can be considered potential emission sources

[1] Carbon adsorber [2] Thermal incinerator [3] Catalytic incinerator

25

3731

[1] Coating application [2] Flashoff: prime coat operation, topcoat operation [3] Oven areas [4] Coating mixing [5] Coating and solvent storage [6] Equipment cleanup [7] All solvent used and not recovered or destroyed can be considered potential emission sources

None

26

3721-28

[1] Coating application [2] Flashoff: prime coat operation, topcoat operating [3] Oven areas [4] Coating and solvent storage [5] Equipment cleanup [6] All solvent used and not recovered or destroyed can be considered potential emission sources

Unknown

26


Associated SIC(s)


Plastic Products

2821, 2823, 3079, 3080, 3081-89, 3432, 3731

Large Ships

Large Aircraft

References 1-6

REFERENCES FOR APPENDIX C

1.

U.S. Environmental Protection Agency. VOC Pollution Prevention Options for the Surface Coating Industry. Research Triangle Park, NC. 1991.

2.

U.S. Environmental Protection Agency. Procedures from the Preparation of Emission Inventories for Carbon Monoxide and Precursors of Ozone, Volume I, EPA-450/4-91-016. Research Triangle Park, NC. 1991.

3.

U.S. Environmental Protection Agency, Stationary Source Compliance Division. Recordkeeping Guidance Document for Surface Coating Operations and the Graphic Arts Industry, EPA-340/1-88-003. Washington, DC. December 1968.

4.

Ron Joseph and Associates, Inc. Environmental and Coatings Training Program. Workbook for presentation by Ron Joseph to EPA Region 1. September 2 and 3, 1987.

5.

The Bureau of National Affairs, "Control Technologies" Air Pollution Control: BNA Policy and Practice Series. Washington, DC. 1992.

6.

Alliance Technologies. VOC Control Policy in the United States: An Overview of Programs and Regulations. December 1991.

7.

U.S. Environmental Protection Agency. Control of Volatile Emissions from Existing Stationary Sources. Volume 11: Surface Coating of Large Appliances, EPA-450/2-77034. Research Triangle Park, NC. 1977

8.

U.S. Environmental Protection Agency. Industrial Surface Coating: Appliances Background Information for Proposed Standards (Draft Environmental Impact Statement), EPA-450/3-80-037A. Research Triangle Park, NC. 1980.

9.

U.S. Environmental Protection Agency. Control of Volatile Organic Emissions from Existing Stationary Sources. Volume 11: Surface Coating of Magnetic Wire, EPA-450/277-033. Research Triangle Park, NC. 1977.

10.

U.S. Environmental Protection Agency. Control of Volatile Organic Emissions from Existing Stationary Sources. Volume 11: Surface Coating of Cans, Coils, Paper, Fabrics, Automobiles and Light-Duty Trucks, EPA-450/2-77-088. Research Triangle Park, NC. 1977.

11.

U.S. Environmental Protection Agency. Enforceability Aspects of RACT for Factory Surface Coating of Flat Wood ing, EPA-340/1-80-005. Washington, DC. 1980.

C-6

12.

U.S. Environmental Protection Agency. Automobile and Light Duty Truck Surface Coating Operations - Background Information for Promulgated Standards, EPA-450/3-79030B. 1980.

13.

U.S. Environmental Protection Agency. Beverage Can Surface Coating Industry Background Information for Proposed Standards, EPA-450/3-80-036A. Research Triangle Park, NC. 1980.

14.

U.S. Environmental Protection Agency. Beverage Can Surface Coating Industry Background Information for Promulgated Standards of Performance, EPA-450/3-80-036B. Research Triangle Park, NC. 1983.

15.

U.S. Environmental Protection Agency. Metal Coil Surface Coating Industry Background Information for Proposed Standards, EPA-450/3-80-035A. Research Triangle Park, NC. 1982.

16.

U.S. Environmental Protection Agency. Metal Coil Surface Coating Industry Background Information for Promulgated Standards, EPA-450/3-80-035B. Research Triangle Park, NC. 1982.

17.

U.S. Environmental Protection Agency. Pressure Sensitive Tape and Label Surface Coating Industry - Background Information for Proposed Standards, EPA-450/3-80-003A. Research Triangle Park, NC. 1980.

18.

U.S. Environmental Protection Agency. Final Environmental Impact Statement Pressure Sensitive Tape and Label Surface Coating Industry - Background Information for Promulgated Standards, EPA-450/3-80-003B. Research Triangle Park, NC. 1983.

19.

U.S. Environmental Protection Agency. Control of Volatile Organic Compound Emissions from Wood Furniture Coating Operations. Draft CTG. Research Triangle Park, NC. October 1991.

20.

U.S. Environmental Protection Agency. Control of Volatile Organic Emissions from Existing Stationary Sources. Volume 11: Surface Coating of Flatwood ing, EPA450/2-78-032. Research Triangle Park, NC. 1978.

21.

U.S. Environmental Protection Agency. Control of Volatile Organic Emissions from Existing Stationary Sources. Volume 11: Surface Coating of Metal Furniture, EPA-450/2-77-032. Research Triangle Park, NC. 1977.

22.

U.S. Environmental Protection Agency. Control of Volatile Organic Emissions from Existing Stationary Sources. Volume 11: Surface Coating of Miscellaneous Metal Parts and Products, EPA-450/2-78-015. Research Triangle Park, NC. 1978.

C-7

23.

U.S. Environmental Protection Agency. Surface Coating of Metal Furniture Background Information for Proposed Standards, EPA-450/3-80-007A. Research Triangle Park, NC. 1980.

24.

U.S. Environmental Protection Agency. Surface Coating of Metal Furniture Background Information for Promulgated Standards, EPA-450/3-80-007B. Research Triangle Park, NC. 1982.

25.

U.S. Environmental Protection Agency. Surface Coating of Plastic Parts for Business Machines - Background Information for Proposed Standards, EPA /450-3-85-019a. Research Triangle Park, NC. 1985.

26.

U.S. Environmental Protection Agency. Source Screening Study. Document summarizes emission control technology for source categories including the surface coating of large ships, large aircraft, and wood furniture. 1980.

C-8

APPENDIX D

SUMMARY OF EMISSION FACTORS LISTED IN THIS DOCUMENT

D-1

TABLE D-1.

SUMMARY OF TOLUENE EMISSION FACTORS (continued) Quality Ratinga

Reference

0.66 lb/1000 gallon throughput

U

4-12

Toluene storage-working loss

Organic Chemical Storage

3.6 lb/1000 gallon throughput

U

4-12

Toluene storage-breathing loss

30125805

Organic Chemical Manufacture-Toluene production-general

1.7x10-4 lb/lb toluene produced

U

4-14

Process emissions-general

407036


4.65x10-4 lb/lb toluene produced

U

4-14

Toluene storage

SIC

SIC Description

SCC

SCC Description

Emission Factor

2869

Industrial Organic Chemicals, n.e.c.

40703616


2869

Industrial Organic Chemicals, n.e.c.

40703616

2865

Cyclic Crudes and Intermediates

2865

Cyclic Crudes and Intermediates

-5

Note

2911

Petroleum Refining

306002

Petroleum Refining Catalytic 2.0x10 lb/lb toluene produced Cracking

U

4-14

Cracking unit-production from catalytic formate

2911

Petroleum Refining

306

Petroleum Refining

21 lb/ton total hydrocarbon

U

4-14

Fugitive emissions-petroleum refining with cracking and reforming-Fugitives are 1.05% toluene

2911

Petroleum Refining

306

Petroleum Refining

2.1 lb/ton total hydrocarbon

U

4-14

Fugitive emissions-petroleum refining without cracking and reforming-Fugitives are 0.105% toluene

3312

By-product Coke Manufacturing

303003

By-product Coke Manufacturing

2.4x10-4 lb/lb coke produced

U

4-14

Coke oven leaks

2865

Cyclic Organic Crudes and Intermediates

30120601

Styrene Production-General

1.52 g/kg styrene produced

U

4-14

Process emissions-general

2865


30120603

Styrene ProductionPurification

1.17 g/kg styrene produced

U

4-14

Styrene purification

2865


30120680

Styrene Production-General

10,358 kg/process unit-annually

U

4-14

Fugitive emissions

2865


40703616


0.66 lb/1,000 gallon throughput

U

4-12

Storage tank working losses

(Continued)

TABLE D-1.

SUMMARY OF TOLUENE EMISSION FACTORS (continued) Quality Ratinga

Reference

3-6 lb/1,000 gallon throughput

U

4-12

Storage tank breathing losses

N/A

2.22x10-5 lb/vehicle mile traveled

U

6-26

Evaporation from automobile fuel tank

N/A

N/A

8.46x10-4 lb/vehicle mile traveled

U

6-26

Automobile exhaust

Marine Cargo Handling

406002

Petroleum Marketing-Marine 33.4 mg/liter transferred Vessels-General

U

6-2 6-32

Uncleaned ship/ocean bargevolatile previous cargouncontrolled

4491


406002

Petroleum Marketing-Marine 21.7 mg/liter transferred Loading-General

U

6-2 6-32

Ballasted ship/ocean barge-volatile previous cargo-uncontrolled

4491


406002


U

6-2 6-32

Cleaned ship/ocean barge-volatile previous cargo-uncontrolled

4491


406002


U

6-2 6-32

Gas-freed ship/ocean barge-volatile previous cargo-uncontrolled

4491


406002


U

6-2 6-32

Any ship/ocean barge-nonvolatile previous cargo-uncontrolled

4491


406002


U

6-2 6-32

Typical ship/ocean barge-any previous cargo-uncontrolled

4491


406002

Marine Vessels-General

49.3 mg/liter transferred

U

6-2 6-32

Uncleaned barge-volatile previous cargo-uncontrolled

4491


406002


U

6-2 6-32

Gas-freed ship/ocean barge-any previous cargo-uncontrolled

4491


406002


U

6-2 6-32

Typical barge-any previous cargouncontrolled

SIC

SIC Description

SCC

SCC Description

Emission Factor

2865


40703615


N/A

N/A

N/A

N/A

N/A

4491

(Continued)

Note

TABLE D-1.

SUMMARY OF TOLUENE EMISSION FACTORS (continued) SIC

SIC Description

SCC

SCC Description

Emission Factor

Quality Ratinga

Reference

Note

5171

Petroleum Bulk Stations and Terminals

404001

Bulk Terminals/ Miscellaneous


U

6-28 6-32

Splash loading of gasoline

5171


404001

Bulk Terminals/ Miscellaneous


U

6-28 6-32

Submerged loading of gasoline, top or bottom

5171


404001

Bulk Terminals/Plants Loading Racks


U

6-28 6-32

Balance service loading of gasoline

5171


404001

Bulk Terminals-Fixed Roof Tanks

3.6 Mg/yr/tank gasoline

U

6-28 6-32

Working loss (typical tank capacity 2,680 m3) 950,000 liters/day terminal with 4 storage tanks

5171


404001

Bulk Terminals-Fixed Roof Tanks


U

6-28 6-32

Breathing loss (typical tank capacity 2,680 m3) 950,000 liters/day with 4 storage tanks

5171


404001

Bulk Terminals-Floating Roof Tanks

9.89x10-7 Q Mg/yr/tank Q is throughput in barrels

U

6-28 6-32

Working loss (typical tank capacity 5,760 m3) 950,000 liters/day with 4 storage tanks

5171


404001

Bulk Terminals-Floating Roof Tanks


U

6-28 6-32

Storage loss (typical tank capacity 5,760 m3) 950,000 liters/day with 4 storage tanks

5171


404002

Bulk Plants-Fixed Roof Tanks

63.6 mg/liter gasoline transferred

U

6-28 6-32

Breathing loss-uncontrolled

5171


404002



U

6-28 6-32

Filling loss-uncontrolled

5171


404002



U

6-28 6-32

Draining loss-uncontrolled

5171


40400250

Bulk Terminals/PlantsLoading Racks


U

6-28 6-32

Submerged loading (Balance Service) (throughput 19,000 l/day)

(Continued)

TABLE D-1.


SIC Description

SCC

SCC Description

Emission Factor

Quality Ratinga

Reference

Note

5171


40400250



U

6-28 6-32

Splash loading (throughput 19,000 l/day)

5171


40400250



U

6-28 6-32

Submerged loading (throughput 19,000 l/day)

5541

Gasoline Service Stations

40600302

Petroleum Marketing-Service 93.3 mg/liter gasoline stored Stations-Stage I-No Control

U

6-28 6-32

Uncontrolled emissions-Submerged filling loss (throughput 190,000 liters/month)

5541


40600301

Petroleum Marketing-Service 146.3 mg/liter gasoline stored Stations-Stage I

U

6-28 6-32

Uncontrolled emissions-Splash filling loss (throughput 190,000 liters/month)

5541


40600306

Petroleum Marketing-Service 4.2 mg/liter gasoline stored Stations-Stage I-Balanced

U

6-28 6-32

Uncontrolled emissions-Balanced submerged filling loss (throughput 190,000 liters/month)

5541


40600307

Petroleum Marketing-Service 12.7 mg/liter gasoline stored Stations-Stage I-BreathingUnderground Tanks

U

6-28 6-32

Uncontrolled emissionsUnderground storage tank breathing loss (throughput 190,000 liters/month)

5541


40600401

Petroleum Marketing-Service 139.9 mg/liter gasoline stored Stations-Stage II-Vapor-No control

U

6-28 6-32

Vehicle refueling-uncontrolled displacement losses (throughput 190,000 liters/month)

5541


40600403

Petroleum Marketing-Service 13.9 mg/liter gasoline stored Stations-Stage II-VaporControlled Displacement

U

6-28 6-32

Vehicle refueling-controlled displacement losses (throughput 190,000 liters/month)

5541


40600402

Petroleum Marketing-Service 8.9 mg/liter gasoline stored Stations-Stage II-Liquid Spill-No Control

U

6-28 6-32

Vehicle refueling spillageuncontrolled (throughput 190,000 liters/month)

N/A

N/A

N/A

N/A

E

6-34

Particle board with carpetemissions from new product

0.061 µg/m2/hr

(Continued)

TABLE D-1.


a

SIC Description

SCC

SCC Description

Emission Factor

Quality Ratinga

Reference

Note

N/A

N/A

N/A

N/A

0.59 µg/g/hr

E

6-38

Synthetic rubber adhesive for walls and ceilings-post application emissions

N/A

N/A

N/A

N/A

62 µg/g/hr

E

6-38

Synthetic rubber adhesive for vinyl carpet-post application emissions

N/A

N/A

N/A

N/A

2.5 µg/g/hr

E

6-38

Unspecified polymer adhesive for subflooring-post application emissions

"U" rating is based on engineering judgement.

(Continued)

TABLE D-2.

SUMMARY OF VOC EMISSION FACTORS SIC

SIC Description

SCC

SCC Description

Emission Factor

Quality Ratinga

Reference

2869

Industrial Organic Chemicals

30125805

Toluene Production-General

0.104 kg/hr/source

U

4-13

Fugitives-Gas/vapor pressure relief seals

2869


30125805


0.00083 kg/hr/source

U

4-13

Fugitives-Flanges

2869


30125805


0.0017 kg/hr/source

U

4-13

Fugitives-Open ended lines

2869


30125805


0.015 kg/hr/source

U

4-13

Fugitives-Sampling connections

2869


30125805


0.0056 kg/hr/source

U

4-13

Fugitives-Gas valves

2869


30125805


0.0071 kg/hr/source

U

4-13

Fugitives-Light liquid valves

2869


30125805


0.00023 kg/hr/source

U

4-13

Fugitives-Heavy liquid valves

2869


30125805


0.0494 kg/hr/source

U

4-13

Fugitives-Light liquid pump seals

2869


30125805


0.0214 kg/hr/source

U

4-13

Fugitives-Heavy liquid pump seals

2869


30125805


0.228 kg/hr/source

U

4-13

Fugitives-Gas/vapor compressor seals

Note: To obtain toluene leak emission factor for each component, multiply VOC emission factor above by the fraction of toluene in the stream. Based on engineering judgement.

a

Note

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