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