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TABLE 5-14. POM COMPOUNDS MEASURED IN UNCONTROLLED COKE OVEN DOOR LEAK SAMPLES
(59)
Benzo(a)phenanthrene
Benzo(e)pyrene
Benzofluoranthenes
Benzo(k)f1uoranthene
Chrysene
Dlbenzanthracenes
Dibenzpyrene
D1methy1benz(a)anthracene
FT uoranthene
Indeno(l,2»3-c,d)pyrene
Naphthalene
Pyrene
Benzo(a)pyrene
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TABLE 5-15. POM COMPOUNDS MEASURED IN CONTROLLED DOOR LEAK SAMPLES (60)
Naphthalene
FTuoranthene
Pyrene
Benz(c)phenanthrene
Chrysene
Benz(a)anth racene
7,12-Dimethylbenz(a)anth racene
Benzof1uoranthenes
Benzo(a)pyrene
Benzo(e)pyrene
Choianthrene
Indeno(l,2,3-c,d)pyrene
Dibenz(a,h)anthracene
Dibenzacridines
Di benz(c,g)carbazole
Dibenzpyrenes
3-Methyl cholanthrene
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TABLE 5-16. POM COMPOUNDS IDENTIFIED IN COKE QUENCH TOWER EMISSIONS
INTERNAL EPA DATA (59)
Anthracene and phenanthrene
Methyl anthracenes
Fluoranthene
Pyrene
Methyl pyrene and fluoranthene
Benzo(c)phenanthrene
Chrysene and benz(a)anthracene
Methyl chyrsenes
Di methylbenz(a)anth racene
Benzo(a)pyrene
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TABLE 5-17. SELECTED POM COMPOUNDS IN COKE QUENCH TOWER SAMPLES
PUBLISHED DATA (61)
Benzo(a)pyrene
3-Methyl cholanthrene
7,12-Dimethylbenz(a)anthracene
Dibenz(a,h)anthracene
Dibenzo(a,h)pyrene
Dibenzo(a»i)pyrene
Benz(a)anth racenes
Pyri dine
Indeno(l,2,3-c,d)pyrene
Phenanthrene
Phenol
Cresol
Quinoline
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CORPORATION
The emission factor was then multiplied by the 1980 coke production
level of 41.8 million metric tons (56) and a typical yield of coke from coal
of 69 percent (57) to yield a national estimate:
/ 6gm POM \ /ton coal charged | | 41.8 x 10 metric tons cokej
^metric ton coal charged! I 0.69 ton coke J \^ yr J
Jjneiric_iojiJ = 3fi3 m@trfc tons POM/yr (400 tons/yr)
v iou gm j
This estimate is likely to represent the low end of the estimated range
of national POM emissions from by-product coke production because only door
leaks and quenching tower emissions are included and it was assumed that clean
water was used in quenching.
5.4.4 Trends Influencing POM Emissions
The two major factors that will influence POM emissions from by-product
coke production are:
o proposal/promulgation of coke oven NESHAPs and
o coke production levels.
Published alternatives being considered for the coke oven NESHAPs are
expected to require between 35 to 80 percent reduction of BSO emissions over
current levels, depending on the emissions source and the alternative selected
(51). These standards would apply to both new and existing coke ovens.
Production levels are related to the iron and steel industry which, as
discussed in Section 5.5.4 1s expected to experience only moderate growth in
the next few years (1 to 3 percent annually).
5.5 IRON AND STEEL PROCESSES
This section describes, in general, some iron and steel processes that
potentially emit POM. The discussion focuses on iron and steel sintering and
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ferroalloy production* two categories for which at least some Information on
POM emissions was located. Because there were Insufficient published total
POM emission data* the development of national emission estimates for iron and
steel sintering was not feasible.
5.5.1 Source Category Description
5.5.1.1 Process Description
Several iron and steel processes may potentially emit POM. Specific
information was located for iron and steel sintering and ferroalloy produc-
tion. The POM emissions from non-ferrous alloy production and other metals
manufacturing may be similar to those described for ferroalloy production.
Sintering—Sintering is the process by which pulverized ore is agglo-
merated before it is used in a blast furnace. A traveling grate moves the ore
over a series of wind boxes where air is pulled through the grate and the ore
is ignited with a burner (62). The ore contains coke and oil scrap and POM
compounds are generated from the burning of this material. Also* coke and
scrap particles with absorbed POM can escape at several points in the process
(62). Much of the POM may be emitted as vapor at sintering process tempera-
tures (62).
Ferroalloy Production—In production of ferroalloys, reducing materials
such as coal or coke and ores are charged to a furnace on a continuous or
cyclic basis. Furnace operation is continuous. In the most commonly used
process (electric arc furnaces) reactions occur in the zones surrounding large
electrodes. Burning of the coal or coke generates carbon monoxide, particu-
late matter, vaporous metallic compounds, and POM (63) which are emitted
through the furnace exhaust. Electric arc furnaces which can be open, closed,
or semi-sealed are also used in ferrous foundries, specialty and alloy steel
production, and nonferrous alloy production.
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5.5.1.2 Emission Controls/Regulations
Sintering—In 1976, two-thirds of the existing Iron and steel sintering
process factilities had no emission controls (62). Possible control technol-
ogies include ESPs, fabric filters, and wet scrubber, all of which would
capture significant amounts of POM. Wet scrubbers would likely be the most
efficient in reducing the total POM because vapor phase compounds would be
condensed in the scrubber. No federal NSPS exists for iron and steel sinter-
ing.
Ferroalloy Production—Exhaust gases from the electric arc furnaces are
typically vented to wet scrubbers or fabric filters, both of which should
provide significant POM control. Fabric filters are used at 26 of the 31
ferroalloy plants in the United States (63). A 1974 NSPS limits particulate
emissions, opacity, and carbon monoxide emissions from "new" electric arc
furnaces producing silicon-, manganese-, and chrome-based alloys. Federal
NSPS also exist for electric arc furnaces in iron and steel producion facil-
ities and non-ferrous alloy manufacture and an NSPS is being developed for
electric arc furnaces used in ferrous foundries (64). Most states also have
particulate emissions regulations applicable to existing metal production
facilities that have required the use of emission control equipment.
5.5.1.3 Source Locations
Sintering—Sintering occurs in conjunction with operation of large
blast furnaces. These plants are concentrated in Ohio, Pennsylvania, and
Indiana (62).
Ferroalloy Production—Production of ferroalloys is concentrated in the
same states as sintering (Ohio, Pennsylvania, and Indiana) as well as in West
Virginia, Alabama, Kentucky, and Tennessee. There are also large facilities
located in Colorado and California (65).
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5.5.2 Emission Factors
Sintering—Only BaP data were available for the sintering process (62).
The BaP emission estimates ranged from 0.66 to 1.1 gm per metric ton of
sinter feed.
Ferroalloy Production—POM emission data were collected from a semi-
sealed and a closed electric arc furnace in a recent study supporting review
of the ferroalloy NSPS (66). POM emissions from the semi-sealed furnace
(producing 50 percent FeSi) were 91.0 gm/Mw-h. This facility was controlled
with a 1ow energy wet scrubber followed by a flare. Emissions were measured
before the flare. Tests on the closed furnace (producing SiMn) showed con-
trolled POM emissions of 1.0 gm/Mw-h. The closed furnace was controlled by a
high pressure drop wet scrubber. Emissions from the closed furnace measured
before the scrubber were 156 gm/Mw-h when the furnace was producing FeMn.
Table 5-18 shows the compounds "detected in the furnace exhausts sampled.
No emission factor data were presented for open furnaces* which are used
1n the large majority of ferroalloy plants (65). However* one report reviewed
did present an annual nationwide POM estimate for open furnaces (see Section
5.5.3).
5.5.3 National Emission Estimates
As stated above* no useful total POM emission factors were available for
the iron and steel sintering. Therefore* development of a national POM emis-
sion estimates for this category was not feasible.
Reference 67 presented total uncontrolled POM emission estimates for
electric submerged-arc furnaces used in ferroalloy production:
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TABLE 5-18. POM EMISSIONS IN FERROALLOY ELECTRIC ARC FURNACE EXHAUST (66)
Semi sea led
Test C-2,
Furnace
during
50% FeS1 Production
FT uorene
Carbazole
Anthracene
Phenanthrene
Cycl openta ( def ) phenanth rene
Methyl anth racenes
FT uoranthene
Pyrene
Me thy Ipy rene
Benzo ( gh 1) f 1 uoranthene
Benzo(a) and benzo(b)f1 uorene
Chrysene
Benz(a) anthracene
Methylchrysenes
7,l2-d1methylbenz(a)anthracene
Benzotelpyrene
Benzofl uoranthene
Benzot 1 ) fl uoranthene
Benzo ( k ) f 1 uoranthene
Benzo(e)acephenanthylene
Perylene
Benzo(a)pyrene
Methyl benzopyrenes
3 -methy 1 chol anth rene
Indeno(l»2»3-c,d)pyrene
Benzo(gh1 )perylene
Anthanthrene
01benzo(ath)anthracene
D1benzo(c,g)carbazole
D1benzo(a1+ah)pyrenes
Coronene
TOTAL
mg/Nm3
75.0
b
18.3
18.3
10.7
1.5
27.4
28.5
0.07
8.9
1.24
8.1
10.5
0.81
3.5
0.16
3.5
0.43
1.64
1.10
3.2
0.83
1.0
g/MW-h
45.9
11.2
11.2
6.5
0.92
16.7
17.4
0.04
5.4
0.75
4.9
6.4
0.49
2.1
0.10
2.1
0.26
1.00
0.67
1.9
0.51
0.61
91.0
Cl c^e,^ Furnace
Test D-2, during Test D-l,
during
S1Mn Production FeMn Production3
mg/Nm3 g/MW-h mg/Nm3
1.5 0.36 16.0
9.6
2.1 0.51 220.0
0.070 0.017 24.0
0.24 0.058 220.0
0.22 0.053 2.3
0.005 0.0012 14.0
0.016 0.0039 49.0
5.2
0.58
51.0
3.1
1.2
0.39
6.0
1.4
0.90
0.079
O.S4
0.51
1.0
g/MW-h
4.0
2.4
54.9
6.0
54.9
0.57
3.5
12.0
1.3
0.14
13.0
0.77
0.30
0.10
1.5
0.35
0.22
0.020
0.13
0.13
156.0
aBefore scrubber.
bBlanks Indicate compound not detected.
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Estimated POM Emissions
Furnace Type (metric tons/vr)
Covered furnaces 209 to 1879
Open furnaces 135 to 1211
These calculations were based on actual emission factor data measured
upstream of emission control devices such as scrubbers and fabric filters.
However* it is likely that such control devices would substantially reduce the
amount of POM emitted to the atmosphere (67). Reported "organic" collection
efficiencies of the scrubbers on five furnaces tested ranged from 16 to 97
percent (67). As noted elsewhere in this report* fabric filters are expected
to achieve significant reductions in POM since the fine particulate onto which
POM is typically adsorbed is efficiently collected by fabric filters.
POM emissions were reportedly significantly higher for closed furnaces
than for open furnaces on the basis of POM emitted (uncontrolled) per unit of
furnace capacity.
5.5.4 Trends Influencing POM Emissions
Only low to moderate growth (1 to 3 percent annually) is foreseen for the
iron and steel Industry (68). Increased metals imports* high capital outlays
required for modernization expenditures to meet environmental regulations, and
the slow growth of steel-intensive industries are the major factors contribut-
ing to sluggish growth in this industry.
Any new capacity will be subject to the NSPS which generally requires the
use of fabric filters or high pressure drop wet scrubbers.
5.6 ASPHALT PRODUCTION - PAVING AND ROOFING
This section describes two asphalt-related sources of POM emissions:
manufacture of asphalt hot mix used in paving and air blowing of asphalt and
subsequent saturation of felt for asphalt roofing products.
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5.6.1 Source Category Description
5.6.1.1 Process Descriptions
Asphalt Hot Mix—Production of asphalt hot mix involves mixing asphalt
aggregates with hot liquid asphalt cement in a batch or continous process. A
large percentage of the hot mix is produced in existing plants using the batch
process shown in Figure 5-5a (71). The drum-mix process, in which wet aggre-
gate is dried and mixed with hot liquid asphalt cement as it is simultaneously
dried in a rotary dryer, has been used in most new plant designs (132). This
process is shown in Figure 5-5b. Drum-mix plants are also being used to re-
cycle salvaged asphalt pavement. Most asphalt mix plants are relatively
small: the average production rate is 160 metric tons/hr (176 tons/hr) (69).
POM compounds are emitted from combustion of gas or oil in the direct-feed
rotary dryer and from the mixer. Because the drum-mix process is based on a
parallel flow design (i.e., hot gases and aggregate flow through the dryer in
the same direction), particulate emissions from this process are less than
from a conventional process. However, because the asphalt is heated to a
higher temperature for a longer time, the drum-mix process may result in
greater POM emissions.
Fugitive emissions of POM may result from asphalt loading and handling.
As with most batch processes, emissions are highly variable.
In recent years, virtually all new plants are drum-mix operations in
which mixing and drying of the aggregates occurs within the same vessel (132).
Asphalt Roofing Products—The two major steps in the production of
asphalt-based roofing products are air blowing of the asphalt and saturating a
felt with the air blown material.
Although the processes are not always carried out at the same plant, air
blowing is an integral part of felt production. Air blowing involves accom-
plishing oxidation by bubbling air through liquid asphalt at 220 to 260°C (428
5-63
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5-65
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RADIAN
to 500°F) for 1 to 4 hours. Emissions are highly variable due to the cyclic
nature of the process (70).
Saturating the felt involves dipping it in airblown asphalt* spraying it
with the asphalt, or, in some cases, a combination of both techniques. The
final felt product, with controlled thickness coating of asphalt, is made into
rolls or shingles (70).
5.6.1.2 Emission Controls/Regulations
Asphalt Hot Mix—Wet scrubbers and fabric filters are typically used at
asphalt hot mix plants (74). No data were located on the effect of these
devices on POM emissions from the hot mix process. However, it can be
expected that both types of control equipment will provide a significant
degree of control of process emissions of POM because of their relatively high
fine particle collection efficiencies. Fugitive emissions from hot mix
production, on the other hand, are largely uncontrolled.
An NSPS for asphalt hot mix production was proposed in June of 1973. The
NSPS limits particulate matter emissions and the opacity of outlet stack gases
from plants (75). The NSPS applies to facilities constructed after June 1973.
The NSPS is currently being reviewed by EPA (132).
Asphalt Roofing Products—Typically, controls for air blowing of as-
phalt consist of a primary cyclone (to catch larger particulate matter) fol-
lowed by a fume incinerator (70). No data were located regarding the effect
of such a control system on POM emissions.
Saturating operations are generally enclosed by fume hoods which are
vented to emission control devices. The control devices used on various
plants include low voltage ESPs, afterburners, and high energy air filter
(HEAP) systems. Limited data showed HEAP systems reduced total POM by about
70 percent, while direct-fired afterburners had no effect on POM (70).
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eomxMumoi
An NSPS limits participate emissions and opacity from saturators and
blowing operations used in manufacturing roofing products and constructed
after November 1980 (75). ESPs, high velocity air filters and afterburners
are expected to be used to meet this NSPS (75).
5.6.1.3 Source Locations
Asphalt Hot Mix—About 20 percent of the 4300 operating asphalt hot mix
plants are mobile (71). Most permanently installed plants are located in
urban areas. As of 1974, states with 5 percent or more of the national
asphalt hot mix capacity were California, Illinois, New York, Pennsylvania,
and Ohio (72).
Asphalt Roofing Products—The majority of asphalt roofing product
plants are also located in urban areas. Six large plants (out of an estimated
200 total plants) were reported to account for 20 percent of production in
1973 (73). Four states were reported to have 15 or more roofing product
plants: California, Illinois, Texas, and New Jersey (73).
5.6.2. Emission Factors
The limited emission factor data located for these categories are
presented below. In both cases, published data were limited to one or two
emission tests conducted at what were considered to be representative
facilities.
Asphalt Hot Mix—Controlled emissions from the stack exhaust and mixer
at a batch production facility were reported to be 13.0 mg per metric ton of
hot mix produced (76). The plant was equipped with a primary cyclone followed
by a wet scrubber. No information was provided on the emission test method
used. Table 5-19 shows the POM compounds identified in the stack exhaust.
Reported analytical errors ranged from 6 to 144 percent for the different
compounds. No fugitive emission factor data were located, nor were data
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TABLE 5-19. POM COMPOUNDS IDENTIFIED IN STACK EXHAUST EMISSIONS FROM A
CONTROLLED ASPHALT HOT MIX PLANT (76)
Dlbenzothiophene
Anthracene/phenanthrene
Methyl anthracenes and phenanthrenes
9-Methy1anth racene
Fluoranthene
Pyrene
Benz(c)phenanth rene
Chrysene/benz(a)anthracene
7»12-Dimethylbenz(a)anthracene
3,4-Benzofluoranthene
Benzo(a)pyrene
Benzo(e)pyrene
Perylene
3-Methylcholanthrene
Dibenz(a,h)anthracene
Indeno(l,2,3-c,d)pyrene
7H-Dibenzo(c,g)carbazole
Dibenzo(a»h and a»i)pyrene
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available for the newer drum-mix facilities. [In the course of its NSPS
review* EPA plans to conduct emission tests at drum-mix facilities (132).]
Asphalt Roofing Products—Controlled POM emissions from air blowing and
saturator operations were reported as (77):
Air blowing: 2.1 mg POM/metric ton felt produced
Saturators: 4.3 mg POM/metric ton felt produced
These data represent the average emissions from two representative facil-
ities. The air blowing operations tested were equipped with fume incinera-
tors. At one air blowing operation, POM compounds were reduced by about 80
percent across the fume incinerator, but at the other facility POM increased
by a factor of two across the incinerator (77).
One of the saturators tested was equipped with a HEAP system which showed
70 percent reduction of POM. The other saturator tested was equipped with a
fume incinerator which reportedly had no effect on POM emissions (77).
The data were collected using a Method 5 sampling train modified by
placing the filter after a series of impingers. Table 5-20 shows the POM
compounds identified in samples from the air blowing operations tested.
5.6.3 National Emission Estimates
The emission estimates for these categories were calculated by
multiplying estimated 1980 national production levels by the emission factors
presented above.
Asphalt Hot Mix—Annual production of hot mix in 1980 was reported to
be 22.1 x 106 metric tons (24.3 x 106 tons) (78). This figure agrees rela-
tively well with a 1976 production level of 20 x 10^ metric tons used in an
earlier study (79), but is an order of magnitude lower than a 1975 estimated
production level of 300 x 106 metric tons attributed to the National
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TABLE 5-20. POM COMPOUNDS IDENTIFIED IN SAMPLES FROM ASPHALT
AIR BLOWING AND FELT SATURATION (77)a
Benz(c)phenanthrene
7,12-01methyl(a)anthracene
Benzo(a)pyrene
Benzo(e)pyrene
3-Methylcholanthrene
D1benz(a»h)pyrene
Dibenz(a,1)pyrene
aSample extracted with methylene chloride and analyzed by GC/MS.
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Asphalt Pavement Association (80). Since the 1980 estimate was more recent
and since the original reference for the higher estimate was not readily
available* the 1980 estimate was used in calculating national emissions:
|22.1 x 1Q6 metric tons hot mixj /13.0 x
I yr J ^metric
10 "3 am PONM /metric ton!
metric ton hot mixy \ 10° gm
= 0.29 metric ton/yr (0.32 ton/yr)
These estimates are based on the emission factors for batch plants and do not
reflect emissions from newer drum-mix plants.
Asphalt Roofing Products—In 1980, an estimated 5.3 x 10& metric tons
(5.8 x 106 tons) of asphalt roofing products were manufactured (78).
Based on the controlled emission estimates presented above national POM
emissions were calculated as follows:
A. 01 4 /5.3 x 106 metric tons fe1t\ [2.1 x 10"3 am POM) /metric ton]
Air Blowing: ^ ^^j ^etrlc ton felt j ( lO* gm )
= 0.011 metric ton/yr (0.025 ton/yr)
04. 4. /5.3 x 106 metric tons fe1t\ (4.3 x 1Q"3 gm POM ) /metric ton |
Saturators: ^ yp J ^ metric ton feu;^l()6gm )
= 0.023 metric ton/yr (0.012 ton/yr)
Total= 0.011 + 0.023 = 0.034 metric ton/yr (0.037 ton/yr)
5.6.4 Trends Influencing POM Emissions
Asphalt Hot Mix—Asphalt hot mix production levels are related directly
to the paving industry. Production levels are likely to remain relatively
steady (79). New or modified plants will be covered by the existing NSPS
which requires particulate emission control. Also, as mentioned above, newer
facilities are likely to be drum-mix designs.
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Asphalt Roofing Products—Production levels of roofing materials are
dependent on the housing industry and there is also a large replacement market
for these products. The 1980 U.S. Industrial Outlook (81) predicts a 2 per-
cent growth in new construction through 1984, although the growth in this
industry is highly dependent on the general state of the economy and on mort-
gage loan interest rates. No information was located regarding the capability
of existing roofing materials production facilities to keep pace with the
anticipated housing industry growth. New or modified plants will be subject
to the NSPS for this category.
5.7 CATALYTIC CRACKING IN PETROLEUM PRODUCTION
This section deals with POM emissions from catalytic cracking as used in
petroleum refining. Catalytic cracking is used to upgrade heavy petroleum
fractions to produce high octane gasoline and distillate fuels.
5.7.1 Source Category Description
5.7.1.1 Process Descriptions
There are three basic types of catalytic cracking techniques currently
used in the petroleum industry:
o fluidized catalytic cracking,
o thermofor catalytic cracking, and
o houdriflow catalytic cracking.
Fluidized catalytic cracking accounted for about 94 percent of the total
refinery catalytic cracking in 1977 (82). The basic process involves heating
a mixture of gas and oil to about 480°C over a silica alumina catalyst and
then fractionating the mixture (82). The spent catalyst is regenerated in a
kiln by burning off the coke that has coated the catalyst particles during
cracking. The regeneration process in carried out about 540°C. Venting of
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the exhaust gases from the regeneration kiln is a potential source of POM
emissions.
5.7.1.2 Emission Controls/Regulations
In many cases, exhaust gases from the regenerator are vented directly to
a carbon monoxide (CO) waste heat boiler to recover the useful energy in the
gases. CO boilers which are fired with auxiliary fuel or contain a catalyst
have been reported to be 99 percent efficient in reducing PAH emissions (82).
Direct-fired afterburners (plume burners) are reportedly not efficient con-
trols for POM.
Catalytic cracking units constructed after June 1973 are subject to an
NSPS that limits CO and particulate matter emission limits (83). The NSPS
generally requires the use of a CO waste heat boiler and an ESP. State
requirements applicable to new and existing catalytic cracking units also
generally require some degree of particulate matter and CO control (84).
5.7.1.3 Source Locations
Refining capacity is centered in Texas, Louisiana, and California, but
most states have at least one refinery (82).
5.7.2 Emission Factors
The most representative POM emission factor would appear to be one that
represents the use of a CO waste heat boiler. A weighted average of the
controlled emission factor data for the three types of catalytic cracking
techniques was reported to be 930 yg POM per cubic meter of oil cracked
(intermediate value in Reference 85). No information was provided regarding
the emission test method or the POM compounds included in the sample.
t>-73
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5.7.3 National Emission Estimates
National POM emission estimates for catalytic cracking were derived by
multiplying the emission factor given above by the reported quantity of oil
subject to catalytic cracking in 1980.
The Oil and Gas Journal (86) reports that as of January 1981, U.S.
catalytic cracking levels totaled 1,017,891 m3/stream-day (6,401,833
bbl/stream day). This figure includes fresh and recycle streams. A stream
day is defined as operation at full capacity for short periods. Catalytic
cracking units generally operate at stream-day capacity about 90 percent of
the time (86).
Based on this information, national POM emissions from catalytic cracking
were estimated as follows:
^1,017.891 m3 cracked\ L9 stream-dav\ /365days\ 1930 x 1Q~6 am Wrnetrictgnl
U
"A1
I stream day I \ day I \ yr J \m^ oil cracked J\ 106 gm
= 0.31 metric tons/yr (0.34 tons/yr)
5.7.4 Trends Influencing POM Emissions
Two factors will influence future POM emissions from catalytic cracking:
oil production levels subject to cracking and recent technology developments
in the cracking process itself.
Estimates of oil production levels fluctuate widely with changes in the
U.S. and world economic situations, but many forecasters predict a drop in
motor gasoline and distillate fuel production as a result of conservation
induced by price increases, more fuel efficient cars, and a switch from dis-
tillate oil to natural gas for home heating. The Oil and Gas Journal pre-
dicted a 2 to 3 percent drop in the amount of oil subject to cracking between
1981 and 1982 (87).
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More complete combustion of CO to C02 in the catalytic cracking process
could lead to reduced POM emissions. Recent developments in this regard
include the UOP hot regeneration and the Amoco Ultracat process. The rela-
tively higher temperature for regeneration used in the UOP process improves
combustion efficiency and thus could reduce POM emissions. However* the high
temperatures require special materials of construction making the UOP process
more suitable for new units than retrofits. The Amoco process, however, is
based on improving the catalytic reactor efficiency, allowing more complete
combustion to occur in the regenerator without having to operate at high
temperatures (88). Thus, the technology similar to the Amoco process may be
suitable for retrofit to existing units.
5.8 COMBUSTION OF MUNICIPAL, INDUSTRIAL, AND COMMERCIAL WASTES
Combustion of waste can be carried out in boilers or incinerators. Waste
fuel-fired boilers recover the heat from combustion to generate steam (or, in
rare cases, electricity). The primary purposes of incinerators, on the other
hand, are to:
o reduce the volume of waste to be disposed of,
o reduce the toxicity of waste, or
o recover valuable resources from the waste.
Although POM emission data were located only for municipal solid waste
(MSW) and commercial incinerators, several other categories are discussed
below because of their similar potential for POM emissions. The categories
discussed here include:
o municipal solid waste combustion (incinerators and
boilers),
o industrial solid and liquid waste combustion (incinerators
and boilers), and
o commercial solid waste combustion.
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Hazardous waste Incinerators were not reviewed 1n this study because of
their extensive coverage under the current RCRA programs (89).
5.8.1 Source Category Description
5.8.1.1 Process Descriptions
POM emissions from waste combustion will be a function of waste composi-
tion and Incinerator or boiler design and operation.
Municipal Waste Combustion—Municipal waste is generally a heterogenous
mixture of wood, paper, metal, glass, and refuse. However, municipal waste
can contain industrial wastes, combustion of which may result 1n relatively
higher POM emissions (90). One source (91) estimates that in 1980 municipal
solid waste contained 5 percent plastics by weight, 20 percent of which was
polyvinyl chloride (PVC). Combustion of plastics may potentially increase POM
emissions. Increasing utilization of plastic products would result in even
higher concentrations. Another factor that may result in relatively higher
POM emissions from municipal waste combustion is the expected higher percent-
ages of organic matter, such as leaves and tree clippings, that is likely to
be present during the Fall.
There are several types of municipal incinerators (90). The waste can be
combusted on a moving belt, in drum-type rolling chambers, or on various types
of grates. Waste can be fed continuously, as is the case for all larger,
modern facilities, or it can be fed in batches, sometimes manually. Batch
operations are typical of older, smaller municipal incinerators many of which
have been shutdown (see following sections). About 150 to 200 percent excess
air is supplied to the incinerator [compared with the 30 to 50 percent excess
air typical of industrial coal-fired boilers (92)]. The large volumes of
combustible exhaust gases generated are sometimes burned in secondary chambers
(multichamber units). The exhaust gases, which contain POM resulting from the
incomplete combustion of organic material in the waste, exit through stacks to
the atmosphere. Large units operating continuously at high temperatures
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achieve more efficient combustion than smaller units and thus produce less POM
per mass of waste material combusted (90).
The average MSW incinerator can process about 16,000 kg/hr [385 metric
tons/day (424 tons/day)] of solid waste (90). At most large facilities, the
waste is burned as received with an effort made only to separate out very
large non-combustible items.
Boilers fired with MSW also burn the waste as received, with only minor
separation. Typical new MSW boilers can process about 181-2720 metric tons/
day (200 to 3000 tons/day) of refuse (133). Heat input capacities of exist-
ing units range from 1.3 to 85 MW (4.5 x 106 to 290 x 106 Btu/hr) (93). [85
MW is approximately equal to 545 metric tons/day of waste burned for these
units.]
Industrial Waste Combustion—Industrial wastes combusted in incinera-
tors consist primarily of processing wastes and plant refuse and contain
paper, plastic, rubber, textiles, and wood. Because of the variety of manu-
facturing operations, waste compositions are highly variable between plants,
but may be fairly consistent within a plant. Also, existing industrial
boilers are used to burn refuse-derived fuel (RDF), either alone or with coal.
In addition, a recenty published paper (89) reports that as much as 18
million metric tons (20 million tons) of hazardous wastes are burned annually
in existing industrial boilers.
Industrial incinerators are basically the same design as municipal
incinerators. Available data (based on a sample of over 300 units) indicate
that 91 percent of the units were multichamber designs, 8 percent were single
chamber designs, and 1 percent were rotary kiln or fluidized bed designs (94).
About 1500 of the estimated 3800 industrial incinerators are used for volume
reduction, 640 units (largely in the petroleum and chemical industries) are
used for toxidty reduction, and the remaining 1700 units are used for re-
source recovery, primarily at copper wire and electric motor plants. Some
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Industrial boilers are specifically designed to fire waste fuels. There are
about 50 of these units, ranging up to about 7.6 MW (26 x 106 Btu/hr) heat
input capacity (93).
Refuse-derived fuel is a solid waste fuel that has been processed or
classified to remove non-combustible materials. RDF can be co-fired with coal
in existing boilers or in boilers designed specifically for RDF. There are an
estimated six facilities either operational or under construction that will
fire only RDF (93).
Apparently some existing coal- and oil-fired industrial boilers are being
used to burn hazardous wastes (89). Characteristics of these boilers were
discussed in Section 5.3.
Commercial Waste Combustion—Incinerators are used to reduce the volume
of wastes from medical"facilities, large office complexes, schools, and com-
mercial facilities. Small multichamber incinerators are typically used and
over 90 percent of the units require firing of an auxiliary fuel. Because of
the inefficient combustion in these units, they can be a potentially signifi-
cant source of POM (95). Operating skills of commercial and industrial
incinerator operators are usually limited.
5.8.1.2 Emission Controls/Regulations
This section presents a summary of the emission controls typically used
on existing waste combustion sources and general information on the air emis-
sion regulations applicable to these sources.
No quantitative data on the effect of emission controls on POM emissions
were located, but the general principles described in Section 5.3 apply here:
o particulate matter control technologies designed to col-
lect fine particles (ESPs, fabric filters) will be effec-
tive in controlling POM compounds which preferentially
condense on smaller particles, and
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o wet scrubbers can be effective in reducing POM emissions
that are 1n the vapor phase* because those compounds are
condensed as the gas Is cooled In the scrubber.
Highlights of the emission regulations applicable to existing and new
waste combustion sources are discussed below.
Municipal Waste Combustion—MSW incinerators and boilers firing MSW
with a capacity of 45 metric ton/day (50 tons/day) or greater and constructed
after August 1971 are subject to an NSPS (96) that requires about 93 percent
control of particulate emissions (97). Boilers and incinerators burning
municipal wastes are also subject to SIP emission and opacity limits in most
states. These are sometimes regulated together under the designation of "fuel-
burning equipment" (98).
New MSW-fired boilers will also be regulated under the industrial boiler
NSPS currently being developed by EPA. The proposed standard will likely
require the use of ESPs.
Industrial Waste Combustion—Industrial incinerators are subject to SIP
particulate and opacity standards in all 50 states. The typical standard
requires that outlet partlculate emissions be controlled to about 0.45
gr/Nm3 (0.2 gr/dscf) at 12 percent (X>2 (99), or slightly greater than 80
percent control (100). Opacity limits generally range between 10 and 30
percent (99). Most industrial incinerators are currently equipped with after-
burners, but new units may be required to have scrubbers or ESPs (101).
New industrial boilers firing waste or RDF will be subject to the NSPS
being developed by EPA, which will likely require the use of scrubbers or
ESPs. Existing industrial boilers are subject to SIP emission limits
depending on location, size, and fuel type. As discussed in Section 5.3.1.2,
emission controls used on existing sources vary from relatively inefficient
mechanical collectors to high efficiency ESPS and fabric filters. At least 40
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percent of the existing RDF and RDF/coal capacity is controlled with ESPs
(102).
Commercial Waste Combustion—No specific information was located for
these sources* but they may be subject to SIP particulate and/or opacity
levels. However* they are unlikely to be equipped with efficient emission
controls. Reference 95 reports that most "commercial" incinerators are
equipped with afterburners* but includes industrial incinerators in their
definition.
5.8.1.3 Source Locations
Municipal Waste Combustion—MSW incineration without heat recovery has
been declining in recent years due to the inability of older units to comply
with applicable air emission regulations. As of 1979-1980* there were slight-
ly more than 100 operating MSW incinerators spread over 19 states* most
located in the eastern and middle portions of the country (103). The highest
concentrations of these sources were in New York City and Chicago.
Most of the MSW-fired boilers are also located near urban population
centers (104).
Industrial Waste Combustion—No specific location data were available
for industrial incinerators or waste-fired boilers. However, the locations of
these units will obviously parallel those of the industries that rely on them.
The lumber and wood products, primary metal, and printing industries are
expected to be the major users of large incinerators. The lumber and wood
products industry is located primarily in the Southeast and Northwest. Pri-
mary metals are concentrated in the Appalachian and Great Lakes regions.
Commercial Waste Combustion—Concentration of these units will follow
urban population patterns.
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5.8.2 Emission Factors
Emission factors for total POM from waste combustion were available only
for MSW incinerators and commercial incinerators, and even these data were
quite limited. Most of the available data were originally reported in a 1967
study (105). No information was provided on the composition of the waste
fired during the tests, a major factor influencing POM emissions.
Table 5-21 shows available PAH emission data for four MSW incinerators
and a commercial incinerator. The PAH compounds reported are indicated in the
footnotes. Two previously described trends are supported by these data:
o Uncontrolled emission factors were highest for the commer-
cial incinerator, followed by the smaller MSW unit. The
larger MSW unit had the lowest uncontrolled emission
factor. These data, although very limited, tend to sup-
port the trend of less POM per unit of refuse burned'for
larger, more efficient incinerators.
o The scrubber and scrubber/ESP combination both showed
significant reduction of PAH relative to uncontrolled.
Emissions of polychlorinated biphenyl compounds (a subset of POM not
included in PAH) have been reported to be between 0.10 to 0.16 gm/metric ton
of municipal solid waste incinerated (based on two studies) (106).
5.8.3 National Emission Estimates
Development of national POM estimates was possible only for MSW incinera-
tors and commercial and industrial incinerators. Due to a lack of data re-
garding the amounts of waste combusted, emissions were developed by multiply-
ing the average unit capacity by the estimated number of units, an average
annual capacity factor, and an emission factor.
The average MSW incinerator capacity has been reported to be 385 metric
tons/day (424 tons/day) and there are an estimated 104 units nationwide (95).
A 70 percent average annual capacity factor was assumed in lieu of specific
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data for MSW incinerators. This assumption was based on a reported average
commercial incinerator capacity utilization of 71 percent (95). The PAH
emission factor presented in Section 5.8.2 for large MSW incinerators
controlled with the scrubber/ESP system was selected as representative of the
current population. The size of the unit tested was similar to the average
size MSW incinerator. The emission factor reported for PCB was not included
because of the relatively small size of the incinerator tested (0.11 metric
tons/day). Thus, the PAH emission factor may result in a low estimate of
total POM. National PAH estimates for MSW incinerators were calculated as:
(365 days) [385 metric tons incinerated] /O. 7 capacity f actoA /104 unitsNx
yr day-unit
0.014 om PAH] metric ton
metric ton \106 gm
= 0.14 metric tons/yr (0.16 tons/yr)
A similar method was used to calculate PAH emissions from commercial and
industrial incinerators:
p65 davs| /0.71 capacity factoA 12.5 metric tons] /100,000 units\ |6.8 gm PAHjx
I yr J \ I \~ unit day I \ I I metric ton/
(metric ton] = 440 metric tons/yr (485 tons/yr)
Average capacity, capacity utilization, and the number of units were obtained
from Reference 95. Industrial incinerators were included with commercial
incinerators in the available data on capacity and number of units. In lieu
of other data being available, the emission factor for commercial units was
assumed to apply to industrial incinerators.
It should be emphasized that these emission estimates are highly uncer-
tain. They are based on a very limited data; they may not reflect total POM
emissions (i.e., polychlorinated biphenyls); and they do not reflect the
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actual composition and amounts of waste combusted. Also* no data were avail-
able to develop accurate POM emission estimates for MSW-fired boilers, indus-
trial incinerators or industrial boilers burning solid waste, hazardous waste-
s, or RDF. Of these sources, industrial incinerators may potentially be the
most significant because of their relatively lower combustion efficiencies and
lack of controls.
5.8.4 Trends Influencing POM Emissions
Municipal Waste Combustion—The trend is toward larger, more efficient
MSW incinerators due to air emission regulations (90). These larger units
will generally be equipped with ESPs. One reference reports that the trend in
emission control selection for MSW incinerators has been forced away from
scrubbers because of the failure of some earlier poorly designed impingement
scrubbers (108).
Reported growth projections for MSW incineration are that about 5 new
units will be built by 1985, each at about 2270 metric tons/day (2,400 tons/
day) capacity. Six large MSW-fired boilers are expected to be built by 1990
(93). These new units will likely be controlled with ESPs or wet scrubbers.
Industrial Waste Combustion—Industrial incineration is expected to
decline, especially for use in volume reduction purposes (109). This trend is
reportedly due to land disposal techniques becoming more economical as a
result of more stringent air emission regulations (109). Exceptions to the
decline in industrial incinerators include (109):
o incineration with heat recovery (especially in the lumber,
pulp, and paper, and other industries with combustible
wastes), and
o resource recovery from copper wire and electric motor
incineration.
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One study has suggested that the complications of RCRA rules and the
associated recordkeeping requirements may lead to increased (and unregulated)
combustion of hazardous wastes in existing boilers (89). This could be a
significant source of POM emissions depending on the types of waste
incinerated, existing emission controls, and regulatory development related to
RCRA.
Six new RDF-fired units with a total heat input capacity of about 380 MW
are expected to be build by 1990 (93). The co-firing of RDF in existing coal-
fired boilers may increase due to general incentives to reduce fuel-related
costs.
Commercial Waste Combustion—No significant changes in capacity or
types of wastes incinerated are expected in this category.
5.9 CARBON BLACK PRODUCTION
5.9.1 Source Category Description
5.9.1.1 Process Description
Carbon black is produced by pyrolysis of an atomized liquid hydrocarbon
mixture. One of its main uses is as a reinforcing agent in rubber tires.
About 90 percent of U.S. carbon black is produced by the oil-furnace process.
Temperatures in the refractory-lined steel furnaces vary between 1320 and
1540°C. The heat for the decomposition reaction is supplied by combustion of
natural gas. The pyrolysis reaction is a source of POM emissions (110).
Hot furnace gas, containing carbon black particles, is cooled to about
230°C and then passed through a fabric filter for recovery of the carbon black
(110). Exhaust gas from the fabric filter is vented to the atmosphere or sent
to an emission control device. The main process vent is the major source of
POM emissions in a carbon black plant. Emissions may depend to some degree
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on the type of carbon black produced due to required differences in furnace
operation as a function of product specifications.
5.9.1.2 Emission Controls/Regulations
About two-thirds of U.S. carbon black plants use a combustion device
(flare, CO boiler, or thermal incinerator) on the main process vent (110). No
quantitative data were available on the effect of these systems on POM emis-
sions. Although the use of a combustion device might be expected to reduce
POM emissions, "high temperatures" (in the combustion devices) could report-
edly lead to formation of additional POM (110). No temperatures were speci-
fied in the reference reviewed.
However, in addition to the combustion control device, most carbon black
furnaces are equipped with fabrip filters for product recovery. Thus, POM
condensed on the captured carbon black particles will be removed from the
exhaust gas stream.
Existing carbon black plants are generally subject to SIP particulate
emission limits. New plants would be covered by prevention of significant
deterioration (PSD) requirements, but no NSPS exists for this source category.
5.9.1.3 Source Locations
Carbon black plants are located in Louisiana, California, West Virginia,
Arkansas, Oklahoma, and New Jersey (111). As of 1977, about 60 percent of the
U.S. production capacity was located in Louisiana.
5.9.2 Emission Factors
Total uncontrolled POM emissions from an oil-furnace carbon black plant
were measured in a previous study using a modified Method 5 sampling train
(110). Samples were extracted, separated by liquid chromatography, and
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analyzed by GC/MS. A total POM emission factor of 1.9 gm/metric ton (3.8 x
10~3 ib/ton) of carbon black produced was reported. Acenaphthylene accounted
for about 46 percent by weight of the POM in the samples collected. Table
5-22 lists the POM compounds detected in the collected samples.
5.9.3 National Emission Estimates
Reference 110 puts the U.S. carbon black production capacity at 1.72 x
10^ metric tons (1.9 x 10^ tons/yr). In 1980, the value of carbon black ship-
ments was $540 million (112). At about $0.50/bulk kg of carbon black (113),
this translates into approximately 1.08 x 10^ metric tons/yr (1.19 x 10^
tons/yr), or 57 percent of capacity. Thus, national POM emisisons from carbon
black production can be estimated as:
(1.08 x 10 metric tons carbon black | f 1.9 gm POM j /metric tonj
yr J Uetric ton produced/ ^ 106 gm J
= 2.05 metric tons/yr (2.26 tons/yr)
This estimate may be somewhat high since it is based on an uncontrolled POM
emission factor (110) and, as stated above, about two-thirds of the plants
currently have combustion devices for emission control. However, no data were
available to quantify the effect of such combustion-type controls on POM emis-
sions.
5.9.4 Trends Influencing POM Emissions
A two to three percent annual growth rate has been projected for the car-
bon black industry (114). Some of this growth appears possible without con-
struction of new facilities as indicated by the 57 percent capacity utiliza-
tion figure presented above. New plants will likely be subject to PSD permit-
ting requirements that require some form of emission control.
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TABLE 5-22. POM COMPOUNDS IN SAMPLES FROM OIL-FURNACE
CARBON BLACK PLANT (110)
Acenaphthylene (46% of total)
Anth racene/phenanth rene
Benzof1uoranthenes
Benzo(g,h»1)fluoranthene
Benzo(g»h,1)perylene/anthanthrene
Di benzanth i ocenes
D1benzo(c,g)carbazole
Dibenzopyrenes
Dibenzothlophene
Dimethyl anthracenes/phenanthrenesa
7,12 Dimethylbenz(a)anthracene
Fluoranthene
Indeno(l,2,3-c,d)pyrene
Methylanthracenes/phenanthrenes3
Methy1cholanth rene
Methylfluoranthene/pyrene
Pyrene (26% of total)
aTogether these groups accounted for 12% of total.
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5.10 WOOD CHARCOAL PRODUCTION
5.10.1 Source Category Description
5.10.1.1 Process Description*
Charcoal* primarily used for outdoor cooking* is manufactured by the
pyrolysis of carbonaceous raw materials. The raw materials used are primarily
medium to dense hardwoods. Softwoods* sawmill residue* nutshells* fruit pits
and vegetable wastes can also be used. (This study was limited to examining
charcoal production from wood.) There are two major types of techniques used
in wood charcoal manufacture:
o Missouri-type batch kiln, and
o Continuous Herreshoff furnace.
The batch process accounts for about 45 percent of the national produc-
tion (a small portion of this capacity is accounted for by older beehive
kilns). Continuous furnaces, which generally have a much larger capacity than
batch kilns, account for the remainder for production capacity. The kiln or
furnace products are sold directly or made into briquettes.
A Missouri-type batch kiln normally processes about 45 to 50 cords of
wood in a 10- to 25-day cycle. Kiln temperatures are in the 450 to 510°C
range and pyrolysis of the wood products is a source of POM emissions.
Missouri-type kilns have exhaust stacks along the side walls. The required
burn time and resulting emissions from the batch kiln vary with kiln capacity,
operational practices* wood species, and wood moisture content.
*The information presented in this subsection is summarized from References
115 and 116.
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Continuous charcoal production is accomplished in Herreshoff multiple
hearth furnaces. Furnace temperatures range between 480° and 650"C. The
off-gases exit through the stacks located on top of the furnace or are used as
a heat source (e.g. predrying of feed, drying of briquettes produced at an
adjacent location, or combustion in a waste heat boiler to produce steam.) Use
of continuous Herreshoff furnaces requires a large and steady source of raw
materials. The typical continuous furnace capacity is 2.5 metric tons/hr
(2.75 tons/hr).
5.10.1.2 Emission Controls/Regulations
Emission control of batch kilns is complicated by the cyclic nature of
the process. Direct-fired afterburners are probably the most feasible control
system, but auxiliary fuel use is required with these devices. If fuels other
than natural gas are used as the auxiliary fuel there is a potential for
additional POM emissions. No data were located on the percentage of batch
kilns equipped with afterburners. No data were located on the effect of
afterburners on POM. Natural gas would likely have to be used as the auxil-
iary fuel to avoid additional POM emissions.
Many of the batch kilns are older and relatively small batch kilns are
likely to be uncontrolled (115,116).
Continuous furnaces can also be controlled by direct-fired afterburners.
Auxilliary fuel firing is required only during start-up or process upsets on
continuous units because of the higher heating value of the exhaust gases. An
incinerator is used to control emissions in at least one continuous furnace
plant, but afterburners are reportedly used on most continuous furnaces (117).
There is no NSPS for charcoal manufacturing, although the feasibility of
developing a standard was investigated (115). Charcoal manufacturing facili-
ties are generally subject to SIP particulate emission limits and opacity
regulations. Some plants may be subject to CO standards.
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5.10.1.3 Source Locations
Charcoal manufacturing facilities are located primarily in Missouri,
Arkansas, and other Southeastern states (118). Missouri accounts for a large
share of the national production, although about 24 states have a wood
charcoal industry.
5.10.2 Emission Factors
POM emission factor data were available only for a Missouri-type batch
kiln (119). An average of five sampling runs showed total POM uncontrolled
emissions of 0.35 gm/hr (770 x 10~6 Ib/hr). Based on limited production
da-ta provided in Reference 119, this translates into about 3.5 gm/metric ton
of charcoal produced (0.007 Ib/ton). The authors report that the samples,
collected with a modified Method 5 apparatus and analyzed by gas chromato-
graph, contained benz(c)phenanthrene, benzo(a)pyrene, and "POM-like" material.
Four POM compounds were analyzed for, but not detected: dibenz(a,h)anthra-
cene, 3-dimethylcholanthrene, 7,12 dimethylbenz(a)anthracene, and 3,4,5,6-
dibenzocarbazole.
It should be noted that the emission tests were considered of question-
able value due to the difficulty of sampling the kiln and "the improvisational
sampling techniques" used. No estimate of the accuracy was provided. Also,
no emission data were reported for the initial ignition process during which
gas can escape from the kiln.
5.10.3 National Emission Estimates
The estimated 1978 charcoal production capacity was 376,340 metric tons
(414,000 tons) distributed as follows (120).
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Process Production % Total
Missouri-type 198,180 52.7
batch kiln
Beehive kiln 2,730 0.73
Continuing Herreshoff 175,460 46.6
furnace
376,370
Charcoal production in 1980 was assumed to be about the same since there has
been no indication of growth in the industry (121).
Based on these data, national POM emissions from Missouri-type kilns were
calculated as:
ii\ (Lj
J \rnei
r!98,180 metric tons charcoal] [3.5 gm POM] [metric ton^
I yr / Imetric tony V 106 gmJ
= 0.69 metric ton/yr (0.76 ton/yr)
Although an emission factor was not available for continuous furnace
production, is is expected that POM emissions will be substantially less (on a
mass per mass of charcoal produced basis) than for batch kilns. This is
because of the capability of the continuous furnace to use non-direct fired
afterburners or incinerators or to recover the heating value of the exhaust
gases through other combustion devices. These techniques should reduce POM
emissions. Thus, at a maximum, total POM emissions from this category should
be:
198,180 + 175,460 metric tons charcoal] [3.5 am POM] /metric ton]
yr \metr1c ton 106 gm
1\ [3.5 am POM] /m
J ynetric tony V
=1.3 metric tons/yr (1.4 tons/yr)
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This is a "worst-case" estimate since it is based on the higher emission
factor of the Missouri-kiln.
5.10.4 Trends Influencing POM Emissions
There is a general trend in the industry toward fewer but larger plants
that are more amenable to emission control than many of the existing small
plants. In addition, small plants have been forced to close in some states
(Florida* Illinois, Ohio, and Oklahoma) because of problems in complying with
state emission regulations (121). Also, the level of charcoal production has
remained relatively stable in recent years. There are no indications of
future growth in the industry, as briquettes are increasingly being manufac-
tured from other materials such as lignite. Thus, POM emissions from this
category are not expected to increase in the future.
5.11 VEHICLE DISPOSAL
5.11.1 Source Category Description
5.11.1.1 Process Description
Three types of techniques are used to remove the organic material from
auto bodies before they are used as scrap by the steel industry (usually in
electric arc furnaces). The organic material can be removed by (122):
o open burning of whole auto bodies
o incineration of whole auto bodies, or
o shredding of auto bodies and incineration of the shredded
steel.
Incineration of shredded steel is generally accomplished in rotary kilns.
The combustion efficiency of the kilns is relatively high, reducing the
potential for POM emissions (122). Open burning has a considerably higher
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potential for POM emissions than incineration because of the low combustion
efficiency typical of open burning.
5.11.1.2 Emission Controls/Regulations
Open burning is generally prohibited especially in most metropolitan
areas, but may still occur either illegally or outside restricted areas.
Incineration of whole auto bodies would likely be subject to SIP particu-
late matter emission limits applicable to incinerators. Mechanical col-
lectors, wet scrubbers, and ESPs are candidate control technologies for incin-
erators. No specific information was located with regard to the application
of controls to incineration of auto bodies.
5.11.1.3 Source Locations
No source location data were readily available. However, incineration of
auto bodies would be expected to coincide with steel industry locations.
5.11.2 Emission Factor Data
No POM emission factors for vehicle disposal were located.
5.11.3 National Emission Estimates
No emission factor or consumption data were located.
5.11.4 Trends Influencing POM Emissions
The demand for auto scrap by the steel industry is increasing due to an
increase in the use of electric arc furnaces. These furnaces can accomodate a
high proportion of scrap in the furnace feed (122). Concurrently, the in-
crease in demand has made shredding and subsequent incineration of auto body
steel in rotary kilns more economically attractive (122). The trend toward
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this higher combustion efficiency technique* combined with continued enforce-
ment of open burning prohibitions, may result in steady or decreased POM
emissions even, as the demand for auto body scrap is increased.
5.12 MOBILE SOURCES
This section discusses the following mobile source categories with
potential for POM emissions:
o gasoline-fueled autos and trucks,
o diesel autos and trucks, and
o rubber tire wear.
5.12.1 Source Category Description
5.12.1.1 Process Descriptions
Gasoline Autos and Trucks—Emissions of POM from combustion of gasoline
in autos and light-duty trucks are dependent on several factors, including
(123):
o inefficient combustion because of less than stoichiometric
air to fuel ratios,
o driver operation techniques that lower fuel efficiency,
o engine deterioration and combustion chamber deposits,
o aromatic content of the gasoline and presence of lead
additives.
The pyrolysis of motor oil deposits built up on the engine may also be a
potential source of POM emissions (123).
Diesel Autos and Trucks—The primary causes of POM emissions from
diesel combustion in autos and trucks are overloading and poor engine main-
tenance (124). However, even under normal operating conditions, diesel autos
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tend to emit more POM than their gasoline-fueled counterparts. The higher
emissions of POM may be due to the relatively lower combustion-chamber temper-
atures typical of diesel engines (124). Diesel autos emit 30 to 100 times
more particulate matter per mile than gasoline autos equipped with catalytic
converters. Diesel particulates are usually less than 1 pro in diameter and
consist of a carbonaceous core. Many different soluble organic compounds are
absorbed on these particles, some of which are POM (125).
Rubber Tire Wear—Carbon black and other tire materials possibly con-
taining POM are released to the atmosphere through oxidation and normal wear
of rubber tires (124).
5.12.1.2 Emission Controls/Regulations
Gasoline Autos and Trucks—The control devices used on recent model
autos have the capability to reduce POM emissions. Exhaust gas recirculation,
which was introduced in 1968, has been reported to reduce PAH emissions by 65
to 80 percent over uncontrolled (123). Catalytic converters, which generally
are used on post-1975 models, have been reported to reduce PAH emissions by up
to 99 percent (123).
Federal and state mobile source emission regulations generally require
the use of unleaded gasoline and catalytic converters for recent year models.
The regulations also limit emissions of NOX, CO, and hydrocarbons (HO and
evaporative losses. Some states have implemented regular inspection and
maintenance (I/M) programs for autos.
Diesel Autos and Trucks—Exhaust controls are not commonly used on
diesel-fueled vehicles. However, proper loading, fueling, and maintenance of
diesel engines can reduce their POM emissions (124).
Federal and California state regulations limit HC, NOX, CO, and evapora-
tive losses from diesel autos and light duty trucks. States have the option
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of implementing either the Federal or California standards, but are restricted
from implementing more stringent standards for diesel-fired vehicles (126).
Rubber Tire Wear—Emission controls or regulations are not applicable
to this source.
5.12.1.3 Source Locations
Source locations data is not applicable to mobile sources, although thei.r
concentrations are obviously higher in urban areas.
5.12.2 Emission Factors
Reference 131 provided emission factors for several PAH compounds emitted
from gasoline and diesel vehicles (Table 5-23). These values were based on
measured emission data and "derived emission factors." The emission factors
were then multiplied by estimated 1979 fuel consumption data for the various
types of mobile sources to develop the total estimates presented in the next
section. The PAH compounds included are listed in Table 5-24.
The authors note that the derived emission factors are quite uncertain
and may vary by a factor of two or more. The two major assumptions used in
developing the emission factors in Table 5-23 were (131):
o that the "PAH distributions" for both gasoline and diesel
vehicles are the same as the distribution for average
light-duty gasoline vehicles not equipped with catalytic
converters, and
o that all PAH emissions are reduced by catalytic converters
as much as BaP emissions are reduced by such devices.
5.12.3 National Emission Estimates
Table 5-25 shows the 1979 estimated PAH emissions from several mobile
source categories including gasoline and diesel autos and trucks, buses,
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