MIDWEST RESEARCH INSTITUTE

Crossroads Corporate Park

5520 Dillard Road

Suite 100

Cary, North Carolina 27511-9232

Telephone (919) 851-8181

FAX (919) 851-3232

Date: July 31, 2000

Subject: MACT Floor, Regulatory Alternatives, and Nationwide Impacts for Storage Tanks

at Miscellaneous Organic Chemical Manufacturing Facilities

Miscellaneous Organic NESHAP

EPA Project No. 95/08; MRI Project No. 104803.1.049

From: David Randall

Jennifer Fields

To: MON Project File

I. Introduction

This memorandum describes our review and analysis of previously developed existing and

new source MACT floors and regulatory alternatives for storage tanks at miscellaneous organic

chemical manufacturing facilities.1 This memorandum also presents estimated emissions and cost

impacts of the MACT floor and a regulatory alternative for existing sources.

II. Review of MACT Floor and Regulatory Alternatives

A. Existing Sources

Our review of the MACT floor analyses began with the Access database created from

information obtained in: (1) responses to the information collection requests that were sent to

facilities with batch processes and (2) permit information from facilities with continuous processes

in seven states. We took the following steps to purge extraneous information from the database:

• Deleted all records containing inorganic compounds.

• Replaced reported scrubber control efficiencies with 0 percent because the fate of the

HAP removed from the emission stream is unknown.

• Excluded all pressurized tanks.

• Excluded all tanks with a capacity <10,000 gal because information was not requested

for such tanks.

• Excluded tanks storing ethyl chloride and ethylene oxide because these compounds are

gaseous at ambient temperatures and are likely to be in pressurized tanks.

• Excluded tanks for which no HAP partial pressure was reported (9 tanks).
2

• Excluded seven tanks from one facility with an unreasonable number of turnovers (i.e.,

more than 10 per day).

• Excluded tanks storing o-toluidiene at one facility because the reported partial

pressure was several orders of magnitude higher than the vapor pressure at ambient

temperature.

• Excluded tanks with reported HAP partial pressures below a de minimis of 0.05 psia

(155 tanks with about 1 percent of the total uncontrolled emissions).

• Unlike the previous analysis, tanks storing maleic anhydride and phthalic anhydride

were not excluded.

The temperature at which the reported partial pressures were determined is unknown. 

However, for those tanks that appear to be storing a single HAP, many of the reported partial

pressures appear to be equal to the vapor pressure at about 77EF. For some tanks, it appears that

partial pressures were determined at higher temperatures. Many, but not all, of these tanks were

identified as constant temperature tanks. In other cases, the partial pressures were lower than the

vapor pressure at 77EF, which may mean the tank stores a mixture of condensable materials, some

of which were not identified because they are not HAP.

The final database contained 1,195 storage tanks at 132 facilities. The MACT floor

performance level is unchanged from the previous analysis (i.e., an IFR, EFR, or control device

achieving an emission reduction of 95 percent or more) because more than 12 percent of the

storage tanks (205 tanks) are controlled using these devices. As in the previous analysis, tanks

storing material with the lowest HAP partial pressures were considered to be the most stringently

controlled, and a partial pressure threshold was developed for each facility. The top 12 percent of

the 132 facilities corresponds to 16 facilities. The average threshold for the top 16 facilities is 1.0

psia (rounded up from (0.9 psia). Thus, the MACT floor for existing sources is unchanged from

the previous analysis.1 Attachment 1 presents the thresholds for each facility.

One regulatory alternative was developed for existing sources. The control level is the

same as the 95 percent level for the MACT floor because this is the maximum reasonable control

for storage tanks. The size cutoff is 10,000 gal, as for the MACT floor, because storage tanks

rarely are smaller than this size. A HAP partial pressure cutoff of 0.5 psia was selected for the

regulatory alternative; this value is the midpoint between zero and the 1.0 psia cutoff for the

MACT floor.

Table 1 summarizes the MACT floor and regulatory alternative for storage tanks at

existing sources.
3

TABLE 1. MACT FLOOR AND REGULATORY ALTERNATIVES

FOR EXISTING AND NEW SOURCES

Regulatory alternative Control requirement

Applicability cutoffs

Tank size, gal

Partial pressure,

psia

Existing sources

MACT floor IFR, EFR, or 95% reduction $10,000 $1.0

Regulatory alternative IFR, EFR, or 95% reduction $10,000 $0.5

New sources

MACT floor IFR, EFR, or 95% reduction $10,000 $0.1

B. New Sources

The best performing source is the one that achieves the highest level of control for the

smallest tanks storing material with the lowest HAP partial pressure. This combination is

considered the best because small tanks tend to have lower emissions than large tanks, and tanks

storing material with low partial pressures tend to have lower emissions than tanks storing

materials with higher partial pressures.

Numerous facilities are controlling all of their tanks to 95 percent. As shown in

Attachment 1, the Cyro Industries facility in Wallingford, Connecticut is one of the best

performing facilities because it is controlling all of its tanks that store material with a HAP partial

pressure greater than 0.09 psia. The tank storing the material with this HAP partial pressure has a

capacity of 20,000 gal. The second and third facilities listed in Attachment 1 are not best

performing sources because their smallest tanks controlled to 95 percent are larger than 20,000

gal. However, the fourth facility in Attachment 1 (the Morton International facility in Patterson,

New Jersey) is the best performing facility for smaller storage tanks. This facility is achieving the

same control level on its only storage tank, which has a capacity of 11,200 gal and stores material

with essentially the same HAP partial pressure as the Cyro Industries facility (i.e., 0.11 psia). 

Thus, the new source MACT floor is 95 percent control of HAP emissions from storage tanks

with a capacity greater than or equal to 10,000 gal that store material with a HAP partial pressure

greater than or equal to 0.1 psia.

No regulatory alternative was developed for storage tanks at new sources. Higher control

efficiencies would require the use of add-on control devices, and the incremental cost to use these

devices would not be reasonable. A HAP partial pressure cutoff less than 0.1 psia would also be

unreasonable.

Table 1 summarizes the new source MACT floor for storage tanks.
4

III. Emissions Impacts

We estimated annual standing and working losses for the storage tanks that are associated

with batch processes using the AP-42 procedures.2 We set parameter values in the calculations

based on the following assumptions and procedures:

• Cylindrical volume with equal tank diameter and height.

• Default breather vent settings.

• Cone roof, tank painted white, and paint in good condition.

• Average liquid height equal 0.6 times the maximum liquid height.

• Shell height equal tank diameter plus one foot.

• Default daily maximum and minimum ambient temperatures were assumed to be 72EF

and 60EF, respectively (i.e., representative national average values); these values were

used in the equations to estimate the minimum and maximum surface temperatures.

• Daily solar insolation factor equal 1,300 Btu/ft2/d.

• Vapor pressures at the minimum and maximum surface temperatures were calculated

using Antoine’s equation or another vapor pressure estimation equation, except for

formaldehyde we used actual laboratory data for 37 weight percent formaldehyde in

water solutions.3,4

• Vapor molecular weight equal to the HAP molecular weight (i.e., because we do not

know the total composition of the stored material, we estimated emissions for each

HAP as if were the only HAP in the tank, and all other stored material has a negligible

vapor pressure).

• Typically, used the reported HAP partial pressures, even though in many cases the

value was significantly higher than the estimated vapor pressure at the default average

liquid surface temperatures for tanks that were not reported to be heated. One

exception was that we replaced the reported partial pressures of 14.7 psia for several

tanks at one facility with the estimated vapor pressures at ambient conditions. A

second exception was for a tank storing both propionaldehyde and acetaldehyde. The

reported partial pressures for this tank appear to have been the pure component vapor

pressures. Because the component throughputs were also reported, we calculated the

applicable partial pressures.

• Typically, the reported throughput was the same for each HAP associated with a

particular tank. However, for some tanks, different throughputs were reported for

each HAP. It is not clear if this is because the tank is used for different materials at

different times during the year or because the facility elected to identify the component

throughput instead of the total. We used the throughput associated with the individual

HAPs, consistent with the decision to estimate emissions for each HAP as if it were

the only condensable material in the tank.
5

• Standing losses were set equal to zero if the tank was reported to be maintained at

constant temperature.

• Included tanks with reported HAP partial pressures <0.05 psia.

Emissions from storage tanks associated with continuous processes were included in the

available permit materials. As noted in previous analyses, the facilities for which permit

information was obtained were assumed to represent half of the nationwide number of continuous

processes in the source category.5 Thus, we estimated the nationwide emissions from storage

tanks associated with continuous processes by doubling the estimated emissions from the tanks

for which data were available.

Nationwide uncontrolled and baseline emissions were estimated to be 846 Mg/yr and

393 Mg/yr, respectively. Uncontrolled and baseline emissions for each tank storing material with

HAP partial pressures above the cutoffs for the MACT floor and regulatory alternative are

presented in Attachments 2 and 3. The sum of the emissions from the tanks listed in the

attachments does not equal the nationwide total because the nationwide emissions include all

tanks larger than 10,000 gal, not just those containing material with HAP partial pressures greater

than the cutoffs.

IV. Cost Estimates

For tanks that are not already controlled to 95 percent, we estimated the cost impacts

associated with both the MACT floor and the regulatory alternative. In both cases, we estimated

impacts assuming the vertical tanks would be controlled by installing a floating roof, and that

horizontal tanks would be controlled by venting emissions through a closed-vent system to a

condenser that reduces the emissions by 95 percent by weight. The estimated costs are presented

in Attachments 2 and 3.

The floating roof costs were estimated in July 1989 dollars using procedures described in

the HON BID.6 The total capital investment include costs to clean and degas the tank, install the

floating roof, and, if necessary, remove an existing condenser that does not achieve the required

control efficiency. The costs were then escalated to February 1999 dollars using the Chemical

Engineering Plant Cost Indexes for February 1999 and July 1989.7,8 Annual costs were

estimated for capital recovery, operation and maintenance, administrative charges, property taxes,

and insurance. In addition, a credit was estimated for recovered product. Capital recovery was

estimated assuming an equipment life of 15 years and an interest rate of 7 percent. Annual

maintenance and inspection costs were estimated to be equal to 6 percent of the TCI, and the

other charges were estimated to be equal to 4 percent of the TCI. The product recovery credit

was estimated assuming the market value of the recovered material is $0.10/lb. The Access

module used to calculate the costs is presented in Attachment 4.

Condenser costs were estimated using procedures described in the OAQPS Control Cost

Manual.9 The condenser was sized based on the HAP with the highest partial pressure in the

tank. Typically, the tanks contained only one HAP; for tanks with multiple HAP, the secondary

HAP had very low partial pressures, well below the cutoffs for the MACT floor and regulatory
6

alternative. The amount of time that the tank was being filled was estimated by dividing the

annual throughput by an estimated average fill rate of 150 gal/min. The capital costs for a

refrigeration unit, including instrumentation, installation, sales tax, and freight costs, were

estimated in third quarter 1990 dollars. These costs were escalated to first quarter 1999 dollars

using Vatavuk cost indexes.10,11 The total capital investment consisted of these costs plus the

costs for a temperature monitoring system (i.e., thermocouple and signal wire to connect to an

existing data acquisition system for process vent monitors). Annual costs were estimated for

labor, electricity, capital recovery, administrative charges, property tax, and insurance. Electricity

costs during non-filling periods were estimated to be equal to 10 percent of the costs during filling

events. Monitoring labor was estimated to be 0.5 hr/d for 365 d/yr. Capital recovery costs were

estimated assuming an equipment life of 15 years and an interest rate of 7 percent. A product

recovery credit was estimated as described above for the floating roofs. The Access module used

to estimate the costs is presented in Attachment 5.

The nationwide costs and cost effectiveness of the controls to meet the MACT floor and

the regulatory alternative are presented in Table 2. 

TABLE 2. IMPACTS OF REGULATORY ALTERNATIVES FOR EXISTING SOURCES

Regulatory

alternative

Total capital

investment, $

Total annual

cost, $/yr

Emission

reduction,

Mg/yr

Cost effectiveness, $/Mg

Relative to

baseline Incremental

MACT floor 6,000,000 2,030,000 262 7,700 N/A

Regulatory

alternative

7,420,000 2,600,000 292 8,900 19,000

V. References

1. Memorandum from C. Zukor and R. Howle, Alpha-Gamma Technologies, Inc., to

Miscellaneous Organic NESHAP Project File. May 20, 1999. Existing Source MACT

Floors for Batch and Continuous Manufacturing Processes Covered by the MON.

2. U. S. Environmental Protection Agency. Compilation of Air Pollutant Emission Factors. 

Volume I: Stationary Point and Area Sources. Fifth Edition. AP-42. January 1995. 

Chapter 7.

3. U.S. Environmental Protection Agency. Alternative Control Techniques Document–Control

of Volatile Organic Compound Emissions from Batch Processes. EPA Publication No. EPA453/R-94-020. February 1994. Appendix A.

4. Letter and attachments from M.L. Mullins, Chemical Manufacturers Association, to

R. McDonald, EPA:ESD. February 28, 1994. Comments on draft CTG document for

control of VOC emissions from batch processes, including laboratory data showing partial
7

pressure of formaldehyde in water solutions at different temperatures. Page 14 and

appendix A.

5. Memorandum from C. Zukor, Alpha-Gamma Technologies, Inc., to Miscellaneous Organic

NESHAP Project File. July 27, 1999. National Impacts Associated with Regulatory Options

for MON Chemical Manufacturing Processes.

6. U. S. Environmental Protection Agency. Hazardous Air Pollutant Emissions From Process

Units in the Synthetic Organic Chemical Manufacturing Industry–Background Information

for Proposed Standards. Research Triangle Park, North Carolina, Office of Air Quality

Planning and Standards. EPA Publication No. EPA-453/D-92-016b. November 1992.

7. Economic Indicators. Chemical Engineering. Plant Cost Index for February 1999. 

June 1999. Page 170.

8. Economic Indicators. Chemical Engineering. Plant Cost Index for July 1989. 

October 1989. Page 230.

9. U. S. Environmental Protection Agency. OAQPS Control Cost Manual. Fourth Edition. 

EPA Publication No. EPA-450/3-90-006. Chapter 8. Refrigerated Condensers.

10. U. S. Environmental Protection Agency. Escalation Indexes for Air Pollution Control Costs. 

EPA Publication No. EPA-452/R-95-006. October 1995. Page 22.

11. Economic Indicators. Chemical Engineering. Vatavuk Air Pollution Control Cost Indexes

for First Quarter 1999. Refrigeration Systems. January 2000. Page 138.
ATTACHMENT 1

MACT Floor Ranking of Facilities
Att.1-1

MACT Floor Ranking of Facilities

Rank Plant Name City State Threshold Total tanks MACT tanks Running Avg

1 Cyro Industries - Wallingford Wallingford CT 0.09 9 9 0.090

2 CCP-Chatham Facility Chatham VA 0.099 1 1 0.095

3 CCP-Marshall Facility Marshall TX 0.099 1 1 0.096

4 Morton International Inc. - Paterson Facility Paterson NJ 0.11 1 1 0.100

5 Dow Joliet Site Channahon IL 0.14 7 7 0.107

6 Exxon Chemical Americas - Baton Rouge Chemical Plant Baton Rouge LA 0.18 1 1 0.119

7 Ashland Chemical Company - Los Angeles - Composite Polymers Los Angeles CA 0.25 9 3 0.138

8 Ashland Chemical Company - Composite Polymers Div. - Philadelphia Plant Philadelphia PA 0.548 20 18 0.189

9 HERCULES FRANKLIN PLANT Courtland VA 0.66 4 4 0.241

10 Novartis Crop Protection, Inc. - St. Gabriel Plant Site St. Gabriel LA 1.02 2 2 0.319

11 Akzo Nobel Chemicals Inc. Morris IL 1.63 3 3 0.438

12 Ciba Specialty Corp. Newport Plant Newport DE 1.86 6 6 0.557

13 Troy Chemical Corporation Newark NJ 1.87 1 1 0.658

14 AIR PRODUCTS, INCORPORATED/HARRIS/HG0011L LA PORTE TX 1.93 5 5 0.749

15 AMOCO CHEMICAL COMPANY/BRAZORIA/BL0002S ALVIN TX 1.93 2 2 0.828

16 Monsanto Gonzalez FL 2.40 1 1 0.926

17 ARISTECH CHEMICAL CORPORATION/HARRIS/HG0825G PASADENA TX 2.93 2 2 1.044

18 CHEVRON CHEMICAL COMPANY/HARRIS/HG0310V BAYTOWN TX 2.93 4 1 1.149

19 EXXON CHEMICAL AMERICAS/CHAMBERS/CI0009P 2.93 2 2 1.243

20 FORMOSA PLASTICS CORP. OF TEXAS/CALHOUN/CB0038Q POINT COMFORT TX 2.93 5 5 1.327

21 HUNTSMAN CORPORATION/JEFFERSON/JE0135Q 2.93 5 1 1.403

22 BASF Corporation - PVP Plant Geismar LA 3.20 1 1 1.485

23 The Lubrizol Corporation - Bayport Plant Pasadena TX 3.39 15 12 1.568

24 Kodak Park - Synthetic Chemicals Division Rochester NY NT 4

25 Akzo Nobel Resins E. St. Louis IL NT 1

26 PPG Industries, Inc. Oak Creek WI NT 19

27 PPG - Circleville Resin Plant Circleville OH NT 28

28 PPG - Delaware Resin Plant Delaware OH NT 5

29 DUPONT FRONT ROYAL SITE FRONT ROYAL VA NT 25

30 Witco Corp. - Sistersville Plant Friendly WV NT 7

31 The NutraSweet Kelco Company Augusta GA NT 3

32 BFGoodrich Co. Akron OH NT 2

33 Du Pont - Fort Madison Plant Fort Madison IA NT 15

34 DynaChem, Inc. Georgetown IL NT 1

35 Flexsys Nitro Plant Nitro WV NT 4

36 E. I. Du Pont de Nemours & Co. Inc. - Washington Works Parkersburg WV NT 5 2

37 Exxon Chemical Americas - Bayway Chemical Plant Linden NJ NT 5

38 Ciba Specialty Chemicals Corp McIntosh AL NT 51 36

39 The Lubrizol Corporation Painesville OH NT 15 2

40 Albright & Wilson Americas Inc. Charleston SC NT 2

41 Arizona Chemical Panama City FL NT 6

42 Huntsman Petrochemical Corporation - Dayton Manufacturing Facility Dayton TX NT 43

43 Akzo Nobel Resins Louisville KY NT 2
Att.1-2

MACT Floor Ranking of Facilities

(continued)

Rank Plant Name City State Threshold Total tanks MACT tanks Running Avg

44 Albemarle Corporation - South Plant Magnolia AR NT 8 4

45 Hercules, Inc. - Hattiesburg, MS Plant Hattiesburg MS NT 5

46 Franklin International - Polymer Division Columbus OH NT 5

47 The Euclid Chemical Co. Cleveland OH NT 1

48 Para-Chem, Inc.- Simpsonville Plant Simpsonville SC NT 3

49 The Glidden Company Huron OH NT 5

50 Evans Chemetics Waterloo NY NT 1

51 THE GOODYEAR TIRE & RUBBER COMPANY NIAGARA FALLS NY NT 4

52 Tennessee Eastman Division Kingsport TN NT 28

53 BPCI - Sand Springs Manufacturing Plant Sand Springs OK NT 17

54 Geo Specialty Chemicals Cedartown GA NT 3

55 Elf Atochem North America, Inc. - Channelview Complex Channelview TX NT 2

56 Union Camp Corporation Dover OH NT 8

57 Cytec Industries Wallingford CT NT 1

58 CCP- Houston Facility Houston TX NT 2 1

59 CCP-North Kansas City Facility North Kansas City MO NT 5

60 CCP-Saukville Facility Saukville WI NT 5

61 HENKEL CORPORATION - LOS ANGELES OPERATIONS LOS ANGELES CA NT 1

62 Morton International Inc. - Ringwood Plant Ringwood IL NT 5

63 Arkansas Eastman Division Batesville AR NT 11

64 ISP Chemicals Inc. Calvert City KY NT 10

65 Henkel Corporation Kankakee IL NT 6

66 DIXIE CHEMICAL COMPANY PASADENA TX NT 38 6

67 Rohm and Haas Company - Bristol Site Bristol PA NT 22

68 E. I. DuPont de Nemours & Co., Inc. - Chamber Works Deepwater NJ NT 3

69 BASF Corporation - Freeport Works Freeport TX NT 2

70 Sigma Chemical Company - Second Street Plant St. Louis MO NT 11

71 Huls America, Inc. Theodore AL NT 4 2

72 Union Carbide Corporation - South Charleston Plant South Charleston WV NT 39 1

73 Zeneca Specialties, Inc. - Mt. Pleasant Site Mt. Pleasant TN NT 4

74 Sartomer Company, Inc. West Chester PA NT 6

75 Stepan Millsdale Plant Elwood IL NT 15

76 Schenectady International, Inc. - Texas Operations Freeport TX NT 3

77 Unitex Chemical Corporation Greensboro NC NT 6

78 3M Decatur Decatur AL NT 4

79 3M Company - Cottage Grove Cottage Grove MN NT 9

80 3M Company - Cordova Cordova IL NT 13

81 National Starch and Chemical Company - Meredosia Meredosia IL NT 8 1

82 Neville Chemical Company - Neville Island Facility Pittsburgh PA NT 6

83 3M SPRINGFIELD ITSD/TMD / SPRINGFIELD, MO SPRINGFIELD MO NT 13 11

84 THE DOW CHEMICAL COMPANY/HARRIS/HG0769O LA PORTE TX NT 1

85 REXENE CORPORATION/ECTOR/EB0108J ODESSA TX NT 1

86 LYONDELL PETROCHEMICAL COMPANY/VICTORIA/VC0065E NT 3
Att.1-3

MACT Floor Ranking of Facilities

(continued)

Rank Plant Name City State Threshold Total tanks MACT tanks Running Avg

87 GOODYEAR TIRE AND RUBBER CO THE/JEFFERSON/JE0039N BEAUMONT TX NT 2

88 EASTMAN CHEMICAL COMPANY/HARRISON/HH0042M NT 12

89 E.I. DU PONT DE NEMOURS AND COMPANY/VICTORIA/VC0008Q VICTORIA TX NT 16 2

90 ANGUS - STERLINGTON OPERATIONS STERLINGTON LA NT 14

91 BAYER CORPORATION/CHAMBERS/CI0016S BAYTOWN TX NT 1

92 Rohm & Haas Texas, Rohm & Haas Lone Star, RohMax Deer Park TX NT 1

93 Buffalo Color Company Buffalo NY NT 3

94 Uniroyal Chemical Co., Inc. Naugatuck CT NT 4

95 Witco Corporation Mapleton IL. NT 1

96 Hickson DanChem Corporation Danville VA NT 3

97 The C. P. Hall Company Bedford Park IL NT 3

98 Niacet Corporation Niagara Falls NY NT 2

99 E.I. DU PONT DE NEMOURS & COMPANY/HARRIS/HG0218K PASADENA TX NT 18

100 The Procter & Gamble Manufacturing Company Sacramento CA NT 2

101 Reilly Industries, Inc. Indianapolis IN NT 80 3

102 Abemarle Coporation Orangeburg SC NT 13 1

103 Kalama Chemical, Inc. Kalama WA NT 1

104 The Lubrizol Corporation - Deer Park Plant Deer Park TX NT 2

105 Zeeland Chemicals, Inc. Zeeland MI NT 4

106 DuPont Sabine River Works Orange TX NT 11 8

107 Blue Ash Polymer/Waterbase Plant Blue Ash OH NT 2

108 Salsbury Chemicals, Inc. Charles City IA NT 1

109 Chemol Co.,Inc. Greensboro NC NT 3

110 DuPont Mt. Clemens Plant Mt. Clemens MI NT 10

111 Great Lakes Chemical Corporation - South El Dorado AR NT 4

112 Amerchol-Edison Edison NJ NT 1

113 Henkel Corporation - Cincinnati Plant Cincinnati OH NT 1

114 Henkel Corporation - Charlotte, NC Plant Charlotte NC NT 3

115 Cincinnati Specialties,Inc. Cincinnati OH NT 1

116 Akzo Nobel Chemicals Inc., Gallipolis Ferry Plant Gallipolis Ferry WV NT 5

117 BFG Henry Plant Henry IL NT 2

118 Olin Corporation Rochester NY NT 4

119 Ashland Chemical Company - Calumet City, Specialty Products and Adhesives Calumet City IL NT 3

120 Ashland Chemical Company - Petrochem Div. - Neville Island Plant Pittsburgh PA NT 26

121 Ashland Chemical Company - Ashtabula Composite Polymers Ashtabula OH NT 14

122 Ashland Chemical Company - Composite Polymers Div. - Bartow Manufacturing

Facility

Bartow FL NT 8

123 Dow Corning Corporation - Midland Plant Midland MI NT 3

124 3V Inc. Georgetown SC NT 22

125 Hercules Incorporated - Jefferson Plant West Elizabeth PA NT 9

126 Allco Chemical Corporation - Jayhawk Plant Galena KS NT 2

127 Hercules - Brunswick Plant Brunswick GA NT 1

128 Hilton Davis Co. Cincinnati OH NT 5
Att.1-4

MACT Floor Ranking of Facilities

(continued)

Rank Plant Name City State Threshold Total tanks MACT tanks Running Avg

129 W.G. Krummrich Plant Sauget IL NT 2

130 Ashland Chemical Company - Jacksonville, AR - Composite Polymers Jacksonville AR NT 9 7

131 WESTVACO DE RIDDER LA NT 9

132 Ashland Chemical Company - Composite Polymers Div. - Colton Facility Colton CA NT 17 15
ATTACHMENT 2:

MACT Floor Impacts for

• Vertical tanks associated with batch processes

• Vertical tanks associated with continuous processes

• Horizontal tanks associated with batch processes
Att.2-1

Vertical Tanks =>10,000 gal. with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure (psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

1 4 T02 38,000 1.70 1,752 Scrubber 0 1,752 1,664 $13,414 $2,648 $3,182

2 4 T03 38,000 1.40 990 Scrubber 0 990 941 $13,414 $2,720 $5,783

3 4 T01 38,000 1.10 4,141 Scrubber 0 4,141 3,934 $13,414 $2,421 $1,231

4 6 6 15,000 1.08 1,641 0 1,641 1,559 $9,627 $1,864 $2,392

5 6 7 15,000 1.08 1,641 0 1,641 1,559 $9,627 $1,864 $2,392

6 10 Tank 18 38,000 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025

7 10 Tank 29 14,000 1.11 551 0 551 523 $9,587 $1,959 $7,491

8 10 Tank 27 38,000 2.02 2,811 Scrubber 0 2,811 2,670 $13,414 $2,547 $1,908

9 10 Tank 26 38,000 2.02 1,694 Scrubber 0 1,694 1,609 $13,414 $2,653 $3,298

10 10 Tank 25 38,000 2.02 1,694 Scrubber 0 1,694 1,609 $13,414 $2,653 $3,298

11 10 Tank 24 38,000 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025

12 10 Tank 19 38,000 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025

13 10 Tank 32 12,000 2.49 1,109 0 1,109 1,053 $8,947 $1,772 $3,365

14 10 Tank 15 14,000 1.29 705 0 705 669 $9,587 $1,944 $5,808

15 10 Tank 13 14,000 1.06 616 0 616 585 $9,587 $1,953 $6,677

16 10 Tank 11 14,000 1.29 262 0 262 248 $9,587 $1,986 $15,988

17 10 Tank 09 23,000 1.29 1,146 0 1,146 1,089 $11,019 $2,203 $4,046

18 10 Tank 01 21,000 1.29 504 0 504 479 $10,953 $2,250 $9,401

19 10 Tank 20 14,000 2.02 1,082 0 1,082 1,028 $9,587 $1,908 $3,711

20 11 TK-0370 24,322 9.50 199 0 199 189 $11,061 $2,302 $24,296

21 11 TK-0930 12,770 1.30 151 0 151 143 $8,981 $1,870 $26,091

22 11 TK-0430 12,886 1.50 419 0 419 398 $8,986 $1,845 $9,264

23 11 TK-0380 24,322 1.00 44 0 44 42 $11,061 $2,316 $110,682

24 11 TK-0014 24,332 2.50 611 0 611 580 $11,061 $2,263 $7,800

25 11 TK-0010 24,583 1.59 1,755 0 1,755 1,667 $11,069 $2,156 $2,586

26 11 TK-0080 117,600 1.20 336 0 336 319 $19,001 $3,955 $24,770

27 11 TK-0011 24,332 2.50 92 0 92 87 $11,061 $2,312 $53,012

28 12 T-528 25,000 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

29 12 T-521 79,000 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160

30 12 T-522 25,000 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

31 12 T-523 25,000 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

32 12 T-524 25,000 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

33 12 T-525 25,000 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

34 12 T-527 25,000 1.70 1,999 Scrubber 0 1,999 1,899 $11,391 $2,200 $2,317

35 12 T-529 25,000 1.70 736 Scrubber 0 736 699 $11,391 $2,320 $6,633

36 12 T-530 79,000 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160

37 12 T-552 65,000 1.70 3,007 Scrubber 0 3,007 2,856 $15,667 $3,001 $2,101

38 12 T-507 12,000 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844

39 12 T-526 25,000 1.70 736 Scrubber 0 736 699 $11,391 $2,320 $6,633

40 12 T-382 100,000 3.15 10,350 Flare 99 104 0 $0 $0 $0

41 12 T-352 11,000 3.15 1,898 Flare 99 19 0 $0 $0 $0

42 12 T-353 30,000 3.15 3,737 Flare 99 37 0 $0 $0 $0

43 12 T-508 12,000 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844

44 12 T-358 14,500 3.15 3,326 Flare 99 33 0 $0 $0 $0
Att.2-2

Vertical Tanks =>10,000 gal. with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure (psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

45 12 T-501 37,000 1.70 472 Scrubber 0 472 449 $13,389 $2,764 $12,318

46 12 T-502 37,000 1.70 2,704 Scrubber 0 2,704 2,569 $13,389 $2,552 $1,987

47 12 T-503 37,000 1.70 2,704 Scrubber 0 2,704 2,569 $13,389 $2,552 $1,987

48 12 T-504 37,000 1.70 1,832 Scrubber 0 1,832 1,740 $13,389 $2,635 $3,029

49 12 T-505 37,000 1.70 1,832 Scrubber 0 1,832 1,740 $13,389 $2,635 $3,029

50 12 T-506 12,000 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844

51 12 T-520 79,000 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160

52 12 T-354 30,000 3.15 3,737 Flare 99 37 0 $0 $0 $0

53 15 S-125 16,075 1.00 1,513 0 1,513 1,438 $9,669 $1,885 $2,622

54 15 S-126 19,000 7.70 2,263 0 2,263 2,150 $10,330 $1,952 $1,816

55 15 S-127 19,000 7.70 2,263 0 2,263 2,150 $10,330 $1,952 $1,816

56 15 S-303 20,000 7.70 18,745 0 18,745 17,808 $10,365 $394 $44

57 15 S-63 14,838 2.00 2,291 0 2,291 2,176 $9,620 $1,801 $1,655

58 25 206 12,000 1.87 1,024 Condenser 95 51 0 $0 $0 $0

59 27 methanol 15,000 1.95 598 0 598 568 $9,627 $1,963 $6,909

60 29 T-14 24,000 1.10 252 0 252 239 $11,051 $2,294 $19,184

61 29 T-19 45,800 1.88 429 0 429 408 $13,846 $2,864 $14,051

62 29 T-3 23,192 2.30 708 0 708 672 $11,025 $2,246 $6,682

63 29 T-4 23,192 1.88 429 0 429 408 $11,025 $2,272 $11,147

64 29 T-5 23,192 1.40 411 0 411 391 $11,025 $2,274 $11,646

65 29 T-8 45,800 1.88 429 0 429 408 $13,846 $2,864 $14,051

66 29 T-9 45,800 1.88 429 0 429 408 $13,846 $2,864 $14,051

67 29 T-13 24,000 1.10 252 0 252 239 $11,051 $2,294 $19,184

68 31 210/3025 10,000 1.80 804 0 804 764 $8,856 $1,782 $4,665

69 31 340/3011 12,700 1.50 1,154 0 1,154 1,096 $8,978 $1,774 $3,237

70 31 333/3001 42,800 1.92 1,863 0 1,863 1,770 $13,222 $2,597 $2,934

71 31 313/3004 307,000 1.92 10,995 0 10,995 10,445 $26,103 $4,432 $849

72 31 242/3001 12,700 1.50 989 0 989 940 $8,978 $1,790 $3,810

73 31 242/3002 12,700 1.50 989 0 989 940 $8,978 $1,790 $3,810

74 33 209 10,000 1.90 329 0 329 313 $8,856 $1,827 $11,690

75 33 646 20,000 1.30 44 0 44 41 $10,365 $2,170 $104,695

76 33 682 20,000 1.90 196 0 196 186 $10,365 $2,156 $23,197

77 34 3202F 15,000 1.02 1,512 Condenser 100 8 0 $0 $0 $0

78 36 RM14 30,500 2.40 5,143 0 5,143 4,885 $11,797 $1,987 $813

79 36 RTK34 15,000 1.93 320 0 320 304 $9,627 $1,989 $13,073

80 38 102 15,000 2.40 3,865 0 3,865 3,672 $9,627 $1,653 $900

81 41 115 12,400 1.40 290 Thermal 93 21 6 $9,274 $1,945 $609,402

82 41 149 10,600 2.20 2,295 0 2,295 2,180 $8,884 $1,646 $1,510

83 41 199 15,300 2.20 3,035 0 3,035 2,883 $9,639 $1,734 $1,203

84 41 CR-164 15,950 2.20 4,103 0 4,103 3,898 $9,664 $1,638 $840

85 41 CR-166 15,950 2.20 4,040 0 4,040 3,838 $9,664 $1,644 $857

86 42 160 13,000 1.22 656 0 656 623 $9,545 $1,940 $6,228

87 42 180 10,600 1.80 341 0 341 324 $8,884 $1,831 $11,289

88 43 5102 10,000 1.35 1,912 0 1,912 1,817 $8,856 $1,676 $1,845
Att.2-3

Vertical Tanks =>10,000 gal. with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure (psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

89 43 5103 10,000 1.53 1,379 0 1,379 1,310 $8,856 $1,727 $2,637

90 43 5101 10,000 1.35 1,912 0 1,912 1,817 $8,856 $1,676 $1,845

91 43 1360 20,000 1.58 580 0 580 551 $10,365 $2,119 $7,688

92 43 1210 20,000 1.17 725 0 725 689 $10,365 $2,106 $6,112

93 43 1200 20,000 3.23 1,108 0 1,108 1,052 $10,365 $2,069 $3,932

94 43 1130 30,000 3.23 2,555 0 2,555 2,427 $11,783 $2,229 $1,837

95 43 1060 20,000 2.73 1,524 0 1,524 1,447 $10,365 $2,030 $2,805

96 43 1030 30,000 3.52 3,823 0 3,823 3,632 $11,783 $2,109 $1,161

97 43 1020 30,000 3.23 2,555 0 2,555 2,427 $11,783 $2,229 $1,837

98 43 1010 30,000 2.73 2,545 0 2,545 2,418 $11,783 $2,230 $1,844

99 43 1150 20,000 1.08 400 0 400 380 $10,365 $2,137 $11,260

100 44 1982-05 13,000 1.86 362 Thermal 99 4 0 $0 $0 $0

101 44 1982-06 15,000 1.86 990 Thermal 99 10 0 $0 $0 $0

102 44 1984-25 15,000 1.86 1,544 Thermal 99 15 0 $0 $0 $0

103 44 1987-35 13,000 1.86 567 Thermal 99 6 0 $0 $0 $0

104 44 1988-15 15,000 1.86 382 Thermal 99 4 0 $0 $0 $0

105 45 T-1534 30,000 1.28 656 Scrubber 0 656 623 $12,093 $2,475 $7,941

106 45 T-596 20,000 1.54 728 0 728 692 $10,365 $2,105 $6,083

107 45 T-1141 20,000 1.54 1,039 0 1,039 987 $10,365 $2,076 $4,207

108 45 T-833 12,000 4.84 1,805 Scrubber 0 1,805 1,714 $9,257 $1,771 $2,066

109 48 VS 2704 30,000 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931

110 48 VS 703 30,000 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931

111 48 VS 704 30,000 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931

112 52 T-2431 25,400 1.00 2,564 0 2,564 2,436 $11,649 $2,200 $1,806

113 52 T-2457 16,632 3.25 3,721 0 3,721 3,535 $10,244 $1,796 $1,016

114 53 11-211 11,000 2.50 509 0 509 483 $8,903 $1,819 $7,529

115 53 11-235 11,000 2.38 349 0 349 331 $8,903 $1,835 $11,082

116 53 16-237 16,000 1.97 93 0 93 88 $9,666 $2,019 $45,814

117 56 91-1339 25,000 2.40 338 0 338 321 $11,082 $2,293 $14,266

118 57 ALA07 13,382 1.95 307 0 307 291 $9,561 $1,977 $13,572

119 57 ALA05/4E 14,015 1.20 2,407 0 2,407 2,287 $9,587 $1,783 $1,559

120 57 ALA01B 10,872 1.20 398 Carbon 99 4 0 $0 $0 $0

121 57 ALA01A 10,872 1.20 398 Carbon 99 4 0 $0 $0 $0

122 60 Tank 61 19,000 2.00 1,225 0 1,225 1,164 $10,330 $2,051 $3,525

123 60 Tank 64 19,000 3.00 1,603 0 1,603 1,523 $10,330 $2,015 $2,647

124 60 Tank 73 19,000 2.00 723 0 723 686 $10,330 $2,099 $6,116

125 63 V-4 15,000 1.05 3,148 Condenser 90 315 157 $9,936 $2,069 $26,287

126 63 V-54 15,000 2.85 3,546 0 3,546 3,369 $9,627 $1,683 $999

127 63 V-53 15,000 2.85 4,448 0 4,448 4,225 $9,627 $1,597 $756

128 63 V-52 15,000 13.63 4,649 0 4,649 4,416 $9,627 $1,578 $715

129 63 V-51 15,000 2.46 1,123 0 1,123 1,067 $9,627 $1,913 $3,586

130 63 V-50 15,000 13.63 2,935 0 2,935 2,788 $9,627 $1,741 $1,249

131 63 V-5 15,000 1.55 595 0 595 565 $9,627 $1,963 $6,947

132 63 V-48 15,000 3.01 3,555 0 3,555 3,378 $9,627 $1,682 $996
Att.2-4

Vertical Tanks =>10,000 gal. with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure (psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

133 63 V-45 10,000 6.79 6,160 Combination 100 6 0 $0 $0 $0

134 63 V-35 15,000 2.83 401 Flare 98 8 0 $0 $0 $0

135 63 V-13 15,000 1.37 1,376 Flare 98 28 0 $0 $0 $0

136 63 V-32 15,000 2.61 2,023 Flare 98 40 0 $0 $0 $0

137 63 V-29 15,000 2.87 2,217 Flare 98 44 0 $0 $0 $0

138 63 V-28 13,500 1.48 2,424 Flare 98 48 0 $0 $0 $0

139 63 V-27 15,000 2.89 3,303 Flare 98 66 0 $0 $0 $0

140 63 V-26 15,000 2.89 3,303 Flare 98 66 0 $0 $0 $0

141 63 V-22 15,000 1.40 74 Flare 98 1 0 $0 $0 $0

142 63 V-18 25,000 1.86 1,963 Flare 98 39 0 $0 $0 $0

143 63 V-16 12,000 1.78 1,983 Flare 98 40 0 $0 $0 $0

144 63 V-15 12,000 1.86 1,270 Flare 98 25 0 $0 $0 $0

145 63 V-33 15,000 6.40 437 0 437 415 $9,627 $1,978 $9,526

146 63 V-47 15,000 3.01 1,557 0 1,557 1,479 $9,627 $1,872 $2,531

147 64 T027 49,073 1.86 693 0 693 658 $13,920 $2,855 $8,677

148 65 VT-1 25,300 3.66 2,416 0 2,416 2,295 $11,645 $2,214 $1,929

149 65 VT-201 25,300 3.66 2,416 0 2,416 2,295 $11,645 $2,214 $1,929

150 67 ST-900A 29,900 2.25 674 Scrubber 0 674 640 $12,090 $2,472 $7,720

151 67 ST-900B 19,570 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792

152 67 ST-918 11,290 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

153 67 ST-919 11,290 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

154 67 ST-920 11,290 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

155 67 ST-921 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

156 67 ST-924 11,290 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

157 67 ST-981 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

158 67 ST-967 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

159 67 ST-968 16,875 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460

160 67 ST-970 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

161 67 ST-971 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

162 67 ST-972 16,875 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460

163 67 ST-973 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

164 67 ST-964 16,875 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460

165 67 ST-975 16,875 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460

166 67 ST-987 19,570 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792

167 67 ST-982 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

168 67 ST-983 16,800 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

169 67 ST-984 21,000 2.25 545 Scrubber 0 545 518 $11,263 $2,311 $8,926

170 67 ST-985 21,000 2.25 545 Scrubber 0 545 518 $11,263 $2,311 $8,926

171 67 ST-986 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

172 67 ST-990 13,500 2.25 431 Scrubber 0 431 409 $9,876 $2,031 $9,928

173 67 ST-923 24,670 2.25 599 Scrubber 0 599 569 $11,381 $2,331 $8,193

174 67 ST-974 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

175 67 ST-929 16,800 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

176 67 ST-994 10,600 2.25 385 Scrubber 0 385 365 $9,194 $1,892 $10,359
Att.2-5

Vertical Tanks =>10,000 gal. with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure (psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

177 67 ST-925 11,290 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

178 67 ST-922 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

179 67 ST-926 16,608 2.25 479 Scrubber 0 479 455 $10,553 $2,168 $9,532

180 67 ST-960 15,277 2.25 458 Scrubber 0 458 435 $9,947 $2,043 $9,384

181 67 ST-928 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

182 67 ST-934 11,290 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

183 67 ST-935 11,290 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

184 67 ST-950 19,570 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792

185 67 ST-927 12,080 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

186 67 ST-951 19,570 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792

187 67 ST-940 16,800 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

188 67 ST-949 16,800 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

189 67 ST-948 16,800 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

190 67 ST-947 16,800 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

191 67 ST-945 16,800 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

192 67 ST-941 16,800 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

193 68 ST6 16,000 1.80 291 0 291 277 $9,666 $2,000 $14,461

194 68 ST7 12,000 1.90 177 0 177 168 $8,947 $1,860 $22,148

195 68 ST1 500,000 1.70 42,893 IFR 95 2,145 0 $0 $0 $0

196 71 1 35,251 2.40 1,451 EFR 95 73 0 $0 $0 $0

197 73 N110 10,000 2.01 495 0 495 471 $8,856 $1,811 $7,696

198 73 T326 20,000 1.06 1,139 Scrubber 0 1,139 1,082 $10,674 $2,131 $3,939

199 74 Y-210 15,300 2.45 426 0 426 404 $9,639 $1,982 $9,803

200 75 D501 15,000 1.90 517 0 517 491 $9,627 $1,971 $8,029

201 78 SN-711 18,650 10.10 11,673 0 11,673 11,089 $10,318 $1,056 $190

202 82 AT-3 10,000 1.91 253 0 253 240 $8,856 $1,834 $15,276

203 82 AT-4 10,000 1.91 175 0 175 166 $8,856 $1,841 $22,154

204 82 AT-6 14,000 1.91 216 0 216 206 $9,587 $1,991 $19,361

205 83 597 10,500 1.90 635 Condenser 90 64 32 $9,189 $1,925 $121,220

206 83 606 25,000 1.90 1,719 Condenser 90 172 86 $11,391 $2,381 $55,408

207 86 T-18 16,500 1.93 593 0 593 563 $10,239 $2,092 $7,428

208 87 2T116 (# 781) 10,000 1.39 122 0 122 116 $8,856 $1,846 $31,888

209 87 4T013 (# 690) 10,000 1.93 194 0 194 185 $8,856 $1,839 $19,927

210 89 T-1121 10,053 2.40 290 0 290 275 $8,858 $1,831 $13,297

211 90 A-177 25,000 3.39 1,058 Incinerator 99 11 0 $0 $0 $0

212 90 C-133 49,000 2.27 5,942 Absorber 0 5,942 5,645 $14,228 $2,420 $857

213 90 B-172 10,100 2.03 704 Incinerator 99 7 0 $0 $0 $0

214 90 A-165 49,000 2.03 1,128 Incinerator 99 11 0 $0 $0 $0

215 90 C-132 49,000 2.27 5,942 Absorber 0 5,942 5,645 $14,228 $2,420 $857

216 91 T01 12,000 1.80 664 0 664 631 $8,947 $1,814 $5,750

217 92 304 15,150 1.51 337 0 337 321 $9,633 $1,989 $12,410

218 92 779 10,152 1.09 255 0 255 242 $8,863 $1,835 $15,153

219 92 778 10,152 1.09 248 0 248 235 $8,863 $1,836 $15,597

220 92 777 10,112 1.09 279 0 279 265 $8,861 $1,833 $13,847
Att.2-6

Vertical Tanks =>10,000 gal. with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure (psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

221 92 727 10,038 1.09 166 0 166 158 $8,857 $1,842 $23,310

222 92 720 10,081 1.10 213 0 213 202 $8,860 $1,839 $18,205

223 92 701 10,362 1.09 230 0 230 218 $8,873 $1,840 $16,856

224 92 622 29,762 1.05 313 0 313 297 $11,777 $2,441 $16,417

225 92 620 29,762 1.11 375 0 375 357 $11,777 $2,435 $13,659

226 92 260 39,317 8.06 8,992 0 8,992 8,542 $13,137 $1,902 $445

227 92 254 19,725 1.35 913 IFR 95 46 0 $0 $0 $0

228 92 253 19,725 1.61 461 0 461 438 $10,355 $2,129 $9,715

229 92 252 19,725 1.61 423 0 423 402 $10,355 $2,132 $10,612

230 92 241 19,731 1.35 380 0 380 361 $10,356 $2,137 $11,854

231 92 216 19,691 1.35 599 0 599 569 $10,354 $2,115 $7,428

232 92 212 19,677 1.35 764 0 764 726 $10,354 $2,100 $5,784

233 92 211 19,677 1.35 516 0 516 491 $10,354 $2,123 $8,654

234 92 111 131,750 1.13 1,996 0 1,996 1,896 $19,755 $3,955 $4,172

235 92 792 14,867 1.09 258 0 258 245 $9,622 $1,994 $16,294

236 92 261 39,317 5.78 5,291 0 5,291 5,026 $13,137 $2,254 $897

237 93 TK-592 20,000 3.20 1,189 Flare 98 24 0 $0 $0 $0

238 105 2770595 13,000 5.11 5,336 0 5,336 5,069 $9,545 $1,496 $590

239 106 T-08 19,080 3.54 2,338 0 2,338 2,221 $10,333 $1,946 $1,752

240 106 T-753 19,080 4.04 715 0 715 679 $10,333 $2,100 $6,185

241 107 T-443 10,030 8.50 1,982 Scrubber 0 1,982 1,883 $9,167 $1,735 $1,843

242 109 V129B 11,000 1.90 351 0 351 333 $8,903 $1,834 $11,013

243 110 V-334 12,500 1.87 206 0 206 196 $8,969 $1,862 $18,988

244 110 V-372 12,500 1.87 206 0 206 196 $8,969 $1,862 $18,988

245 110 V-374 12,500 1.87 206 0 206 196 $8,969 $1,862 $18,988

246 110 V-376 12,500 1.87 206 0 206 196 $8,969 $1,862 $18,988

247 112 03TK305B 14,700 1.96 290 0 290 276 $9,615 $1,990 $14,429

248 112 04TK433 23,700 2.34 1,281 0 1,281 1,217 $11,041 $2,195 $3,606

249 112 03V381 16,000 1.12 319 Condenser 319 303 $9,975 $2,063 $13,630

250 112 02TK101 16,500 2.34 978 0 978 929 $10,239 $2,055 $4,424

251 112 03V310 18,000 2.16 229 Condenser 229 218 $10,604 $2,203 $20,231

252 112 03V309 16,000 1.21 139 Condenser 139 132 $9,975 $2,080 $31,605

253 112 03TK310 16,000 1.12 319 Condenser 319 303 $9,975 $2,063 $13,630

254 112 02TK254 18,700 1.96 355 0 355 338 $10,320 $2,131 $12,626

255 112 02TK150 15,000 1.68 435 0 435 413 $9,627 $1,978 $9,568

256 112 02TK104 19,200 2.11 2,723 0 2,723 2,587 $10,337 $1,910 $1,477

257 112 02TK102 19,400 2.29 1,381 0 1,381 1,312 $10,344 $2,039 $3,108

258 112 02TK103 48,000 1.96 904 0 904 858 $13,896 $2,830 $6,593

259 112 02TK255 18,700 2.16 245 0 245 233 $10,320 $2,142 $18,398

260 119 T-128 11,900 1.87 246 0 246 234 $8,943 $1,853 $15,871

261 119 T-114 12,700 2.35 880 0 880 836 $8,978 $1,800 $4,308

262 124 Tank 15 15,000 1.38 249 0 249 237 $9,627 $1,996 $16,857

263 124 Tank 30 CS2 15,000 6.27 8,366 0 8,366 7,947 $9,627 $1,225 $308

264 125 101 14,000 1.95 255 Condenser 71 74 61 $9,896 $2,070 $67,706
Att.2-7

Vertical Tanks =>10,000 gal. with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure (psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

265 133 PT0019 12,900 7.11 1,914 Afterburner 99 19 0 $0 $0 $0

266 133 PT0020 291,000 1.63 3,443 Afterburner 99 34 0 $0 $0 $0

267 133 PT0083 12,900 4.65 1,314 Afterburner 99 13 0 $0 $0 $0

268 134 TF-42 50,000 4.60 3,194 0 3,194 3,034 $13,940 $2,621 $1,728

269 134 TF-49 50,000 3.23 1,676 0 1,676 1,592 $13,940 $2,765 $3,474

270 134 TF-32 50,000 2.26 3,053 0 3,053 2,901 $13,940 $2,635 $1,817

271 135 TF-13A 20,000 2.90 394 0 394 374 $10,365 $2,137 $11,414

272 135 TF-2 50,000 2.07 1,701 0 1,701 1,616 $13,940 $2,763 $3,419

273 136 101-A-03 50,000 3.53 1,116 0 1,116 1,060 $13,940 $2,819 $5,318

274 137 C-10 15,350 1.35 486 0 486 462 $9,641 $1,976 $8,558

275 137 C-11 15,350 1.36 489 0 489 465 $9,641 $1,976 $8,507

276 137 C-12 15,350 1.78 627 0 627 596 $9,641 $1,963 $6,587

277 141 CRU-#068 25,000 1.76 3,358 0 3,358 3,190 $11,082 $2,006 $1,258

278 141 CRU-#072 14,500 1.72 2,926 0 2,926 2,780 $9,607 $1,738 $1,250

279 147 3080 10,000 1.80 2,974 Boiler 99 30 0 $0 $0 $0

280 147 T-6240 17,000 2.30 35 Scrubber 0 35 33 $10,567 $2,214 $133,813

281 147 T-6250 17,000 2.30 35 Scrubber 0 35 33 $10,567 $2,214 $133,813

282 149 S404 20,000 2.35 1,210 0 1,210 1,149 $10,365 $2,060 $3,585

283 149 S405 20,000 1.66 435 0 435 414 $10,365 $2,133 $10,314

284 150 V-56 12,000 2.18 344 N2 Blkt 344 327 $9,257 $1,909 $11,683

285 150 V-57 12,000 2.18 286 N2 Blkt 286 272 $9,257 $1,915 $14,098

286 150 V-53 12,000 2.18 189 N2 Blkt 189 179 $9,257 $1,924 $21,468

287 153 TS-11

(Meth.Rec.)

30,250 3.87 4,321 0 4,321 4,105 $11,790 $2,063 $1,005

288 153 TS-11(Textile) 25,000 4.60 5,377 0 5,377 5,108 $11,082 $1,814 $710

289 153 TS-15 (Meth.

Rec.)

30,250 3.87 4,321 0 4,321 4,105 $11,790 $2,063 $1,005

290 156 DT-09B 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743

291 156 DT-23 11,655 1.77 104 0 104 99 $8,932 $1,864 $37,637

292 156 DT-02B 10,879 1.77 469 0 469 445 $8,897 $1,822 $8,184

293 156 DT-11 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743

294 156 DT-30A 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743

295 156 DT-09C 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743

296 156 DT-08C 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743

297 156 DT-06 10,613 1.77 525 0 525 498 $8,885 $1,814 $7,280

298 156 DT-02A 10,879 1.77 562 0 562 534 $8,897 $1,813 $6,789

299 156 DT-08A 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743

300 156 DT-09A 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743

301 158 441-031 12,000 1.11 231 0 231 219 $8,947 $1,855 $16,928

302 158 445-008 12,000 1.11 231 0 231 219 $8,947 $1,855 $16,928

303 158 441-281 15,200 6.00 1,976 0 1,976 1,878 $9,635 $1,834 $1,953

304 158 441-027 12,000 6.00 1,296 0 1,296 1,231 $8,947 $1,754 $2,850

305 158 441-015 20,700 1.11 198 0 198 188 $10,943 $2,277 $24,189

306 158 422-199 13,500 1.03 101 Insulated but 101 96 $9,876 $2,062 $42,790
Att.2-8

Vertical Tanks =>10,000 gal. with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure (psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

307 158 441-452 30,500 1.11 243 0 243 231 $11,797 $2,452 $21,248

308 161 T-1 16,000 6.38 2,104 Condenser 22 1,641 1,536 $9,975 $1,939 $2,524

309 162 141-T-6 (5004) 17,625 1.76 985 0 985 936 $10,281 $2,063 $4,408

310 163 68C 12,000 8.60 2,431 0 2,431 2,310 $8,947 $1,646 $1,425

311 163 83C 15,000 5.03 1,554 0 1,554 1,476 $9,627 $1,872 $2,536

312 167 Tank 714 10,147 6.99 2,895 Condenser 86 414 269 $9,172 $1,897 $14,091

313 167 Tank 521 15,066 2.94 881 None 0 881 837 $9,939 $2,002 $4,786

Total 483,720 362,829 341,268 $2,918,341 $578,142 $3,338
Att.2-9

Horizontal Tanks with HAP Partial Pressure => 1.0 psia and Condenser Cost (MACT Floor)

Facil. # Tank ID Tank capacity

HAP partial

pressure

(psia)

Uncontrolled

HAP emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

1 28 TLI-5 26,000 9.55 23,330 Carbon adsorber 81 4,433 3,266 $50,917 $44,238 $27,088

2 28 TLI-4 12,500 9.55 11,964 Carbon adsorber 81 2,273 1,675 $50,917 $44,366 $52,978

3 20 S-6402 10,000 8.90 3,361 Scrubber 0 3,361 3,193 $32,459 $41,345 $25,901

4 167 Tank 1141 63,676 3.40 3,974 Thermal oxidizer 99 40 0 $0 $0 $0

5 167 Tank 1142 192,528 3.40 8,233 Thermal oxidizer 99 82 0 $0 $0 $0

6 167 Tank 1143 63,676 3.40 3,974 Thermal oxidizer 99 40 0 $0 $0 $0

7 167 Tank 364 54,457 2.94 3,812 Thermal oxidizer 99 38 0 $0 $0 $0

8 167 Tank 376 52,209 2.94 1,806 Thermal oxidizer 99 18 0 $0 $0 $0

9 167 Tank 1215 10,153 2.94 2,062 Thermal oxidizer 99 21 0 $0 $0 $0

10 167 Tank 377 42,336 2.94 1,701 Thermal oxidizer 99 17 0 $0 $0 $0

11 134 23-6 30,000 2.79 812 0 812 771 $30,701 $40,872 $105,977

12 161 T-16 10,750 2.78 974 0 974 926 $25,509 $40,067 $86,562

13 166 TP930 HT13 12,000 2.10 335 None 0 335 318 $31,764 $41,025 $258,132

14 166 TP930 HT-1 12,000 2.10 335 None 0 335 318 $31,764 $41,025 $258,132

15 166 TP930 HT-6 12,000 2.10 335 None 0 335 318 $31,764 $41,025 $258,132

16 137 U-8 15,000 1.95 471 0 471 447 $32,029 $41,044 $183,525

17 137 U-9 15,000 1.95 541 0 541 514 $32,029 $41,038 $159,817

18 10 Tank 05 13,000 1.93 1,037 Scrubber 0 1,037 985 $27,125 $40,189 $81,614

19 44 1340-01 11,550 1.86 167 Thermal oxidizer 99 2 0 $0 $0 $0

20 156 G-65-1 29,151 1.77 359 0 359 341 $32,376 $41,095 $240,974

21 84 T014 30,000 1.70 5,031 0 5,031 4,779 $25,037 $39,514 $16,537

22 84 T013 30,000 1.70 5,031 0 5,031 4,779 $25,037 $39,514 $16,537

23 130 T-325A 10,000 1.70 1,437 0 1,437 1,365 $24,640 $39,821 $58,329

24 141 PO-#129 15,000 1.63 749 0 749 712 $30,100 $40,701 $114,351

25 28 TS-146 12,500 1.62 243 0 243 231 $32,091 $41,047 $355,436

26 167 Tank 1219 40,218 1.61 2,537 Thermal oxidizer 99 25 0 $0 $0 $0

27 167 Tank 1119 40,218 1.61 2,537 Thermal oxidizer 99 25 0 $0 $0 $0

28 70 TA-951 45,000 1.60 1,197 Carbon adsorber 95 60 0 $0 $0 $0

29 40 TF_ST104 10,000 1.49 483 0 483 459 $30,483 $40,773 $177,807

30 87 4T003 (# 672) 10,000 1.37 263 0 263 250 $30,851 $40,840 $326,358

31 57 ALA05 240,385 1.20 5,835 0 5,835 5,543 $14,185 $37,725 $13,611

32 2 T035 25,000 1.16 2,409 0 2,409 2,288 $29,726 $40,463 $35,367

33 2 T038 25,000 1.16 2,409 0 2,409 2,288 $29,726 $40,463 $35,367

34 2 T037 25,000 1.16 2,409 0 2,409 2,288 $29,726 $40,463 $35,367

35 2 T036 25,000 1.16 2,409 0 2,409 2,288 $29,726 $40,463 $35,367

36 34 3104F 10,000 1.02 603 Condenser 99 6 0 $0 $0 $0

Total 105,161 44,344 40,342 $740,682 $979,116 $48,541
Att.2-10

Continuous Vertical Tanks with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure

(psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

1 M126 METHANOL TANK 41/MEOH 50,000 1.93 1,340 NONE 0 1,340 1,273 $13,940 $2,797 $4,394

2 M126 METHANOL TANK 41/MEOH 50,000 1.93 1,560 NONE 0 1,560 1,482 $13,940 $2,776 $3,746

3 M126 CRUDE DIBASIC ESTER 18,000 1.93 3,880 VAPOR

RECOVERY 

0 3,880 3,686 $10,604 $1,856 $1,007

4 M146 D-123 CHILLED WATER 32,000 1.93 0 NONE 0 0 0 $12,393 $2,600 $13,684,211

5 M257 FRESH METHANOL 59,000 1.93 4,640 IFR 95 232 0 $0 $0 $0

6 M257 MOTHER LIQUOR 220,000 1.93 12,000 IFR 95 600 0 $0 $0 $0

7 M257 MOTHER LIQUOR 220,000 1.93 12,000 IFR 95 600 0 $0 $0 $0

8 M257 RECOVERED METHANOL 220,000 1.93 9,560 IFR 95 478 0 $0 $0 $0

9 M257 SEAL FLUSH METHANOL 59,000 1.93 5,200 IFR 95 260 0 $0 $0 $0

10 M258 DRY METHANOL STORAGE 150,000 1.93 11,600 IFR 95 580 0 $0 $0 $0

11 M258 SPENT HEXANE STORAGE 500,000 2.93 27,200 IFR 95 1,360 0 $0 $0 $0

12 M262 HEXANE STORAGE TANKS D. 130,900 2.93 156,000 FLARE &

CONDENSER

100 468 0 $0 $0 $0

13 M262 HEXANE STORAGE TANKS D. 40,500 2.93 9,067 FLARE &

CONDENSER

100 27 0 $0 $0 $0

14 M270 TANK STORAGE/TK-401/29 10,000 2.93 2,440 NONE 0 2,440 2,318 $8,856 $1,626 $1,403

15 M270 TANK STORAGE/TK-902/03 12,000 2.93 723 NONE 0 723 687 $8,947 $1,808 $5,265

16 M270 HEXANE STORAGE 80,000 2.93 8,400 IFR 95 420 0 $0 $0 $0

17 M279 POLYMER TANK 57,000 1.93 2,782 VAPORCONDENSERS89 306 18 $14,953 $3,120 $339,869

18 M279 WASHWATER 37,000 1.93 89 NONE 0 89 85 $13,079 $2,736 $64,719

19 M279 VINYL ACETATE (B 95,000 3.54 358 VAPORCONDENSERS83 61 7 $17,857 $3,742 $1,025,768

20 M279 VINYL ACETATE (A 95,000 3.54 200 VAPORCONDENSERS83 34 4 $17,857 $3,744 $1,835,294

21 M279 VINYL ACETATE "B" DAY 158,000 1.61 4,745 NONE 0 4,745 4,508 $20,653 $3,882 $1,722

22 M279 VINYL ACETATE "A" DAY 158,000 1.61 5,765 NONE 0 5,765 5,477 $20,653 $3,785 $1,382

23 M279 VINYL "C" 375,000 1.61 8,684 NONE 0 8,684 8,249 $27,800 $5,007 $1,214

24 M279 VINYL "C" DAY 158,000 1.61 944 NONE 0 944 897 $20,653 $4,243 $9,461

25 M279 VINYL "B" 375,000 1.61 6,919 NONE 0 6,919 6,573 $27,800 $5,175 $1,575

26 M279 POLYMER TANK 57,000 1.93 7,276 VAPORCONDENSERS89 800 48 $14,953 $3,094 $128,852

27 M279 MILLION GAL VAM. 1,000,000 1.61 17,270 VAPORCONDENSERS82 3,074 393 $40,364 $8,247 $41,919

28 M279 METHYL ACETATE 84,000 1.93 9 VAPORCONDENSERS77 2 0 $17,121 $3,592 $17,844,014

29 M279 METHANOL STORAGE 210,000 1.93 883 NONE 0 883 839 $22,924 $4,726 $11,265

30 M279 INHIBITOR STORAGE 18,000 1.93 433 NONE 0 433 412 $10,295 $2,119 $10,293

31 M279 CENTRATE AND WASH 375,000 1.93 175 NONE 0 175 167 $27,800 $5,816 $69,807

32 M279 "B" PLANT CONVERTIBLE 110,000 1.93 2,386 VAPORCONDENSERS79 492 77 $18,644 $3,874 $101,031

33 M279 VINYL "A" 375,000 1.61 8,784 NONE 0 8,784 8,345 $27,800 $4,998 $1,198

34 M279 SODIUM METHYLATE 11,000 1.93 0 NONE 0 0 0 $8,903 $1,868 $3,269,217,

35 M280 B CRUDE RECEIVER 38,000 1.93 22 NONE 0 22 21 $13,105 $2,747 $267,739
Att.2-11

Continuous Vertical Tanks with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure

(psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

36 M280 NO. 4 TWKA RECEIVER 50,000 1.93 15 NONE 0 15 14 $13,940 $2,923 $404,848

37 M280 NO. 3 TWKA STORAGE TANK 500,000 1.93 2 NONE 0 2 2 $30,975 $6,498 $8,550,000

38 M280 NO. 3 TWKA RECEIVER 50,000 1.93 15 NONE 0 15 14 $13,940 $2,923 $404,848

39 M280 NO. 2 RECYCLE VA 50,000 1.61 18,716 IFR 95 936 0 $0 $0 $0

40 M280 HMI STORAGE 19,000 1.93 5 NONE 0 5 5 $10,330 $2,167 $912,421

41 M280 F CRUDE DCH STORAGE 160,000 1.93 22 NONE 0 22 21 $20,678 $4,336 $407,519

42 M280 E REWORK 160,000 1.93 4 NONE 0 4 4 $20,678 $4,338 $2,403,324

43 M280 CRUDE KA TANK - OP 104,000 1.93 18 NONE 0 18 17 $18,244 $3,826 $457,656

44 M280 BIG A CRUDE 552,000 1.93 84 NONE 0 84 80 $31,893 $6,683 $167,096

45 M280 A CRUDE RECEIVER 38,000 1.93 3 NONE 0 3 3 $13,105 $2,749 $1,702,167

46 M280 WASTE COLLECTION 11,000 1.93 0 NONE 0 0 0 $8,903 $1,868 $19,663,158

47 M280 BIG B CRUDE 552,000 1.93 8 NONE 0 8 8 $31,893 $6,690 $1,676,692

48 M280 RECYCLE AQUA COLUMN 12,000 1.93 0 NONE 0 0 0 $8,947 $1,877 $19,757,895

49 M280 WASTE ORGANIC STORAGE 18,000 1.93 215 NONE 0 215 204 $10,295 $2,139 $20,964

50 M280 VINYL ACETATE 100,000 1.61 18,716 IFR 95 936 0 $0 $0 $0

51 M281 STORAGE 12,000 2.24 60 0 60 57 $9,257 $1,936 $67,930

52 M281 STORAGE 17,000 13.29 60 0 60 57 $10,567 $2,211 $77,579

53 M281 STORAGE TANK 43 33,000 13.29 420 0 420 399 $12,730 $2,631 $13,188

54 M281 STORAGE TANK 215,000 13.29 2,300 0 2,300 2,185 $23,288 $4,667 $4,272

55 M281 REJECT 50,000 1.93 10 0 10 10 $14,250 $2,989 $629,263

56 M281 MOLTEN STORAGE 93,280 2.93 562 0 562 534 $17,829 $3,687 $13,812

57 M281 MIX TANK/ EP008T34/008T34 14,000 1.93 38 0 38 36 $9,896 $2,073 $114,848

58 M281 FLUX OIL TANK 67,600 3.16 1,528 0 1,528 1,451 $15,717 $3,152 $4,343

59 M281 CRUDE NPG 40,000 1.93 460 0 460 437 $13,464 $2,781 $12,728

60 M281 MOLTEN STORAGE 93,280 2.93 562 VAPOR

RECOVERY

0 562 534 $17,829 $3,687 $13,812

61 M281 TANK 25,600 13.29 240 0 240 228 $11,964 $2,487 $21,816

62 M283 HEXANE STORAGE TANK 53,000 2.93 18,000 IFR 95 900 0 $0 $0 $0

63 M283 HEXANE STORAGE TANK 160,000 2.93 22,000 IFR 95 1,100 0 $0 $0 $0

64 M289 TANK T-503/ 5T6040/5T6040 85,140 2.93 320 IFR 95 16 0 $0 $0 $0

65 M289 TANK T-502/ 5T6020/5T6020 85,140 2.93 120 IFR 95 6 0 $0 $0 $0

66 M289 TANK T-501/ 5T6010/5T6010 85,140 2.93 320 IFR 95 16 0 $0 $0 $0

67 M289 TANK 2T-502/ 5T6030/5T6030 85,140 2.93 320 IFR 95 16 0 $0 $0 $0

68 M289 TANK 2T-503/ 5T6050/5T6050 85,140 2.93 320 IFR 95 16 0 $0 $0 $0

69 M293 STORAGE 451,000 1.68 0 NONE 0 0 0 $30,061 $6,307 $33,194,737

70 M293 STORAGE 24,000 1.68 507 NONE 0 507 482 $11,051 $2,270 $9,422

71 M300 TANK 21,000 1.93 318 NONE 0 318 302 $10,953 $2,268 $15,015

72 M300 TANK 109,000 2.93 200 IFR 95 10 0 $0 $0 $0

73 M300 TANK 42,000 2.06 81 NONE 0 81 77 $13,203 $2,762 $71,787

74 M306 TANK/2A/2A 20,700 2.93 1,280 NONE 0 1,280 1,216 $10,943 $2,174 $3,576

75 M306 TANK/2B/2B 20,700 2.93 1,280 NONE 0 1,280 1,216 $10,943 $2,174 $3,576

76 M330 POLY ETHYLENE PLANT 15,200 2.32 8,868 NONE 0 8,868 8,425 $9,635 $1,179 $280

77 M343 R-1372 SCRUBBER/TKR372 10,000 1.93 12 NONE 0 12 11 $8,856 $1,857 $325,789
Att.2-12

Continuous Vertical Tanks with HAP Partial Pressure => 1.0 psia and IFR Control Cost (MACT Floor)

(continued)

Facil. # Tank ID

Tank

capacity

HAP partial

pressure

(psia)

Uncontrolled

HAP

emissions

(lb/yr) Control device

Control

efficiency

Baseline

HAP

emissions

(lb/yr)

HAP

reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

78 M358 2-9,800 GALLON ROSIN 19,600 1.93 3,882 None 0 3,882 3,688 $10,351 $1,803 $978

79 M358 RESIN PRODUCT 30,000 1.93 3,882 None 0 3,882 3,688 $11,783 $2,103 $1,140

80 M358 3-150,000 GALLON POND 450,000 1.93 4,500 None 0 4,500 4,275 $30,053 $5,878 $2,750

81 M358 RXN. OIL, HEADS OR PITCH 20,000 1.93 4,500 None 0 4,500 4,275 $10,365 $1,747 $817

82 M358 2-16,900 GALLON RESIN 33,800 1.93 7,765 None 0 7,765 7,377 $12,442 $1,873 $508

83 M358 NEW ROSIN TANK, ST-25, PT 15,200 1.93 3,882 None 0 3,882 3,688 $9,635 $1,653 $896

84 M44 TANKS 360 AND 250,000 1.93 7,938 VAPORCONDENSERS68 2,540 686 $24,761 $4,980 $14,523

85 M44 TANKS 25,000 1.68 5,040 SCRUBBER 0 50 48 $11,391 $1,911 $79,825

86 M44 TANKS 25,000 3.62 766 NONE 0 766 728 $11,082 $2,252 $6,189

87 M44 TANKS 25,000 1.68 1,450 NONE 0 1,450 1,378 $11,082 $2,187 $3,175

88 M44 TANKS 37,000 1.68 1,448 NONE 0 1,448 1,376 $13,079 $2,607 $3,790

89 M44 TANK 100,000 1.93 14,600 FLARE-WASTE 98 292 0 $0 $0 $0

90 M44 TANK 48,000 1.93 113 VAPORCONDENSERS68 36 10 $14,205 $2,977 $612,551

91 M44 T-352,353,&354/

FB03T0354/EB

30,000 1.93 18 PROCESS

CHANGE

0 18 17 $12,093 $2,535 $296,491

92 M44 T-352,353,&354/

FB03T0354/EB

30,000 1.93 130 NONE 0 130 124 $11,783 $2,460 $39,838

93 M44 1100 PROCESS 10,000 6.93 2,916 NONE 0 2,916 2,770 $8,856 $1,581 $1,141

94 M44 TANKS 20,000 2.06 218 NONE 0 218 207 $10,365 $2,154 $20,782

95 M44 1100 PROCESS 10,000 1.38 108 NONE 0 108 103 $8,856 $1,848 $36,023

Total: 494,501 118,495 98,031 $1,170,333 $234,836 $4,791

National Total: 989,001 236,990 196,062 $2,340,666 $469,672
ATTACHMENT 3:

Regulatory Alternative Impacts for

• Vertical tanks associated with batch processes

• Vertical tanks associated with continuous processes

• Horizontal tanks associated with batch processes
Att. 3-1

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

1 4 T01 1.10 4,141 Scrubber 0 4,141 3,934 $13,414 $2,421 $1,231

2 4 T02 1.70 1,752 Scrubber 0 1,752 1,664 $13,414 $2,648 $3,182

3 4 T03 1.40 990 Scrubber 0 990 941 $13,414 $2,720 $5,783

4 6 6 1.08 1,641 0 1,641 1,559 $9,627 $1,864 $2,392

5 6 7 1.08 1,641 0 1,641 1,559 $9,627 $1,864 $2,392

6 10 Tank 01 1.29 504 0 504 479 $10,953 $2,250 $9,401

7 10 Tank 07 0.52 1,331 0 1,331 1,264 $11,019 $2,185 $3,456

8 10 Tank 09 1.29 1,146 0 1,146 1,089 $11,019 $2,203 $4,046

9 10 Tank 11 1.29 262 0 262 248 $9,587 $1,986 $15,988

10 10 Tank 13 1.06 616 0 616 585 $9,587 $1,953 $6,677

11 10 Tank 15 1.29 705 0 705 669 $9,587 $1,944 $5,808

12 10 Tank 16 0.54 433 0 433 412 $9,587 $1,970 $9,571

13 10 Tank 18 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025

14 10 Tank 19 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025

15 10 Tank 20 2.02 1,082 0 1,082 1,028 $9,587 $1,908 $3,711

16 10 Tank 21 0.76 615 0 615 584 $11,019 $2,253 $7,714

17 10 Tank 23 0.76 628 0 628 597 $11,019 $2,252 $7,544

18 10 Tank 24 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025

19 10 Tank 25 2.02 1,694 Scrubber 0 1,694 1,609 $13,414 $2,653 $3,298

20 10 Tank 26 2.02 1,694 Scrubber 0 1,694 1,609 $13,414 $2,653 $3,298

21 10 Tank 27 2.02 2,811 Scrubber 0 2,811 2,670 $13,414 $2,547 $1,908

22 10 Tank 28 0.91 344 0 344 327 $9,587 $1,979 $12,110

23 10 Tank 29 1.11 551 0 551 523 $9,587 $1,959 $7,491

24 10 Tank 30 0.60 998 0 998 948 $9,587 $1,916 $4,041

25 10 Tank 32 2.49 1,109 0 1,109 1,053 $8,947 $1,772 $3,365

26 11 TK-0010 1.59 1,755 0 1,755 1,667 $11,069 $2,156 $2,586

27 11 TK-0011 2.50 92 0 92 87 $11,061 $2,312 $53,012

28 11 TK-0014 2.50 611 0 611 580 $11,061 $2,263 $7,800

29 11 TK-0020 0.70 25 0 25 24 $11,069 $2,320 $192,751

30 11 TK-0080 1.20 336 0 336 319 $19,001 $3,955 $24,770

31 11 TK-0130 0.50 12 0 12 11 $8,947 $1,876 $336,535

32 11 TK-0370 9.50 199 0 199 189 $11,061 $2,302 $24,296

33 11 TK-0380 1.00 44 0 44 42 $11,061 $2,316 $110,682

34 11 TK-0430 1.50 419 0 419 398 $8,986 $1,845 $9,264

35 11 TK-0930 1.30 151 0 151 143 $8,981 $1,870 $26,091

36 12 T-352 3.15 1,898 Flare 99 19 0 $0 $0 $0

37 12 T-353 3.15 3,737 Flare 99 37 0 $0 $0 $0

38 12 T-354 3.15 3,737 Flare 99 37 0 $0 $0 $0

39 12 T-358 3.15 3,326 Flare 99 33 0 $0 $0 $0

40 12 T-382 3.15 10,350 Flare 99 104 0 $0 $0 $0

41 12 T-501 1.70 472 Scrubber 0 472 449 $13,389 $2,764 $12,318

42 12 T-502 1.70 2,704 Scrubber 0 2,704 2,569 $13,389 $2,552 $1,987

43 12 T-503 1.70 2,704 Scrubber 0 2,704 2,569 $13,389 $2,552 $1,987

44 12 T-504 1.70 1,832 Scrubber 0 1,832 1,740 $13,389 $2,635 $3,029

45 12 T-505 1.70 1,832 Scrubber 0 1,832 1,740 $13,389 $2,635 $3,029
Att. 3-2

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

46 12 T-506 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844

47 12 T-507 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844

48 12 T-508 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844

49 12 T-520 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160

50 12 T-521 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160

51 12 T-522 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

52 12 T-523 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

53 12 T-524 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

54 12 T-525 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

55 12 T-526 1.70 736 Scrubber 0 736 699 $11,391 $2,320 $6,633

56 12 T-527 1.70 1,999 Scrubber 0 1,999 1,899 $11,391 $2,200 $2,317

57 12 T-528 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627

58 12 T-529 1.70 736 Scrubber 0 736 699 $11,391 $2,320 $6,633

59 12 T-530 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160

60 12 T-552 1.70 3,007 Scrubber 0 3,007 2,856 $15,667 $3,001 $2,101

61 15 S-125 1.00 1,513 0 1,513 1,438 $9,669 $1,885 $2,622

62 15 S-126 7.70 2,263 0 2,263 2,150 $10,330 $1,952 $1,816

63 15 S-127 7.70 2,263 0 2,263 2,150 $10,330 $1,952 $1,816

64 15 S-303 7.70 18,745 0 18,745 17,808 $10,365 $394 $44

65 15 S-63 2.00 2,291 0 2,291 2,176 $9,620 $1,801 $1,655

66 22 70S0148 0.64 382 0 382 363 $8,856 $1,822 $10,036

67 24 S0124 0.64 243 0 243 231 $9,595 $1,990 $17,210

68 25 206 1.87 1,024 Condenser 95 51 0 $0 $0 $0

69 27 methanol 1.95 598 0 598 568 $9,627 $1,963 $6,909

70 29 T-13 1.10 252 0 252 239 $11,051 $2,294 $19,184

71 29 T-14 1.10 252 0 252 239 $11,051 $2,294 $19,184

72 29 T-19 1.88 429 0 429 408 $13,846 $2,864 $14,051

73 29 T-3 2.30 708 0 708 672 $11,025 $2,246 $6,682

74 29 T-4 1.88 429 0 429 408 $11,025 $2,272 $11,147

75 29 T-5 1.40 411 0 411 391 $11,025 $2,274 $11,646

76 29 T-8 1.88 429 0 429 408 $13,846 $2,864 $14,051

77 29 T-9 1.88 429 0 429 408 $13,846 $2,864 $14,051

78 31 210/3025 1.80 804 0 804 764 $8,856 $1,782 $4,665

79 31 242/3001 1.50 989 0 989 940 $8,978 $1,790 $3,810

80 31 242/3002 1.50 989 0 989 940 $8,978 $1,790 $3,810

81 31 313/3004 1.92 10,995 0 10,995 10,445 $26,103 $4,432 $849

82 31 333/3001 1.92 1,863 0 1,863 1,770 $13,222 $2,597 $2,934

83 31 340/3011 1.50 1,154 0 1,154 1,096 $8,978 $1,774 $3,237

84 32 71T6 0.56 1,607 0 1,607 1,527 $13,154 $2,607 $3,414

85 33 209 1.90 329 0 329 313 $8,856 $1,827 $11,690

86 33 508 0.66 71 0 71 67 $8,978 $1,877 $55,663

87 33 645 0.77 10 0 10 9 $10,368 $2,174 $458,335

88 33 646 1.30 44 0 44 41 $10,365 $2,170 $104,695

89 33 682 1.90 196 0 196 186 $10,365 $2,156 $23,197
Att. 3-3

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

90 33 953 0.85 201 0 201 191 $8,879 $1,844 $19,294

91 34 3202F 1.02 1,512 Condenser 100 8 0 $0 $0 $0

92 36 RM14 2.40 5,143 0 5,143 4,885 $11,797 $1,987 $813

93 36 RTK34 1.93 320 0 320 304 $9,627 $1,989 $13,073

94 38 102 2.40 3,865 0 3,865 3,672 $9,627 $1,653 $900

95 40 RP_ST199 0.77 288 0 288 273 $8,969 $1,854 $13,574

96 41 115 1.40 290 Thermal 93 21 6 $9,274 $1,945 $609,402

97 41 138 0.60 743 Thermal 93 54 16 $11,974 $2,510 $306,910

98 41 139 0.60 320 Thermal 93 23 7 $11,974 $2,511 $712,252

99 41 149 2.20 2,295 0 2,295 2,180 $8,884 $1,646 $1,510

100 41 199 2.20 3,035 0 3,035 2,883 $9,639 $1,734 $1,203

101 41 CR-164 2.20 4,103 0 4,103 3,898 $9,664 $1,638 $840

102 41 CR-166 2.20 4,040 0 4,040 3,838 $9,664 $1,644 $857

103 41 CR-186 0.73 45 0 45 43 $8,947 $1,873 $87,983

104 42 160 1.22 656 0 656 623 $9,545 $1,940 $6,228

105 42 180 1.80 341 0 341 324 $8,884 $1,831 $11,289

106 42 185 0.50 854 0 854 811 $11,009 $2,229 $5,497

107 43 1010 2.73 2,545 0 2,545 2,418 $11,783 $2,230 $1,844

108 43 1012 0.57 110 0 110 105 $8,856 $1,847 $35,207

109 43 1020 3.23 2,555 0 2,555 2,427 $11,783 $2,229 $1,837

110 43 1030 3.52 3,823 0 3,823 3,632 $11,783 $2,109 $1,161

111 43 1060 2.73 1,524 0 1,524 1,447 $10,365 $2,030 $2,805

112 43 1070 0.79 570 0 570 542 $10,365 $2,120 $7,830

113 43 1080 0.79 271 0 271 258 $10,365 $2,149 $16,684

114 43 1130 3.23 2,555 0 2,555 2,427 $11,783 $2,229 $1,837

115 43 1150 1.08 400 0 400 380 $10,365 $2,137 $11,260

116 43 1180 0.79 589 0 589 559 $10,365 $2,119 $7,580

117 43 1200 3.23 1,108 0 1,108 1,052 $10,365 $2,069 $3,932

118 43 1210 1.17 725 0 725 689 $10,365 $2,106 $6,112

119 43 1240 0.79 289 0 289 275 $10,365 $2,147 $15,634

120 43 1360 1.58 580 0 580 551 $10,365 $2,119 $7,688

121 43 1370 0.79 213 0 213 202 $10,365 $2,154 $21,325

122 43 3073 0.56 623 0 623 592 $11,783 $2,413 $8,152

123 43 5101 1.35 1,912 0 1,912 1,817 $8,856 $1,676 $1,845

124 43 5102 1.35 1,912 0 1,912 1,817 $8,856 $1,676 $1,845

125 43 5103 1.53 1,379 0 1,379 1,310 $8,856 $1,727 $2,637

126 44 1982-05 1.86 362 Thermal 99 4 0 $0 $0 $0

127 44 1982-06 1.86 990 Thermal 99 10 0 $0 $0 $0

128 44 1984-25 1.86 1,544 Thermal 99 15 0 $0 $0 $0

129 44 1987-35 1.86 567 Thermal 99 6 0 $0 $0 $0

130 44 1988-15 1.86 382 Thermal 99 4 0 $0 $0 $0

131 45 T-1141 1.54 1,039 0 1,039 987 $10,365 $2,076 $4,207

132 45 T-1534 1.28 656 Scrubber 0 656 623 $12,093 $2,475 $7,941

133 45 T-596 1.54 728 0 728 692 $10,365 $2,105 $6,083
Att. 3-4

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

134 45 T-833 4.84 1,805 Scrubber 0 1,805 1,714 $9,257 $1,771 $2,066

135 48 VS 2704 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931

136 48 VS 703 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931

137 48 VS 704 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931

138 52 T-1409 0.76 1,122 Condenser 99 11 0 $0 $0 $0

139 52 T-2421 0.58 281 0 281 267 $11,044 $2,290 $17,143

140 52 T-2431 1.00 2,564 0 2,564 2,436 $11,649 $2,200 $1,806

141 52 T-2457 3.25 3,721 0 3,721 3,535 $10,244 $1,796 $1,016

142 52 T-9962 0.65 94 Carbon 99 1 0 $0 $0 $0

143 52 T-9964 0.65 94 Carbon 99 1 0 $0 $0 $0

144 53 11-211 2.50 509 0 509 483 $8,903 $1,819 $7,529

145 53 11-213 0.54 19 0 19 18 $8,903 $1,866 $207,278

146 53 11-231 0.76 96 0 96 91 $8,903 $1,859 $40,881

147 53 11-233 0.57 133 0 133 126 $8,903 $1,855 $29,466

148 53 11-235 2.38 349 0 349 331 $8,903 $1,835 $11,082

149 53 11-241 0.57 45 0 45 43 $8,903 $1,863 $87,134

150 53 11-245 0.95 138 0 138 131 $8,903 $1,855 $28,295

151 53 16-217 0.55 22 0 22 21 $9,666 $2,026 $196,408

152 53 16-237 1.97 93 0 93 88 $9,666 $2,019 $45,814

153 56 48-515 0.51 127 Condenser 92 10 4 $9,936 $2,084 $1,094,242

154 56 91-1339 2.40 338 0 338 321 $11,082 $2,293 $14,266

155 57 ALA01A 1.20 398 Carbon 99 4 0 $0 $0 $0

156 57 ALA01B 1.20 398 Carbon 99 4 0 $0 $0 $0

157 57 ALA05/4E 1.20 2,407 0 2,407 2,287 $9,587 $1,783 $1,559

158 57 ALA07 1.95 307 0 307 291 $9,561 $1,977 $13,572

159 59 A-17 0.66 157 Carbon 95 8 0 $0 $0 $0

160 59 A86 0.66 157 Carbon 95 8 0 $0 $0 $0

161 59 A87 0.66 214 Carbon 95 11 0 $0 $0 $0

162 60 Tank 61 2.00 1,225 0 1,225 1,164 $10,330 $2,051 $3,525

163 60 Tank 64 3.00 1,603 0 1,603 1,523 $10,330 $2,015 $2,647

164 60 Tank 73 2.00 723 0 723 686 $10,330 $2,099 $6,116

165 63 V-1 0.50 128 0 128 122 $9,627 $2,008 $33,004

166 63 V-13 1.37 1,376 Flare 98 28 0 $0 $0 $0

167 63 V-15 1.86 1,270 Flare 98 25 0 $0 $0 $0

168 63 V-16 1.78 1,983 Flare 98 40 0 $0 $0 $0

169 63 V-18 1.86 1,963 Flare 98 39 0 $0 $0 $0

170 63 V-2 0.50 123 0 123 117 $9,627 $2,008 $34,321

171 63 V-22 1.40 74 Flare 98 1 0 $0 $0 $0

172 63 V-23 0.61 67 Flare 98 1 0 $0 $0 $0

173 63 V-26 2.89 3,303 Flare 98 66 0 $0 $0 $0

174 63 V-27 2.89 3,303 Flare 98 66 0 $0 $0 $0

175 63 V-28 1.48 2,424 Flare 98 48 0 $0 $0 $0

176 63 V-29 2.87 2,217 Flare 98 44 0 $0 $0 $0

177 63 V-32 2.61 2,023 Flare 98 40 0 $0 $0 $0
Att. 3-5

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

178 63 V-33 6.40 437 0 437 415 $9,627 $1,978 $9,526

179 63 V-34 0.74 2,072 Flare 98 41 0 $0 $0 $0

180 63 V-35 2.83 401 Flare 98 8 0 $0 $0 $0

181 63 V-39 0.74 2,072 Flare 98 41 0 $0 $0 $0

182 63 V-4 1.05 3,148 Condenser 90 315 157 $9,936 $2,069 $26,287

183 63 V-43 0.96 323 Combination 100 0 0 $0 $0 $0

184 63 V-44 0.79 515 Combination 100 1 0 $0 $0 $0

185 63 V-45 6.79 6,160 Combination 100 6 0 $0 $0 $0

186 63 V-47 3.01 1,557 0 1,557 1,479 $9,627 $1,872 $2,531

187 63 V-48 3.01 3,555 0 3,555 3,378 $9,627 $1,682 $996

188 63 V-5 1.55 595 0 595 565 $9,627 $1,963 $6,947

189 63 V-50 13.63 2,935 0 2,935 2,788 $9,627 $1,741 $1,249

190 63 V-51 2.46 1,123 0 1,123 1,067 $9,627 $1,913 $3,586

191 63 V-52 13.63 4,649 0 4,649 4,416 $9,627 $1,578 $715

192 63 V-53 2.85 4,448 0 4,448 4,225 $9,627 $1,597 $756

193 63 V-54 2.85 3,546 0 3,546 3,369 $9,627 $1,683 $999

194 64 T027 1.86 693 0 693 658 $13,920 $2,855 $8,677

195 64 T191 0.87 392 0 392 373 $11,078 $2,287 $12,270

196 65 VT-1 3.66 2,416 0 2,416 2,295 $11,645 $2,214 $1,929

197 65 VT-201 3.66 2,416 0 2,416 2,295 $11,645 $2,214 $1,929

198 67 ST-900A 2.25 674 Scrubber 0 674 640 $12,090 $2,472 $7,720

199 67 ST-900B 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792

200 67 ST-918 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

201 67 ST-919 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

202 67 ST-920 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

203 67 ST-921 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

204 67 ST-922 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

205 67 ST-923 2.25 599 Scrubber 0 599 569 $11,381 $2,331 $8,193

206 67 ST-924 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

207 67 ST-925 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

208 67 ST-926 2.25 479 Scrubber 0 479 455 $10,553 $2,168 $9,532

209 67 ST-927 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

210 67 ST-928 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

211 67 ST-929 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

212 67 ST-934 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

213 67 ST-935 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100

214 67 ST-940 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

215 67 ST-941 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

216 67 ST-945 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

217 67 ST-947 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

218 67 ST-948 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

219 67 ST-949 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

220 67 ST-950 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792

221 67 ST-951 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792
Att. 3-6

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

222 67 ST-960 2.25 458 Scrubber 0 458 435 $9,947 $2,043 $9,384

223 67 ST-964 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460

224 67 ST-967 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

225 67 ST-968 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460

226 67 ST-970 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

227 67 ST-971 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

228 67 ST-972 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460

229 67 ST-973 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

230 67 ST-974 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

231 67 ST-975 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460

232 67 ST-981 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

233 67 ST-982 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

234 67 ST-983 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482

235 67 ST-984 2.25 545 Scrubber 0 545 518 $11,263 $2,311 $8,926

236 67 ST-985 2.25 545 Scrubber 0 545 518 $11,263 $2,311 $8,926

237 67 ST-986 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819

238 67 ST-987 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792

239 67 ST-990 2.25 431 Scrubber 0 431 409 $9,876 $2,031 $9,928

240 67 ST-994 2.25 385 Scrubber 0 385 365 $9,194 $1,892 $10,359

241 68 ST1 1.70 42,893 IFR 95 2,145 0 $0 $0 $0

242 68 ST12 0.70 717 0 717 681 $8,947 $1,809 $5,309

243 68 ST2 0.60 631 0 631 600 $11,783 $2,412 $8,045

244 68 ST6 1.80 291 0 291 277 $9,666 $2,000 $14,461

245 68 ST7 1.90 177 0 177 168 $8,947 $1,860 $22,148

246 71 1 2.40 1,451 EFR 95 73 0 $0 $0 $0

247 73 N110 2.01 495 0 495 471 $8,856 $1,811 $7,696

248 73 T312 0.52 155 0 155 147 $8,856 $1,843 $25,027

249 73 T326 1.06 1,139 Scrubber 0 1,139 1,082 $10,674 $2,131 $3,939

250 74 Y-210 2.45 426 0 426 404 $9,639 $1,982 $9,803

251 75 D501 1.90 517 0 517 491 $9,627 $1,971 $8,029

252 78 SN-711 10.10 11,673 0 11,673 11,089 $10,318 $1,056 $190

253 80 RS-48 0.76 687 0 687 652 $8,856 $1,793 $5,496

254 82 AT-3 1.91 253 0 253 240 $8,856 $1,834 $15,276

255 82 AT-4 1.91 175 0 175 166 $8,856 $1,841 $22,154

256 82 AT-6 1.91 216 0 216 206 $9,587 $1,991 $19,361

257 83 597 1.90 635 Condenser 90 64 32 $9,189 $1,925 $121,220

258 83 606 1.90 1,719 Condenser 90 172 86 $11,391 $2,381 $55,408

259 86 T-18 1.93 593 0 593 563 $10,239 $2,092 $7,428

260 87 2T116 (# 781) 1.39 122 0 122 116 $8,856 $1,846 $31,888

261 87 4T013 (# 690) 1.93 194 0 194 185 $8,856 $1,839 $19,927

262 89 T-1121 2.40 290 0 290 275 $8,858 $1,831 $13,297

263 90 A-165 2.03 1,128 Incinerator 99 11 0 $0 $0 $0

264 90 A-177 3.39 1,058 Incinerator 99 11 0 $0 $0 $0

265 90 A-208 0.74 285 Incinerator 99 3 0 $0 $0 $0
Att. 3-7

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

266 90 A-217 0.86 551 0 551 523 $11,082 $2,273 $8,685

267 90 A-402 0.76 807 Flare 98 16 0 $0 $0 $0

268 90 B-172 2.03 704 Incinerator 99 7 0 $0 $0 $0

269 90 B-242 0.74 787 Incinerator 99 8 0 $0 $0 $0

270 90 B-257 0.74 1,103 Incinerator 99 11 0 $0 $0 $0

271 90 B-271 0.74 2,408 Incinerator 99 24 0 $0 $0 $0

272 90 B-404 0.74 821 Flare 98 16 0 $0 $0 $0

273 90 B-431 0.74 821 Flare 98 16 0 $0 $0 $0

274 90 C-132 2.27 5,942 Absorber 0 5,942 5,645 $14,228 $2,420 $857

275 90 C-133 2.27 5,942 Absorber 0 5,942 5,645 $14,228 $2,420 $857

276 90 C-216 0.74 1,858 Incinerator 99 19 0 $0 $0 $0

277 90 C-451 0.74 2,053 Flare 98 41 0 $0 $0 $0

278 91 T01 1.80 664 0 664 631 $8,947 $1,814 $5,750

279 91 T12 0.60 892 0 892 847 $9,627 $1,935 $4,567

280 91 T15 0.50 586 Scrubber 0 586 557 $12,093 $2,481 $8,910

281 91 T23 0.50 3,903 0 3,903 3,708 $24,451 $4,759 $2,567

282 92 11 0.68 193 0 193 184 $9,633 $2,003 $21,811

283 92 111 1.13 1,996 0 1,996 1,896 $19,755 $3,955 $4,172

284 92 12 0.68 186 0 186 177 $9,633 $2,003 $22,656

285 92 13 0.68 181 0 181 172 $9,632 $2,004 $23,306

286 92 14 0.68 172 0 172 164 $9,632 $2,004 $24,461

287 92 211 1.35 516 0 516 491 $10,354 $2,123 $8,654

288 92 212 1.35 764 0 764 726 $10,354 $2,100 $5,784

289 92 216 1.35 599 0 599 569 $10,354 $2,115 $7,428

290 92 236 0.68 376 0 376 357 $12,393 $2,564 $14,373

291 92 241 1.35 380 0 380 361 $10,356 $2,137 $11,854

292 92 252 1.61 423 0 423 402 $10,355 $2,132 $10,612

293 92 253 1.61 461 0 461 438 $10,355 $2,129 $9,715

294 92 254 1.35 913 IFR 95 46 0 $0 $0 $0

295 92 260 8.06 8,992 0 8,992 8,542 $13,137 $1,902 $445

296 92 261 5.78 5,291 0 5,291 5,026 $13,137 $2,254 $897

297 92 304 1.51 337 0 337 321 $9,633 $1,989 $12,410

298 92 331 0.87 367 0 367 349 $10,981 $2,269 $13,008

299 92 535 0.57 418 0 418 397 $8,932 $1,834 $9,231

300 92 536 0.57 453 0 453 431 $8,932 $1,831 $8,501

301 92 542 0.66 349 0 349 331 $8,932 $1,841 $11,121

302 92 546 0.66 510 0 510 485 $8,932 $1,825 $7,531

303 92 620 1.11 375 0 375 357 $11,777 $2,435 $13,659

304 92 622 1.05 313 0 313 297 $11,777 $2,441 $16,417

305 92 632 0.52 176 0 176 167 $11,776 $2,454 $29,311

306 92 701 1.09 230 0 230 218 $8,873 $1,840 $16,856

307 92 710 0.77 2,454 0 2,454 2,332 $24,536 $4,914 $4,215

308 92 719 0.58 109 0 109 103 $8,860 $1,848 $35,752

309 92 720 1.10 213 0 213 202 $8,860 $1,839 $18,205
Att. 3-8

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

310 92 721 0.86 179 0 179 170 $8,860 $1,842 $21,682

311 92 726 0.67 105 0 105 100 $8,857 $1,848 $36,957

312 92 727 1.09 166 0 166 158 $8,857 $1,842 $23,310

313 92 777 1.09 279 0 279 265 $8,861 $1,833 $13,847

314 92 778 1.09 248 0 248 235 $8,863 $1,836 $15,597

315 92 779 1.09 255 0 255 242 $8,863 $1,835 $15,153

316 92 792 1.09 258 0 258 245 $9,622 $1,994 $16,294

317 93 TK-592 3.20 1,189 Flare 98 24 0 $0 $0 $0

318 94 505#1 0.55 1,377 0 1,377 1,308 $13,940 $2,794 $4,272

319 94 505#3 0.55 633 0 633 602 $10,365 $2,114 $7,029

320 105 2770171 0.59 1,095 0 1,095 1,040 $9,545 $1,899 $3,651

321 105 2770595 5.11 5,336 0 5,336 5,069 $9,545 $1,496 $590

322 106 T-08 3.54 2,338 0 2,338 2,221 $10,333 $1,946 $1,752

323 106 T-753 4.04 715 0 715 679 $10,333 $2,100 $6,185

324 107 T-443 8.50 1,982 Scrubber 0 1,982 1,883 $9,167 $1,735 $1,843

325 109 V129B 1.90 351 0 351 333 $8,903 $1,834 $11,013

326 110 V-334 1.87 206 0 206 196 $8,969 $1,862 $18,988

327 110 V-372 1.87 206 0 206 196 $8,969 $1,862 $18,988

328 110 V-374 1.87 206 0 206 196 $8,969 $1,862 $18,988

329 110 V-376 1.87 206 0 206 196 $8,969 $1,862 $18,988

330 112 02TK101 2.34 978 0 978 929 $10,239 $2,055 $4,424

331 112 02TK102 2.29 1,381 0 1,381 1,312 $10,344 $2,039 $3,108

332 112 02TK103 1.96 904 0 904 858 $13,896 $2,830 $6,593

333 112 02TK104 2.11 2,723 0 2,723 2,587 $10,337 $1,910 $1,477

334 112 02TK150 1.68 435 0 435 413 $9,627 $1,978 $9,568

335 112 02TK254 1.96 355 0 355 338 $10,320 $2,131 $12,626

336 112 02TK255 2.16 245 0 245 233 $10,320 $2,142 $18,398

337 112 03TK305B 1.96 290 0 290 276 $9,615 $1,990 $14,429

338 112 03TK310 1.12 319 Condenser 319 303 $9,975 $2,063 $13,630 $0

339 112 03V309 1.21 139 Condenser 139 132 $9,975 $2,080 $31,605 $0

340 112 03V310 2.16 229 Condenser 229 218 $10,604 $2,203 $20,231 $0

341 112 03V369 0.76 126 Condenser 126 119 $9,975 $2,081 $34,837 $0

342 112 03V374 0.62 79 Condenser 79 75 $9,975 $2,085 $55,396 $0

343 112 03V381 1.12 319 Condenser 319 303 $9,975 $2,063 $13,630 $0

344 112 04TK433 2.34 1,281 0 1,281 1,217 $11,041 $2,195 $3,606

345 118 T-141 0.51 815 0 815 774 $9,623 $1,942 $5,019

346 118 T-224 0.55 271 Afterburner 95 14 0 $0 $0 $0

347 119 T-114 2.35 880 0 880 836 $8,978 $1,800 $4,308

348 119 T-128 1.87 246 0 246 234 $8,943 $1,853 $15,871

349 124 Tank 15 1.38 249 0 249 237 $9,627 $1,996 $16,857

350 124 Tank 30 CS2 6.27 8,366 0 8,366 7,947 $9,627 $1,225 $308

351 125 101 1.95 255 Condenser 71 74 61 $9,896 $2,070 $67,706

352 131 1155-01 0.66 3,294 IFR 95 165 0 $0 $0 $0

353 131 1250-01 0.90 2,865 IFR 95 143 0 $0 $0 $0
Att. 3-9

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

354 131 1250-02 0.66 3,294 IFR 95 165 0 $0 $0 $0

355 131 1650-01 0.66 8,548 IFR 95 427 0 $0 $0 $0

356 133 PT0019 7.11 1,914 Afterburner 99 19 0 $0 $0 $0

357 133 PT0020 1.63 3,443 Afterburner 99 34 0 $0 $0 $0

358 133 PT0083 4.65 1,314 Afterburner 99 13 0 $0 $0 $0

359 134 TF-32 2.26 3,053 0 3,053 2,901 $13,940 $2,635 $1,817

360 134 TF-33 0.74 1,432 0 1,432 1,360 $13,940 $2,789 $4,101

361 134 TF-42 4.60 3,194 0 3,194 3,034 $13,940 $2,621 $1,728

362 134 TF-49 3.23 1,676 0 1,676 1,592 $13,940 $2,765 $3,474

363 135 TF-13A 2.90 394 0 394 374 $10,365 $2,137 $11,414

364 135 TF-14 0.87 379 0 379 360 $10,365 $2,139 $11,872

365 135 TF-17 0.95 430 0 430 409 $10,365 $2,134 $10,447

366 135 TF-2 2.07 1,701 0 1,701 1,616 $13,940 $2,763 $3,419

367 135 TF-3B 0.53 460 0 460 437 $13,940 $2,881 $13,177

368 135 TF-6 0.66 1,016 0 1,016 965 $13,940 $2,828 $5,859

369 136 101-A-01 0.80 743 0 743 706 $13,940 $2,854 $8,084

370 136 101-A-03 3.53 1,116 0 1,116 1,060 $13,940 $2,819 $5,318

371 136 398-A-32 0.55 282 0 282 268 $10,365 $2,148 $16,054

372 136 398-A-34 0.65 190 0 190 180 $10,365 $2,157 $23,931

373 137 C-10 1.35 486 0 486 462 $9,641 $1,976 $8,558

374 137 C-11 1.36 489 0 489 465 $9,641 $1,976 $8,507

375 137 C-12 1.78 627 0 627 596 $9,641 $1,963 $6,587

376 137 C-9 0.75 282 0 282 268 $9,641 $1,996 $14,915

377 141 CRU-#068 1.76 3,358 0 3,358 3,190 $11,082 $2,006 $1,258

378 141 CRU-#072 1.72 2,926 0 2,926 2,780 $9,607 $1,738 $1,250

379 143 T1201 0.54 450 0 450 428 $9,643 $1,980 $9,255

380 143 T1202 0.54 450 0 450 428 $9,643 $1,980 $9,255

381 143 T1215 0.54 776 0 776 738 $9,667 $1,954 $5,298

382 143 T1216 0.54 811 0 811 771 $10,955 $2,221 $5,763

383 143 T203 0.54 1,231 0 1,231 1,170 $8,879 $1,746 $2,986

384 147 3056 0.60 177 0 177 168 $8,856 $1,841 $21,934

385 147 3080 1.80 2,974 Boiler 99 30 0 $0 $0 $0

386 147 T-6240 2.30 35 Scrubber 0 35 33 $10,567 $2,214 $133,813

387 147 T-6250 2.30 35 Scrubber 0 35 33 $10,567 $2,214 $133,813

388 149 S262 0.55 337 Thermal 99 3 0 $0 $0 $0

389 149 S404 2.35 1,210 0 1,210 1,149 $10,365 $2,060 $3,585

390 149 S405 1.66 435 0 435 414 $10,365 $2,133 $10,314

391 149 S410 0.55 187 Thermal 99 2 0 $0 $0 $0

392 150 V-53 2.18 189 N2 Blkt 189 179 $9,257 $1,924 $21,468 $0

393 150 V-56 2.18 344 N2 Blkt 344 327 $9,257 $1,909 $11,683 $0

394 150 V-57 2.18 286 N2 Blkt 286 272 $9,257 $1,915 $14,098 $0

395 150 V-61 0.51 88 N2 Blkt 88 83 $9,257 $1,934 $46,452 $0

396 150 V-63 0.54 137 N2 Blkt 137 130 $9,257 $1,929 $29,666 $0

397 150 V-64 0.55 84 N2 Blkt 84 80 $9,257 $1,934 $48,306 $0
Att. 3-10

Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

398 150 V-69 0.66 63 N2 Blkt 63 60 $9,257 $1,936 $65,066 $0

399 153 TS-11 3.87 4,321 0 4,321 4,105 $11,790 $2,063 $1,005

400 153 TS-11(Textile) 4.60 5,377 0 5,377 5,108 $11,082 $1,814 $710

401 153 TS-15 (Meth. 3.87 4,321 0 4,321 4,105 $11,790 $2,063 $1,005

402 156 DT-02A 1.77 562 0 562 534 $8,897 $1,813 $6,789

403 156 DT-02B 1.77 469 0 469 445 $8,897 $1,822 $8,184

404 156 DT-06 1.77 525 0 525 498 $8,885 $1,814 $7,280

405 156 DT-08A 1.77 359 0 359 341 $8,897 $1,832 $10,743

406 156 DT-08C 1.77 359 0 359 341 $8,897 $1,832 $10,743

407 156 DT-09A 1.77 359 0 359 341 $8,897 $1,832 $10,743

408 156 DT-09B 1.77 359 0 359 341 $8,897 $1,832 $10,743

409 156 DT-09C 1.77 359 0 359 341 $8,897 $1,832 $10,743

410 156 DT-11 1.77 359 0 359 341 $8,897 $1,832 $10,743

411 156 DT-22 0.66 2,117 0 2,117 2,011 $8,897 $1,666 $1,657

412 156 DT-23 1.77 104 0 104 99 $8,932 $1,864 $37,637

413 156 DT-30A 1.77 359 0 359 341 $8,897 $1,832 $10,743

414 156 XT-04A 0.66 1,932 0 1,932 1,835 $11,089 $2,143 $2,335

415 157 TK 5731 0.57 298 0 298 283 $8,903 $1,839 $13,007

416 158 422-199 1.03 101 Insulated but 101 96 $9,876 $2,062 $42,790 $0

417 158 441-015 1.11 198 0 198 188 $10,943 $2,277 $24,189

418 158 441-025 0.74 245 0 245 233 $8,947 $1,854 $15,921

419 158 441-027 6.00 1,296 0 1,296 1,231 $8,947 $1,754 $2,850

420 158 441-028 0.74 75 0 75 71 $8,947 $1,870 $52,566

421 158 441-031 1.11 231 0 231 219 $8,947 $1,855 $16,928

422 158 441-281 6.00 1,976 0 1,976 1,878 $9,635 $1,834 $1,953

423 158 441-421 0.72 186 0 186 177 $11,797 $2,457 $27,830

424 158 441-422 0.72 167 0 167 158 $11,797 $2,459 $31,066

425 158 441-452 1.11 243 0 243 231 $11,797 $2,452 $21,248

426 158 445-008 1.11 231 0 231 219 $8,947 $1,855 $16,928

427 161 T-1 6.38 2,104 Condenser 22 1,641 1,536 $9,975 $1,939 $2,524

428 162 141-T-6 (5004) 1.76 985 0 985 936 $10,281 $2,063 $4,408

429 163 29C 0.95 476 0 476 452 $8,947 $1,832 $8,107

430 163 68C 8.60 2,431 0 2,431 2,310 $8,947 $1,646 $1,425

431 163 83C 5.03 1,554 0 1,554 1,476 $9,627 $1,872 $2,536

432 167 Tank 521 2.94 881 None 0 881 837 $9,939 $2,002 $4,786

433 167 Tank 714 6.99 2,895 Condenser 86 414 269 $9,172 $1,897 $14,091

Total 567,122 384,600 $3,891,330 $777,939 $4,045
Att. 3-11

Horizontal Tanks with HAP Partial Pressure =>0.5 psia and Condenser Cost (Above Floor)

Facil. # Tank ID

HAP partial

pressure (psia)

Uncontrolled HAP

emissions (lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

1 28 TLI-4 9.55 11,964 Carbon adsorber 81 2,273 1,675 $50,917 $44,861 $53,569

2 28 TLI-5 9.55 23,330 Carbon adsorber 81 4,433 3,266 $50,917 $45,290 $27,732

3 20 S-6402 8.90 3,361 Scrubber 0 3,361 3,193 $32,459 $41,477 $25,984

4 167 Tank 1141 3.40 3,974 Thermal oxidizer 99 40 0 $0 $0 $0

5 167 Tank 1142 3.40 8,233 Thermal oxidizer 99 82 0 $0 $0 $0

6 167 Tank 1143 3.40 3,974 Thermal oxidizer 99 40 0 $0 $0 $0

7 167 Tank 364 2.94 3,812 Thermal oxidizer 99 38 0 $0 $0 $0

8 167 Tank 376 2.94 1,806 Thermal oxidizer 99 18 0 $0 $0 $0

9 167 Tank 1215 2.94 2,062 Thermal oxidizer 99 21 0 $0 $0 $0

10 167 Tank 377 2.94 1,701 Thermal oxidizer 99 17 0 $0 $0 $0

11 134 23-6 2.79 812 0 812 771 $30,701 $40,965 $106,218

12 161 T-16 2.78 974 0 974 926 $25,509 $40,112 $86,659

13 166 TP930 HT13 2.10 335 None 0 335 318 $31,764 $41,069 $258,409

14 166 TP930 HT-6 2.10 335 None 0 335 318 $31,764 $41,069 $258,409

15 166 TP930 HT-1 2.10 335 None 0 335 318 $31,764 $41,069 $258,409

16 137 U-9 1.95 541 0 541 514 $32,029 $41,130 $160,175

17 137 U-8 1.95 471 0 471 447 $32,029 $41,117 $183,852

18 10 Tank 05 1.93 1,037 Scrubber 0 1,037 985 $27,125 $40,472 $82,188

19 44 1340-01 1.86 167 Thermal oxidizer 99 2 0 $0 $0 $0

20 156 G-65-1 1.77 359 0 359 341 $32,376 $41,193 $241,549

21 84 T013 1.70 5,031 0 5,031 4,779 $25,037 $39,988 $16,735

22 84 T014 1.70 5,031 0 5,031 4,779 $25,037 $39,988 $16,735

23 130 T-325A 1.70 1,437 0 1,437 1,365 $24,640 $39,973 $58,552

24 141 PO-#129 1.63 749 0 749 712 $30,100 $40,754 $114,500

25 28 TS-146 1.62 243 0 243 231 $32,091 $41,051 $355,471

26 167 Tank 1219 1.61 2,537 Thermal oxidizer 99 25 0 $0 $0 $0

27 167 Tank 1119 1.61 2,537 Thermal oxidizer 99 25 0 $0 $0 $0

28 70 TA-951 1.60 1,197 Carbon adsorber 95 60 0 $0 $0 $0

29 40 TF_ST104 1.49 483 0 483 459 $30,483 $40,808 $177,960

30 87 4T003 (# 672) 1.37 263 0 263 250 $30,851 $40,849 $326,430

31 57 ALA05 1.20 5,835 0 5,835 5,543 $14,185 $37,934 $13,687

32 2 T035 1.16 2,409 0 2,409 2,288 $29,726 $40,679 $35,556

33 2 T036 1.16 2,409 0 2,409 2,288 $29,726 $40,679 $35,556

34 2 T037 1.16 2,409 0 2,409 2,288 $29,726 $40,679 $35,556

35 2 T038 1.16 2,409 0 2,409 2,288 $29,726 $40,679 $35,556

36 34 3104F 1.02 603 Condenser 99 6 0 $0 $0 $0

37 167 Tank 368 0.96 1,055 Thermal oxidizer 99 11 0 $0 $0 $0

38 167 Tank 369 0.96 1,107 Thermal oxidizer 99 11 0 $0 $0 $0

39 40 TF_ST144 0.60 293 0 293 279 $18,617 $38,972 $279,763

40 70 TA-960 0.59 258 Carbon adsorber 95 13 0 $0 $0 $0

41 54 C-749 0.58 786 0 786 746 $39,251 $42,412 $113,646

42 54 C-751 0.58 1,039 0 1,039 987 $39,251 $42,460 $86,062

43 70 TA-950 0.55 3,416 Carbon adsorber 95 171 0 $0 $0 $0

44 70 TA-952 0.55 1,386 Carbon adsorber 95 69 0 $0 $0 $0

45 40 TF_ST118 0.54 858 0 858 815 $16,524 $38,642 $94,847

46 134 23-4 0.50 343 0 343 326 $22,656 $39,550 $242,529

Total 115,702 47,937 43,495 $876,981 $1,185,92 $54,532
Att. 3-12

Continuous Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

Facil. # Tank ID

HAP partial

pressure

(psia)

Uncontrolled

HAP emissions

(lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

1 M126 CRUDE DIBASIC 1.93 3,880 VAPOR RECOVERY 0 3,880 3,686.00 $11,578 $2,451 $1,330

2 M126 METHANOL TANK 1.93 1,340 NONE 0 1,340 1,273.00 $15,221 $3,648 $5,731

3 M126 METHANOL TANK 1.93 1,560 NONE 0 1,560 1,482.00 $15,221 $3,623 $4,889

4 M146 D-123 CHILLED 1.93 0 NONE 0 0 0.38 $13,532 $3,377 $17,773,684

5 M257 FRESH METHANOL 1.93 4,640 IFR 95 232 0.00 $0 $0 $0

6 M257 MOTHER LIQUOR 1.93 12,000 IFR 95 600 0.00 $0 $0 $0

7 M257 MOTHER LIQUOR 1.93 12,000 IFR 95 600 0.00 $0 $0 $0

8 M257 RECOVERED 1.93 9,560 IFR 95 478 0.00 $0 $0 $0

9 M257 SEAL FLUSH 1.93 5,200 IFR 95 260 0.00 $0 $0 $0

10 M258 DRY METHANOL 1.93 11,600 IFR 95 580 0.00 $0 $0 $0

11 M258 SPENT HEXANE 2.93 27,200 IFR 95 1,360 0.00 $0 $0 $0

12 M262 HEXANE STORAGE 2.93 156,000 FLARE &

CONDENSER

100 468 0.00 $0 $0 $0

13 M262 HEXANE STORAGE 2.93 9,067 FLARE &

CONDENSER

100 27 0.00 $0 $0 $0

14 M270 HEXANE STORAGE 2.93 8,400 IFR 95 420 0.00 $0 $0 $0

15 M270 TANK 2.93 2,440 NONE 0 2,440 2,318.00 $9,669 $2,138 $1,845

16 M270 TANK 2.93 723 NONE 0 723 686.85 $9,769 $2,357 $6,863

17 M279 "B" PLANT 1.93 2,386 VAPORCONDENSERS79 492 76.69 $20,357 $5,037 $131,361

18 M279 CENTRATE AND 1.93 175 NONE 0 175 166.63 $30,354 $7,556 $90,692

19 M279 INHIBITOR 1.93 433 NONE 0 433 411.73 $11,240 $2,757 $13,392

20 M279 METHANOL 1.93 883 NONE 0 883 839.04 $25,030 $6,148 $14,655

21 M279 METHYL ACETATE 1.93 9 VAPORCONDENSERS77 2 0.40 $18,693 $4,666 $23,179,334

22 M279 MILLION GAL VAM. 1.61 17,270 VAPORCONDENSERS82 3,074 393.47 $44,072 $10,737 $54,576

23 M279 POLYMER TANK 1.93 2,782 VAPORCONDENSERS89 306 18.36 $16,327 $4,055 $441,721

24 M279 POLYMER TANK 1.93 7,276 VAPORCONDENSERS89 800 48.02 $16,327 $4,023 $167,541

25 M279 SODIUM 1.93 0 NONE 0 0 0.00 $9,720 $2,426 $4,245,782,

26 M279 VINYL "A" 1.61 8,784 NONE 0 8,784 8,345.18 $30,354 $6,583 $1,578

27 M279 VINYL "B" 1.61 6,919 NONE 0 6,919 6,572.86 $30,354 $6,794 $2,067

28 M279 VINYL "C" DAY 1.61 944 NONE 0 944 896.99 $22,551 $5,522 $12,312

29 M279 VINYL "C" 1.61 8,684 NONE 0 8,684 8,249.42 $30,354 $6,595 $1,599

30 M279 VINYL ACETATE "A" 1.61 5,765 NONE 0 5,765 5,476.56 $22,551 $4,977 $1,818

31 M279 VINYL ACETATE "B" 1.61 4,745 NONE 0 4,745 4,507.94 $22,551 $5,092 $2,259

32 M279 VINYL ACETATE (A 3.54 200 VAPORCONDENSERS83 34 4.08 $19,498 $4,864 $2,384,314

33 M279 VINYL ACETATE (B 3.54 358 VAPORCONDENSERS83 61 7.30 $19,498 $4,862 $1,332,785

34 M279 WASHWATER 1.93 89 NONE 0 89 84.55 $14,281 $3,554 $84,069

35 M280 A CRUDE 1.93 3 NONE 0 3 3.23 $14,309 $3,571 $2,211,146

36 M280 B CRUDE 1.93 22 NONE 0 22 20.52 $14,309 $3,569 $347,856

37 M280 BIG A CRUDE 1.93 84 NONE 0 84 79.99 $34,823 $8,682 $217,077

38 M280 BIG B CRUDE 1.93 8 NONE 0 8 7.98 $34,823 $8,691 $2,178,195
Att. 3-13

Continuous Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure

(psia)

Uncontrolled

HAP emissions

(lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

39 M280 CRUDE KA TANK - 1.93 18 NONE 0 18 16.72 $19,920 $4,970 $594,498

40 M280 E REWORK 1.93 4 NONE 0 4 3.61 $22,578 $5,635 $3,121,884

41 M280 F CRUDE DCH 1.93 22 NONE 0 22 21.28 $22,578 $5,633 $529,417

42 M280 HMI STORAGE 1.93 5 NONE 0 5 4.75 $11,279 $2,815 $1,185,263

43 M280 NO. 2 RECYCLE VA 1.61 18,716 IFR 95 936 0.00 $0 $0 $0

44 M280 NO. 3 TWKA 1.93 15 NONE 0 15 14.44 $15,221 $3,797 $525,900

45 M280 NO. 3 TWKA 1.93 2 NONE 0 2 1.52 $33,821 $8,441 $11,106,579

46 M280 NO. 4 TWKA 1.93 15 NONE 0 15 14.44 $15,221 $3,797 $525,900

47 M280 RECYCLE AQUA 1.93 0 NONE 0 0 0.19 $9,769 $2,438 $25,663,158

48 M280 VINYL ACETATE 1.61 18,716 IFR 95 936 0.00 $0 $0 $0

49 M280 WASTE 1.93 0 NONE 0 0 0.19 $9,720 $2,426 $25,536,842

50 M280 WASTE ORGANIC 1.93 215 NONE 0 215 204.06 $11,240 $2,781 $27,257

51 M281 CRUDE NPG 1.93 460 0 460 437.00 $14,701 $3,617 $16,554

52 M281 FLUX OIL TANK 3.16 1,528 0 1,528 1,451.41 $17,161 $4,111 $5,665

53 M281 MIX 1.93 38 0 38 36.10 $10,805 $2,693 $149,197

54 M281 MOLTEN STORAGE 2.93 562 0 562 533.90 $19,467 $4,796 $17,966

55 M281 MOLTEN STORAGE 2.93 562 VAPOR RECOVERY 0 562 533.90 $19,467 $4,796 $17,966

56 M281 REJECT 1.93 10 0 10 9.50 $15,559 $3,882 $817,263

57 M281 STORAGE TANK 13.29 2,300 0 2,300 2,185.00 $25,427 $6,087 $5,572

58 M281 STORAGE TANK 43 13.29 420 0 420 399.00 $13,899 $3,422 $17,153

59 M281 STORAGE 2.24 60 0 60 57.00 $10,107 $2,516 $88,281

60 M281 STORAGE 13.29 60 0 60 57.00 $11,538 $2,873 $100,807

61 M281 TANK 13.29 240 0 240 228.00 $13,063 $3,233 $28,360

62 M283 HEXANE STORAGE 2.93 22,000 IFR 95 1,100 0.00 $0 $0 $0

63 M283 HEXANE STORAGE 2.93 18,000 IFR 95 900 0.00 $0 $0 $0

64 M289 TANK 2.93 320 IFR 95 16 0.00 $0 $0 $0

65 M289 TANK 2.93 320 IFR 95 16 0.00 $0 $0 $0

66 M289 TANK 2.93 320 IFR 95 16 0.00 $0 $0 $0

67 M289 TANK 2.93 120 IFR 95 6 0.00 $0 $0 $0

68 M289 TANK 2.93 320 IFR 95 16 0.00 $0 $0 $0

69 M293 STORAGE 1.68 0 NONE 0 0 0.38 $32,823 $8,192 $43,115,789

70 M293 STORAGE 1.68 507 NONE 0 507 481.84 $12,066 $2,954 $12,261

71 M300 TANK 1.93 318 NONE 0 318 302.10 $11,960 $2,949 $19,523

72 M300 TANK 2.06 81 NONE 0 81 76.95 $14,416 $3,589 $93,281

73 M300 TANK 2.93 200 IFR 95 10 0.00 $0 $0 $0

74 M306 TANK/2A/2A 2.93 1,280 NONE 0 1,280 1,216.00 $11,949 $2,838 $4,668

75 M306 TANK/2B/2B 2.93 1,280 NONE 0 1,280 1,216.00 $11,949 $2,838 $4,668

76 M306 TANK/3/3 0.71 260 NONE 0 260 247.00 $9,695 $2,391 $19,360

77 M330 POLY ETHYLENE 2.32 8,868 NONE 0 8,868 8,424.60 $10,520 $1,623 $385

78 M343 R-1372 1.93 12 NONE 0 12 11.40 $9,669 $2,412 $423,158

79 M358 2-16,900 GALLON 1.93 7,765 None 0 7,765 7,376.75 $13,585 $2,513 $681

80 M358 2-9,800 GALLON 1.93 3,882 None 0 3,882 3,687.90 $11,302 $2,382 $1,292

81 M358 3-150,000 GALLON 1.93 4,500 None 0 4,500 4,275.00 $32,814 $7,682 $3,594

82 M358 NEW ROSIN TANK, 1.93 3,882 None 0 3,882 3,687.90 $10,520 $2,187 $1,186
Att. 3-14

Continuous Vertical Tanks with HAP Partial Pressure => 0.5 psia and IFR Control Cost (Above Floor)

(continued)

Facil. # Tank ID

HAP partial

pressure

(psia)

Uncontrolled

HAP emissions

(lb/yr) Control device

Control

efficiency

Baseline HAP

emissions

(lb/yr)

HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton)

83 M358 RESIN PRODUCT 1.93 3,882 None 0 3,882 3,687.90 $12,866 $2,773 $1,504

84 M358 RESINATE TANKS, 0.71 6,666 None 0 6,666 6,332.70 $12,045 $2,253 $712

85 M358 RXN. OIL, HEADS 1.93 4,500 None 0 4,500 4,275.00 $11,317 $2,316 $1,084

86 M358 ST-26 RESINATE 0.71 2,244 None 0 2,244 2,131.80 $12,739 $2,926 $2,745

87 M358 TOLUENE TANK 0.71 1,498 None 0 1,498 1,423.10 $12,049 $2,838 $3,988

88 M44 1100 PROCESS 6.93 2,916 NONE 0 2,916 2,770.20 $9,669 $2,084 $1,505

89 M44 1100 PROCESS 1.38 108 NONE 0 108 102.60 $9,669 $2,401 $46,803

90 M44 T-352,353,&354/FB03 1.93 130 NONE 0 130 123.50 $12,866 $3,197 $51,773

91 M44 T-352,353,&354/FB03 1.93 18 PROCESS CHANGE 0 18 17.10 $13,204 $3,294 $385,263

92 M44 TANK 1.93 113 VAPORCONDENSERS68 36 9.72 $15,510 $3,868 $795,885

93 M44 TANK 1.93 14,600 FLARE-WASTE 98 292 0.00 $0 $0 $0

94 M44 TANKS 360 AND 1.93 7,938 VAPORCONDENSERS68 2,540 685.80 $27,035 $6,493 $18,936

95 M44 TANKS 1.68 1,448 NONE 0 1,448 1,375.60 $14,281 $3,401 $4,945

96 M44 TANKS 1.68 1,450 NONE 0 1,450 1,377.50 $12,100 $2,856 $4,147

97 M44 TANKS 1.68 5,040 SCRUBBER 0 50 47.88 $12,438 $2,535 $105,890

98 M44 TANKS 3.62 766 NONE 0 766 727.70 $12,100 $2,934 $8,064

99 M44 TANKS 2.06 218 NONE 0 218 207.29 $11,317 $2,800 $27,015

Total 129,163 108,165 $1,324,380 $316,633 $5,855

National Total 509,121 216,331 $2,648,760 $633,266
ATTACHMENT 4:

Internal Floating Roof Cost Module
Att. 4-1

Option Compare Database

Option Explicit

Public Sub IFRCost()

 Dim dbs As Database

 Dim rst As Recordset

 Dim TankSize As Double 'tank capacity, gal

 Dim TankDia As Double 'tank diameter, ft

 Dim Degas As Double 'cleaning and degassing of tank, $

 Dim FlRoof As Double 'new NSPS floating roof, $

 'Dim SecSeal As Double 'addition of secondary seal, $

 'Dim CtrlDeck As Double 'addition of control deck fittings, $

 Dim CtrlDev As Variant 'control device

 Dim CtrlEff As Variant 'control device efficiency (percent)

 Dim BaseEmiss As Double 'calculated emissions (lb/yr)

 Dim EmissRed As Double 'reduction in emissions, lb/yr

 Const Price As Double = 0.1 'price for recovered voc, $

 Dim RemovCond As Double 'removing existing condenser, $

 Dim TAC As Double 'total annualized cost, $

 Dim CapCost As Double 'capitalized cost, $

 Dim PEC As Double 'purchased equipment cost, $

 Dim TCI As Double 'total capital investment, $

 Dim RC As Double 'recovery credit, $

 Dim DAC As Double 'direct annual cost, $

 Dim OandM As Double 'operating and maintenance cost

Const Mirror As Single = 0 'monitoring, recordkeeping and

 'reporting cost

Dim CAR As Double 'annualized capital cost

Const RecvCrdt As Single = 0 'recovery credit is 0 because no recovery

Dim PP As Double 'HAP PP

 Set dbs = CurrentDb

 Set rst = dbs.OpenRecordset("Vertical Tanks w/pp 0,1 psia and Control Cost")

 rst.MoveFirst

 Do While Not rst.EOF

 TankSize = rst![Tank Capacity]

 CtrlDev = rst![Control Device]

 CtrlEff = rst![Tank Control Device Efficiency (percent)]

 BaseEmiss = rst![Baseline HAP Emissions (lb/yr)]

 EmissRed = rst![HAP Reduction (lb/yr)]

 PP = rst![HAP Partial Pressure (psia)]

 

 Degas = 7.61 * (TankSize) ^ (0.5132)

 

 TankDia = Int((TankSize / 7.481) ^ (1 / 3)) + 1 'assumes cylindrical vol= pi (D^2)h/4

 'and D=(cylindrical vol)^(1/3) and

 '1 cuft = 7.481 gal

 FlRoof = 509 * (TankDia) + 1160

 RemovCond = 284 'per tank

If Not IsNull(CtrlDev) Then

 CapCost = (Degas + FlRoof + RemovCond) * (387.9 / 356)

 'escalate using cost indices from Feb 99

 'and July 1989

Else

 CapCost = (Degas + FlRoof) * (387.9 / 356)

End If 'escalate using cost indices from Feb 99

 'and July 1989

 TAC = ((CapCost * 0.2098) - (EmissRed * 0.1))

 

 

 OandM = 0.1 * CapCost

 CAR = CapCost * 0.1098 'assuming 15 yr life and 7% interest

 RC = EmissRed * 0.1
Att. 4-2

 

 rst.Edit

 

 If CtrlEff >= 95 Then

 rst![HAP Reduction (lb/yr)] = 0

 rst!IFR_TCC = 0

 rst!IFR_TAC = 0

 rst![O&M ($)] = 0

 rst![ACR ($)] = 0

 rst![MRR ($)] = Mirror

 rst![RC ($)] = 0

 Else

 rst!IFR_TCC = CapCost

 rst!IFR_TAC = TAC

 rst![O&M ($)] = OandM

 rst![ACR ($)] = CAR

 rst![MRR ($)] = Mirror

 rst![RC ($)] = RC

 End If

 

 rst.Update

 

 rst.MoveNext

 Loop

 End Sub

 
ATTACHMENT 5:

Condenser Cost Module
Att. 5-1

Attribute VB_Name = "CondenserCostCalc"

Option Compare Database

Option Explicit

Public Sub CondenserCostCalc()

Dim dbs As Database

Dim rst As Recordset

Dim PPpsia As Double 'partial pressure of 5% HAP

Dim PPmmHg As Double 'partial pressure converted from psia to mmHg

Dim HAPpsia As Double 'HAP partial pressure from table 5 of ICR

Dim Tcon As Double 'temperature of condensation, degF

Dim VOCin As Double 'VOC flow rate in the inlet, lb-mole/hr

Const Qtot As Double = 20 'Flow (scfm)

Dim Cvoc As Variant 'concentration of VOC, ppmv

Dim antA As Double 'a is antoine constant

Dim antB As Double 'b is antoine constant

Dim antC As Double 'c is antoin constant

Dim VOCout As Double 'voc flow rate in the outlet, lb-mole/hr

Const RE As Double = 95 'recovery efficiency is 95%

Dim VOCcon As Double 'flow rate of condensed VOC, lb-mole/hr

Dim dHcon As Double 'enthalpy change of the condensed VOC, Btu/lbmol

Const dHvoc As Double = 15000 'heat of condensation of the voc, Btu/hr

Const Cpvoc As Double = 20 'heat capacity of voc, btu/lb-mole-degF

Const CPair As Double = 6.95 'heat capacity of air, Btu/lb-mole-degF

Const Tin As Single = 68 'inlet stream temperature, degF

Dim dHuncon As Double 'enthalpy change of uncondensed voc, Btu/hr

Dim dHnoncon As Double 'enthalpy change of noncondensibleair, Btu/hr

Dim Hload As Double 'condenser heat load, Btu/hr

Dim Tcooli As Double 'coolant inlet temperature, degF

Dim Tcoolo As Double 'coolant outlet temperature, degF

Dim dTlm As Double 'log mean temperature difference, degF

Dim Acon As Double 'condenser surface area, sqft

Const U As Single = 20 'overall heat transfer coefficient, Btu/hr-ft2-degF

Dim Qcoolant As Double 'coolant flow rate, lb/hr

Const Cpcool As Double = 0.65 'heat capacity of coolant, Btu/hr

Dim Ref As Double 'required refrigeration capacity, tons

Dim Qrec As Double 'quantity of recovered voc, lb/yr

Dim MW As Double 'molecular weight of voc, lb/lb-mole

Dim ECr As Double 'refrigeration unit cost, $

Dim ECcon As Double 'voc condenser cost in third quart, 1990 $

Dim ECtank As Double 'recovery tank cost, $

Dim Density As Variant 'density of HAP, lb/lb-mole

Dim Qtank As Double 'recovery tank capacity requirement, gal

Const ECpre As Single = 0 'precooler equipment cost

Const ECaux As Single = 0 'auxiliary equipment cost

Dim ECc As Double 'total equipment cost, $

Dim PEC As Double 'purchased equipment cost, $

Dim TCC As Double 'total capital investment, $

Const n As Single = 8760 'operating hours for refrigeration unit are

 '24 hr/day and 7 days/week

Const e As Double = 0.059 'electricity cost, $/kWh

Const s As Double = 0.1 'salvage value of recovered voc (see Handbook -

 'pg 4-63)

Dim LaborCost As Double 'operating labor cost, $

Dim SupervCost As Double 'supervisory labor, $

Dim MaintCost As Double 'maintenance labor, $

Dim MaintMat As Double 'maintenance material, $

Dim DC As Double 'direct annual cost

Dim Ce As Double 'electrical cost intermediate, $/yr

Dim Overhead As Double

Dim PropTax As Double

Dim Admin As Double

Dim CapRecov As Double

Dim Insur As Double 'insurance

Dim RC As Double 'recovery credit

Dim IC As Double 'total indirect cost
Att. 5-2

Dim TAC As Double 'total annual cost

Dim Electric As Double 'electricity required, kWh/yr

Dim ElectricCost As Double 'electrical cost, total $,yr

Dim OandM As Double 'operating and maintenance cost

Const M As Double = 780 'monitoring, recordkeeping and reporting cost

Dim CAR As Double 'annualized capital cost

Dim EmisRed As Double 'hap reduction, lb/yr

Dim Thruput As Double '1995 tank throughput, gal/yr

Dim Filltime As Double 'Time required to fill tank

Dim Nonfill As Double 'Time not filling tank

Dim UNChap As Double 'Working losses, lb/yr

Dim CtrlEff As Double 'Control efficiency

Set dbs = CurrentDb

Set rst = dbs.OpenRecordset("Horizontal Tanks w/pp 0,1 psia and Control Cost")

rst.MoveFirst

Do While Not rst.EOF

 HAPpsia = rst![HAP Partial Pressure (psia)]

 UNChap = rst![WORKING LOSS, LBS]

 MW = rst![HAP MW]

 Density = rst![HAP Density]

 antA = rst!a

 antB = rst!b

 antC = rst!c

 EmisRed = rst![HAP Reduction (lb/yr)]

 Thruput = rst![1995 Tank Throughput]

 CtrlEff = rst![Tank Control Device Efficiency (percent)]

 

 ' ********Condenser Sizing*******

Filltime = (Thruput * 0.13368 / Qtot) / 60 'calculate required fill time/yr

Nonfill = n - Filltime 'non-fill is balance of year

 

PPmmHg = 760 * ((HAPpsia / 14.7 * (1 - RE / 100)) / (1 - (HAPpsia / 14.7) * (RE / 100)))

'PPmmHg = PPpsia * 760 / 14.69 'to convert from psia to mmHg

Tcon = (antB / (antA - (Log(PPmmHg) / Log(10))) - antC) * 1.8 + 32

VOCin = UNChap / Filltime / MW '385 scf/lb-mole at 68 degF and 1atm

VOCout = VOCin * (1 - (RE / 100))

VOCcon = VOCin - VOCout 'flow rate of condensed voc

dHcon = VOCcon * (dHvoc + Cpvoc * (Tin - Tcon)) 'enthalpy change of condensed

 'voc

dHuncon = VOCout * Cpvoc * (Tin - Tcon) 'enthalpy change due to

 'uncondensed voc

dHnoncon = ((Qtot * 60 / 385) - VOCin) * CPair * (Tin - Tcon) 'enthalpy change of

 'noncondensible air

Hload = dHcon + dHuncon + dHnoncon 'condenser heat load

Tcooli = Tcon - 15

Tcoolo = Tcooli + 25

dTlm = ((Tin - Tcoolo) - (Tcon - Tcooli)) / Log((Tin - Tcoolo) / (Tcon - Tcooli))

 'log mean temperature diff

Acon = Hload / (U * dTlm) 'condenser surface area

Qcoolant = Hload / (Cpcool * (Tcoolo - Tcooli)) 'coolant flow rate

Ref = Hload / 12000 'refrigeration capacity

Qrec = Int(VOCcon * MW) + 1 'quantity recovered/hr

 '********Cost Calculation********

 

If Tcon > -20 And Ref < 10 Then

 ECr = Exp(9.83 - 0.014 * Tcon + 0.34 * Log(Ref)) 'refrigeration unit cost for

 'single stage

ElseIf Tcon > -20 And Ref >= 10 Then

 ECr = Exp(9.26 - 0.007 * Tcon + 0.627 * Log(Ref)) 'refrigeration cost for

 'single stage

ElseIf Tcon < -20 Then

 ECr = Exp(9.73 - 0.012 * Tcon + 0.584 * Log(Ref)) 'refrigeration cost for

 'multistage
Att. 5-3

End If

'ECcon = 34 * Acon + 3775 'voc condenser cost 3rd quart,

 '1990 $

'Qtank = Qrec / Density * 24 'assuming 24-hr daily

 'operation

'If Qtank >= 50 Then

' ECtank = 2.72 * Qtank + 1960 'recovery tank cost, 1990$

'Else

' ECtank = 2.72 * 50 + 1960

'End If

'ECc = ECr + ECcon + ECtank + ECpre + ECaux 'equipment cost

ECc = 1.25 * ECr + ECaux 'Equipment cost

PEC = 1.08 * ECc 'PEC including instrumentation,

 'controls,taxes and freight

'**Filling cost**

If Tcon >= 40 Then 'these estimates were

 'developed from

 Ce = (Ref * 1.3 / 0.85) * Filltime * e 'product literature from

 'one vendor

ElseIf Tcon >= 20 And Tcon < 40 Then 'using equation

 'Ce=(Ref*E/0.85)*n*e

 Ce = (Ref * 2.2 / 0.85) * Filltime * e 'where E=electricity

 'requirement, kW/ton

ElseIf Tcon >= -20 And Tcon < 20 Then

 Ce = (Ref * 4.7 / 0.85) * Filltime * e

ElseIf Tcon >= -50 And Tcon < -20 Then

 Ce = (Ref * 5 / 0.85) * Filltime * e

ElseIf Tcon < -50 Then

 Ce = (Ref * 11.7 / 0.85) * Filltime * e

End If

ElectricCost = Ce + Ce / Filltime * Nonfill * 0.1 'Total electricity cost

 'non filling is assumed to be

 '10% of filling usage, $/yr.

Electric = ElectricCost / e 'Electricity use kWhr/yr

'RC = Qrec * Filltime * s 'recovery credit

RC = 0.1 * EmisRed

If Ref < 7 Then

 LaborCost = 0

Else: LaborCost = 0.5 / 8 * n * 15.64 'labor cost is $15.64 /hr

End If

SupervCost = 0.15 * LaborCost '15% of labor cost

MaintCost = 0.5 / 8 * n * 17.21 'maintenance labor is

 '$17.21/hr

MaintMat = MaintCost

DC = ElectricCost + LaborCost + MaintCost + MaintMat + SupervCost 'DC

Overhead = 0.6 * (LaborCost + SupervCost + MaintCost + MaintMat) '60% of labor and

 'maintenance

TCC = (1.15 * PEC) * (106.1 / 100) * (99.3 / 103.3) + M 'multiplying by Vatavuk

 'cost indexes for

 '1st quarter 99$

 'relative to 3rd

 'quarter 90$

Admin = 0.02 * TCC

PropTax = 0.01 * TCC

Insur = 0.01 * TCC

CAR = 0.1098 * TCC 'capital recovery for a 15

 'year lifetime and 7%

 'interest rate
Att. 5-4

IC = Overhead + Admin + PropTax + Insur + CAR

TAC = (DC + IC - RC) + 5940 'add $5940 for monitoring costs

OandM = TAC - CAR + RC

rst.Edit

If CtrlEff >= 95 Then

 rst!CondenserTCC = 0

 rst!CondenserTAC = 0

 rst![Electricity (kWh/yr)] = 0

 rst![O&M ($)] = 0

 rst![MRR ($)] = 0

 rst![ACR ($)] = 0

 rst![RC ($)] = 0

 rst![Recovery] = Qrec

 rst![T cond] = Tcon

 

 Else

 rst![Conc] = Cvoc

 'rst![VOCin] = VOCin

 'rst![VOCout] = VOCout

 'rst![VOC] = VOCcon

 'rst![Hload] = Hload

 'rst![Tlogmean] = dTlm

 'rst![Condarea] = Acon

 'rst![Qcool] = Qcoolant

 'rst![ECr] = ECr

 'rst![ECc] = ECc

 'rst![PEC] = PEC

 'rst![LaborCost] = LaborCost

 'rst![SupervCost] = SupervCost

 'rst![MaintCost] = MaintCost

 'rst![DC] = DC

 'rst![Overhead] = Overhead

 'rst![IC] = IC

 rst!CondenserTCC = TCC

 rst!CondenserTAC = TAC

 rst![Electricity (kWh/yr)] = Electric

 rst![O&M ($)] = OandM

 rst![MRR ($)] = M

 rst![ACR ($)] = CAR

 rst![RC ($)] = RC

 rst![Recovery] = Qrec

 rst![T cond] = Tcon

 End If

 

 rst.Update

 rst.MoveNext

Loop

End Sub