P.1 

OAR Box 1672 

Prepped by Charmelle Mathews 

Document Number: 

f)/Jffl\\-B-7 

Docket Number: 

A-98-13 

Printed 9/30/2008 11:01:00 AM Sheet 13 of 132 
T P.2 

,t £Pa(= 3 

A-W3 

MEMORANDUM 

TO: 

FROM: 

DATE: 

SUBJECT: 

Project File 

Organic Liquids Distribution NESHAP 

ESD Project No. 96/05 

Bernd Haneke 

Pacific Environmental Services, Inc. (PES) 

April 28,1998 

Site Visit to GATX Terminals Corporation facility in Philadelphia, 

Pennsylvania 

I. Purpose 

The purpose of this site visit was to tour the facility to educate EPA and contractor 

personnel concerning organic liquids distribution operations and to collect information related 

to air emissions from the operations. This work is in support of the development of national 

emission standards for hazardous air pollutants (NESHAP) for the organic liquids distribution 

(non-gasoline) source category. 

II. Location and Date 

GATX Terminals Corporation 

3300 N. Delaware Avenue 

Philadelphia, Pennsylvania 

December 19,1997 (8:30 am -12:30 pm) 

EPA AIR DOCKET 

III. Participants 

GATX Terminals Corporation 

Steven Kuhrtz - Vice President, Environment and Safety 

Alfred J. Shay - Operations Manager 

Christopher D. Cary - Environmental Manager EPA/DOT/USCG Programs 

Thomas J. Stafiniak - Manager, Environment, Health and Safety 

Environmental Protection Agency 

Stephen Shedd - Project Officer, OAQPS/ESD/WCPG 

Research Triangle Park, NC 

Pacific Environmental Services. Inc. (PES) 

Greg LaFlam - Environmental Engineer, RTP, NC 

TL 
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Site Visit Memo/GATX-Philadelphia 

April 28,1998 

Page 2 

Bernd Haneke - Environmental Scientist, RTP, NC 

Jay Helms - Environmental Engineer, RTP, NC 

IV. Pre-Tour Discussion 

Introduction 

After the participants introduced themselves, Steve Kuhrtz, GATX, opened the meeting 

with an introduction to the GATX Terminals Corporation. GATX currently operates 25 

terminals in the U.S. and 20 overseas terminals in Europe and Asia. GATX terminals handle 

approximately 80 percent petroleum products and 20 percent chemicals. Five of the GATX 

terminals handle chemicals exclusively. The Philadelphia terminal handles primarily 

chemicals, with the exception of aviation gasoline. 

Steve Shedd, EPA, followed Mr. Kuhrtz with a discussion of the background and 

rationale for EPA's regulation of hazardous air pollutant (HAP) emissions. Prior to the Clean 

Air Act Amendments of 1990 (CAAA), regulations were on the basis of individual HAP and 

few regulations were enacted. The CAAA included a list of HAP and mandated that national 

emission standards for HAP (NESHAP) be developed for categories of sources of the HAPs. 

The stringency of the Organic Liquids Distribution (non-gasoline) NESHAP (for existing 

sources) will be based on a level of control representing the average control achieved by the top 

12 percent of facilities in the category. The Organic Liquids Distribution standards are slated to 

be proposed in 1999, with promulgation of the final rule in November 2000. 

Mr. Shedd stated that the EPA has prepared an industry questionnaire and distributed it 

to trade organizations for their review and comment. The questionnaire, when final, will be 

sent to several companies within the Organic Liquid Distribution source category. He also 

described the EPA's procedures for handling information that the company considers to be 

confidential business information (CBI). Mr. Shedd inquired and GATX representatives did 

not claim anything during the EPA site visit as confidential. The company will have an 

opportunity to review the draft site visit report prepared by PES, to comment on its accuracy 

and to identify anything in the report they consider to be CBI. This report, with any CBI 

withheld, will be made a part of the public record for this rulemaking. 

Facility Description 

The Philadelphia facility is a bulk storage terminal located on approximately 35 acres of 

property on the Delaware River just north of downtown Philadelphia. The terminal has 

approximately 100 tanks with a total storage capacity of 1.2 million barrels. The storage tanks 

located at the terminal range in size from 715 to 100,000 barrels. Products are handled by 
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Site Visit Memo/GATX-Philadelphia 

April 28,1998 

Page 3 

marine vessel (barge and tanker ship), railcars, and trucks. There are two marine docks, one for 

both ships and barges (berth #2) and the other berth (berth #1) is for barges only. In 1990, a 

new above ground pipeline system was constructed for the marine loading and unloading. In 

general, the facility is graduating from underground toward above ground dedicated pipelines. 

The facility has 17 tank truck loading/unloading stations which have the ability to service 

multiple tanks. 

Liquid chemicals are brought into the facility and sent out from the facility by marine 

vessel, railcar, and tank truck. The facility receives and ships out products owned by others on 

a for-hire basis. The facility blends various recipes at the on site denatured spirits plant, 

inlcuding brucine and alcohol. Some proprietary blending of ethyl alcohol based materials is 

also performed at the denatured spirits plant. The facility also blends other acides such as 

formic and acetic acid. Most of the blending that occurs here is "in-line blending", that is to 

say that liquids are blended as they are being transferred into tank trucks. Liquids that move 

through the terminal in large quantities are phenol, benzene, cumene, acetone, organic acids, 

and fuel grade ethanol. 

GATX/Philadelphia handles both domestic and international shipments. The 

approximate quantities handled per year, by delivery mode, are: 

- 24 million gallons/year by tank trucks 

- 12 million gallons/year by railcars 

— 66 million gallons/year by barges 

— 12 million gallons/year by tanker ships 

The storage tanks at the facility consist of cone roof, specialty dome roof, and aluminum 

as well as steel internal floating roof tanks. A few of the storage tanks are dedicated to certain 

products, such as the benzene tank, which has an internal floating roof. Some of the storage 

tanks are subject to the NSPS requirements for storage tanks (Subpart K, Ka, or Kb). 

Emissions Inventory 

GATX/Philadelphia is currently trying to obtain a synthetic minor status. Tank 

emissions, fugitive emissions, and loading loss summaries are included in Attachments 1 

through 3. A plot plan of the facility is contained in Attachment 4. Separate inventories are 

shown for tank emissions, fugitive emissions, and loading losses. A copy of the 1996 

emissions inventory was obtained during the site visit, and emissions from the facility are 

shown as follows: 

3 
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Site Visit Memo/GATX-Philadelphia 

April 28,1998 

Page 4 

TABLE 1. SUMMARY OF 1996 EMISSIONS INVENTORY (Compiled by EPA/PES 

project team using information supplied by GATX/Philadelphia) 

Emission Source 

Fugitive Emissions 

Storage Tanks 

Loading Losses 

Wastewater 

Total 

VOC(tpy) 

1.00 

20.08 

10.43 

Not Available 

31.51 

HAP(tpy) 

0.40 

16.22 

4.02 

Not Available 

20.64 

According to the emissions inventory supplied to the EPA/PES project team, the facility is not 

a major source for HAPs. No information was obtained regarding the emission factors that 

were used to calculate fugitive emissions. 

Products Handled 

Company representatives distributed a listing of the HAP liquid products handled by the 

facility in 1996. The facility handles primarily chemicals, with the exception of aviation-grade 

gasoline. The chemicals handled are primarily benzene, cumene, methanol, methyl chloroform, 

methyl ethyl ketone, methylene chloride, phenol, and trichloroethylene. Cumene is the primary 

chemical, comprising approximately 33 percent of all chemicals handled. Among the acids 

handled and stored at the terminal, acetic acid, which has a freezing point of 62 degrees 

Fahrenheit (°F), is transferred and stored in insulated lines and heated tanks. 

Control Measures 

The company has incorporated certain control measures to reduce air emissions of 

volatile chemical products at the GATX facility. One specific control system is in use: an 

enclosed combustion system (thermal oxidizer) with a backup system of four carbon canisters. 

The thermal oxidizer, supplied by National Air Oil (NAO), is used to control vapors 

displaced during tank truck loading of benzene and aviation gasoline, and also emissions from 

the fixed-roof tank storage of acrylates (for odor control purposes). This system is 

approximately 2.4 meters (8 feet) in diameter, and has a backup of four carbon canisters, in case 

of problems resulting in the temporary shutdown of the unit. The unit utilizes No. 2 fuel oil to 

maintain the proper operating temperature. Additionally, the thermal oxidizer has a capacity of 

250 scfm. Temperature is monitored continuously at the thermal oxidizer to ensure that it is 

functioning properly. The ideal operating temperature has been set at 1,250°F. As mentioned 

4-
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Site Visit Memo/GATX-Philadelphia 

April 28,1998 

Page 5 

above, should the thermal oxidizer malfunction, there is a four carbon canister (carbon 

adsorption) backup system. 

Benzene, as well as other vapors that are routed to the thermal oxidizer are first stored 

and accumulated in two 30,000 gallon tanks that were previously used to store liquified 

petroleum gas (LPG). The system operates under 5 inches of vacuum, and when capacity is 

reached, the vapors are vented to the thermal oxidizer. 

The GATX facility also monitors its equipment for leaks on a regular basis. There is a 

monthly monitoring program for equipment that is in benzene service (pumps, flanges, valves, 

etc.). Additionally, pumps that are in benzene service are monitored for leaks on a weekly 

basis. Equipment handling VOC is monitored on a quarterly basis. Besides the monitoring 

programs mentioned here, equipment is visually monitored on an ongoing basis by GATX 

personnel. All equipment handling VOC's with a RVP greater than 4 are monitored on a 

monthly basis as specified in the RACT plan. 

The facility does not employ any type of wastewater treatment system, except for an 

oil/water separator that treats contaminated waste water. The treated storm water is discharged 

into a publicly owned treatment works facility (POTW). It is estimated that an average of 40 

gal/min discharge from the API oil/water separator is a typical value for storm events. 

Wastewater at GATX is primarily a product of tank and pipeline cleanings, and spills. 

An average of 15 tanks/year are cleaned at the facility. Tanks are cleaned with a hot water 

caustic wash. Alternatively, tanks are stripped of all product prior to being either caustic 

washed, detergent washed, fresh water washed or air dried. A member of the EPA/PES project 

team inquired as to the availability of emission factors for tank cleanings. GATX 

representatives replied that no such factors were in existence at this time. 

Drums are used for the storage of hazardous waste and non-hazardous wastes are stored 

in several small tanks. Waste water which is a product of tank washings is disposed of off-site 

by a contractor within 90 days of generation. Later conversations between Mr. Shay and Mr. 

Haneke indicated that approximately 30,000 gallons of waste water are generated on the facility 

on an annual basis and treated off-site by a contractor. 

V. Items Requested by the EPA Project Team 

Various items were requested by the EPA project team during the site visit. In 

particular, Mr. LaFlam requested: 

1. The results of the efficiency test of the thermal oxidizer, 

2. The operating costs of the thermal oxidizer, 

£ 
P.7 

Site Visit Memo/GATX-Philadelphia 

April 28,1998 

Page 6 

3. The dollar amount of the thermal oxidizer's annual service contract, and 

4. The dollar amount of the capital costs for installing the thermal oxidizer. 

Other items requested by the EPA/PES project team included: 

1. The volumes of wastewater (non-stormwater) generated per year at the facility, 

2. The HAP concentration of the wastewater (if known), and 

3. Emission factors used to calculate fugitive emissions for the facility. 

V. Plant Tour 

At the conclusion of the discussion summarized in Section IV above, Mr. Shay took the 

EPA/PES team on a walking tour of the facility. 

The tour began with a trip across Delaware Avenue to the ship loading dock which 

borders the Delaware River. Mr. Shay explained to the group the process of loading and 

unloading a marine vessel. Numerous hoses were observed that served to unload ships and 

barges. These hoses were connected to above ground pipelines that convey liquids to the main 

facility. Mr. Shay also explained the means by which pipelines are pigged. Pigging of 

pipelines serves the purpose of cleaning as well as the removal of the majority of the product 

from the line prior to using the line for similar products. 

Next, Mr. Shay led the group to one of the railcar loading racks. He explained the 

process by which a railcar is loaded and unloaded. The cars are usually top loaded and bottom 

unloaded with various liquids. Some rail car positions have vapor recovery lines. Additionally, 

rail car tanks can be purged or blanketed with nitrogen or heated with steam. When loading 

acetic acid, it is necessary to heat the liquid due to its high freezing point. At the time of the 

site visit, the facility was not loading any products into railcars that required vapor recovery. 

Next, the tour continued on to the denatured spirits plant, which is where the facility's 

small blending operations take place. The operation involves eight 5,000 gallon tanks as well 

as products in 55 gallon drums used for the denaturing process. There are also four main 

storage tanks that have a total capacity of 2,342,000 gallons that store ethanol. 

Following the denatured spirits plant, Mr. Shay led the group to the thermal oxidizer. 

The thermal oxidizer was discussed and viewed on site, and an alarm was serviced during the 

EPA/PES project team site visit. Four carbon canisters which serve as backups to the thermal 

oxidizer were also viewed at this location, as was the No. 2 fuel oil tank which provides fuel for 

the thermal oxidizer. 

At one point in the facility, a series of two pressure vessels were observed that serve to 

6 
P.8 

Site Visit Memo/GATX-Philadelphia 

April 28,1998 

Page 7 

capture vapors from storage tanks. These vapors are collected in the storage vessels and 

subsequently are sent to the thermal oxidizer. 

Loading racks and their associated loading arms were also observed at the GATX plant 

site. A rack that handles aviation grade gasoline was observed, along with its vapor return 

lines. There were also racks with dedicated benzene service, along with a rack handling 

acrylates. 

VI. Post-Tour Discussion 

Following the plant tour, a brief discussion was held to review the content of the tour 

and additional questions were asked. The EPA/PES team also reviewed the items it wished to 

have sent following the site visit (see Section V, Items Requested by the EPA Project 

Team). The EPA/PES team expressed their thanks and the visit was concluded. 

VII. Action Items 

The EPA and PES will prepare a draft site visit trip report, which will be sent out to the 

GATX facility for technical review and identification of any CBI. The EPA/PES project team 

expressed a desire to receive the requested information within a reasonable amount of time. 

7-
GAfX Terminals Corporation Tank Emissions Summary • 1996 

Tonk It Type Product(s) 

(H.I.V) 

Tank# Type Producl(s) 

(H.I.V) 

51 V 

52 V 

53 V 

54 V 

55 V 

56 V 

57 V 

58 V 

104 V 

105 V 

106 V 

107 1 

108 V 

121 V 

122 V 

123 1 

124 1 

124 1 

125 V 

126 V 

JQ12 7 V 

128 V 

129 V 

130 V 

131 V 

133 V 

134 V 

134 V 

135 V 

135 V 

137 V 

140 V 

141 V 

142 V 

143 1 

144 V 

145 V 

145 V 

146 V 

147 V 

148 I 

148 1 

Methyl Isobutyl Ketone 

Methyl Isobutyl Ketone 

Isopropyl Alcohol 

Ethyl Acetate 

Ethanol 

Ethanol 

Methyl Alcohol 

Butyl Alcohol (-lert) 

Oioctyl Phthalate 

Methyl Methacrylate 

Oicyclopentadiene 

Jet Naptha 

empty 

Cyclohexane 

Nonylphenol Ethoxylale 

Cumene 

Xylene 

Cyclohexane 

Cumene 

Cyclohexane 

Empty 

Dicyclopentadiene 

Caustic Soda 

Cumene Wash Water 

Empty 

Phenol Wash Water 

Cumene 

Phenol 

Phenol 

Cumene 

2-Ethyl Hexanol 

Empty 

Nonylphenol Ethoxylale 

Isobutyl Alcohol 

Ethyl AcetateNot Used . 

Isopherone • 

Furfural • 

Empty • 

2-Ethyl Hexyl Alcohol 

Cumene 

Xylene ' 

Tank CapacThruput Breathing Losses 

1000 gallon 1000 gallon (Ib/yr) 

Tank CapacThruput 

(T/yr) 

Breathing Losses 

1000 gallon 1000 gallon (Ib/yr) 

5 

5 

5 

5 

5 

5 

5 

5 

409 

409 

533 

123 

122 

207 

411 

650 

1511 

1511 

2047 

208 

933 

409 

708 

121 

121 

817 

410 

410 

612 

612 

207 

122 

411 

204 

387 

410 

410 

410 

411 

410 

762 

762 

0 

5 

46 

1.2 

51 

28 

9 

15 

0 

1477 

422 

417 

0 

1055 

645 

4235 

235 

6920 

56863 

945 

0 

76 

0 

1298 

0 

463 

790 

0 

384 

1559 

212 

0 

0 

0 

476 

0 

381 

230 

0 

1265 

24 

17 

9.44 

9.44 

14.31 

55.19 

24.87 

24.87 

27.7 

15.3 

272.27 

1166.45 

76.09 

285.63 

1573.78 

111.45 

33.73 

26.08 

1063.66 

908.18 

1573.78 

112.91 

0 

7.08 

74.16 

99.13 

29.58 

67.2 

47.24 

6.26 

68.73 

192.53 

437 

205.9 

3.22 

13.58 

13.26 

8.08 

(T/yr) 

0.0047 

0.0047 

0.0072 

0.0276 

0.0124 

0.0124 

0.0139 

0.0077 

0.1361 

0.5832 

0.038 

0.1428 

0 

0.7869 

0.0557 

0.0169 

0.013 

0.5319 

0.4541 

0.7869 

0 

0.0565 

0.0035 

0 

0.0371 

0.0496 

0.0148 

0.0336 

0.0236 

0.0031 

0 

0.0344 

0.0963 

0.2185 

0 

0.103 

0.0016 

0 

0.0068 

0.0066 

0.004 

Working Losses 

(Ib/yr) (T/yr) 

Working Losses 

(Ib/yr) 

0 

2.35 

27.84 

2.58 

51.48 

28.1 

8.35 

9.5 

0 

1299.9 

13.61 

2.93 

2289 

37.46 

16.48 

0.62 

16.17 

7117.8 

2050.1 

0 

0 

24.33 

19.71 

111.28 

0 

16.35 

166.84 

2.09 

0 

0 

2.64 

63.23 

4.24 

12.45 

0.17 

0.13 

(T/yr) 

0 

0.001 

0.014 

0.001 

0.026 

0.014 

0.004 

0.005 

0 

0.65 

0.007 

0.001 

0 

1.145 

0.019 

0.008 

0.000 

0.008 

3.559 

1.025 

0 

0 

0.012 

0 

0.01 

0.056 

0 

0.008 

0.083 

0.001 

0 

0 

0 

0.001 

0 

0.032 

0.002 

0 

0.006 

0.000 

0.000 

Uncontrolled Emis ControEfficiVOC Breathing 

(Ib/yr) (T/yr) (%) (Y/N) (T/yr) 

Uncontrolled Emis ControEfficiVOC Breathing 

(Ib/yr) 

9.44 

11.79 

42.15 

57.77 

76.35 

52.97 

36.05 

24.80 

272.27 

2466.30 

89.70 

288.56 

0.00 

3862.79 

148.91 

50.21 

26.70 

1080.03 

8025.93 

3623.85 

0.00 

112.91 

0.00 

31.41 

0.00 

93.87 

210.41 

29.58 

0.00 

83.55 

214.08 

0.00 

8.35 

0.00 

68.73 

192.53 

439.64 

0.00 

269.13 

7.46 

0.00 

26.03 

13.43 

8.21 

TNKSUM96.WK4 

(T/yr) 

0.0047 None 

0.0059 None 

0.0211 None 

0.0289 None 

0.0382 None 

0.0265 None 

0.0180 None 

0.0124 None 

0.1361 None 

1.2332 Inclne 

0.0449 None 

0.1443 None 

0.0000 None 

1.9314 77? 

0.0745 None 

0.0251 None 

0.0134 None 

0.5400 None 

4.0130 None 

1.8119??? 

0.0000 Incine 

0.0565 None 

0.0157 None 

0.0000 Incine 

0.0469 None 

0.1052 None 

0.0148 None 

0.0418 None 

0.1070 None 

0.0042 None 

0.0000 Incine 

0.0344 None 

0.0963 None 

0.2198 None 

0.0000 None 

0.1346 None 

0.0037 None 

0.0000 None 

0.0130 None 

0.0067 None 

0.0041 None 

(%) (Y/N) (T/yr) 

OY 

OY 

OY 

OY 

OY 

0 Y 

OY 

0 Y 

0 Y 

99 Y 

OY 

0 Y 

ON 

99 Y 

0 Y 

OY 

0 Y 

OY 

OY 

99 Y 

99 N 

OY 

N 

OY 

99 N 

0 Y 

0 Y 

0 Y 

0 Y 

•• 0 Y 

OY 

99 N 

OY 

ON 

0 Y 

ON 

0 Y 

OY 

ON 

0 Y 

0 Y 

0 Y 

0.00472 

0.00472 

0.007155 

0.027595 

0.012435 

0.012435 

0.01385 

0.00765 

0.136135 

0.005832 

0.038045 

0.142815 

0.007869 

0.055725 

0.016865 

0.01304 

0.53193 

0.45409 

0.007869 

0.056455 

0.00354 

0.03708 

0.049565 

0.01479 

0.0336 

0.02362 

0.00313 

0.034365 

0.2185 

0.10295 

0.00161. 

0.00679 

0.00663 

0.00404 

Working HAP Breathing 

(T/yr) (Y/N) (T/yr) 

Working HAP Breathing 

(T/yr) (Y/N) (T/yr) 

OY 

0.001175 Y 

0.01392 N 

0.00129 N 

0.02574 N 

0.01405 N 

0.004175 Y 

0.00475 N 

ON 

0.006499 Y 

0.006805 N 

0.001465 N 

N 

0.011445 N 

0.01873 N 

0.00824 Y 

0.00031 Y 

0.008085 N 

3.558875 Y 

0.01025 N 

N 

0 N 

N 

0.012165 Y 

N 

0.009855 Y 

0.05564 Y 

0 Y 

0.008175 Y 

0.08342 Y 

0.001045 N 

N 

ON 

N 

0.00132 N 

N 

0.031615 N 

0.00212 N 

N 

0.006225 N 

0.000085 Y 

0.000065 Y 

0.00472 

0.00472 

0.01385 

0.005832 

0.016865 

0.01304 

0.45409 

0.00354 

0.03708 

0.049565 

0.01479 

0.0336 

0.02362 

0.00663 

0.00404 

Working 

(T/yr) 

Working 

(T/yr) 

0 

0.001175 

0.004175 

0.006499 

0.00824 

0.00031 

3.558875 

0.012165 

0.009855 

0.05564 

0 

0.008175 

0.08342 

0.000085 

0.000065 

Page 1 05/12/97 cd 

CO 
GATX Terminals Corporation Tank Emissions Summary -1996 

Tank U Type Product(s) 

(H.I.V) 

/ 149 I 

>/ 150 1 

151 1 

152 1 

153 V 

154 V 

155 V 

156 V 

157 V 

158 V 

159 1 

160 1 

161 I 

162 I 

163 1 

164 I 

. 198 V 

r\19 9 v 

^20 0 V 

201 V 

202 V 

203 V 

204 1 

205 V 

206 V 

207 V 

208 V 

209 V 

210 V 

211 V 

212 V 

212 V 

-/'213 1 

214 V 

S 215 1 

sr 216 1 

''216 1 

217 V 

218 V 

219 V 

220 V 

221 V 

222 V 

Xylene 

Trichloroethylene ,. 

Cumene 

Benzene 

Mineral Spirits' 

Mineral Spirits 

Parrafin Wax 

Parrafin Wax 

alpha-Methyl Styrene 

Plasticizer 160 

Acetone 

Acetone 

Acetone 

Acetone 

Acetone 

Cumene 

Phenol 

Neo-Pentyl Glycol Slurry 

Acetic Acid 

Formic Acid 

Propionic Acid 

Aceliv Anhydride 

Cumene 

Methyl Ethyl Ketoxime 

1,2-Dichlorobenzene 

Cumene 

Cumene 

Em.pty 

Nonene 

Cumene 

Cumene 

Cyclohexanone 

Methylene Chloride 

n-Butyl Acetate 

Trichloroethylene 

Trichloroethylene 

Methylene Chloride 

Isooctene 

Nonene 

Nonene 

Nonene 

Heptene 

Heplene 

Tank CapacThruput 

1000 gallon 

384 

387 

773 

768 

411 

411 

818 

815 

411 

410 

798 

798 

798 

798 

798 

798 

301 

300 

301 

301 

207 

207 

1237 

494 

494 

494 

494 

494 

494 

494 

493 

493 

256 

279 

279 

281 

281 

496 

496 

495 

494 

495 

495 

1000 gallon 

0 

47 

3914 

3287 

4186 

233 

3527 

826 

1634 

53 

10576 

10248 

9490 

9505 

7641 

2081 

1767 

574 

1897 

1382 

392 

794 

25903 

256 

536 

676 

1297 

0 

1236 

530 

465 

305 

466 

631 

303 

63 

133 

192 

2538 

3087 

2480 

1529 

1179 

Breathing Losses 

(Ib/yr) 

5.89 

268.06 

37.45 

648.54 

114:28 

89.41 

0.01 

0.01 

80.64 

0 

973.69 

1012.27 

910.45 

1012.27 

2119.44 

13.78 

55.74 

303.19 

469.83 

1114.45 

35.22 

170.55 

40.2 

80.46 

72.81 

52.24-

205.59 

237.18 

52.24 

52.24 

70.08 

3498.28 

259.46 

253.01 

214.02 

367.83 

2334.88 

237.18 

237.18 

237.18 

2331.76 

2331.76 

(T/yr) 

0.0029 

0.134 

0.0187 

0.3243 

0.0571 

0.0447 

5E-06 

5E-06 

0.0403 

0 

0.4868 

0.5061 

0.4552 

0.5061 

1.0597 

0.0069 

0.0279 

0.1516 

0.2349 

0.5572 

0.0176 

0.0853 

0.0201 

0.0402 

0.0364 

0.0261 

0.1028 

*0 

0.1186 

0.0261 

0.0261 

0.035 

1.7491 

0.1297 

0.1265 

0.107 

0.1839 

1.1674 

0.1186 

0.1186 

0.1166 

1.1659 

1.1659 

Working Losses Uncontrolled Emis ControEfficiVOC Breathing 

(Ib/yr) 

0 

0.18 

14.41 

12.43 

345.93 

14.2 

0 

0 

95.13 

0 

36.67 

38.82 

29.29 

35.94 

28.98 

6.42 

75.21 

95.39 

478.62 

817.93 

11.13 

108.44 

83.93 

20.5 

23.87 

88.41 

162.4 

178.37 

69.33 

60.76 

43.69 

4.85 

186.29 

3.66 

0.74 

1.42 

261.64 

366.22 

445.34 

357.84 

2142.1 

1650.8 

(T/yr) (Ib/yr) 

0 5.89 

0.000 268.24 

0.007 51.86 

0.006 660.97 

0.173 460.21 

0.007 103.61 

0 0.01 

0 0.01 

0.048 175.77 

0 0.00 

0.018 1010.36 

0.019 1051.09 

0.015 939.74 

0.018 1048.21 

0.014 2148.42 

0.00 

0.003 20.20 

0.00 

0.038 130.95 

0.048 398.58 

0.239 948.45 

0.409 1932.38 

0.006 46.35 

0.054 278.99 

0.042 124.13 

0.01 100.96 

0.012 96.68 

0.044 140.65 

0.081 367.99 

0 0.00 

0.089 415.55 

0.035 121.57 

0.03 113.00 

0.022. 113.77 

0.002 3503.13 

0.093 445.75 

0.002 256.67 

0.000 214.76 

0.001 369.25 

0.131 2596.52 

0.183 603.40 

0.223 682.52 

0.179 595.02 

1.071 4473.88 

0.825 3982.56 

TNKSUM96.WK4 

(T/yr) 

0.0029 None 

0.1341 None 

0.0259 None 

0.3305 None 

0.2301 None 

0.0518 None 

0.0000 None 

0.0000 None 

0.0879 None 

0.0000 None 

0.5052 None 

0.5255 None 

0.4699 None 

0.5241 None 

1.0742 None 

0.0101 None 

0.0655 None 

0.1993 None 

0.4742 None 

0.9662 None 

0.0232 None 

0.1395 None 

0.0621 None 

0.0505 None 

0.0483 None 

0.0703 None 

0.1840 None 

0.0000 None 

0.2078 None 

0.0608 None 

0.0565 None 

0.0569 None 

1.7516 None 

0.2229 None 

0.1283 None 

0.1074 None 

0.1646 None 

1.2983 None 

0.3017 None 

0.3413 None 

0.2975 None 

2.2369 None 

1.9913 None 

(%) (Y/N) (T/yr) 

0 Y 

ON 

OY 

OY 

0 Y 

0 Y 

OY 

OY 

OY 

OY 

ON 

ON 

ON 

ON 

ON 

•• O Y 

0 Y 

0 Y 

OY 

OY 

OY 

0 Y 

0 Y 

0 Y 

0 Y 

0 Y 

0 Y 

0 N 

0 Y 

0 Y 

0 Y 

0 Y 

0 N 

0 Y 

ON 

ON 

0 N 

0 Y 

0 Y 

0 Y 

0 Y 

0 Y 

0 Y 

0.002945 

0.018725 

0.32427 

0.05714 

0.044705 

5.0E-06 

5.0E-06 

0.04032 

0 

0.00689 

0.02787 

0.151595 

0.234915 

0.557225 

0.01761 

0.085275 

0.0201 

0.04023 

0.036405 

0.02612 

0.102795 

0.11859 

0.02612 

0.02612 

0.03504 

0.12973 

1.16744* 

0.11859 

0.11859 

0.11859 

1.16588 

1.16588 

Working HAP Breathing 

(T/yr) (Y/N) (T/yr) 

0 Y 

Y 

0.007205 Y 

0.006215 Y 

0.172965 N 

0.0071 N 

0 N 

0 N 

0.047565 N 

0 N 

N 

N 

N 

N 

N 

0.00321 Y 

0.037605 Y 

0.047695 N 

0.23931 N 

0.408965 N 

0.005565 N 

0.05422 N 

0.041965 Y 

0.01025 N 

0.011935 N 

0.044205 Y 

0.0812 Y 

N 

0.089185 N 

0.034665 Y 

0.03038 Y 

0.021845 N 

Y 

0.093145 N 

Y 

Y 

Y 

0.13082 N 

0.18311 N 

0.22267 N 

0.17892 N 

1.07106 N 

0.8254 N 

0.002945 

0.13403 

0.018725 

0.32427 

0.00689 

0.02787 

0.0201 

0.02612 

0.102795 

0.02612 

0.02612 

1.74914 

0.126505 

0.10701 

0.183915 

Working 

(T/yr) 

0 

0.00009 

0.007205 

0.006215 

0*00321 

0.037605 

0.041965 

0.044205 

0.0812 

0.034665 

0.03038 

0.002425 

0.00183 

0.00037 

0.00071 

Page 2 05/12/97 cd 
GATX Terminals Corporation Tank Emissions Summary • 1996 

J 

nk # Type Product(s) 

(H.I.V) 

223 I 

224 I 

225 1 

226 1 

227 1 

228 1 

301 1 

302 1 

303 1 

304 1 

305 V 

420 H 

440 V 

450 V 

450 V 

451 V 

460 H 

470 H 

471 H 

481 H 

482 H 

483 H 

484 H 

485 H 

486 H 

487 H 

488 H 

488 H 

Ethyl Acetate 

1,1.1 • Trichloroethane 

Ethanol 

Ethanol 

Ethanol 

Ethanol 

Ethanol 

Empty 

Empty 

Empty 

Acetic Acid 

No. 2 Fuel Oil 

Cyclohexanone 

Methylene Chloride 

Cyclohexane 

Neo-Pentyl Glycol Slurry 

Gasoline (RVP 10) 

Distillate fuel oil No. 2 

Distillate fuel oil No. 2 

Methylene Chloride 

1.1.1 -Trichloroethane 

1.1.1 -Trichloroethane 

Cyclohexane 

Motor Oil 

Empty 

Empty 

Methylene Chloride 

No. 2Fuel Oil 

Tank CapacThruput Breathing Losses 

1000 gallon 1000 gallon (ib/yr) 

458 

452 

454 

454 s 

494 

964 

1050 

3532 

1002 

3835 

301 

20 

32 

30 

30 

30 

12 

10 

2 

28 

28 

28 

28 

28 

28 

28 

28 

28 

737 

5 

2139 

1671 

876 

5067 

0 

0 

0 

0 

1168 

207 

105 

56 

23 

160 

6 

0 

2 

54 

0 

0 

38 

598 

0 

0 

46 

13 

662.72 

1503.34 

50.49 

50.49 

80.71 

80.71 

597.91 

215.12 

2.68 

10.27 

782.34 

62.79 

24.01 

214.21 

1.33 

0.26 

5245.6 

1606.28 

1576.05 

679.89 

1637.98 

4702.45 

0.43 

(T/yr) 

0.3314 

0.7517 

0.0252 

0.0252 

0.0404 

0.0404 

0.299 

0 

0 

0 

0.1076 

0.0013 

0.0051 

0.3912 

0.0314 

0.012 

0.1071 

0.0007 

0.0001 

2.6228 

0.8031 

0.788 

0.3399 

0.819 

0 

0 

2.3512 

0.0002 

Working Losses 

(Ib/yr) 

4.16 

0 

10.25 

8.01 

4.35 

24.62 

0 

243.86 

3.62 

11.61 

728.58 

46.12 

23.95 

42.27 

0 

0.03 

560.4 

0 

0 

82.3 

3089.4 

501.9 

0.19 

(T/yr) 

0.002 

0 

0.005 

0.004 

0.002 

0.012 

0 

0 

0 

0 

0.122 

0.002 

0.006 

0.364 

0.023 

0.012 

0.021 

0 

0.000 

0.28 

0 

0 

0.041 

1.545 

0 

0 

0.251 

0.000 

Uncontrolled Emis ControEfficiVOC Breathing 

(Ib/yr) 

666.88 

1503.34 

0.00 

60.74 

58.50 

85.06 

105.33 

597.91 

0.00 

0.00 

0.00 

458.98 

6.30 

21.88 

1510.92 

108.91 

47.96 

256.48 

1.33 

0.29 

5806.00 

1606.28 

1576.05 

762.19 

4727.33 

0.00 

0.00 

5204.35 

0.62 

(T/yr) 

0.3334 None 

0.7517 None 

0.0304 None 

0.0293 None 

0.0425 None 

0.0527 None 

0.2990 None 

0.0000 None 

0.0000 None 

0.0000 None 

0.2295 None 

0.0032 None 

0.0109 None 

0.7555 None 

0.0545 None 

0.0240 None 

0.1282 None 

0.0007 None 

0.0001 None 

2.9030 None 

0.8031 None 

0.7880 None 

0.3811 None 

2.3637 None 

0.0000 None 

0.0000 None 

2.6022 None 

0.0003 None 

(%) (Y/N)(T/yr) 

0 Y 

ON 

0 Y 

0 Y 

0 Y 

OY 

OY 

ON 

ON 

0 N 

0 Y 

0 Y 

0 Y 

ON 

0 Y 

0 Y 

0 Y 

0 Y 

OY 

0 N 

ON 

ON 

0 Y 

0 Y 

ON 

OY 

ON 

OY 

0.33136 

0.025245 

0.025245 

0.040355 

0.040355 

0.298955 

0.10756 

0.00134 

0.005135 

0.031395 

0.012005 

0.107105 

0.000665 

0.00013 

0.339945 

0.81899 

0 

0.000215 

10.27 

Working HAP Breathing 

(T/yr) (Y/N) (T/yr) 

0.00208 N 

Y 

0.005125 N 

0.004005 N 

0.002175 N 

0.01231 N 

0 N 

N 

N 

N 

0.12193 N 

0.00181 N 

0.005805 N 

Y 

0.02306 N 

0.011975 N 

0.021135 N 

0 N 

0.000015 N 

Y 

Y 

Y 

0.04115 N 

1.544675 N 

Y 

0 N 

Y 

0.000095 Pk 

9.81 \ 

0.75167 

0.39117 

2.6228 

0.80314 

0.788025 

0 

2.351225 

11.28 

Working 

(T/yr) 

0 

0.36429 

0.2802 

0 

0 

0 

0.25095 

4.94 

TNKSUM96.WK4 Page 3 05/12/97 cdc 
•GATX Terminals Corporation Fugitive Emissions • 1996 

TANK PRODNAME V IN 

51 BP RUB.SOLV. T 0 

NETGALPUMPI TIME IN S FUGITIVE COM EMISSION FACTORS ANNUAL VOC VOC Emissions HAP HAP Emissions 

gpm HOURS PUMVAL FLAN PUMPSVALVE FLANG EMISSIONS (Y/N) (Y/N) 

(LB/HR (LB/HR (LB/HR (lb/year) (T/yr) (lb/year) (T/yr) (lb/year) (T/yr) 

157.0 200 0.01 1 18 35 0.109 0.016 0.002 0.006018 3.0E-06 Y 0.006018 3.0E-06 Y 0.006 3.0E-06 

U 

52 BPSPARE/MIBK 

52 BPSPARE/MIBK 

53 BPISOPROPYL 

53 BPISOPROPYL 

54 BP ETHYL ACE 

54 BP ETHYL ACE 

55 

55 

55 

56 

56 

56 

T 

T 

T 

T 

T 

T 

BRUCINEC 

BRUCINET 

BRUCINET 

BITREX C 

BITREXT 

BITREX T 

57 METHANOL T 

57 METHANOLT 

58 

58 

104 DOP 

105 METHYL 

105 METHYL 

105 METHYL 

106 DCPD 

106 DCPD 

106 DCPD 

106 DCPD 

107 AV GAS 

107 AV GAS 

TBA MIXT 

TBA MIXT 

METH 

METH 

METH 

121 CYCLOHEXANE 

121 CYCLOHEXANE 

122 ULTRA 95 

122 ULTRA 95 

123 CUMENE 

123 CUMENE 

123 CUMENE 

T 

s 

T 

T 

T 

c 

c 

s 

T 

T 

s 

c 

s 

T 

B 

B 

s 

1 

0 

0 

1 

0 

1 

0 

0 

1 

0 

0 

1 

1 

0 

0 

1 

0 

1 

1 

0 

0 

1 

0 

1 

0 

1 

1 

0 

1 

0 

0 

1 

1 

4025.0 

2248.0 

33903.0 

34779.0 

461.0 

918.0 

16799.0 

21874.0 

348.0 

8923.0 

10106.0 

46.0 

6490.0 

5861.0 

758.0 

7824.0 

113999.0 

1099121.0 

8480.0 

1199309.0 

2294.0 

47867.0 

464555.0 

268872.0 

234533.0 

312904.0 

622343.0 

789919.0 

483544.0 

495483.0 

1972722.0 

463983.0 

2712516.0 

200 

• 200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

1750 

200 

200 

200 

200 

200 

1750 

200 

200 

1750 

200 

1750 

200 

1400 

1400 

1750 

0.34 

0.19 

2.83 

2.90 

0.04 

0.08 

1.40 

1.82 

0.03 

0.74 

0.84 

0.00 

0.54 

0.49 

0.06 

0.65 

9.50 

10.47 1 

0.71 1 

99.94 1 

0.19 1 

3.99 1 

38.71 1 

2.56 1 

19.54 1 

26.08 1 

5.93 1 

65.83 2 

4.61 1 

41.29 1 

23.48 1 

5.52 1 

25.83 1 

1 18 

1 18 

1 18 

1 18 

1 18 

1 18 

1 37 

1 37 

1 37 

1 37 

1 37 

1 37 

1 70 

70 

17 

17 

2 

14 

2 

2 

2 

3 

3 

14 

4 

4 

18 

14 

12 

4 

18 

18 

18 

35 

35 

35 

35 

35 

35 

74 

74 

74 

74 

74 

74 

139 

139 

35 

35 

17 

24 

17 

17 

17 

16 

16 

24 

5 

5 

22 

26 

20 

15 

24 

24 

24 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

FUGITV96.WK1 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.154292 

0.086173 

1.299615 

1.333195 

0.017672 

0.03519 

1.16781 

1.520608 

0.024192 

0.620297 

0.702535 

0.003198 

0.800001 

0.722466 

0.028046 

0.289488 

1.630186 

3.937994 

0.121264 

17.15012 

0.032804 

0.741141 

7.19286 

0.96333 

3.557084 

4.745711 

2.587761 

32.17603 

1.551946 

8.25805 

10.338 

2.431492 

11.3719 

0.000077 Y 

0.000043 Y 

0.00065 Y 

0.000667 Y 

8.8E-06 Y 

0.000018 Y 

0.000584 Y 

0.00076 Y 

0.000012 Y 

0.00031 Y 

0.000351 Y 

1.6E-06 Y 

0.0004 Y 

0.000361 Y 

0.000014 Y 

0.000145 Y 

0.000815 Y 

0.001969 Y 

0.000061 Y 

0.008575 Y 

0.000016 Y 

0.000371 Y 

.0.003596 Y 

0.000482 Y 

0.001779 Y 

0.002373 Y 

0.001294 Y 

0.016088 Y 

0.000776 Y 

0.004129 Y 

0.005169 Y 

0.001216 Y 

0.005686 Y 

0.154292 

0.086173 

1.299615 

1.333195 

0.017672 

0.03519 

1.16781 

1.520608 

0.024192 

0.620297 

0.702535 

0.003198 

0.800001 

0.722466 

0.028046 

0.289488 

1.630186 

3.937994 

0.121264 

17.15012 

0.032804 

0.741141 

7.19286 

0.96333 

3.557084 

4.745711 

2.587761 

32.17603 

1.551946 

8.25805 

10.338 

2.431492 

11.3719 

0.000077 Y 

0.000043 Y 

0.00065 N 

0.000667 N 

8.8E-06 N 

0.000018 N 

0.000584 N 

0.00076 N 

0.000012 N 

0.00031 N 

0.000351 N 

1.6E-06 N 

0.0004 Y 

0.000361 Y 

0.000014 N 

0.000145 N 

0.000815 N 

0.001969 Y 

0.000061 Y 

0.008575 Y 

0.000016 N 

0.000371 N 

0.003596 N 

0.000482 N 

0.001779 N 

0.002373 N 

0.001294 N 

0.016086 N 

0.000776 N 

0.004129 N 

0.005169 Y 

0.001216 Y 

0.005686 Y 

0.1543 

0.0862 

0.8 

0.7225 

3.938 

0.1213 

17.15 

10.338 

2.4315 

11.372 

0.000077 

0.000043 

0.0004 

0.000361 

0.001969 

0.000061 

0.008575 

0.005169 

0.001216 

0.005686 

Page 1 05/12/97 cd 

to 
GATX Terminals Corporation Fugitive Emissions • 1996 

TANK PRODNAME V IN 

124 CYCLOHEXANE B 1 

124 CYCLOHEXANE s 1 

124 CYCLOHEXANE C 1 

124 CYCLOHEXANE C 0 

124 CYCLOHEXANE T 0 

124 XYLENE s 0 

124 XYLENE T 0 

124 XYLENE T 1 

125 CUMENE B 1 

125 CUMENE B 0 

125 CUMENE s 1 

126 CYCLOHEXANE S 1 

126 CYCLOHEXANE C 0 

128 OCPO S 1 

128 DCPD T 0 

-4^130 WASH WATER s 1 

130 WASH WATER T 0 

133 PHENOL B 0 

133 PHENOL B 1 

134 CUMENE B 0 

134 CUMENE s 1 

134 PHENOL B 0 

135 CUMENE B 0 

135 CUMENE s 1 

135 PHENOL B 1 

135 PHENOL B 0 

135 PHENOL s 0 

137 2-EHA T 0 

137 2-EHA S 1 

141 ULTRA 60 T 0 

142 HULS-ISOBUT. T 0 

143 VINYUETHY;L ACEl 1 

143 VINYL7ETHY;L ACET 0 

NETGALPUMPI TIME IN SFUGITIVE COM EMISSION FACTORS ANNUAL 

gpm HOURS PUMVAL FLAN PUMPSVALVE FLANG EMISSIONS 

(LB/HR (LB/HR (LB/HR (lb/year) (T/yr) 

VOC VOC Emissions 

(Y/N) 

(lb/year) (T/yr) 

HAP HAP Emissions 

(Y/N) 

(lb/year) (T/yr) 

667222.0 

4349552.0 

170711.0 

4853505.0 

10488.0 

1485734.0 

6580.0 

25721.0 

564875.0 

709463.0 

57104.0 

184656.0 

963791.0 

967134.0 

293347.0 

347297.0 

314727.0 

789883.0 

543806.0 

1169263.0 

288043.0 

274146.0 

31263.0 

137483.0 

158981.0 

118200.0 

189494.0 

255919.0 

1260 

1750 

200 

200 

200 

1240 

200 

200 

1093711.0 1750 

40913353.0 1400 

38020168.0 1750 

1750 

200 

1750 

200 

1750 

200 

700 

1750 

1400 

1750 

23364.0 700 

1400 

1750 

1750 

700 

700 

200 

1750 

6556.0 200 

200 

200 

200 

8.83 

41.42 

14.23 

404.46 

0.87 

19.97 

0.55 

2.14 

10.42 

487.06 

362.10 

5.38 

59.12 

0.54 

15.39 

9.18 

80.59 

6.98 

3.31 

3.75 

7.52 

0.56 

6.47 

11.14 

2.74 

6.53 

0.74 

11.46 

1.51 

0.55 

9.85 

15.79 

21.33 

13 

18 

13 

13 

13 

13 

13 

13 

15 

15 

15 

12 

0 

12 

0 

12 

0 

20 

20 

10 

10 

If 

11 

11 

11 

11 

5 

11 

22 

24 

22 

22 

22 

0.109 

0.109 

0.109 

0.109 

0.109 

22 0.109 

22 0.109 

22 0.109 

24 0.109 

24 0.109 

24 0.109 

27 

14 

27 

14 

27 

14 

25 

25 

26 

26 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

3.14724 

18.23498 

5.072962 

144.23 

0.311668 

7.121139 

0.195536 

0.764342 

4.085271 

191.0264 

142.0144 

1.880765 

7.934161 

0.190129 

2.06507 

3.208965 

10.81578 

3.31063 

1.567798 

1.183224 

2.375667 

0.001574 Y 

0.009117 Y 

0.002536 Y 

0.072115 Y 

0.000156 Y 

0.003561 Y 

0.000098 Y 

0.000382 Y 

0.002043 Y 

0.095513 Y 

0.071007 Y 

0.00094 Y 

0.003967 Y 

0.000095 Y 

0.001033 Y 

0.001604 Y 

0.005408 Y 

0.001655 Y 

0.000784 Y 

0.000592 Y 

0.001188 Y 

10 26 0.109 0.016 0.002 0.175675 0.000088 Y 

24 

24 

24 

24 

24 

6 

24 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

2.124728 

3.654782 

0.90034 

2.142255 

0.244298 

2.289092 

0.496929 

0.001062 Y 

0.001827 Y 

0.00045 Y 

0.001071 Y 

0.000122 Y 

0.001145 Y 

0.000248 Y 

15 0.109 0.016 0.002 0.091784 0.000046 Y 

15 0.109 

15 0.109 

15 0.109 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

1.97 

3.158233 

4.265317 

0.000985 Y 

0.001579 Y 

0.002133 Y 

3.14724 

18.23498 

5.072962 

144.23 

0.311668 

0.001574 N 

0.009117 N 

0.002536 N 

0.072115 N 

0.000156 N 

7.121139 0.003561 Y 

0.195536 0.000098 Y 

0.764342 0.000382 Y 

4.085271 0.002043 Y 

191.0264 0.095513 Y 

142.0144 0.071007 Y 

1.880765 

7.934161 

0.190129 

2.06507 

3.208965 

10.81578 

3.31063 

1.567798 

1.183224 

2.375667 

0.00094 N 

0.003967 N 

0.000095 N 

0.001033 N 

0.001604 N 

0.005408 N 

0.001655 Y 

0.000784 Y 

0.000592 Y 

0.001188 Y 

0.175675 0.000088 Y 

2.124728 

3.654782 

0.90034 

2.142255 

0.244298 

2.289092 

0.496929 

0.001062 Y 

0.001827 Y 

0.00045 Y 

0.001071 Y 

0.000122 Y 

0.001145 N 

0.000248 N 

0.091784 0.000046 N 

1.97 

3.158233 

4.265317 

0.000985 N 

0.001579 Y 

0.002133 Y 

7.1211 0.003561 

0.1955 0.000098 

0.7643 0.000382 

4.0853 0.002043 

191.03 0.095513 

142.01 0.071007 

3.3106 

1.5678 

1.1832 

2.3757 

0.001655 

0.000784 

0.000592 

0.001188 

0.1757 0.000088 

2.1247 

3.6548 

0.001062 

0.001827 

0.9003 0.00045 

2.1423 0.001071 

0.2443 0.000122 

3.1582 

4.2653 

0.001579 

0.002133 

FUGITV96.WK1 Page 2 05/12/97 cdc 
GATX Terminals Corporation Fugitive Emissions • 1996 

TANK PRODNAME V IN NETGALPUMPI TIME INS FUGITIVE COM EMISSION FACTORS ANNUAL VOC VOC Emissions 

145 ISOPHO/FURFUR S 1 

145 ISOPHO/FURFUR T 0 

145 ISOPHO/FURFUR C 1 

145 ISOPHO/FURFUR C 0 

147 X-ALCOHOL T 0 

147 X-ALCOHOL S 1 

148 XYLENE S 1 

148 XYLENE B 0 

148 XYLENE T 0 

149 XYLENE/149 T 0 

•' 150 ACI-TCE T 0 

v^' 150 ACI-TCE T 1 

151 CUMENE T 0 

151 CUMENE S 1 

152 BENZENE B 1 

/•w 152 BENZENE C 1 

^ 152 BENZENE S 1 

152 BENZENE T 1 

152 BENZENE T 0 

153 SUN SPIRITS C 1 

153 SUN SPIRITS T 0 

154 SPIRITS 66 C 1 

154 SPIRITS 66 TO 

155 SLACKWAX C 0 

155 SLACKWAX S 1 

155 SLACKWAX T 0 

156 WAX 156 C 0 

156 WAX 156 S 1 

156 WAX 156 T 0 

157 AMS C 1 

157 AMS C 0 

157 AMS S 0 

157 AMS T 1 

157 AMS T 0 

158 PLASTIC 160 T O 

158 PLASTIC 160 T 1 

418697.0 

318075.0 

40046.0 

60368.0 

889565.0 

948393.0 

gpm HOURS PUM VAL FLAN PUMPSVALVE FLANG EMISSIONS (Y/N) 

(LB/HR (LB/HR (LB/HR (lb/year) (T/yr) 

4 15 0.109 0.016 0.002 0.797518 0.000399 Y 

4 15 0.109 0.016 0.002 5.30125 0.002651 Y 

4 15 0.109 0.016 0.002 0.667433 0.000334 Y 

4 15 0.109 0.016 0.002 1.006133 0.000503 Y 

78961.0 

35412.0 

1589224.0 

2923249.0 

418867.0 

1450341.0 

428029.0 

168385.0 

2669977.0 

3139807.0 

2953280.0 

174552.0 

268487.0 

672969.0 

2645548.0 

1487562.0 

84895.0 

619853.0 

616803.0 

75284.0 

40381.0 

1180020.0 

1150309.0 

113786.0 

38465.0 

39804.0 

1750 

200 

200 

200 

200 

1750 

1458509.0 1750 

16422.0 200 

556.0 200 

722.0 200 

200 

200 

200 

1750 

1750 

200 

1750 

200 

200 

200 

200 

200 

200 

200 

1750 

200 

200 

1750 

200 

200 

200 

1240 

200 

200 

200 

200 

3.99 

26.51 

3.34 

5.03 

74.13 

9.03 

13.89 

1.37 

0.05 

0.06 

6.58 

2.95 

132.44 

27.84 

3.99 

120.86 

4.08 

14.03 

222.50 

261.65 

246.11 

14.55 

22.37 

56.08 

25.20 

123.96 

7.07 

5.90 

51.40 

6.27 

3.37 

15.86 

95.86 

9.48 

3.21 

3.32 

4 

4 

4 

12 

12 

3 

12 

3 

3 

4 

4 

4 

4 

*» 

5 

11 

5 

5 

11 

5 

5 

5 

11 

5 

5 

12 

12 

15 

15 

15 

26 

95 

15 

95 

15 

15 

15 

15 

15 

15 

15 

15 

18 

15 

15 

30 

30 

0.109 

0.109 

0.016 0.002 

0.016 0.002 

15 0.109 

15 0.109 

15 0.109 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

14.82608 

1.806463 

2.778112 

0.2737 

0.009267 

0.007413 Y 

0.000903 Y 

0.001389 Y 

0.000137 Y 

4.6E-06 Y 

15 0.109 0.016 0.002 0.012033 6.0E-06 Y 

15 0.109 0.016 0.002 

15 0.109 0.016 0.002 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

15 0.109 

14 0.109 

15 0.109 

15 0.109 

14 0.109 

15 0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

Q.002 

0.002 

1.316017 

0.5902 

26.48707 

9.682914 

1.882907 

22.23856 

1.924092 

2.581903 

40.93965 

52.33012 

49.22133 

2.9092 

4.474783 

0.000658 N 

0.000295 N 

0.013244 Y 

0.004841 Y 

0.000941 Y 

0.011119 Y 

0.000962 Y 

0.001291 Y 

0.02047 Y 

0,026165 Y 

0.024611 Y 

0.001455 Y 

0.002237 Y 

12.11344 0.006057 Y 

7.815705 0.003908 Y 

26.77612 0.013388 Y 

1.52811 0.000764 Y 

1.831223 0.000916 Y 

11.10245 0.005551 Y 

1.355112 

0.726858 

5.034118 

20.70556 

2.048148 

1.137923 

1.177535 

0.000678 Y 

0.000363 Y 

0.002517 Y 

0.010353 Y 

0.001024 Y 

0.000569 Y 

0.000589 Y 

(lb/year) (T/yr) 

0.797518 0.000399 N 

5.30125 0.002651 N 

0.667433 0.000334 N 

1.006133 0.000503 N 

HAP HAP Emissions 

(Y/N) 

(lb/year) (T/yr) 

14.82608 

1.806463 

2.778112 

0.2737 

0.009267 

0.007413 N 

0.000903 N 

0.001389 Y 

0.000137 Y 

4.6E-06 Y 

0.012033 6.0E-06 Y 

Y 

Y 

26.48707 

9.682914 

1.882907 

22.23856 

1.924092 

2.581903 

40.93965 

52.33012 

49.22133 

2.9092 

4.474783 

12.11344 

7.815705 

26.77612 

1.52811 

1.831223 

11.10245 

1.355112 

0.726858 

5.034118 

20.70556 

2.048148 

1.137923 

1.177535 

0.013244 Y 

0.004841 Y 

0.000941 Y 

0.011119 Y 

0.000962 Y 

0.001291 Y 

0.02047 Y 

0.026165 N 

0.024611 N 

0.001455 N 

0.002237 N 

0.006057 N 

0.003908 N 

0.013388 N 

0.000764 N 

0.000916 N 

0.005551 N 

0.000678 N 

0.000363 N 

0.002517 N 

0.010353 N 

0.001024 N 

0.000569 N 

0.000589 N 

2.7781 0.001389 

0.2737 0.000137 

0.0093 4.6E-06 

0.012 6.0E-06 

1.316 

0.5902 

26.487 

9.6829 

1.8829 

22.239 

1.9241 

2.5819 

40.94 

0.000658 

0.000295 

0.013244 

0.004841 

0.000941 

0.011119 

0.000962 

0.001291 

0.02047 

FUGITV96.WK1 Page 3 05/12/97 cdc 
GATX Terminals Corporation Fugitive Emissions • 1996 

TANK PRODNAME 

164 CUMENE 

164 CUMENE 

201 FORMIC 

201 FORMIC 

201 FORMIC 

TcT 202 PROPIONIC 

O 202 PROPIONIC 

202 PROPIONIC 

204 CUMENE 

204 CUMENE 

205 MEKO 

205 MEKO 

205 MEKO 

205 MEKO 

V IN 

S 0 

B 0 

198 SYN. PHENOL C 0 

198 SYN. PHENOL C 1 

198 SYN. PHENOL S 0 

198 SYN. PHENOL T 1 

199 NEOL/HOECHST S 1 

199 NEOL/HOECHST T 0 

199 NEOL/HOECHST C 0 

199 NEOL/HOECHST T 1 

200 ACETIC ACID C 0 

200 ACETIC ACID S 1 

200 ACETIC ACID T 0 

C 0 

S 1 

T 0 

C 1 

S 1 

T 0 

203 ACEANHYDRIDE C 1 

203 ACEANHYDRIDE S 1 

203 ACEANHYDRIDE T 0 

B 0 

S 1 

C 

C 

T 

T 

NETGALPUMPI TIME INS FUGITIVE COM EMISSION FACTORS ANNUAL 

gpm HOURS PUMVAL FLAN PUMPS VALVE FLANG EMISSIONS 

(LB/HR (LB/HR (LB/HR (lb/year) (T/yr) 

1560413.0 

673238.0 

2030 

1400 

4607.0^ 200 

57339.0 200 

1212276.0 700 

1267705.0 200 

425748.0 1750 

379072.0 200 

75693.0 200 

4931.0 200 

41243.0 

1422478.0 

1341702.0 

187792.0 

106149.0 

297849.0 

450343.0 

144937.0 

656171.0 

18442826.0 

19379816.0 

39177.0 

62788.0 

215208.0 

192938.0 

200 

1750 

200 

277176.0 200 

1036740.0 1750 

789327.0 200 

200 

1750 

200 

200 

1750 

200 

1400 

1750 

200 

200 

200 

200 

12.81 

8.01 

0.38 

4.78 

28.86 

105.64 

4.05 

31.59 

6.31 

0.41 

3.44 

13.55 

111.81 

23.10 

9.87 

65.78 

15.65 

1.01 

24.82 

37.53 

1.38 

54.68 

219.56 

184.57 

3.26 

5.23 

17.93 

16.08 

14 

14 

4 

4 

7 

12 

11 

4 

4 

4 

9 

12 

9 

9 

12 

9 

12 

9 

14 

14 

18 

18 

18 

18 

41 

41 

0.109 

0.109 

15 0.109 

15 0.109 

10 0.109 

33 0.109 

25 0.109 

15 0.109 

15 0.109 

15 0.109 

19 0.109 

19 0.109 

19 0.109 

19. 0.109 

19 0.109 

19 0.109 

9 19 0.109 

12 19 0.109 

9 19 0.109 

19 0.109 

19 0.109 

19 0.109 

22 

22 

0.109 

0.109 

23 0.109 

23 0.109 

23 0.109 

23 0.109 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

5.211626 

3.260395 

0.076783 

0.95565 

6.898428 

38.07341 

1.338065 

6.317867 

1.26155 

0.082183 

0.987082 

4.541092 

32.1?14 

6.633746 

3.309669 

18.89123 

4.494489 

0.338868 

7.128519 

10.77821 

0.462694 

15.70436 

81.80711 

68.77066 

1.431266 

2.293855 

7.862266 

7.048668 

V O C VO C Emissions HAP HAP Emissions 

(Y/N) (Y/N) 

(lb/year) (T/yr) (lb/year) (T/yr) 

0.002606 Y 5.211626 0.002606 Y 5.2116 0.002606 

0;00163 Y 3.260395 0.00163 Y 3.2604 0.00163 

0.000038 Y 

0.000478 Y 

0.003449 Y 

0.019037 Y 

0.000669 Y 

0.003159 Y 

0.000631 Y 

0.000041 Y 

0.000494 Y 

0.002271 Y 

0.016056 Y 

0.003317 Y 

0.001655 Y 

0.009446 Y 

0.002247 Y 

0.000169 Y 

0.003564 Y 

0.005389 Y 

0.000231 Y 

0.007852 Y 

0.040904 Y 

0.034385 Y 

0.000716 Y 

0.001147 Y 

0.003931 Y 

0.003524 Y 

0.076783 0.000038 Y 

0.95565 0.000478 Y 

6.898428 0.003449 Y 

38.07341 0.019037 Y 

1.338065 0.000669 N 

6.317867 0.003159 N 

1.26155 0.000631 N 

0.082183 0.000041 N 

0.987082 

4.541092 

32.1114 

6.633746 

3.309669 

18.89123 

0.000494 N 

0.002271 N 

0.016056 N 

0.003317 N 

0.001655 N 

0.009446 N 

4.494489 0.002247 N 

0.338868 0.000169 N 

7.128519 0.003564 N 

10.77821 0.005389 N 

0.462694 0.000231 N 

15.70436 0.007852 N 

81.80711 

68.77066 

1.431266 

2.293855 

7.862266 

7.048668 

0.040904 Y 

0.034385 Y 

0.000716 N 

0.001147 N 

0.003931 N 

0.003524 N 

0.0768 0.000038 

0.9557 0.000478 

6.8984 0.003449 

38.073 0.019037 

81.807 

68.771 

0.040904 

0.034385 

206 ODCB 

206 ODCB 

206 ODCB 

456234.0 

401641.0 

32776.0 

1240 

200 

200 

6.13 

33.47 

2.73 

1 14 

2 18 

2 18 

29 

20 

20 

0.109 

0.109 

0.109 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

2.362115 

18.14079 

1.480383 

0.001181 Y 

0.00907 Y 

0.00074 Y 

2.362115 0.001181 N 

18.14079 0.00907 N 

1.480383 0.00074 N 

207 CUMENE 

207 CUMENE 

207 CUMENE 

207 CUMENE 

208 CUMENE 

208 CUMENE 

S 

T 

B 

S 

B 

S 

484631.0 

191485.0 

484398.0 

169041.0 

485949.0 

973042.0 

1750 

200 

1400 

1240 

1400 

1750 

4.62 

15.96 

5.77 

2.27 

5.79 

9.27 

14 

18 

14 

14 

14 

14 

29 

37 

22 

29 

29 

29 

0.109 

0.109 

0.109 

0.109 

0.109 

0.109 

0.016 

0.016 

0.016 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

1.777903 

7.397704 

2.148651 

0.875196 

2.228423 

3.569674 

0.000889 Y 

0.003699 Y 

0.001074 Y 

0.000438 Y 

0.001114 Y 

0.001785 Y 

1.777903 

7.397704 

2.148651 

0.875196 

2.228423 

3.569674 

0.000889 Y 

0.003699 Y 

0.001074 Y 

0.000438 Y 

0.001114 Y 

0.001785 Y 

1.7779 

7.3977 

2.1487 

0.8752 

2.2284 

3.5697 

0.000889 

0.003699 

0.001074 

0.000438 

0.001114 

0.001785 

FUGITV96.WK1 Page 4 05/12/97 cdc 

Tl 
GATX Terminals Corporation Fugitive Emissions • 1996 ~l 

TANK 

21C 

210 

211 

211 

211 

211 

PRODNAME 

NONENE 

NONENE 

CUMENE 

CUMENE 

CUMENE 

CUMENE 

212 CUMENE 

212 CUMENE 

212 CYCLOHEXANE 

212 CYCLOHEXANE 

212 CYCLOHEXANE 

/ 213 

/ 213 

214 

214 

214 

J

 215 

• 215 

M. CHLORIDE 

M. CHLORIDE 

N-B ACETATE 

N-B ACETATE 

N-B ACETATE 

PETRO-TCE 

PETRO-TCE 

V 

C 

T 

B 

S 

S 

T 

B 

T 

T 

T 

C 

S 

T 

S 

T 

T 

S 

T 

216 METHYLENE CHLO S 

' 216 METHYLENE CHLO T 

/ 216 TCE T 

V

1 7 

218 

218 

219 

219 

220 

220 

221 

221 

222 

222 

223 

223 

ISO-OCTENE 

TEX NONENE 

TEX NONENE 

TEX NONENE 

TEX NONENE 

TEX NONENE 

TEX NONENE 

TEX HEPTENE 

TEX HEPTENE 

TEX HEPTENE 

TEX HEPTENE 

ETHYL ACETAT 

ETHYL ACETAT 

T 

S 

T 

S 

T 

S 

T 

S 

T 

S 

T 

S 

T 

IN 

1 

0 

0 

0 

1 

1 

0 

1 

1 

0 

1 

1 

0 

1 

1 

0 

1 

0 

1 

0 

0 

1 

0 

1 

0 

1 

0 

1 

0 

1 

0 

1 

1 

0 

NETGALPUMPI TIME IN S FUGITIVE COM EMISSION FACTORS ANNUAL VOC VOC Emissions HAP HAP Emissions 

gpm HOURS PUM VAL FLAN PUMPSVALVE FLANG EMISSIONS (Y/N) (Y/N) 

(LB/HR (LB/HR (LB/HR (lb/year) (T/yr) (lb/year) (T/yr) (lb/year) (T/yr) 

927209.0 200 77.27 1 18 5 0.109 0.016 0.002 31.37057 0.015685 Y 31.37057 0.015685 N 

721091.0 200 60.09 1 18 5 0.109 0.016 0.002 24.39691 0.012198 Y 24.39691 0.012198 N 

67901.0 

446054.0 

67916.0 

462285.0 

447087.0 

464674.0 

286175.0 

304235.0 

19308.0 

335633.0 

160478.0 

473166.0 

452.0 

474841.0 

183524.0 

88914.0 

98920.0 

66978.0 

49851.0 

144170.0 

1884754.0 

1903713.0 

2054092.0 

2314985.0 

1573312.0 

1860134.0 

844234.0 

1147061.0 

714892.0 

683968.0 

552666.0 

492945.0 

s 1400 

1240 

1750 

200 

1400 

200 

200 

200 

200 

1750 

200 

1750 

200 

200 

1750 

200 

1750 

200 

200 

200 

1240 

200 

1240 

200 

1240 

200 

1240 

200 

1240 

200 

1750 

200 

0.81 

6.00 

0.65 

38.52 

5.32 

38.72 

23.85 

25.35 

1.61 

3.20 

15.04 

4.51 

0.04 

39.57 

1.75 

7.41 

0.94 

5.58 

4.15 

12.01 

25.33r 

158.64 

27.61 

192.92 

21.15 

155.01 

11.35 

95.59 

9.61 

73.66 

5.26 

41.08 

1 14 

1 14 

1 14 

1 18 

1 14 

1 18 

1 18 

1 18 

1 18 

1 13 

1 12 

1 14 

1 18 

1 18 

1 14 

1 18 

1 14 

2 18 

2 18 

1 12 

1 13 

2 12 

1 13 

1 12 

1 13 

1 12 

1 14 

2 12 

1 14 

1 12 

1 13 

1 12 

29 

29 

29 

37 

29 

37 

37 

37 

5 

23 

7 

29 

5 

5 

29 

5 

29 

5 

5 

12 

24 

12 

23 

12 

24 

12 

26 

12 

24 

12 

23 

7 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 . 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.109 0.016 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.002 

0.311375 

2.309409 

0.249155 

17.85961 

2.050213 

17.95191 

11.05589 

11.75361 

0.653254 

1.145627 

4.716492 

1.735843 

0.015293 

16.06545 

0.673271 

3.008257 

0.362895 

2.874473 

2.139439 

3.87577 

9.124844 

68.47021 

9.894981 

62.23451 

7.617029 

50.0066 

4.309678 

41.25596 

3.614817 

23.76401 

1.886433 

12.8823 

0.000156 Y 

0.001155 Y 

0.000125 Y 

0.00893 Y 

0.001025 Y 

0.008976 Y 

0.005528 Y 

0.005877 Y 

0.000327 Y 

0.000573 N 

0.002358 N 

0.000868 Y 

7.6E-06 Y 

0.008033 Y 

0.000337 N 

0.001504 N 

0.000181 N 

0.001437 N 

0.00107 N 

0.001938 Y 

0.004562 Y 

6.034235 Y 

0.004947 Y 

0.031117 Y 

0.003809 Y 

0.025003 Y 

0.002155 Y 

0.020628 Y 

0.001807 Y 

0.011882 Y 

0.000943 Y 

0.006441 Y 

0.311375 

2.309409 

0.249155 

17.85961 

2.050213 

17.95191 

11.05589 

11.75361 

0.653254 

1.735843 

0.015293 

16.06545 

3.87577 

9.124844 

66.47021 

9.894981 

62.23451 

7.617029 

50.0066 

4.309678 

41.25596 

3.614817 

23.76401 

1.686433 

12.8823 

0.000156 Y 

0.001155 Y 

0.000125 Y 

0.00893 Y 

0.001025 Y 

0.008976 Y 

0.005528 N 

0.005877 N 

0.000327 N 

Y 

Y 

0.000868 N 

7.6E-06 N 

0.008033 N 

Y 

Y 

Y 

Y 

Y 

0.001938 N 

0.004562 N 

0.034235 N 

0.004947 N 

0.031117 N 

0.003809 N 

0.025003 N 

0.002155 N 

0.020628 N 

0.001807 N 

0.011882 N 

O.00O943 N 

0.006441 N 

0.3114 

2.3094 

0.2492 

17.86 

2.0502 

17.952 

1.1456 

4.7165 

0.6733 

3.0083 

0.3629 

2.8745 

2.1394 

0.000156 

0.001155 

0.000125 

0.00893 

0.001025 

0.008976 

0.000573 

0.002358 

0.000337 

0.001504 

0.000181 

0.001437 

0.00107 

FUGITV96.WK1 Page 5 05/12/97 cdc 

-o 

CD 
GATX Terminals Corporation Fugitive Emissions -1996 

TANK PRODNAME 

v 224 TRI-ETHANE 

,.' 224 TRI-ETHANE 

225 BP ETHANOL 

225 BP ETHANOL 

225 BP ETHANOL 

226 BP ETHANOL 

226 BP ETHANOL 

226 BP ETHANOL 

227 BP ETHANOL 

227 BP ETHANOL 

227 BP ETHANOL 

228 BP ETHANOL 

228 BP ETHANOL 

228 BP ETHANOL 

301 ETHANOL/301 

*-r305 ACETIC ACID 

° Q 305 ACETIC ACID 

440 NO 2 FUEL OIL 

' 440 CYCLOHEXANON 

440 CYCLOHEXANON 

450 CYCLOHEXANE 

./ 450 METHYLENE 

451 NEOL-SLURRY 

451 NEOL-SLURRY 

451 NEOL-SLURRY 

460 GASOLINE 

471 #2 FUEL OIL 

V IN 

T * 0 

T 1 

NETGALPUMPI 

gpm 

TIME IN S FUGITIVE COM 

HOURS PUMVAL FLAN 

y 481 METHYLENE CHLO 

y 482 TRI-AEROSOL 

w 483 TRI-AEROSOL 

484 CYCLOHEXANE 

484 CYCLOHEXANE 

C 

S 

T 

C 

S 

T 

C 

s 

T 

C 

s 

T 

C 

T 

T 

T 

T 

T 

C 

T 

T 

T 

T 

T 

T 

T 

T 

c 

0 

1 

0 

0 

1 

0 

0 

1 

0 

0 

1 

0 

178297.0 

4019.0 

200 

200 

471470.0 200 

1604348.0 1750 

690106.0 200 

372484.0 200 

1253238.0 1750 

534518.0 200 

448254.0 200 

657007.0 1750 

244751.0 200 

1472501.0 200 

3799567.0 1750 

2159832.0 200 

63662.0 200 

875656.0 

1055196.0 

78868.0 

91003.0 

6535.0 

52073.0 

104899.0 

128001.0 

14890.0 

4295.0 

1236.0 

31078.0 

11231.0 

6918.0 

5919.0 

28461.0 

200 

200 

155053.0 200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

200 

14.86 

0.33 

39.29 

15.28 

57.51 

31.04 

11.94 

44.54 

37.35 

6.26 

20.40 

122.71-

36.19 

179.99 

5.31 

72.97 

87.93 

12.92 

6.57 

7.58 

0.54 

4.34 

8.74 

10.67 

1.24 

0.36 

0.10 

2.59 

0.94 

0.58 

0.49 

2.37 

12 

12 

2 

11 

2 

2 

12 

2 

2 

11 

2 

3 

9 

3 

7 

7 

7 

34 

7 

10 

30 

10 

10 

27 

10 

7 

29 

7 

EMISSION FACTORS 

PUMPSVALVE FLANG 

(LB/HR (LB/HR (LB/HR 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

0.109 0.016 0.002 

ANNUAL VOC VOC Emissions 

EMISSIONS (Y/N) 

(lb/year) (T/yr) (lb/year) (T/yr) 

4.659495 0.00233 N 

0.10503 0.000053 N 

HAP HAP Emissions 

(Y/N) 

(lb/year) (T/yr) 

Y 4.6595 0.00233 

Y 0.105 0.000053 

6.034816 0.003017 Y 

5.289765 0.002645 Y 

8.833357 0.004417 Y 

4.935413 0.002468 Y 

4.237138 0.002119 Y 

7.082364 0.003541 Y 

5.939366 0.00297 Y 

2.087405 0.001044 Y 

3.242951 0.001621 Y 

20.81135 0.010406 Y 

11.04407 Of.005522Y 

30.52563 0.015263 Y 

30 0.109 0.016 0.002 1.034508 0.000517 Y 

8 0.109 0.016 0.002 16.00991 0.008005 Y 

8 0.109 0.016 0.002 19.2925 0.009646 Y 

10 20 0.109 0.016 0.002 3.94093 0.00197 Y 

10 20 0.109 0.016 0.002 2.004562 0.001002 Y 

10 20 0.109 0.016 0.002 2.312993 0.001156 Y 

5 6 0.109 0.016 0.002 0.108808 0.000054 Y 

5 6 0.109 0.016 0.002 0.667015 0.000434 N 

5 6 0.109 0.016 0.002 1.746568 0.000873 Y 

5 6 0.109 0.016 0.002 2.131217 0.001066 Y 

5 6 0.109 0.016 0.002 0.247919 0.000124 Y 

2 6 0.109 0.016 0.002 0.054332 0.000027 Y 

4. 0 0.109 0.016 0.002 0.006592 3.3E-06 Y 

6 6 0.109 0.016 0.002 0.841178 0.000421 N 

6 6 0.109 0.016 0.002 0.201971 0.000101 N 

6 6 0.109 0.016 0.002 0.124409 0.000062 N 

5 6 0.109 0.016 0.002 0.098551 0.000049 Y 

6 6 0.109 0.016 0.002 0.511824 0.000256 Y 

6.034816 0.003017 N 

5.289765 0.002645 N 

8.833357 0.004417 N 

4.935413 0.002468 N 

4.237138 0.002119 N 

7.082364 0.003541 N 

5.939366 0.00297 N 

2.087405 0.001044 N 

3.242951 0.001621 N 

20.81135 0.010406 N 

11.04407 0.005522 N 

30.52563 0.015263 N 

1.034508 0.000517 N 

16.00991 0.008005 N 

19.2925 0.009646 N 

3.94093 0.00197 N 

2.004562 0.001002 N 

2.312993 0.001156 N 

0.108808 0.000054 N 

Y 

1.746568 0.000873 N 

2.131217 0.001066 N 

0.247919 0.000124 N 

0.054332 0.000027 N 

0.006592 3.3E-06 N 

Y 

Y 

Y 

0.098551 0.000049 N 

0.511824 0.000256 N 

0.867 0.000434 

0.8412 0 000421 

0.202 0.000101 

0.1244 0.000062 

FUGITV96.WK1 Page 6 05/12/97 cdc 
GATX Terminals Corporation Fugitive Emissions • 1996 

TANA PRODNAME 

485 MOTOR OIL 

485 MOTOR OIL 

485 MOTOR OIL 

485 MOTOR OIL 

V IN NETGALPUMPI TIME IN SFUGITIVE COM EMISSION FACTORS ANNUAL 

gpm HOURS PUMVAL FLAN PUMPSVALVE FLANG EMISSIONS 

(LB/HR (LB/HR (LB/HR (lb/year) (T/yr) 

363854.0 

63679.0 

84465.0-

389696.0 

200 

200 

200 

200 

VOC VOC Emissions 

(Y/N) 

(lb/year) (T/yr) 

30.32 

5.31 

7.04 

32.47 

6 

6 

6 

6 

6 

6 

6 

6 

0.109 

0.109 

0.109 

0.109 

0.016 

0.016 

0.016 

0.016 

0.002 

0.002 

0.002 

0.002 

6.543308 

1.145161 

1.518962 

7.008033 

HAP HAP Emissions 

(Y/N) 

(lb/year) (T/yr) 

0.003272 Y 

0.000573 Y 

0.000759 Y 

0.003504 Y 

6.543308 0.003272 N 

1.145161 0.000573 N 

1.518962 0.000759 N 

7.008033 0.003504 N 

/ 488 METHYLENE T 1 44804.0 200 3.73 0 6 6 0.109 0.016 0.002 0.398756 0.000199 N 

/ 488 METHYLENE T 0 42143.0 200 3.51 0 6 6 0.109 0.016 0.002 0.375073 0.000188 N 

Y 0.3988 0.000199 

Y 0.3751 0.000188 

235205.61 6867.95 2040.298 1.020149 2015.899 1.007949 814.42 0.407211 

thousand gallons througput 

-o 

FUGITV96.WK1 Page 7 05/12/97 cdc 

TJ 

co 
\3ATX Terminals Corporation Loading Losses • 1000 

so 

\NK PRODNAME 

51 BP RUB.SOLV. 

52 BPSPARE/MIBK 

53 BP ISOPROPYL 

54 BP ETHYL ACE 

55 BRUCINE 

55 BRUCINE 

56 BITREX 

56 BITREX 

57 METHANOL 

58 TBA MIX 

104 DOP 

104 OOP 

105 METHYL METH 

10S DCPD 

106 OCPO 

107 AV GAS 

108 CHEP 

121 CYCLOHEXANE 

122 ULTRA 95 

123 CUMENE 

124 XYLENE 

124 XYLENE 

124 CYCLOHEXANE 

124 CYCLOHEXANE 

125 CUMENE 

126 CYCLOHEXANE 

128 OCPO 

131 CUMENE WASH WA 

133 PHENOL WASH WAT 

134 PHENOL 

134 CUMENE 

135 PHENOL 

135 PHENOL 

135 CUMENE 

137 2-ETHYL HEXANOL 

141 ULTRA 60 

142 HULS-ISOBUT 

143 ETHYL ACETATE 

143 VINYL ACETAT 

145 FURFURAL 

145 ISOPHORONE 

145 ISOPHORONE 

146 ISODECYU146 

147 2-ETHYL HEXANOL 

148 XYLENE 

148 XYLENE 

149 XYLENE/149 

150 ACI-TCE 

152 BENZENE 

153 SUN SPIRITS 

154 SPIRITS 66 

155 SLACKWAX 

155 SLACKWAX 

156 WAX 156 

156 WAX 156 

157 AMS 

157 AMS 

157 AMS 

VEH 

T 

T 

T 

T 

C 

T 

T 

C 

T 

T 

T 

s 

T 

c 

T 

T 

T 

c 

T 

B 

T 

s 

' c 

T 

B 

c 

T 

T 

C 

c 

B 

B 

T 

B 

9 

C 

T 

C 

T 

S 

T 

C 

NETGAL Vap Press Mole Wl. 

157.0 

22480 

33903.0 

461.0 

16799.0 

21874.0 

10106.0 

8923.0 

5861.0 

758 0 

113999.0 

0.0 

1199309.0 

464S5S.0 

2294.0 

234533.0 

0.0 

789919.0 

495483.0 

1972722.0 

6580.0 

1485734.0 

4853505.0 

10488.0 

40913353.0 

709463.0 

184656 0 

9671.0 

2933.0 

233640 

314727.0 

274146.0 

31263.0 

543806.0 

137483.0 

6556.0 

118200.0 

193657.0 

62262.0 

16325.0 

60368.0 

301750.0 

889565.0 

556.0 

16422.0 

722.0 

78961.0 

2669977.0 

2953280.0 

268487.0 

672969.0 

1487562.0 

64895.0 

616803.0 

1180020.0 

113786.0 

40381.0 

0.212 

0.212 

0.483 

1.102 

0.619 

0.619 

0.619 

0.619 

1412 

0.425 

0.031 

0.031 

0.348 

0.02 

0.02 

1.27 

0.135 

1.216 

0.0019 

0.051 

0.129 

0.129 

1.21B 

1.218 

0.051 

1.218 

0.02 

0.051 

0.019 

0.019 

0.051 

0.019 

0.019 

0 051 

0.004 

0.004 

0.135 

1.102 

1.296 

0.01382 

0.0469 

0.0469 

0.0005 

0.004 

0.129 

0.129 

0.129 

0.889 

1.16 

0.03 

0.03 

0 

0 

0 

0 

0.02S 

0.025 

0.025 

100.2 

100.2 

180.1 

88.1 

46.07 

46.07 

• 46.07 

46.07 

32.04 

74.12 

390.6 

390.6 

100.11 

132.21 

132.21 

80 

130.2 

84.18 

400 

120.02 

106.17 

106.17 

84.16 

84.16 

120.02 

84.16 

132.21 

120.02 

94.1 

94.1 

120.02 

94.1 

94.1 

120.02 

130.23 

130.23 

74.12 

88.1 

66.09 

96.09 

138.21 

138.21 

158.29 

130.23 

106.17 

106.17 

106.17 

131.4 

78.11 

132 

132 

312 

312 

912 

312 

118.2 

118.2 

118.2 

S Factor Loss Factor Uncontrolled Emissions Control Oa 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.2 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

O.S 

0.6 

0.2 

0.6 

0.6 

0.5 

0.6 

0.6 

0.6 

0.6 

0.6 

0.5 

05 

0.6 

O.S 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

O.S 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.2 

0.6 

0.6 

0.3054 

0.3054 

1.250624 

1.395801 

0.409991 

0.409991 

0.409991 

0.409991 

0.650419 

0.452887 

0.174084 

0.058028 

0.500867 

0.038015 

0.038015 

1.460695 

0.252703 

1.473734 

0.010926 

0.073335 

0.196S0S 

0.065635 

1.473734 

1.473734 

0.073335 

1.473734 

0.038015 

0.086001 

0.025705 

0.02S705 

0.073335 

0.02142 

0.025705 

0.073335 

0.007489 

0.007489 

0.143858 

1.395801 

1.604071 

0.019093 

0.093192 

0.093192 

0.001138 

0.007469 

0.19690S 

0.164068 

0.196905 

1.679435 

1.302658 

0.056933 

0.056933 

0 

0 

0 

0 

0.014161 

0.042484 

0.042464 

(Ib/yr) 

0.047948 

0.68654 

42.39991 

0.643464 

6.887447 

8.968153 

4.143374 

3.658354 

3.812105 

0.343289 

19.84545 

0 

600.6946 

17.66027 

0.087207 

342.5813 

0 

1164.13 

5.413876 

144.6686 

1.295637 

97.51632 

7152.773 

15.45652 

3000.361 

1045.559 

7.019783 

0.851062 

0.075391 

0.60056 

23.08036 

5.872322 

0.8036 

39.87976 

1.029641 

0.049099 

17.00406 

270.3066 

"99,87268 

0.3117 

5.62581 

28.12066 

0 

6.662154 

0.109479 

2.694649 

0.142166 

132.6098 

3478.068 

168.138 

15.28567 

0 

0 

0 

0 

16.71058 

4.834063 

1.715539 

(T/yr) 

0.000024 None 

0.000343 None 

0.0212 None 

0.000322 None 

0.003444 None 

0.004484 None 

0.002072 None 

0.001829 None 

0.001906 None 

0.000172 None 

0.009923 None 

0 None 

0.300347 Incinerator 

0.00883 None 

0.000044 Incinerator 

0.171291 Nona 

0 Nona 

0.582065 None 

0.002707 None 

0.072334 Nona 

0.000648 Nona 

0.048758 None 

3.576387 None 

0.007728 None 

1.500181 None 

0.52278 None 

0.00351 Incinerator 

0.000426 Incinerator 

0.000038 None 

0.0003 None 

0.01154 None 

0.002936 None 

0.000402 Incinerator 

0.01994 None 

0.000515 Incinerator 

0.000025 None 

0.008502 None 

0.135153 Nona 

0.049936 None 

0.0001S6 None 

0.002813 Nona 

0.01406 Nona 

0 Nona 

0.003331 Incinerator 

0.000055 Incinerator 

0.001347 Nona 

0.000071 Nona 

0.068305 None 

1.739034 Incinerator 

0.084069 None 

0.007643 None 

0 None 

0 None 

0 None 

0 None 

0.008355 None 

0.002417 None 

0.000858 None 

LOAONG96.WK1 

(%) 

cy 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

99 

0 

99 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

99 

99 

0 

0 

0 

0 

99 

0 

99 

0 

0 

0 

0 

0 

0 

0 

0 

99 

99 

0 

0 

0 

99 

0 

0 

0 

0 

0 

0 

0 

0 

0 

Controlled Emissions VOC VOC Emissions HAP HAP Emissions 

(Ib/yr) 

0.047948 

0.68654 

42.39991 

0.643464 

6.887447 

8.968153 

4.143374 

3.658354 

3.812105 

0.343289 

19.84545 

0 

6.006946 

17.66027 

0.000872 

342.5813 

0 

1164.13 

5.413676 

* 144.6666 

1.295637 

97.51632 

7152.773 

15.45652 

3000.361 

1045.559 

0.070198 

0.008511 

0.075391 

O.60056 

23.08036 

5.872322 

0.008036 

39.87976 

0.010296 

0.049099 

17.00406 

270.3066 

99.87266 

0.3117 

5.62581 

28.12066 

0 

0.066622 

0.001095 

2.694649 

0.142166 

132.6098 

34.78068 

168.138 

15.28567 

0 

0 

0 

0 

16.71058 

4.834063 

1.715539 

(T/yr) 

0.000024 Y 

0.O00343 Y 

0.0212 Y 

0.000322 Y 

0.003444 Y 

0.004484 Y 

0.002072 Y 

0.001829 Y 

0.001906 Y 

0.000172 Y 

0.009923 Y 

0 Y 

0.003003 Y 

0.00883 Y 

4.4E-07 Y 

0.171291 Y 

0 Y 

0.582065 Y 

0.002707 Y 

0.072334 Y 

0.000648 Y 

0.048758 Y 

3.576387 Y 

0.007728 Y 

1.500181 Y 

0.52278 Y 

0.000035 Y 

4.3E-06 Y 

0.000038 Y 

0.0003 Y 

0.01154 Y 

0.002936 Y 

4.0E-06 Y 

0.01994 Y 

5.1 E-06 Y 

0.000025 Y 

0.008502 Y 

0.135153 Y 

0.049936 Y 

0.000156 Y 

0.002813 N 

0.01406 Y 

0 Y 

0.000033 Y 

5.5E-07 Y 

0.001347 Y* 

0.000071 Y 

0.O66305 N 

0.01739 Y 

0.084069 Y 

0.007643 Y 

0 Y 

0 Y 

0 Y 

0 Y 

0.008355 Y 

0.002417 Y 

0.000856 Y 

(Ib/yr) 

0.047948 

0.66654 

42.39991 

0.643464 

6.887447 

8.968153 

4.143374 

3.658354 

3.812105 

0.343289 

19.84545 

0 

6.006946 

17.66027 

0.000872 

342.5813 

0 

1164.13 

5.413876 

144.6666 

1.295637 

97.51632 

7152.773 

15.45652 

3000.361 

1045.559 

0.070198 

0.008511 

0.075391 

0.60056 

23.08036 

5.872322 

0.008036 

39.87976 

0.010296 

0.049099 

17.00406 

270.3066 

99.87266 

0.3117 

28.12066 

0 

0.066622 

0.001095 

1.347325 

0.142166 

34.78068 

168.138 

15.28567 

O 

O 

0 

0 

16.71058 

4.834063 

1.715539 

(T/yr) 

0.000024 Y 

0.000343 Y 

0.0212 N 

0.000322 N 

0.003444 N 

0.004484 N 

0.002072 N 

0.001829 N 

0.001906 Y 

0.000172 N 

0.009923 N 

0 N 

0.003003 Y 

0.00883 N 

4.4E-07 Y 

0.171291 N 

0 N 

0.582065 N 

0.002707 N 

0.072334 Y 

0.000648 N 

0.048758 Y 

3.576387 N 

0.007728 N 

1.500181 Y 

0.52278 N 

0.000035 N 

4.3E-06 Y 

0.000038 N 

0.0003 N 

0.01154 Y 

0.002936 Y 

4.0E-06 Y 

0.01994 Y 

5.1 E-06 N 

0.000025 N 

0.008502 N 

0.135153 Y 

0.049936 Y 

0.000156 N 

Y 

0.01406 N 

0 N 

0.000033 N 

5.5E-07 Y 

0.000674 N 

0.000071 Y 

Y 

0.01739 Y 

0.084069 N 

0.007643 N 

0 N 

0 N 

0 N 

0 N 

0.008355 N 

0.002417 N 

0.000858 N 

(Ib/yr) 

0.047948 

0.08654 

3.812105 

6.006946 

0.000872 

144.6686 

97.51632 

3000.361 

0.008511 

23.08036 

5.872322 

0.008036 

39.87976 

270.3066 

99.87268 

5.62581 

0.001095 

0.142166 

132.6098 

34.78068 

(T/yr) 

0.000024 

0.000343 

0.001906 

0.003003 

4.4E-07 

0.072334 

0.048758 

1.500181 

4.3E-06 

0.01154 

0.002936 

4.0E-06 

0.01994 

0.135153 

0.049936 

0.002813 

5.5E-07 

0.000071 

0.066305 

0.01739 

Page 1 05/12/97 cdc 

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33, 

> 
GATX Terminals Corporation Loading Losses -1996 

227 

228 

228 

301 

305 

440 

•y 450 

450 

451 

481 

•/' 482 

463 

484 

485 

,48S 

v 488 

CHEMPl 

CHILBAR 

JO TANK 

SEABUL 

PRODNAME 

BP ETHANOL 

BP ETHANOL 

BP ETHANOL 

ETHANOL/301 

ACETIC ACID 

CYCLOHEXANON 

METHYLENE 

CYCLOHEXANE 

NEOL-SLURRY 

METHYLENE 

TRI-AEROSOL 

TRI-AEROSOL 

CYCLOHEXANE 

MOTOR OIL 

MOTOR OIL 

METHYLENE 

CUMENE 

CUMENE 

CUMENE 

CUMENE 

VEH 

c 

C 

T 

B 

B 

B 

B 

NETGAL Vap Press Mole Wl. 

.244751.0 

1473501.0 

2159832.0 

63662.0 

10551960 

91003.0 

52073.0 

6535.0 

128001.0 

31078.0 

11231.0 

6918.0 

5919.0 

389696.0 

63679.0 

42143.0 

32368.0 

47867.0 

719082.0 

47759.0 

111753014 

0.619 

0.619 

0619 

0.619 

0.169 

0.054 

5.434 ^ 

1.218 

0.064 

5.434 

1.586 

1.586 

1.218 

0031 

0.031 

5.414 

0.051 

0.051 

0.051 

0.051 

46.07 

46.07 

46.07 

4607 

60.05 

98.2 

64.94 

84.16 

104.15 

84.94 

133.42 

133.42 

84.16 

60.1 

60.1 

84.94 

120.02 

120.02 

120.02 

120.02 

S Factor Loss Factor Uncontrolled Emissions Control DeviEfficieney 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

0.6 

O.S 

0.5 

0.5 

O.S 

TOTALS 

0.409991 

0.409991 

0.409991 

0.409991 

0.145903 

0.076236 

6.63587 

1.473734 

0.095831 

6.63587 

3.042216 

3.042216 

1.473734 

0.026786 

0.026786 

6.63587 

0.073335 

0.073335 

0.073335 

0.073335 

(lb/yr> 

100.3458 

604.1228 

865.5127 

26.10088 

153.9566 

6.937882 

345.5496 

6.630849 

12.26644 

206.2296 

34.16713 

21.04605 

8.723029 

10.43826 

1.705683 

279.6555 

2.373692 

3.510304 

52.73354 

3.502364 

27942.3 

(T/yr) 

0.050173 None 

0.302061 None 

0.442756 None 

0.01305 None 

0.076978 None 

0.003469 None 

0.172775 None 

0.004815 Nona 

0.006133 Nona 

0.103115 None 

0.017084 Nona 

0.010523 None 

0.004362 None 

O.00S219 Nona 

0.000853 None 

0.139828 None 

0.001187 None 

0.001755 None 

0.026367 None 

0.001751 None 

13.97115 

(%) 0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

0 

Controlled Emissions VOC VOC Emissions HAP HAP Emissions 

(Ib/yr) 

100.3458 

604.1228 

885.5127 

26.10088 

153.9566 

6.937882 

345.5496 

8.630849 

12.26644 

206.2296 

34.16713 

21.04605 

8.723029 

10.43826 

1.705683 

279.6555 

2.373692 

3.510304 

52.73354 

0 - 3.502384 

23887.92 

(T/yr) 

0.050173 Y 

0.302061 Y 

0.442756 Y 

0.01305 Y 

0.076978 Y 

0.003469 Y 

0.172775 N 

0.004815 Y 

0.006133 Y 

0.103115 N 

0.017084 N 

0.010523 N 

0.004362 Y 

0.005219 Y 

0.000653 Y 

0.139828 N 

0.001187 Y 

0.001755 Y 

0.026367 Y 

0.001751 Y 

11.94396 

(Ib/yr) 

100.3458 

604.1228 

885.5127 

26.10088 

153.9568 

6.937882 

9.630849 

12.26644 

8.723029 

10.43826 

1.705683 

2.373692 

3.510304 

52.73354 

3.502384 

20865.41 

VOC Ib/yr 

(T/yr) 

0.050173 N 

0.302061 N 

0.442756 N 

0.01305 N 

0.076978 N 

0.003469 N 

Y 

0.004815 N 

0.006133 N 

N 

Y 

N 

0.004362 N 

0.005219 N 

0.000853 N 

Y 

0.001187 Y 

0.001755 Y 

0.026367 Y 

0.001751 Y 

10.4327 

VOC T/yr 

(Ib/yr) 

345.5496 

34.16713 

279.6555 

2.373692 

3.510304 

52.73354 

3.502384 

8042.129 

HAP Ib/yr 

(T/yr) 

0.172775 

0.017084 

0.139828 

0.001187 

0.001755 

0.026367 

0.001751 

4.021065 

HAP T/yr 

111/53.0 thousand gallons throughput 

so 

LOADNG96.WK1 Page 3 05/12/97 cdc 

Tl 
G A U PHILADELPHIA. PA 

TERMINAL 

^ .Mi.ll.ll l *ll t PLAN