+ All Categories
Home > Documents > United States Environmental Protec ,ion Research ...infohouse.p2ric.org/ref/15/14212.pdf ·...

United States Environmental Protec ,ion Research ...infohouse.p2ric.org/ref/15/14212.pdf ·...

Date post: 25-Apr-2018
Category:
Upload: hoangnhi
View: 216 times
Download: 3 times
Share this document with a friend
12
SEPA Air and Energy Engineering Research Laboratory Research Triangle Park NC 27711 EPN600/S7-86/036 Feb. 1987 Y United States Environmental Protec ,ion Agency Research and Development pwx &PcEL1 5TC 33-00 Project Summary Iron and Steel Industry Particulate Emissions: Source Category Report John Jeffery and Joseph Vay The objective of this study was to de- velop particulate emission factors based on cutoff size for inhalable parti- cles for the iron and steel industry. After reviewing available information characterizing particulate emissions from iron and steel plants, the data were summarized and rated in terms of reliability. Size specific emission factors were developed from these data for the major processes used in the manufac- ture of iron and steel. A detailed proc- ess description was presented with em- phasis on those factors affecting the generation of emissions. A replacement for Section 7.5 (Iron and Steel Produc- tion) of EPA report AP-42, A Compila- tion of Air Pollutant Emissions Factors, was prepared, containing the size specific emission factors developed during this program. This Project Summary was devel- oped b y EPA 's Air and Energy Engineer- ing Research Laboratory, Research Tri- angle Park, NC, to announce key findings of the research project that is fully documented in a separate report of the same title (see Project Report or- dering information at back). Introduction The purpose of this program was to summarize the best available informa- tion on emissions of inhalable particu- late matter in the iron and steel indus- try. The main objective of the program was to develop reliable size-specific emission factois for the various proc- esses used in the production of iron and steel. Both uncontrolled and controlled emission factors are presented in the re- port. The uncontrolled factors represent emissions which would result if the par- ticulate control device (baghouse, scrubber, etc.) were bypassed, and the controlled factors represent emissions emanating from a particular type of con- trol system. The size-specific emission factors are generally based on the re- sults of simultaneous sampling con- ducted at the inlet and outlet of the con- trol device(s), utilizing a variety of particle sizing techniques. Other objec- tives of this program were to present current information on the iron and steel industry as well as prepare a re- placement for Section 7.5 of EPA report AP-42, "A Compilation of Air Pollutant Emissions Factors." The above objectives were met by a thorough literature search which in- cluded the following sources: 0 Data from inhalable particulate characterization program, 0 Fine Particle Emissions Inventory System (FPEIS), 0 AP-42 background file at EPA's Of- fice of Air Quality Planning and Standards (OAQPS), 0 GCA files, and 0 Various industry sources (e.g., American Iron and Steel Institute). The emission data contained in 45 ref- erence documents were reviewed, ana- lyzed, summarized, and ranked accord- ing to the criteria established by OAQPS as published in the report, "Technical Procedures for Developing AP-42 Emis- sion Factors and Preparing AP-42 Sec- tions," April 1980. After ranking the data, emission factors were calculated using the highest quality data available. The quality of the data used to develop
Transcript

SEPA

Air and Energy Engineering Research Laboratory Research Triangle Park NC 2771 1

EPN600/S7-86/036 Feb. 1987

Y United States Environmental Protec ,ion Agency

Research and Development

pwx &PcEL1 5 T C 33-00

Project Summary

Iron and Steel Industry Particulate Emissions: Source Category Report

John Jeffery and Joseph Vay

The objective of this study was to de- velop part iculate emission factors based on cutoff size for inhalable parti- cles for the iron and steel industry. After reviewing available information characterizing particulate emissions from iron and steel plants, the data were summarized and rated in terms of reliability. Size specific emission factors were developed from these data for the major processes used in the manufac- ture of iron and steel. A detailed proc- ess description was presented with em- phasis on those factors affecting the generation of emissions. A replacement for Section 7.5 (Iron and Steel Produc- tion) of EPA report AP-42, A Compila- tion of Air Pollutant Emissions Factors, was prepared, containing the size specific emission factors developed during this program.

This Project Summary was devel- oped b y EPA 's Air and Energy Engineer- ing Research Laboratory, Research Tri- angle Park, NC, t o announce key findings o f the research project that is fully documented in a separate report of the same title (see Project Report or- dering information a t back).

Introduction The purpose of this program was to

summarize the best available informa- tion on emissions of inhalable particu- late matter in the iron and steel indus- try. The main objective of the program was to develop reliable size-specific emission factois for the various proc- esses used in the production of iron and steel. Both uncontrolled and controlled emission factors are presented in the re- port. The uncontrolled factors represent

emissions which would result if the par- t iculate control device (baghouse, scrubber, etc.) were bypassed, and the controlled factors represent emissions emanating from a particular type of con- trol system. The size-specific emission factors are generally based on the re- sults of simultaneous sampling con- ducted at the inlet and outlet of the con- trol device(s), utilizing a variety of particle sizing techniques. Other objec- tives of this program were to present current information on the iron and steel industry as well as prepare a re- placement for Section 7.5 of EPA report AP-42, "A Compilation of Air Pollutant Emissions Factors."

The above objectives were met by a thorough literature search which in- cluded the following sources:

0 Data from inhalable particulate characterization program,

0 Fine Particle Emissions Inventory System (FPEIS),

0 AP-42 background file at EPA's Of- fice of Air Quality Planning and Standards (OAQPS),

0 GCA files, and 0 Various industry sources (e.g.,

American Iron and Steel Institute).

The emission data contained in 45 ref- erence documents were reviewed, ana- lyzed, summarized, and ranked accord- ing to the criteria established by OAQPS as published in the report, "Technical Procedures for Developing AP-42 Emis- sion Factors and Preparing AP-42 Sec- tions," April 1980. After ranking the data, emission factors were calculated using the highest quality data available. The quality of the data used to develop

I

each emission factor is indicated by the emission factor rating.

Process control system operating data as well as general industry infor- mation were also obtained and summa- rized as general background informa- tion. It was not part of this program to provide detailed engineering analyses, product specifications, or detailed eval- uation of trends in the industry.

Summary of Results Particulate emissions are generated

from several iron and steel facility activ- ities, including sintering, iron and steel product ion, semif in ished product preparation, and open dust sources. The most significant source of emis- sions from sintering operations is the windbox exhaust. Windbox emissions may be controlled by cyclones, electro- static precipitators (ESPs), scrubbers, or fabric filters. Most plants use cyclones as pretreatment to remove large partic- ulate from the gas stream to reduce fan wear. Most plants use ESPs or scrub- bers for windbox emission controls.

The casthouse is the major source of particulate emissions associated with blast furnace operations. A variety of techniques for capturing emissions from new casthouses and for retrofit-

ting other casthouses have been ap- plied. Several shops have experimented with and installed total casthouse evac- uation, partial casthouse evacuation, local hoods, runner evacuation, or pas- sive emission suppression systems. Fabric filters are used to clean collected gas for all collection techniques.

Emissions from basic oxygen fur- naces (BOFs) are divided into two cate- gories, primary and secondary. Primary emissions refer to any emissions gener- ated while the furnace is in an upright position. Secondary emissions refer to any emission generated while the fur- nace is tilted; i.e., charging, turndowns, tapping, and slagging. Primary emis- sions are captured by open or closed hoods. ESPs are the predominant gas cleaner used in conjunction with open hood systems, and venturi scrubbers are used with closed hood systems. Secondary emissions are captured by one or more of the fol lowing tech- niques: complete furnace enclosures with or without charge- and tap-side in- terior hoods, partial furnace enclosures, local hoods, deflector mechanisms to direct fumes toward the primary hood in open hood systems, and careful oper- ating and maintenance procedures using the existing primary hood.

Emissions from electric arc furnaces (EAFs) occur during charging, melting, oxygen-blowing, and tapping opera- tions. Fugitive dust emissions are gen- erated by scrap and raw material un- loading, storage, and transfer activities. A variety of systems have been devel- oped to capture emissions from EAFs inc lud ing direct shel l evacuation through a fourth hole in the furnace cover, total building evacuation, canopy hoods, and local hoods. Almost all EAFs use fabric filters to clean furnace emis- sions.

External desulfurization is becoming increasingly popular. The injection and subsequent reaction of desulfurization reagents with the hot metal (iron) create significant amounts of fume. Emissions are captured by collection hoods lo- cated above or alongside the mouth of the furnace. The most common gas cleaning devices used for controlling desulfurization fumes are fabric filters.

The total mass controlled and uncon- trolled emission factors for iron and steel product ion are presented i n Table 1. The size-specific controlled and uncontrolled emission factors are pre- sented in Table 2. Uncontrolled particu- late emission factors for open dust sources in an iron and steel plant are presented in Table 3.

Table 1. Particulate Emission Factors for Iron and Steel Mills

Emission Particle Factor Size

Source Units Emission Factor Rating Data

Sintering Windbox kg/Mg (Ib/ton) finished

sinter Uncontrolled

Leaving grate After coarse particulate removal

Controlled by dry ESP Controlled by wet ESP Controlled by venturi scrubber Controlled by cyclone

5.56 ( 1 7 . 1 ) 4.35 (8.7) 0.8 I1.6) 0.085 (0.17) 0.235 (0.47) 0.5 (1.0)

Yes

Yes Yes Yes

Sinter discharge (breaker and hot screens)

Uncontrolled Controlled by baghouse Controlled by venturi scrubber

Windbox and discharge

Controlled by baghouse

Blast furnace Slip Uncontrolled casthouse

Roof monitora

kg/Mg (Ibkon) finished sinter

3.4 (6.8) 0.05 (0.1) 0.295 (0.59)

kg/Mg (lbkon) finished sinter

kg/Mg (Ib/ton) slip kg/Mg (lb/ton) hot metal

0.15 (0.3)

39.5 (87.0)

0.3 (0.6)

B B A

A

D

B

Yes

Yes

2

Table 1. (Continued)

Source Units

Emission Particle Factor Size

Emission Factor Rating Data

Furnace with local evacuationb Taphole and trough only (not

runners)

Hot metal desulfurization Uncon trolledC Controlled by baghouse

Basic oxygen furnace (BOF) Top blown furnace melting and

refining Uncontrolled Controlled by open hood

vented to: ESP Scrubber

vented to: Scrubber

Controlled by closed hood

BOF Charging At source At building monitor Controlled by baghouse

BOF Tapping At source At building monitor Controlled by baghouse

Hot metal transfer At source At building

BOF monitor (all sources)

0-BOF melting and refining Controlled by scrubber

Electric arc furnace Melting and refining

Uncontrolled carbon steel

Charging, tapping, and slagging Uncontrolled emissions escap-

ing monitor Melting, refining, charging, tap-

ping, and slagging Uncontrolled

Alloy steel Carbon steel

Controlled by: Building evacuation to bag-

house for alloy steel

Direct shell evacuation (plus charging hood) vented to common baghouse for car- bon steel

Open hearth furnace Melting and refining

Uncontrolled Con trolled by ESP

Roof monitor

0.65 (1.3)

0.15 (0.3)

kg/Mg (lbkon) hot metal 0.55 (7.09) 0.0045 (0,009)

kg/Mg (Ib/ton) steel 14.25 (28.5)

0.065 (0.13) 0.045 (0.09)

0.0034 (0.0068)

kg/Mg (lb/ton) hot metal

kgiMg (Iblton) steel

kg/Mg (lb/ton) hot metal

kg/Mg Ilb/ton) steel

kg/Mg (Iblton) steel

kg/Mg (Ib/ton) steel

kg/Mg (Ib/ton) steel

0.3 (0.6) 0.07 1 (0.142) 0.0003 (0.0006)

0.46 (0.92)

0.00 13 (0.0026) 0.1.45 (0.291

0.095 (0.79) 0.028 (0.056)

0.25 (0.5)

0.028 (0.056)

19.0 (38.0)

0.7 (1.4)

W M g (lblton) steel

5.65 (11.3) 25.0 (50.0)

0.15 (0.3)

0.02 15 (0.043)

kg/Mg (lbkon) steel 10.55 (21.1) 0.14 (0.28) 0.084 (0.168)

B

B

D D

B

A B

A

D B B

D B B

A B

B

B

c

C

A C

A

E

D D C

Yes

Yes Yes

Yes

Yes

Yes

Yes

Yes

Yes

Yes

Yes

Yes Yes

3

~ ~~~~~

Table 1. (Continued)

Source Units

Particle Emission Factor Size

Emission Factor Rating Data

Teeming Leaded steel

Uncontrolled (measured at

Controlled by side draft hood source)

vented to baghouse

Unleaded steel

source)

vented to baghouse

Uncontrolled (measured at

Controlled by side draft hood

Machine scarfing Uncontrolled

Controlled by ESP

Miscellaneous combustion sourcese Boiler, soaking pit, and slab re-

heat Blast furnace gasf Coke oven gasf

kg/Mg (Ib/tonl steel

0.405 (0.81) A

0.0079 (0.0038) A

0.035 (0.071 A

0.0008 (0.00 16) A

kg/Mg (Ib/ton) metal through scarfer

B

A

0.05 (0.7)

0.01 15 (0.023)

e e

kg/109 J (lb/106 B&) 0.0 15 (0.035) D 0.0052 (0.0 12) D

'Typical of older furnaces with no controls, or for canopy hoods or total casthouse evacuation. *Typical of large, new furnaces with local hoods and covered evacuated runners. Emissions are higher than without capture systems be-

CEmission factor of 0.55 kg/Mg (1.09 Ib/ton) represents one torpedo car, 1.26 kg/Mg (2.53 Ib/ton) for two torpedo cars, and 1.37 kg/Mg (2.74

dBuilding evacuation collects all process emissions, and direct shell evacuation collects only melting and refining emissions. eFor various fuels, use the emission factors in Chapter 1 of AP-42. The emission factor rating for these fuels in boilers is A, and is soaking pits and slab reheat furnace is 0.

'Based on methane content and cleaned particulate loading.

cause they are not diluted by outside environment.

Ib/ton) for three torpedo cars.

Table 2. Size Specific Emission Factors

Emission Cumulative Factor Particle Mass % 5

Source Rating Size, pma Stated Size

Sintering Windbox emissions

Uncontrolled leaving grate D 0.5 4 b

1.0 4 2.5 5 5.0 9

10 15 15 2oc

d 100

Controlled by wet ESP

Controlled by venturi scrub- ber

C

C

0.5 1.0 2.5 5.0

10 15

d

0.5 1.0

Cumulative Mass Emission Factor

kg/Mg (Iblton)

0.22 (0.441 0.22 (0.44) 0.28 (0.56) 0.50 (1.00) 0.83 (7.67) 1.71 (2.22) 5.56 (1 1 . 7 )

7 8 6 0.015 (0.03) 25 0.02 1 (0.04) 33 0.028 (0.06) 48 0.04 1 (0.08) 596 0.050 io. 7 0) 69 0.059 (0.12)

100 0.085 (0.7 7)

55 0.729 (0.26) 75 0.176 (0.35)

4

Table 2. (Continued) I

Cumulative Mass Emission factor Emission Cumulative

Factor Particle Mass % I Source Rating Size, wma Stated Size kg/Mg (lb/ton)

2.5 5.0

70 15

d

89 93 96 98

100

0.209 0.219 0.226 0.230 0.235

(0.42) (0.44) (0.45) (0.46) (0.47)

Controlled by cy- clonee 25c

37b 52 64 74 80

100

0.13 0.19 0.26 0.32 0.37 0.40 0.5

(0.25) (0.37) (0.52) (0.64) (0.74) (0.80) (1.0)

C 0.5 1.0 2.5 5.0

10 15

d

Controlled by baghouse 3.0

9.0 27.0 47.0 69.0 79.0

100.0

0.005 0.014 0.04 1 0.071 0.704 0.119 0.15

(0.009) (0.027) (0.08 1) (0.141) (0.207) (0.237) (0.31

C 0.5 1.0 2.5 5.0

10.0 15.0

d

Sinter discharge (breaker and hot

screens) con- trolled by bag- house C 0.5

1.0 2.5 5.0

10 15

d

2b 0.00 1 4 0.002

11 0.006 20 0.010 326 0.076 426 0.021

100 0.05

(0.002) (0.004) (0.07 1) (0.020) (0.032) (0.042) (0.1)

Blast furnace Uncontrolled cast-

house emissions Roof monitor' C (0.02)

(0.09) (0.14) (0.21) (0.31) (0.37) (0.6)

(0. 09) (0.12) (0.20) (0.26) (0.31) (0.34) 11.3)

0.5 1.0 2.5 5.0

10 15

d

4 0.01 15 0.05 23 0.07 35 0.11 51 0. 15 61 0.18

100 0.3

7c 0.04 9 0.06

15 0.10 20 0.13 24 0.16 26 0.17

100 0.65

Furnace with local evacuations C 0.5

1.0 2.5 5.0

70 15

d

Hot metal desulfurizationh Uncontrolled

E 0.5 1.0 2.5 5.0

70 15

d

/

zc 0.07 11 0.06 19 0.10 19 0.10 21 0.12

100 0.55

(0.02) (0.12) (0.22) (0.22) (0.23) (1.09)

5

Table 2. (Continued)

Emission Cumulative Factor Particle Mass % 5

Source Rating Size, pma Stated Size

Controlled bag- house D 0.5 8

1.0 18 2.5 42 5.0 62 10 74 15 78 d 700

Basic oxygen furnace Top blown furnace

melting and refin- ing controlled by closed hood and vented to scrub- ber c 0.5

1.0 2.5 5.0 10 15

d

BOF Charging At sourcek

Controlled by bag- house

BOF Tapping At sourcek

BOF Tapping

house Controlled by bag-

Q-BOP melting and refining controlled by scrubber

E 0.5 1.0 2.5 5.0 10 15

d

D 0.5 1.0 2.5 5.0 10 15

d

E 0.5 1.0 2.5 5.0 10 15

d

D 0.5 1.0 2.5 5.0 10 15

d

D 0.5 1.0

34 55 65 66 67 72c 100

8c 12 22 35 46 56 IO0

3 IO 22 31 45 60 100

i 17 37 43 45 50 IO0

4 7 16 22 30 40 IO0

45 52

Cumulative Mass Emission factor

ka Ma (lb ton)

0.0004 (0.0007) 0.0009 (0.00 16) 0.0079 (0.0038) 0.0028 (0.0056) 0.0033 (0.0067) 0.0035 (0.0070) 0.0045 (0.009)

0.0012 (0.0023) 0.0019 (0.0037) 0.0022 (0.0044) 0,0022 (0.0045) 0.0023 (0.0046) 0.0024 (0.0049) 0.0034 (0.0068)

0.02 (0.05) 0.04 (0.07) 0.07 (0.13) 0.10 (0.21) 0.14 (0.28) 0.17 (0.34) 0.3 (0.6)

9.0 x 10-6 3.0 x 10-5

9.3 x 10-5 (0.0002)

1.8 x 10-5 6.0 x 10-5

6.6 x (0.0001)

0.000 1 (0.0003) 0.0002 (0.0004) 0.0003 (0.0006)

i 1

0.05 (0. IO) 0.17 (0.34) 0.20 (0.40) 0.21 (0.41) 0.23 (0.46) 0.46 (0.92)

5.2 x 10-5 (o.oooi) 0.000 1 (0.0002) 0.0002 (0.0004) 0.0003 (0.0006) 0.0004 (0.0008) 0.0005 (0.00 IO) 0.0013 (0.0026)

0.013 (0.025) 0.015 (0.029)

6

Table 2. (Continued) ,

Cumulative Mass Emission Factor Emission Cumulative

Factor Particle Mass % 5 Source Rating Size, pma Stated Size kg/Mg (Ib/ton)

2.5 56 0.016 (0.03 1) 5.0 58 0.016 (0.032) 10 68 0.019 (0.038) 15 85c 0.024 (0.048)

d 100 0.028 (0.056)

Electric arc furnace Melting and refining

carbon steel un- controlledm D 0.5 8 1.52 (3.04)

1.0 23 4.37 (8.74) 2.5 43 8.17 (1 6.34) 5.0 53 10.07 (20.14)

10 58 11.02 122.04) 15 61 11.59 (23.18)

d 100 19.0 (38.0)

Melting, refining, charging, tapping, slagging Controlled by

direct shell evacu- ation (plus charg- ing hood) vented to common bag- house for carbon steel" E 0.5 74b 0.0159 (0.03 18)

1.0 74 0.0159 (0.03 18) 2.5 74 0.0159 (0.03 18) 5.0 74 0.0159 (0.03 18) 10 76 0.0163 (0.032 7) 15 80 0.0172 (0.0344)

d 100 0.0215 (0.043)

Open hearth furnace Melting and refining

Uncontrolled E 0.5 lb 0.17 (0.21) 1.0 21 2.22 (4.43)

. 2.5 60 6.33 ( 12.66) 5.0 79 8.33 (1 6.67) 10 83 8.76 (17.51) 15 85c 8.97 ( 1 7.94)

d 100 10.55 (21.7)

Controlled by E S P E 0.5 lob 0.01 (0.02)

1.0 21 0.03 (0.06) 2.5 39 0.05 (0.10) 5.0 47 0.07 (0.13) 70 536 0.07 (0.15) 15 5lP 0.08 (0.16)

d 100 0.14 10.28)

aParticle aerodynamic diameter micrometers ( km) as define by Task Group on Lung Dy-

blnterpolated data used to develop size distribution. CExtrapolated, using engineering estimates. dTotal particulate based on Method 5 total catch. See Table 7. eAverage of various cyclone efficiencies. 'Total casthouse evacuation control system. gEvacuation runner covers and local hood over taphole, typical of new state of the art blast

namics. (Particle density = 7 g/cm31.

furnace technology.

7

Table 2. (Continued)

hTorpedo ladle desulfurization with CaC, and CaCO,. /Unable to extrapolate because of insufficient data and/or curve exceeding limits. kDoghouse type furnace enclosure using front and back sliding doors, totally enclosing the

mFull cycle emissions captured by canopy and side draft hoods. “Information on control system not available. PMay not be representative. Test outlet size distribution was larger than inlet may indicate

furnace, with emissions vented to hoods.

reentrainment problem.

Table 3. Uncontrolled Particulate Emission Factors for Open Dust Sources at Iron and Steel Millsa

Operation

Emissions by Particle Size Range (aerodynamic diameter) Emission

Factor 530 pm 5 1 5 p m s 1 0 p m 5 5 pm 52.5 pm Unitsb Rating

Continuous drop Conveyor transfer station sin-

ter

Pile formation stacker pellet ore

Lump ore

Coal

Batch drop Front end loaderkruck

High silt slag

Low silt slag

Vehicle travel on unpaved roads Light duty vehicle

Medium duty vehicle

Heavy duty vehicle

Vehicle travel on paved roads Light/heavy vehicle mix

13 0.026

1.2 0.0024

0.15 0.00030

0.055 0.0001 1

13 0.026

4.4 0,0088

0.51 1.8

2.1 7.3

3.9 14

0.22 0.78

9.0 0.018

0.75 0.0015

0.095 0.000 19

0.034 0.000068

8.5 0.017

2.9 0.0058

0.37 1.3

1.5 5.2

2.7 9.7

0.16 0.58

6.5 0.013

0.55 0.001 1

0.075 0.000 15

0.026 0.000052

6.5 0.013

2.2 0.0043

0.28 1.0

7.2 4.1

2.1 7.6

0.12 0.44

4.2 0.0084

0.32 0.00064

0.040 0.00008 1

0.014 0.000028

4.0 0.0080

1.4 0.0028

0.18 0.64

0.70 2.5

1.4 4.8

0.079 0.28

2.3 0.0046

0.17 0.00034

0.022 0.000043

0.0075 0.0000 15

2.3 0.0046

0.80 0.0016

0.10 0.36

0.42 1.5

0.76 2.7

0.042 0. 15

gm7 D Iblton D

g m l B

g/&l C

9 m l E

Iblton B

Iblton C

Ib/ton E

g/Mg C

g” C

Iblton C

Ib/’?on C

kgiVKT C IbNKT C

kg/VKT C Ib, VKT C

kg VKT B Ib/VKT B

kg/VKT C IbNKT C

a Predictive emission factor equations are generally preferred over these single value emission factors Predictive emission factor estimates

bUnits/unit of material transferred or units/unit of distance traveled are presented in Chapter 11, Section 17.2 of AP-42 VKT = Vehicle kilometer traveled VMT = Vehicle mile traveled

8

J. Jeffery and J. Vay are wi th GCA/Technology Division, Bedford, M A 01 730. Dale L. Harmon is the EPA Project Officer (see below). The complete report, entit led "Iron and Steel Industry Particulate Emissions:

Source Category Report, "(Order No. PB 8 7 - 1 19 889/AS; Cost: $13.95, subject to change) w i l l be available only from:

National Technical Information Service 5285 Port Royal Road Springfield, VA 22 16 1 Telephone: 703-487-4650

The EPA Project Officer can be contacted at: Air and Energy Engineering Research Laboratory U.S. Environmental Protection Agency Research Triangle Park, NC 2771 1

1 L

9

United States Environmental Protection Agency

- Center tor tnv i ronmenta l Hesearch Information Cincinnati OH 45268

~

Official Bus iness Penalty for Private Use, $300

EPAl600IS7-86l036


Recommended