### 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.1This 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).

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•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.1Attachment 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.

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TABLE 1. MACT FLOOR AND REGULATORY ALTERNATIVES

FOR EXISTING AND NEW SOURCES

Regulatory alternative Control requirement Applicability cutoffs

Tank size, galPartial pressure,

psia Existing sources

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

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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.2We 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.

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•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.5Thus, 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.6The 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 1989.7,8Annual 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.9The 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

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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.10,11The 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–Controlof 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

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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 FacilitiesAtt.1-1 

# MACT Floor Ranking of Facilities

RankPlant Name City StateThreshold Total tanksMACT tanksRunning 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 10Novartis Crop Protection, Inc. - St. Gabriel Plant Site St. Gabriel LA 1.02 2 2 0.319 11Akzo Nobel Chemicals Inc. Morris IL 1.63 3 3 0.438 12Ciba Specialty Corp. Newport Plant Newport DE 1.86 6 6 0.557 13Troy Chemical Corporation Newark NJ 1.87 1 1 0.658 14AIR PRODUCTS, INCORPORATED/HARRIS/HG0011L LA PORTE TX 1.93 5 5 0.749 15AMOCO CHEMICAL COMPANY/BRAZORIA/BL0002S ALVIN TX 1.93 2 2 0.828 16Monsanto Gonzalez FL 2.40 1 1 0.926 17ARISTECH CHEMICAL CORPORATION/HARRIS/HG0825G PASADENA TX 2.93 2 2 1.044 18CHEVRON CHEMICAL COMPANY/HARRIS/HG0310V BAYTOWN TX 2.93 4 1 1.149 19EXXON CHEMICAL AMERICAS/CHAMBERS/CI0009P 2.93 2 2 1.243 20FORMOSAPLASTICS CORP. OF TEXAS/CALHOUN/CB0038Q POINT COMFORTTX 2.93 5 5 1.327 21HUNTSMAN CORPORATION/JEFFERSON/JE0135Q 2.93 5 1 1.403 22BASF Corporation - PVP Plant Geismar LA 3.20 1 1 1.485 23The Lubrizol Corporation - Bayport Plant Pasadena TX 3.39 15 12 1.568 24Kodak Park - Synthetic Chemicals Division Rochester NY NT 4 25Akzo Nobel Resins E. St. Louis IL NT 1 26PPG Industries, Inc. Oak Creek WI NT 19 27PPG - Circleville Resin Plant Circleville OH NT 28 28PPG - Delaware Resin Plant Delaware OH NT 5 29DUPONT FRONT ROYAL SITE FRONT ROYAL VA NT 25 30Witco Corp. - Sistersville Plant Friendly WV NT 7 31The NutraSweet Kelco Company Augusta GA NT 3 32BFGoodrich Co. Akron OH NT 2 33Du Pont - Fort Madison Plant Fort Madison IA NT 15 34DynaChem, Inc. Georgetown IL NT 1 35Flexsys Nitro Plant Nitro WV NT 4 36E. I. Du Pont de Nemours & Co. Inc. - Washington Works Parkersburg WV NT 5 2 37Exxon Chemical Americas - Bayway Chemical Plant Linden NJ NT 5 38Ciba Specialty Chemicals Corp McIntosh AL NT 51 36 39The Lubrizol Corporation Painesville OH NT 15 2 40Albright & Wilson Americas Inc. Charleston SC NT 2 41Arizona Chemical Panama City FL NT 6 42Huntsman Petrochemical Corporation - Dayton Manufacturing Facility Dayton TX NT 43 43Akzo Nobel Resins Louisville KY NT 2Att.1-2 

# MACT Floor Ranking of Facilities

(continued)

RankPlant Name City StateThreshold Total tanksMACT tanksRunning Avg 44Albemarle Corporation - South Plant Magnolia AR NT 8 4 45Hercules, Inc. - Hattiesburg, MS Plant Hattiesburg MS NT 5 46Franklin International - Polymer Division Columbus OH NT 5 47The Euclid Chemical Co. Cleveland OH NT 1 48Para-Chem, Inc.- Simpsonville Plant Simpsonville SC NT 3 49The Glidden Company Huron OH NT 5 50Evans Chemetics Waterloo NY NT 1 51THE GOODYEAR TIRE & RUBBER COMPANY NIAGARA FALLS NY NT 4 52Tennessee Eastman Division Kingsport TN NT 28 53BPCI - Sand Springs Manufacturing Plant Sand Springs OK NT 17 54Geo Specialty Chemicals Cedartown GA NT 3 55Elf Atochem North America, Inc. - Channelview Complex Channelview TX NT 2 56Union Camp Corporation Dover OH NT 8 57Cytec Industries Wallingford CT NT 1 58CCP- Houston Facility Houston TX NT 2 1 59CCP-North Kansas City Facility North Kansas CityMO NT 5 60CCP-Saukville Facility Saukville WI NT 5 61HENKEL CORPORATION - LOS ANGELES OPERATIONS LOS ANGELES CA NT 1 62Morton International Inc. - Ringwood Plant Ringwood IL NT 5 63Arkansas Eastman Division Batesville AR NT 11 64ISP Chemicals Inc. Calvert City KY NT 10 65Henkel Corporation Kankakee IL NT 6 66DIXIE CHEMICAL COMPANY PASADENA TX NT 38 6 67Rohm and Haas Company - Bristol Site Bristol PA NT 22 68E. I. DuPont de Nemours & Co., Inc. - Chamber Works Deepwater NJ NT 3 69BASF Corporation - Freeport Works Freeport TX NT 2 70Sigma Chemical Company - Second Street Plant St. Louis MO NT 11 71Huls America, Inc. Theodore AL NT 4 2 72Union Carbide Corporation - South Charleston Plant South Charleston WV NT 39 1 73Zeneca Specialties, Inc. - Mt. Pleasant Site Mt. Pleasant TN NT 4 74Sartomer Company, Inc. West Chester PA NT 6 75Stepan Millsdale Plant Elwood IL NT 15 76Schenectady International, Inc. - Texas Operations Freeport TX NT 3 77Unitex Chemical Corporation Greensboro NC NT 6 783M Decatur Decatur AL NT 4 793M Company - Cottage Grove Cottage Grove MN NT 9 803M Company - Cordova Cordova IL NT 13 81National Starch and Chemical Company - Meredosia Meredosia IL NT 8 1 82Neville Chemical Company - Neville Island Facility Pittsburgh PA NT 6 833M SPRINGFIELD ITSD/TMD / SPRINGFIELD, MO SPRINGFIELD MO NT 13 11 84THE DOW CHEMICAL COMPANY/HARRIS/HG0769O LA PORTE TX NT 1 85REXENE CORPORATION/ECTOR/EB0108J ODESSA TX NT 1 86LYONDELL PETROCHEMICAL COMPANY/VICTORIA/VC0065E NT 3Att.1-3 

# MACT Floor Ranking of Facilities

(continued)

RankPlant Name City StateThreshold Total tanksMACT tanksRunning Avg 87GOODYEAR TIRE AND RUBBER CO THE/JEFFERSON/JE0039N BEAUMONT TX NT 2 88EASTMAN CHEMICAL COMPANY/HARRISON/HH0042M NT 12 89E.I. DU PONT DE NEMOURS AND COMPANY/VICTORIA/VC0008Q VICTORIA TX NT 16 2 90ANGUS - STERLINGTON OPERATIONS STERLINGTON LA NT 14 91BAYER CORPORATION/CHAMBERS/CI0016S BAYTOWN TX NT 1 92Rohm & Haas Texas, Rohm & Haas Lone Star, RohMax Deer Park TX NT 1 93Buffalo Color Company Buffalo NY NT 3 94Uniroyal Chemical Co., Inc. Naugatuck CT NT 4 95Witco Corporation Mapleton IL. NT 1 96Hickson DanChem Corporation Danville VA NT 3 97The C. P. Hall Company Bedford Park IL NT 3 98Niacet Corporation Niagara Falls NY NT 2 99E.I. DU PONT DE NEMOURS & COMPANY/HARRIS/HG0218K PASADENA TX NT 18 100The Procter & Gamble Manufacturing Company Sacramento CA NT 2 101Reilly Industries, Inc. Indianapolis IN NT 80 3 102Abemarle Coporation Orangeburg SC NT 13 1 103Kalama Chemical, Inc. Kalama WA NT 1 104The Lubrizol Corporation - Deer Park Plant Deer Park TX NT 2 105Zeeland Chemicals, Inc. Zeeland MI NT 4 106DuPont Sabine River Works Orange TX NT 11 8 107Blue Ash Polymer/Waterbase Plant Blue Ash OH NT 2 108Salsbury Chemicals, Inc. Charles City IA NT 1 109Chemol Co.,Inc. Greensboro NC NT 3 110DuPont Mt. Clemens Plant Mt. Clemens MI NT 10 111Great Lakes Chemical Corporation - South El Dorado AR NT 4 112Amerchol-Edison Edison NJ NT 1 113Henkel Corporation - Cincinnati Plant Cincinnati OH NT 1 114Henkel Corporation - Charlotte, NC Plant Charlotte NC NT 3 115Cincinnati Specialties,Inc. Cincinnati OH NT 1 116Akzo Nobel Chemicals Inc., Gallipolis Ferry Plant Gallipolis Ferry WV NT 5 117BFG Henry Plant Henry IL NT 2 118Olin Corporation Rochester NY NT 4 119Ashland Chemical Company - Calumet City, Specialty Products and Adhesives Calumet City IL NT 3 120Ashland Chemical Company - Petrochem Div. - Neville Island Plant Pittsburgh PA NT 26 121Ashland Chemical Company - Ashtabula Composite Polymers Ashtabula OH NT 14 122Ashland Chemical Company - Composite Polymers Div. - Bartow Manufacturing Facility Bartow FL NT 8

123Dow Corning Corporation - Midland Plant Midland MI NT 3 1243V Inc. Georgetown SC NT 22 125Hercules Incorporated - Jefferson Plant West Elizabeth PA NT 9 126Allco Chemical Corporation - Jayhawk Plant Galena KS NT 2 127Hercules - Brunswick Plant Brunswick GA NT 1 128Hilton Davis Co. Cincinnati OH NT 5Att.1-4 

# MACT Floor Ranking of Facilities

(continued)

RankPlant Name City StateThreshold Total tanksMACT tanksRunning Avg 129W.G. Krummrich Plant Sauget IL NT 2 130Ashland Chemical Company - Jacksonville, AR - Composite Polymers Jacksonville AR NT 9 7 131WESTVACO DE RIDDER LA NT 9 132Ashland 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 processesAtt.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 $0Att.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 $1,845Att.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 $996Att.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 $10,359Att.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 $13,847Att.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 1052770595 13,000 5.11 5,336 0 5,336 5,069 $9,545 $1,496 $590 239 106T-08 19,080 3.54 2,338 0 2,338 2,221 $10,333 $1,946 $1,752 240 106T-753 19,080 4.04 715 0 715 679 $10,333 $2,100 $6,185 241 107T-443 10,030 8.50 1,982 Scrubber 0 1,982 1,883 $9,167 $1,735 $1,843 242 109V129B 11,000 1.90 351 0 351 333 $8,903 $1,834 $11,013 243 110V-334 12,500 1.87 206 0 206 196 $8,969 $1,862 $18,988 244 110V-372 12,500 1.87 206 0 206 196 $8,969 $1,862 $18,988 245 110V-374 12,500 1.87 206 0 206 196 $8,969 $1,862 $18,988 246 110V-376 12,500 1.87 206 0 206 196 $8,969 $1,862 $18,988 247 11203TK305B 14,700 1.96 290 0 290 276 $9,615 $1,990 $14,429 248 11204TK433 23,700 2.34 1,281 0 1,281 1,217 $11,041 $2,195 $3,606 249 11203V381 16,000 1.12 319 Condenser 319 303 $9,975 $2,063 $13,630 250 11202TK101 16,500 2.34 978 0 978 929 $10,239 $2,055 $4,424 251 11203V310 18,000 2.16 229 Condenser 229 218 $10,604 $2,203 $20,231 252 11203V309 16,000 1.21 139 Condenser 139 132 $9,975 $2,080 $31,605 253 11203TK310 16,000 1.12 319 Condenser 319 303 $9,975 $2,063 $13,630 254 11202TK254 18,700 1.96 355 0 355 338 $10,320 $2,131 $12,626 255 11202TK150 15,000 1.68 435 0 435 413 $9,627 $1,978 $9,568 256 11202TK104 19,200 2.11 2,723 0 2,723 2,587 $10,337 $1,910 $1,477 257 11202TK102 19,400 2.29 1,381 0 1,381 1,312 $10,344 $2,039 $3,108 258 11202TK103 48,000 1.96 904 0 904 858 $13,896 $2,830 $6,593 259 11202TK255 18,700 2.16 245 0 245 233 $10,320 $2,142 $18,398 260 119T-128 11,900 1.87 246 0 246 234 $8,943 $1,853 $15,871 261 119T-114 12,700 2.35 880 0 880 836 $8,978 $1,800 $4,308 262 124Tank 15 15,000 1.38 249 0 249 237 $9,627 $1,996 $16,857 263 124Tank 30 CS2 15,000 6.27 8,366 0 8,366 7,947 $9,627 $1,225 $308 264 125101 14,000 1.95 255 Condenser 71 74 61 $9,896 $2,070 $67,706Att.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 133PT0019 12,900 7.11 1,914 Afterburner 99 19 0 $0 $0 $0 266 133PT0020 291,000 1.63 3,443 Afterburner 99 34 0 $0 $0 $0 267 133PT0083 12,900 4.65 1,314 Afterburner 99 13 0 $0 $0 $0 268 134TF-42 50,000 4.60 3,194 0 3,194 3,034 $13,940 $2,621 $1,728 269 134TF-49 50,000 3.23 1,676 0 1,676 1,592 $13,940 $2,765 $3,474 270 134TF-32 50,000 2.26 3,053 0 3,053 2,901 $13,940 $2,635 $1,817 271 135TF-13A 20,000 2.90 394 0 394 374 $10,365 $2,137 $11,414 272 135TF-2 50,000 2.07 1,701 0 1,701 1,616 $13,940 $2,763 $3,419 273 136101-A-03 50,000 3.53 1,116 0 1,116 1,060 $13,940 $2,819 $5,318 274 137C-10 15,350 1.35 486 0 486 462 $9,641 $1,976 $8,558 275 137C-11 15,350 1.36 489 0 489 465 $9,641 $1,976 $8,507 276 137C-12 15,350 1.78 627 0 627 596 $9,641 $1,963 $6,587 277 141CRU-#068 25,000 1.76 3,358 0 3,358 3,190 $11,082 $2,006 $1,258 278 141CRU-#072 14,500 1.72 2,926 0 2,926 2,780 $9,607 $1,738 $1,250 279 1473080 10,000 1.80 2,974 Boiler 99 30 0 $0 $0 $0 280 147T-6240 17,000 2.30 35 Scrubber 0 35 33 $10,567 $2,214$133,813 281 147T-6250 17,000 2.30 35 Scrubber 0 35 33 $10,567 $2,214$133,813 282 149S404 20,000 2.35 1,210 0 1,210 1,149 $10,365 $2,060 $3,585 283 149S405 20,000 1.66 435 0 435 414 $10,365 $2,133 $10,314 284 150V-56 12,000 2.18 344 N2 Blkt 344 327 $9,257 $1,909 $11,683 285 150V-57 12,000 2.18 286 N2 Blkt 286 272 $9,257 $1,915 $14,098 286 150V-53 12,000 2.18 189 N2 Blkt 189 179 $9,257 $1,924 $21,468 287 153TS-11

(Meth.Rec.) 30,250 3.87 4,321 0 4,321 4,105 $11,790 $2,063 $1,005

288 153TS-11(Textile) 25,000 4.60 5,377 0 5,377 5,108 $11,082 $1,814 $710 289 153TS-15 (Meth.

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

290 156DT-09B 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743 291 156DT-23 11,655 1.77 104 0 104 99 $8,932 $1,864 $37,637 292 156DT-02B 10,879 1.77 469 0 469 445 $8,897 $1,822 $8,184 293 156DT-11 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743 294 156DT-30A 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743 295 156DT-09C 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743 296 156DT-08C 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743 297 156DT-06 10,613 1.77 525 0 525 498 $8,885 $1,814 $7,280 298 156DT-02A 10,879 1.77 562 0 562 534 $8,897 $1,813 $6,789 299 156DT-08A 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743 300 156DT-09A 10,879 1.77 359 0 359 341 $8,897 $1,832 $10,743 301 158441-031 12,000 1.11 231 0 231 219 $8,947 $1,855 $16,928 302 158445-008 12,000 1.11 231 0 231 219 $8,947 $1,855 $16,928 303 158441-281 15,200 6.00 1,976 0 1,976 1,878 $9,635 $1,834 $1,953 304 158441-027 12,000 6.00 1,296 0 1,296 1,231 $8,947 $1,754 $2,850 305 158441-015 20,700 1.11 198 0 198 188 $10,943 $2,277 $24,189 306 158422-199 13,500 1.03 101 Insulated but 101 96 $9,876 $2,062 $42,790Att.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 158441-452 30,500 1.11 243 0 243 231 $11,797 $2,452 $21,248 308 161T-1 16,000 6.38 2,104 Condenser 22 1,641 1,536 $9,975 $1,939 $2,524 309 162141-T-6 (5004) 17,625 1.76 985 0 985 936 $10,281 $2,063 $4,408 310 16368C 12,000 8.60 2,431 0 2,431 2,310 $8,947 $1,646 $1,425 311 16383C 15,000 5.03 1,554 0 1,554 1,476 $9,627 $1,872 $2,536 312 167Tank 714 10,147 6.99 2,895 Condenser 86 414 269 $9,172 $1,897 $14,091 313 167Tank 521 15,066 2.94 881 None 0 881 837 $9,939 $2,002 $4,786 Total483,720 362,829 341,268$2,918,341 $578,142 $3,338Att.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 $48,541Att.2-10



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

Facil. # Tank ID Tank capacityHAP partial

pressure (psia) Uncontrolled

HAP emissions (lb/yr) Control device Control efficiencyBaseline

HAP emissions (lb/yr) HAP

reduction (lb/yr) TCI ($) TAC ($/yr) CE ($/ton) 1M126METHANOL TANK 41/MEOH 50,000 1.93 1,340 NONE 0 1,340 1,273 $13,940 $2,797 $4,394 2M126METHANOL TANK 41/MEOH 50,000 1.93 1,560 NONE 0 1,560 1,482 $13,940 $2,776 $3,746 3M126CRUDE DIBASIC ESTER 18,000 1.93 3,880 VAPOR RECOVERY 0 3,880 3,686 $10,604 $1,856 $1,007

4M146D-123 CHILLED WATER 32,000 1.93 0 NONE 0 0 0 $12,393 $2,600 $13,684,211 5M257FRESH METHANOL 59,000 1.93 4,640 IFR 95 232 0 $0 $0 $0 6M257MOTHER LIQUOR 220,000 1.93 12,000 IFR 95 600 0 $0 $0 $0 7M257MOTHER LIQUOR 220,000 1.93 12,000 IFR 95 600 0 $0 $0 $0 8M257RECOVERED METHANOL 220,000 1.93 9,560 IFR 95 478 0 $0 $0 $0 9M257SEAL FLUSH METHANOL 59,000 1.93 5,200 IFR 95 260 0 $0 $0 $0 10M258DRY METHANOL STORAGE 150,000 1.93 11,600 IFR 95 580 0 $0 $0 $0 11M258SPENT HEXANE STORAGE 500,000 2.93 27,200 IFR 95 1,360 0 $0 $0 $0 12M262HEXANE STORAGE TANKS D.130,900 2.93 156,000 FLARE & CONDENSER 100 468 0 $0 $0 $0

13M262HEXANE STORAGE TANKS D.40,500 2.93 9,067 FLARE & CONDENSER 100 27 0 $0 $0 $0

14M270TANK STORAGE/TK-401/29 10,000 2.93 2,440 NONE 0 2,440 2,318 $8,856 $1,626 $1,403 15M270TANK STORAGE/TK-902/03 12,000 2.93 723 NONE 0 723 687 $8,947 $1,808 $5,265 16M270HEXANE STORAGE 80,000 2.93 8,400 IFR 95 420 0 $0 $0 $0 17M279POLYMER TANK 57,000 1.93 2,782 VAPORCONDENSERS 89 306 18 $14,953 $3,120 $339,869

18M279WASHWATER 37,000 1.93 89 NONE 0 89 85 $13,079 $2,736 $64,719 19M279VINYL ACETATE (B 95,000 3.54 358 VAPORCONDENSERS 83 61 7 $17,857 $3,742 $1,025,768

20M279VINYL ACETATE (A 95,000 3.54 200 VAPORCONDENSERS 83 34 4 $17,857 $3,744 $1,835,294

21M279VINYL ACETATE "B" DAY 158,000 1.61 4,745 NONE 0 4,745 4,508 $20,653 $3,882 $1,722 22M279VINYL ACETATE "A" DAY 158,000 1.61 5,765 NONE 0 5,765 5,477 $20,653 $3,785 $1,382 23M279VINYL "C" 375,000 1.61 8,684 NONE 0 8,684 8,249 $27,800 $5,007 $1,214 24M279VINYL "C" DAY 158,000 1.61 944 NONE 0 944 897 $20,653 $4,243 $9,461 25M279VINYL "B" 375,000 1.61 6,919 NONE 0 6,919 6,573 $27,800 $5,175 $1,575 26M279POLYMER TANK 57,000 1.93 7,276 VAPORCONDENSERS 89 800 48 $14,953 $3,094 $128,852

27M279MILLION GAL VAM. 1,000,000 1.61 17,270 VAPORCONDENSERS 82 3,074 393 $40,364 $8,247 $41,919

28M279METHYL ACETATE 84,000 1.93 9 VAPORCONDENSERS 77 2 0 $17,121 $3,592 $17,844,014

29M279METHANOL STORAGE 210,000 1.93 883 NONE 0 883 839 $22,924 $4,726 $11,265 30M279INHIBITOR STORAGE 18,000 1.93 433 NONE 0 433 412 $10,295 $2,119 $10,293 31M279CENTRATE AND WASH 375,000 1.93 175 NONE 0 175 167 $27,800 $5,816 $69,807 32M279"B" PLANT CONVERTIBLE 110,000 1.93 2,386 VAPORCONDENSERS 79 492 77 $18,644 $3,874 $101,031

33M279VINYL "A" 375,000 1.61 8,784 NONE 0 8,784 8,345 $27,800 $4,998 $1,198 34M279SODIUM METHYLATE 11,000 1.93 0 NONE 0 0 0 $8,903 $1,868 $3,269,217, 35M280B CRUDE RECEIVER 38,000 1.93 22 NONE 0 22 21 $13,105 $2,747 $267,739Att.2-11



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

Facil. # Tank ID Tank capacityHAP partial

pressure (psia) Uncontrolled

HAP emissions (lb/yr) Control device Control efficiencyBaseline

HAP emissions (lb/yr) HAP

reduction (lb/yr) TCI ($) TAC ($/yr) CE ($/ton) 36M280NO. 4 TWKA RECEIVER 50,000 1.93 15 NONE 0 15 14 $13,940 $2,923 $404,848 37M280NO. 3 TWKA STORAGE TANK500,000 1.93 2 NONE 0 2 2 $30,975 $6,498 $8,550,000 38M280NO. 3 TWKA RECEIVER 50,000 1.93 15 NONE 0 15 14 $13,940 $2,923 $404,848 39M280NO. 2 RECYCLE VA 50,000 1.61 18,716 IFR 95 936 0 $0 $0 $0 40M280HMI STORAGE 19,000 1.93 5 NONE 0 5 5 $10,330 $2,167 $912,421 41M280F CRUDE DCH STORAGE 160,000 1.93 22 NONE 0 22 21 $20,678 $4,336 $407,519 42M280E REWORK 160,000 1.93 4 NONE 0 4 4 $20,678 $4,338 $2,403,324 43M280CRUDE KA TANK - OP 104,000 1.93 18 NONE 0 18 17 $18,244 $3,826 $457,656 44M280BIG A CRUDE 552,000 1.93 84 NONE 0 84 80 $31,893 $6,683 $167,096 45M280A CRUDE RECEIVER 38,000 1.93 3 NONE 0 3 3 $13,105 $2,749 $1,702,167 46M280WASTE COLLECTION 11,000 1.93 0 NONE 0 0 0 $8,903 $1,868 $19,663,158 47M280BIG B CRUDE 552,000 1.93 8 NONE 0 8 8 $31,893 $6,690 $1,676,692 48M280RECYCLE AQUA COLUMN 12,000 1.93 0 NONE 0 0 0 $8,947 $1,877 $19,757,895 49M280WASTE ORGANIC STORAGE 18,000 1.93 215 NONE 0 215 204 $10,295 $2,139 $20,964 50M280VINYL ACETATE 100,000 1.61 18,716 IFR 95 936 0 $0 $0 $0 51M281STORAGE 12,000 2.24 60 0 60 57 $9,257 $1,936 $67,930 52M281STORAGE 17,000 13.29 60 0 60 57 $10,567 $2,211 $77,579 53M281STORAGE TANK 43 33,000 13.29 420 0 420 399 $12,730 $2,631 $13,188 54M281STORAGE TANK 215,000 13.29 2,300 0 2,300 2,185 $23,288 $4,667 $4,272 55M281REJECT 50,000 1.93 10 0 10 10 $14,250 $2,989 $629,263 56M281MOLTEN STORAGE 93,280 2.93 562 0 562 534 $17,829 $3,687 $13,812 57M281MIX TANK/ EP008T34/008T34 14,000 1.93 38 0 38 36 $9,896 $2,073 $114,848 58M281FLUX OIL TANK 67,600 3.16 1,528 0 1,528 1,451 $15,717 $3,152 $4,343 59M281CRUDE NPG 40,000 1.93 460 0 460 437 $13,464 $2,781 $12,728 60M281MOLTEN STORAGE 93,280 2.93 562 VAPOR RECOVERY 0 562 534 $17,829 $3,687 $13,812

61M281TANK 25,600 13.29 240 0 240 228 $11,964 $2,487 $21,816 62M283HEXANE STORAGE TANK 53,000 2.93 18,000 IFR 95 900 0 $0 $0 $0 63M283HEXANE STORAGE TANK 160,000 2.93 22,000 IFR 95 1,100 0 $0 $0 $0 64M289TANK T-503/ 5T6040/5T6040 85,140 2.93 320 IFR 95 16 0 $0 $0 $0 65M289TANK T-502/ 5T6020/5T6020 85,140 2.93 120 IFR 95 6 0 $0 $0 $0 66M289TANK T-501/ 5T6010/5T6010 85,140 2.93 320 IFR 95 16 0 $0 $0 $0 67M289TANK 2T-502/ 5T6030/5T6030 85,140 2.93 320 IFR 95 16 0 $0 $0 $0 68M289TANK 2T-503/ 5T6050/5T6050 85,140 2.93 320 IFR 95 16 0 $0 $0 $0 69M293STORAGE 451,000 1.68 0 NONE 0 0 0 $30,061 $6,307 $33,194,737 70M293STORAGE 24,000 1.68 507 NONE 0 507 482 $11,051 $2,270 $9,422 71M300TANK 21,000 1.93 318 NONE 0 318 302 $10,953 $2,268 $15,015 72M300TANK 109,000 2.93 200 IFR 95 10 0 $0 $0 $0 73M300TANK 42,000 2.06 81 NONE 0 81 77 $13,203 $2,762 $71,787 74M306TANK/2A/2A 20,700 2.93 1,280 NONE 0 1,280 1,216 $10,943 $2,174 $3,576 75M306TANK/2B/2B 20,700 2.93 1,280 NONE 0 1,280 1,216 $10,943 $2,174 $3,576 76M330POLY ETHYLENE PLANT 15,200 2.32 8,868 NONE 0 8,868 8,425 $9,635 $1,179 $280 77M343R-1372 SCRUBBER/TKR372 10,000 1.93 12 NONE 0 12 11 $8,856 $1,857 $325,789Att.2-12



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

Facil. # Tank ID Tank capacityHAP partial

pressure (psia) Uncontrolled

HAP emissions (lb/yr) Control device Control efficiencyBaseline

HAP emissions (lb/yr) HAP

reduction (lb/yr) TCI ($) TAC ($/yr) CE ($/ton) 78M3582-9,800 GALLON ROSIN 19,600 1.93 3,882 None 0 3,882 3,688 $10,351 $1,803 $978 79M358RESIN PRODUCT 30,000 1.93 3,882 None 0 3,882 3,688 $11,783 $2,103 $1,140 80M3583-150,000 GALLON POND 450,000 1.93 4,500 None 0 4,500 4,275 $30,053 $5,878 $2,750 81M358RXN. OIL, HEADS OR PITCH 20,000 1.93 4,500 None 0 4,500 4,275 $10,365 $1,747 $817 82M3582-16,900 GALLON RESIN 33,800 1.93 7,765 None 0 7,765 7,377 $12,442 $1,873 $508 83M358NEW ROSIN TANK, ST-25, PT 15,200 1.93 3,882 None 0 3,882 3,688 $9,635 $1,653 $896 84M44TANKS 360 AND 250,000 1.93 7,938 VAPORCONDENSERS 68 2,540 686 $24,761 $4,980 $14,523

85M44TANKS 25,000 1.68 5,040 SCRUBBER 0 50 48 $11,391 $1,911 $79,825 86M44TANKS 25,000 3.62 766 NONE 0 766 728 $11,082 $2,252 $6,189 87M44TANKS 25,000 1.68 1,450 NONE 0 1,450 1,378 $11,082 $2,187 $3,175 88M44TANKS 37,000 1.68 1,448 NONE 0 1,448 1,376 $13,079 $2,607 $3,790 89M44TANK 100,000 1.93 14,600 FLARE-WASTE 98 292 0 $0 $0 $0 90M44TANK 48,000 1.93 113 VAPORCONDENSERS 68 36 10 $14,205 $2,977 $612,551

91M44T-352,353,&354/

FB03T0354/EB 30,000 1.93 18 PROCESS CHANGE 0 18 17 $12,093 $2,535 $296,491

92M44T-352,353,&354/

FB03T0354/EB 30,000 1.93 130 NONE 0 130 124 $11,783 $2,460 $39,838

93M441100 PROCESS 10,000 6.93 2,916 NONE 0 2,916 2,770 $8,856 $1,581 $1,141 94M44TANKS 20,000 2.06 218 NONE 0 218 207 $10,365 $2,154 $20,782 95M441100 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 processesAtt. 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 10Tank 01 1.29 504 0 504 479 $10,953 $2,250 $9,401 7 10Tank 07 0.52 1,331 0 1,331 1,264 $11,019 $2,185 $3,456 8 10Tank 09 1.29 1,146 0 1,146 1,089 $11,019 $2,203 $4,046 9 10Tank 11 1.29 262 0 262 248 $9,587 $1,986 $15,988 10 10Tank 13 1.06 616 0 616 585 $9,587 $1,953 $6,677 11 10Tank 15 1.29 705 0 705 669 $9,587 $1,944 $5,808 12 10Tank 16 0.54 433 0 433 412 $9,587 $1,970 $9,571 13 10Tank 18 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025 14 10Tank 19 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025 15 10Tank 20 2.02 1,082 0 1,082 1,028 $9,587 $1,908 $3,711 16 10Tank 21 0.76 615 0 615 584 $11,019 $2,253 $7,714 17 10Tank 23 0.76 628 0 628 597 $11,019 $2,252 $7,544 18 10Tank 24 2.02 1,837 Scrubber 0 1,837 1,745 $13,414 $2,640 $3,025 19 10Tank 25 2.02 1,694 Scrubber 0 1,694 1,609 $13,414 $2,653 $3,298 20 10Tank 26 2.02 1,694 Scrubber 0 1,694 1,609 $13,414 $2,653 $3,298 21 10Tank 27 2.02 2,811 Scrubber 0 2,811 2,670 $13,414 $2,547 $1,908 22 10Tank 28 0.91 344 0 344 327 $9,587 $1,979 $12,110 23 10Tank 29 1.11 551 0 551 523 $9,587 $1,959 $7,491 24 10Tank 30 0.60 998 0 998 948 $9,587 $1,916 $4,041 25 10Tank 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 12T-352 3.15 1,898 Flare 99 19 0 $0 $0 $0 37 12T-353 3.15 3,737 Flare 99 37 0 $0 $0 $0 38 12T-354 3.15 3,737 Flare 99 37 0 $0 $0 $0 39 12T-358 3.15 3,326 Flare 99 33 0 $0 $0 $0 40 12T-382 3.15 10,350 Flare 99 104 0 $0 $0 $0 41 12T-501 1.70 472 Scrubber 0 472 449 $13,389 $2,764 $12,318 42 12T-502 1.70 2,704 Scrubber 0 2,704 2,569 $13,389 $2,552 $1,987 43 12T-503 1.70 2,704 Scrubber 0 2,704 2,569 $13,389 $2,552 $1,987 44 12T-504 1.70 1,832 Scrubber 0 1,832 1,740 $13,389 $2,635 $3,029 45 12T-505 1.70 1,832 Scrubber 0 1,832 1,740 $13,389 $2,635 $3,029Att. 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 12T-506 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844 47 12T-507 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844 48 12T-508 1.70 240 Scrubber 0 240 228 $9,257 $1,919 $16,844 49 12T-520 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160 50 12T-521 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160 51 12T-522 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627 52 12T-523 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627 53 12T-524 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627 54 12T-525 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627 55 12T-526 1.70 736 Scrubber 0 736 699 $11,391 $2,320 $6,633 56 12T-527 1.70 1,999 Scrubber 0 1,999 1,899 $11,391 $2,200 $2,317 57 12T-528 1.70 737 Scrubber 0 737 700 $11,391 $2,320 $6,627 58 12T-529 1.70 736 Scrubber 0 736 699 $11,391 $2,320 $6,633 59 12T-530 1.70 2,167 Scrubber 0 2,167 2,058 $16,479 $3,252 $3,160 60 12T-552 1.70 3,007 Scrubber 0 3,007 2,856 $15,667 $3,001 $2,101 61 15S-125 1.00 1,513 0 1,513 1,438 $9,669 $1,885 $2,622 62 15S-126 7.70 2,263 0 2,263 2,150 $10,330 $1,952 $1,816 63 15S-127 7.70 2,263 0 2,263 2,150 $10,330 $1,952 $1,816 64 15S-303 7.70 18,745 0 18,745 17,808 $10,365 $394 $44 65 15S-63 2.00 2,291 0 2,291 2,176 $9,620 $1,801 $1,655 66 2270S0148 0.64 382 0 382 363 $8,856 $1,822 $10,036 67 24S0124 0.64 243 0 243 231 $9,595 $1,990 $17,210 68 25206 1.87 1,024 Condenser 95 51 0 $0 $0 $0 69 27methanol 1.95 598 0 598 568 $9,627 $1,963 $6,909 70 29T-13 1.10 252 0 252 239 $11,051 $2,294 $19,184 71 29T-14 1.10 252 0 252 239 $11,051 $2,294 $19,184 72 29T-19 1.88 429 0 429 408 $13,846 $2,864 $14,051 73 29T-3 2.30 708 0 708 672 $11,025 $2,246 $6,682 74 29T-4 1.88 429 0 429 408 $11,025 $2,272 $11,147 75 29T-5 1.40 411 0 411 391 $11,025 $2,274 $11,646 76 29T-8 1.88 429 0 429 408 $13,846 $2,864 $14,051 77 29T-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 3271T6 0.56 1,607 0 1,607 1,527 $13,154 $2,607 $3,414 85 33209 1.90 329 0 329 313 $8,856 $1,827 $11,690 86 33508 0.66 71 0 71 67 $8,978 $1,877 $55,663 87 33645 0.77 10 0 10 9 $10,368 $2,174 $458,335 88 33646 1.30 44 0 44 41 $10,365 $2,170 $104,695 89 33682 1.90 196 0 196 186 $10,365 $2,156 $23,197Att. 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 33953 0.85 201 0 201 191 $8,879 $1,844 $19,294 91 343202F 1.02 1,512 Condenser 100 8 0 $0 $0 $0 92 36RM14 2.40 5,143 0 5,143 4,885 $11,797 $1,987 $813 93 36RTK34 1.93 320 0 320 304 $9,627 $1,989 $13,073 94 38102 2.40 3,865 0 3,865 3,672 $9,627 $1,653 $900 95 40RP_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 42160 1.22 656 0 656 623 $9,545 $1,940 $6,228 105 42180 1.80 341 0 341 324 $8,884 $1,831 $11,289 106 42185 0.50 854 0 854 811 $11,009 $2,229 $5,497 107 431010 2.73 2,545 0 2,545 2,418 $11,783 $2,230 $1,844 108 431012 0.57 110 0 110 105 $8,856 $1,847 $35,207 109 431020 3.23 2,555 0 2,555 2,427 $11,783 $2,229 $1,837 110 431030 3.52 3,823 0 3,823 3,632 $11,783 $2,109 $1,161 111 431060 2.73 1,524 0 1,524 1,447 $10,365 $2,030 $2,805 112 431070 0.79 570 0 570 542 $10,365 $2,120 $7,830 113 431080 0.79 271 0 271 258 $10,365 $2,149 $16,684 114 431130 3.23 2,555 0 2,555 2,427 $11,783 $2,229 $1,837 115 431150 1.08 400 0 400 380 $10,365 $2,137 $11,260 116 431180 0.79 589 0 589 559 $10,365 $2,119 $7,580 117 431200 3.23 1,108 0 1,108 1,052 $10,365 $2,069 $3,932 118 431210 1.17 725 0 725 689 $10,365 $2,106 $6,112 119 431240 0.79 289 0 289 275 $10,365 $2,147 $15,634 120 431360 1.58 580 0 580 551 $10,365 $2,119 $7,688 121 431370 0.79 213 0 213 202 $10,365 $2,154 $21,325 122 433073 0.56 623 0 623 592 $11,783 $2,413 $8,152 123 435101 1.35 1,912 0 1,912 1,817 $8,856 $1,676 $1,845 124 435102 1.35 1,912 0 1,912 1,817 $8,856 $1,676 $1,845 125 435103 1.53 1,379 0 1,379 1,310 $8,856 $1,727 $2,637 126 441982-05 1.86 362 Thermal 99 4 0 $0 $0 $0 127 441982-06 1.86 990 Thermal 99 10 0 $0 $0 $0 128 441984-25 1.86 1,544 Thermal 99 15 0 $0 $0 $0 129 441987-35 1.86 567 Thermal 99 6 0 $0 $0 $0 130 441988-15 1.86 382 Thermal 99 4 0 $0 $0 $0 131 45T-1141 1.54 1,039 0 1,039 987 $10,365 $2,076 $4,207 132 45T-1534 1.28 656 Scrubber 0 656 623 $12,093 $2,475 $7,941 133 45T-596 1.54 728 0 728 692 $10,365 $2,105 $6,083Att. 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 45T-833 4.84 1,805 Scrubber 0 1,805 1,714 $9,257 $1,771 $2,066 135 48VS 2704 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931 136 48VS 703 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931 137 48VS 704 2.50 2,442 0 2,442 2,320 $11,783 $2,240 $1,931 138 52T-1409 0.76 1,122 Condenser 99 11 0 $0 $0 $0 139 52T-2421 0.58 281 0 281 267 $11,044 $2,290 $17,143 140 52T-2431 1.00 2,564 0 2,564 2,436 $11,649 $2,200 $1,806 141 52T-2457 3.25 3,721 0 3,721 3,535 $10,244 $1,796 $1,016 142 52T-9962 0.65 94 Carbon 99 1 0 $0 $0 $0 143 52T-9964 0.65 94 Carbon 99 1 0 $0 $0 $0 144 5311-211 2.50 509 0 509 483 $8,903 $1,819 $7,529 145 5311-213 0.54 19 0 19 18 $8,903 $1,866 $207,278 146 5311-231 0.76 96 0 96 91 $8,903 $1,859 $40,881 147 5311-233 0.57 133 0 133 126 $8,903 $1,855 $29,466 148 5311-235 2.38 349 0 349 331 $8,903 $1,835 $11,082 149 5311-241 0.57 45 0 45 43 $8,903 $1,863 $87,134 150 5311-245 0.95 138 0 138 131 $8,903 $1,855 $28,295 151 5316-217 0.55 22 0 22 21 $9,666 $2,026 $196,408 152 5316-237 1.97 93 0 93 88 $9,666 $2,019 $45,814 153 5648-515 0.51 127 Condenser 92 10 4 $9,936 $2,084 $1,094,242 154 5691-1339 2.40 338 0 338 321 $11,082 $2,293 $14,266 155 57ALA01A 1.20 398 Carbon 99 4 0 $0 $0 $0 156 57ALA01B 1.20 398 Carbon 99 4 0 $0 $0 $0 157 57ALA05/4E 1.20 2,407 0 2,407 2,287 $9,587 $1,783 $1,559 158 57ALA07 1.95 307 0 307 291 $9,561 $1,977 $13,572 159 59A-17 0.66 157 Carbon 95 8 0 $0 $0 $0 160 59A86 0.66 157 Carbon 95 8 0 $0 $0 $0 161 59A87 0.66 214 Carbon 95 11 0 $0 $0 $0 162 60Tank 61 2.00 1,225 0 1,225 1,164 $10,330 $2,051 $3,525 163 60Tank 64 3.00 1,603 0 1,603 1,523 $10,330 $2,015 $2,647 164 60Tank 73 2.00 723 0 723 686 $10,330 $2,099 $6,116 165 63V-1 0.50 128 0 128 122 $9,627 $2,008 $33,004 166 63V-13 1.37 1,376 Flare 98 28 0 $0 $0 $0 167 63V-15 1.86 1,270 Flare 98 25 0 $0 $0 $0 168 63V-16 1.78 1,983 Flare 98 40 0 $0 $0 $0 169 63V-18 1.86 1,963 Flare 98 39 0 $0 $0 $0 170 63V-2 0.50 123 0 123 117 $9,627 $2,008 $34,321 171 63V-22 1.40 74 Flare 98 1 0 $0 $0 $0 172 63V-23 0.61 67 Flare 98 1 0 $0 $0 $0 173 63V-26 2.89 3,303 Flare 98 66 0 $0 $0 $0 174 63V-27 2.89 3,303 Flare 98 66 0 $0 $0 $0 175 63V-28 1.48 2,424 Flare 98 48 0 $0 $0 $0 176 63V-29 2.87 2,217 Flare 98 44 0 $0 $0 $0 177 63V-32 2.61 2,023 Flare 98 40 0 $0 $0 $0Att. 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 63V-33 6.40 437 0 437 415 $9,627 $1,978 $9,526 179 63V-34 0.74 2,072 Flare 98 41 0 $0 $0 $0 180 63V-35 2.83 401 Flare 98 8 0 $0 $0 $0 181 63V-39 0.74 2,072 Flare 98 41 0 $0 $0 $0 182 63V-4 1.05 3,148 Condenser 90 315 157 $9,936 $2,069 $26,287 183 63V-43 0.96 323 Combination 100 0 0 $0 $0 $0 184 63V-44 0.79 515 Combination 100 1 0 $0 $0 $0 185 63V-45 6.79 6,160 Combination 100 6 0 $0 $0 $0 186 63V-47 3.01 1,557 0 1,557 1,479 $9,627 $1,872 $2,531 187 63V-48 3.01 3,555 0 3,555 3,378 $9,627 $1,682 $996 188 63V-5 1.55 595 0 595 565 $9,627 $1,963 $6,947 189 63V-50 13.63 2,935 0 2,935 2,788 $9,627 $1,741 $1,249 190 63V-51 2.46 1,123 0 1,123 1,067 $9,627 $1,913 $3,586 191 63V-52 13.63 4,649 0 4,649 4,416 $9,627 $1,578 $715 192 63V-53 2.85 4,448 0 4,448 4,225 $9,627 $1,597 $756 193 63V-54 2.85 3,546 0 3,546 3,369 $9,627 $1,683 $999 194 64T027 1.86 693 0 693 658 $13,920 $2,855 $8,677 195 64T191 0.87 392 0 392 373 $11,078 $2,287 $12,270 196 65VT-1 3.66 2,416 0 2,416 2,295 $11,645 $2,214 $1,929 197 65VT-201 3.66 2,416 0 2,416 2,295 $11,645 $2,214 $1,929 198 67ST-900A 2.25 674 Scrubber 0 674 640 $12,090 $2,472 $7,720 199 67ST-900B 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792 200 67ST-918 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100 201 67ST-919 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100 202 67ST-920 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100 203 67ST-921 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 204 67ST-922 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 205 67ST-923 2.25 599 Scrubber 0 599 569 $11,381 $2,331 $8,193 206 67ST-924 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100 207 67ST-925 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100 208 67ST-926 2.25 479 Scrubber 0 479 455 $10,553 $2,168 $9,532 209 67ST-927 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 210 67ST-928 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 211 67ST-929 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482 212 67ST-934 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100 213 67ST-935 2.25 396 Scrubber 0 396 376 $9,225 $1,898 $10,100 214 67ST-940 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482 215 67ST-941 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482 216 67ST-945 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482 217 67ST-947 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482 218 67ST-948 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482 219 67ST-949 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482 220 67ST-950 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792 221 67ST-951 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792Att. 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 67ST-960 2.25 458 Scrubber 0 458 435 $9,947 $2,043 $9,384 223 67ST-964 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460 224 67ST-967 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 225 67ST-968 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460 226 67ST-970 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 227 67ST-971 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 228 67ST-972 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460 229 67ST-973 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 230 67ST-974 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 231 67ST-975 2.25 483 Scrubber 0 483 459 $10,563 $2,170 $9,460 232 67ST-981 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 233 67ST-982 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 234 67ST-983 2.25 482 Scrubber 0 482 458 $10,560 $2,170 $9,482 235 67ST-984 2.25 545 Scrubber 0 545 518 $11,263 $2,311 $8,926 236 67ST-985 2.25 545 Scrubber 0 545 518 $11,263 $2,311 $8,926 237 67ST-986 2.25 408 Scrubber 0 408 388 $9,260 $1,904 $9,819 238 67ST-987 2.25 524 Scrubber 0 524 498 $10,660 $2,187 $8,792 239 67ST-990 2.25 431 Scrubber 0 431 409 $9,876 $2,031 $9,928 240 67ST-994 2.25 385 Scrubber 0 385 365 $9,194 $1,892 $10,359 241 68ST1 1.70 42,893 IFR 95 2,145 0 $0 $0 $0 242 68ST12 0.70 717 0 717 681 $8,947 $1,809 $5,309 243 68ST2 0.60 631 0 631 600 $11,783 $2,412 $8,045 244 68ST6 1.80 291 0 291 277 $9,666 $2,000 $14,461 245 68ST7 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 73N110 2.01 495 0 495 471 $8,856 $1,811 $7,696 248 73T312 0.52 155 0 155 147 $8,856 $1,843 $25,027 249 73T326 1.06 1,139 Scrubber 0 1,139 1,082 $10,674 $2,131 $3,939 250 74Y-210 2.45 426 0 426 404 $9,639 $1,982 $9,803 251 75D501 1.90 517 0 517 491 $9,627 $1,971 $8,029 252 78SN-711 10.10 11,673 0 11,673 11,089 $10,318 $1,056 $190 253 80RS-48 0.76 687 0 687 652 $8,856 $1,793 $5,496 254 82AT-3 1.91 253 0 253 240 $8,856 $1,834 $15,276 255 82AT-4 1.91 175 0 175 166 $8,856 $1,841 $22,154 256 82AT-6 1.91 216 0 216 206 $9,587 $1,991 $19,361 257 83597 1.90 635 Condenser 90 64 32 $9,189 $1,925 $121,220 258 83606 1.90 1,719 Condenser 90 172 86 $11,391 $2,381 $55,408 259 86T-18 1.93 593 0 593 563 $10,239 $2,092 $7,428 260 872T116 (# 781) 1.39 122 0 122 116 $8,856 $1,846 $31,888 261 874T013 (# 690) 1.93 194 0 194 185 $8,856 $1,839 $19,927 262 89T-1121 2.40 290 0 290 275 $8,858 $1,831 $13,297 263 90A-165 2.03 1,128 Incinerator 99 11 0 $0 $0 $0 264 90A-177 3.39 1,058 Incinerator 99 11 0 $0 $0 $0 265 90A-208 0.74 285 Incinerator 99 3 0 $0 $0 $0Att. 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 90A-217 0.86 551 0 551 523 $11,082 $2,273 $8,685 267 90A-402 0.76 807 Flare 98 16 0 $0 $0 $0 268 90B-172 2.03 704 Incinerator 99 7 0 $0 $0 $0 269 90B-242 0.74 787 Incinerator 99 8 0 $0 $0 $0 270 90B-257 0.74 1,103 Incinerator 99 11 0 $0 $0 $0 271 90B-271 0.74 2,408 Incinerator 99 24 0 $0 $0 $0 272 90B-404 0.74 821 Flare 98 16 0 $0 $0 $0 273 90B-431 0.74 821 Flare 98 16 0 $0 $0 $0 274 90C-132 2.27 5,942 Absorber 0 5,942 5,645 $14,228 $2,420 $857 275 90C-133 2.27 5,942 Absorber 0 5,942 5,645 $14,228 $2,420 $857 276 90C-216 0.74 1,858 Incinerator 99 19 0 $0 $0 $0 277 90C-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 9211 0.68 193 0 193 184 $9,633 $2,003 $21,811 283 92111 1.13 1,996 0 1,996 1,896 $19,755 $3,955 $4,172 284 9212 0.68 186 0 186 177 $9,633 $2,003 $22,656 285 9213 0.68 181 0 181 172 $9,632 $2,004 $23,306 286 9214 0.68 172 0 172 164 $9,632 $2,004 $24,461 287 92211 1.35 516 0 516 491 $10,354 $2,123 $8,654 288 92212 1.35 764 0 764 726 $10,354 $2,100 $5,784 289 92216 1.35 599 0 599 569 $10,354 $2,115 $7,428 290 92236 0.68 376 0 376 357 $12,393 $2,564 $14,373 291 92241 1.35 380 0 380 361 $10,356 $2,137 $11,854 292 92252 1.61 423 0 423 402 $10,355 $2,132 $10,612 293 92253 1.61 461 0 461 438 $10,355 $2,129 $9,715 294 92254 1.35 913 IFR 95 46 0 $0 $0 $0 295 92260 8.06 8,992 0 8,992 8,542 $13,137 $1,902 $445 296 92261 5.78 5,291 0 5,291 5,026 $13,137 $2,254 $897 297 92304 1.51 337 0 337 321 $9,633 $1,989 $12,410 298 92331 0.87 367 0 367 349 $10,981 $2,269 $13,008 299 92535 0.57 418 0 418 397 $8,932 $1,834 $9,231 300 92536 0.57 453 0 453 431 $8,932 $1,831 $8,501 301 92542 0.66 349 0 349 331 $8,932 $1,841 $11,121 302 92546 0.66 510 0 510 485 $8,932 $1,825 $7,531 303 92620 1.11 375 0 375 357 $11,777 $2,435 $13,659 304 92622 1.05 313 0 313 297 $11,777 $2,441 $16,417 305 92632 0.52 176 0 176 167 $11,776 $2,454 $29,311 306 92701 1.09 230 0 230 218 $8,873 $1,840 $16,856 307 92710 0.77 2,454 0 2,454 2,332 $24,536 $4,914 $4,215 308 92719 0.58 109 0 109 103 $8,860 $1,848 $35,752 309 92720 1.10 213 0 213 202 $8,860 $1,839 $18,205Att. 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 92721 0.86 179 0 179 170 $8,860 $1,842 $21,682 311 92726 0.67 105 0 105 100 $8,857 $1,848 $36,957 312 92727 1.09 166 0 166 158 $8,857 $1,842 $23,310 313 92777 1.09 279 0 279 265 $8,861 $1,833 $13,847 314 92778 1.09 248 0 248 235 $8,863 $1,836 $15,597 315 92779 1.09 255 0 255 242 $8,863 $1,835 $15,153 316 92792 1.09 258 0 258 245 $9,622 $1,994 $16,294 317 93TK-592 3.20 1,189 Flare 98 24 0 $0 $0 $0 318 94505#1 0.55 1,377 0 1,377 1,308 $13,940 $2,794 $4,272 319 94505#3 0.55 633 0 633 602 $10,365 $2,114 $7,029 320 1052770171 0.59 1,095 0 1,095 1,040 $9,545 $1,899 $3,651 321 1052770595 5.11 5,336 0 5,336 5,069 $9,545 $1,496 $590 322 106T-08 3.54 2,338 0 2,338 2,221 $10,333 $1,946 $1,752 323 106T-753 4.04 715 0 715 679 $10,333 $2,100 $6,185 324107T-443 8.50 1,982 Scrubber 0 1,982 1,883 $9,167 $1,735 $1,843 325 109V129B 1.90 351 0 351 333 $8,903 $1,834 $11,013 326 110V-334 1.87 206 0 206 196 $8,969 $1,862 $18,988 327110V-372 1.87 206 0 206 196 $8,969 $1,862 $18,988 328 110V-374 1.87 206 0 206 196 $8,969 $1,862 $18,988 329 110V-376 1.87 206 0 206 196 $8,969 $1,862 $18,988 330 11202TK101 2.34 978 0 978 929 $10,239 $2,055 $4,424 331 11202TK102 2.29 1,381 0 1,381 1,312 $10,344 $2,039 $3,108 332 11202TK103 1.96 904 0 904 858 $13,896 $2,830 $6,593 333 11202TK104 2.11 2,723 0 2,723 2,587 $10,337 $1,910 $1,477 33411202TK150 1.68 435 0 435 413 $9,627 $1,978 $9,568 335 11202TK254 1.96 355 0 355 338 $10,320 $2,131 $12,626 336 11202TK255 2.16 245 0 245 233 $10,320 $2,142 $18,398 33711203TK305B 1.96 290 0 290 276 $9,615 $1,990 $14,429 338 11203TK310 1.12 319 Condenser 319 303 $9,975 $2,063 $13,630 $0 339 11203V309 1.21 139 Condenser 139 132 $9,975 $2,080 $31,605 $0 340 11203V310 2.16 229 Condenser 229 218 $10,604 $2,203 $20,231 $0 341 11203V369 0.76 126 Condenser 126 119 $9,975 $2,081 $34,837 $0 342 11203V374 0.62 79 Condenser 79 75 $9,975 $2,085 $55,396 $0 343 11203V381 1.12 319 Condenser 319 303 $9,975 $2,063 $13,630 $0 34411204TK433 2.34 1,281 0 1,281 1,217 $11,041 $2,195 $3,606 345 118T-141 0.51 815 0 815 774 $9,623 $1,942 $5,019 346 118T-224 0.55 271 Afterburner 95 14 0 $0 $0 $0 347119T-114 2.35 880 0 880 836 $8,978 $1,800 $4,308 348 119T-128 1.87 246 0 246 234 $8,943 $1,853 $15,871 349 124Tank 15 1.38 249 0 249 237 $9,627 $1,996 $16,857 350 124Tank 30 CS2 6.27 8,366 0 8,366 7,947 $9,627 $1,225 $308 351 125101 1.95 255 Condenser 71 74 61 $9,896 $2,070 $67,706 352 1311155-01 0.66 3,294 IFR 95 165 0 $0 $0 $0 353 1311250-01 0.90 2,865 IFR 95 143 0 $0 $0 $0Att. 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 1311250-02 0.66 3,294 IFR 95 165 0 $0 $0 $0 355 1311650-01 0.66 8,548 IFR 95 427 0 $0 $0 $0 356 133PT0019 7.11 1,914 Afterburner 99 19 0 $0 $0 $0 357133PT0020 1.63 3,443 Afterburner 99 34 0 $0 $0 $0 358 133PT0083 4.65 1,314 Afterburner 99 13 0 $0 $0 $0 359 134TF-32 2.26 3,053 0 3,053 2,901 $13,940 $2,635 $1,817 360 134TF-33 0.74 1,432 0 1,432 1,360 $13,940 $2,789 $4,101 361 134TF-42 4.60 3,194 0 3,194 3,034 $13,940 $2,621 $1,728 362 134TF-49 3.23 1,676 0 1,676 1,592 $13,940 $2,765 $3,474 363 135TF-13A 2.90 394 0 394 374 $10,365 $2,137 $11,414 364135TF-14 0.87 379 0 379 360 $10,365 $2,139 $11,872 365 135TF-17 0.95 430 0 430 409 $10,365 $2,134 $10,447 366 135TF-2 2.07 1,701 0 1,701 1,616 $13,940 $2,763 $3,419 367135TF-3B 0.53 460 0 460 437 $13,940 $2,881 $13,177 368 135TF-6 0.66 1,016 0 1,016 965 $13,940 $2,828 $5,859 369 136101-A-01 0.80 743 0 743 706 $13,940 $2,854 $8,084 370 136101-A-03 3.53 1,116 0 1,116 1,060 $13,940 $2,819 $5,318 371 136398-A-32 0.55 282 0 282 268 $10,365 $2,148 $16,054 372 136398-A-34 0.65 190 0 190 180 $10,365 $2,157 $23,931 373 137C-10 1.35 486 0 486 462 $9,641 $1,976 $8,558 374137C-11 1.36 489 0 489 465 $9,641 $1,976 $8,507 375 137C-12 1.78 627 0 627 596 $9,641 $1,963 $6,587 376 137C-9 0.75 282 0 282 268 $9,641 $1,996 $14,915 377141CRU-#068 1.76 3,358 0 3,358 3,190 $11,082 $2,006 $1,258 378 141CRU-#072 1.72 2,926 0 2,926 2,780 $9,607 $1,738 $1,250 379 143T1201 0.54 450 0 450 428 $9,643 $1,980 $9,255 380 143T1202 0.54 450 0 450 428 $9,643 $1,980 $9,255 381 143T1215 0.54 776 0 776 738 $9,667 $1,954 $5,298 382 143T1216 0.54 811 0 811 771 $10,955 $2,221 $5,763 383 143T203 0.54 1,231 0 1,231 1,170 $8,879 $1,746 $2,986 3841473056 0.60 177 0 177 168 $8,856 $1,841 $21,934 385 1473080 1.80 2,974 Boiler 99 30 0 $0 $0 $0 386 147T-6240 2.30 35 Scrubber 0 35 33 $10,567 $2,214 $133,813 387147T-6250 2.30 35 Scrubber 0 35 33 $10,567 $2,214 $133,813 388 149S262 0.55 337 Thermal 99 3 0 $0 $0 $0 389 149S404 2.35 1,210 0 1,210 1,149 $10,365 $2,060 $3,585 390 149S405 1.66 435 0 435 414 $10,365 $2,133 $10,314 391 149S410 0.55 187 Thermal 99 2 0 $0 $0 $0 392 150V-53 2.18 189 N2 Blkt 189 179 $9,257 $1,924 $21,468 $0 393 150V-56 2.18 344 N2 Blkt 344 327 $9,257 $1,909 $11,683 $0 394150V-57 2.18 286 N2 Blkt 286 272 $9,257 $1,915 $14,098 $0 395 150V-61 0.51 88 N2 Blkt 88 83 $9,257 $1,934 $46,452 $0 396 150V-63 0.54 137 N2 Blkt 137 130 $9,257 $1,929 $29,666 $0 397150V-64 0.55 84 N2 Blkt 84 80 $9,257 $1,934 $48,306 $0Att. 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 150V-69 0.66 63 N2 Blkt 63 60 $9,257 $1,936 $65,066 $0 399 153TS-11 3.87 4,321 0 4,321 4,105 $11,790 $2,063 $1,005 400 153TS-11(Textile) 4.60 5,377 0 5,377 5,108 $11,082 $1,814 $710 401 153TS-15 (Meth. 3.87 4,321 0 4,321 4,105 $11,790 $2,063 $1,005 402 156DT-02A 1.77 562 0 562 534 $8,897 $1,813 $6,789 403 156DT-02B 1.77 469 0 469 445 $8,897 $1,822 $8,184 404156DT-06 1.77 525 0 525 498 $8,885 $1,814 $7,280 405 156DT-08A 1.77 359 0 359 341 $8,897 $1,832 $10,743 406 156DT-08C 1.77 359 0 359 341 $8,897 $1,832 $10,743 407156DT-09A 1.77 359 0 359 341 $8,897 $1,832 $10,743 408 156DT-09B 1.77 359 0 359 341 $8,897 $1,832 $10,743 409 156DT-09C 1.77 359 0 359 341 $8,897 $1,832 $10,743 410 156DT-11 1.77 359 0 359 341 $8,897 $1,832 $10,743 411 156DT-22 0.66 2,117 0 2,117 2,011 $8,897 $1,666 $1,657 412 156DT-23 1.77 104 0 104 99 $8,932 $1,864 $37,637 413 156DT-30A 1.77 359 0 359 341 $8,897 $1,832 $10,743 414156XT-04A 0.66 1,932 0 1,932 1,835 $11,089 $2,143 $2,335 415 157TK 5731 0.57 298 0 298 283 $8,903 $1,839 $13,007 416 158422-199 1.03 101 Insulated but 101 96 $9,876 $2,062 $42,790 $0 417158441-015 1.11 198 0 198 188 $10,943 $2,277 $24,189 418 158441-025 0.74 245 0 245 233 $8,947 $1,854 $15,921 419 158441-027 6.00 1,296 0 1,296 1,231 $8,947 $1,754 $2,850 420 158441-028 0.74 75 0 75 71 $8,947 $1,870 $52,566 421 158441-031 1.11 231 0 231 219 $8,947 $1,855 $16,928 422 158441-281 6.00 1,976 0 1,976 1,878 $9,635 $1,834 $1,953 423 158441-421 0.72 186 0 186 177 $11,797 $2,457 $27,830 424158441-422 0.72 167 0 167 158 $11,797 $2,459 $31,066 425 158441-452 1.11 243 0 243 231 $11,797 $2,452 $21,248 426 158445-008 1.11 231 0 231 219 $8,947 $1,855 $16,928 427161T-1 6.38 2,104 Condenser 22 1,641 1,536 $9,975 $1,939 $2,524 428 162141-T-6 (5004) 1.76 985 0 985 936 $10,281 $2,063 $4,408 429 16329C 0.95 476 0 476 452 $8,947 $1,832 $8,107 430 16368C 8.60 2,431 0 2,431 2,310 $8,947 $1,646 $1,425 431 16383C 5.03 1,554 0 1,554 1,476 $9,627 $1,872 $2,536 432 167Tank 521 2.94 881 None 0 881 837 $9,939 $2,002 $4,786 433 167Tank 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 $4,045Att. 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 10167 Tank 377 2.94 1,701 Thermal oxidizer 99 17 0 $0 $0 $0 11134 23-6 2.79 812 0 812 771 $30,701 $40,965 $106,218 12161 T-16 2.78 974 0 974 926 $25,509 $40,112 $86,659 13166 TP930 HT13 2.10 335 None 0 335 318 $31,764 $41,069 $258,409 14166 TP930 HT-6 2.10 335 None 0 335 318 $31,764 $41,069 $258,409 15166 TP930 HT-1 2.10 335 None 0 335 318 $31,764 $41,069 $258,409 16137 U-9 1.95 541 0 541 514 $32,029 $41,130 $160,175 17137 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 20156 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 23130 T-325A 1.70 1,437 0 1,437 1,365 $24,640 $39,973 $58,552 24141 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 26167 Tank 1219 1.61 2,537 Thermal oxidizer 99 25 0 $0 $0 $0 27167 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 37167 Tank 368 0.96 1,055 Thermal oxidizer 99 11 0 $0 $0 $0 38167 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 46134 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 $54,532Att. 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 efficiencyBaseline HAP

emissions (lb/yr) HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton) 1 M126CRUDE DIBASIC 1.93 3,880 VAPOR RECOVERY 0 3,880 3,686.00 $11,578 $2,451 $1,330 2M126METHANOL TANK 1.93 1,340 NONE 0 1,340 1,273.00 $15,221 $3,648 $5,731 3M126METHANOL TANK 1.93 1,560 NONE 0 1,560 1,482.00 $15,221 $3,623 $4,889 4M146D-123 CHILLED 1.93 0 NONE 0 0 0.38 $13,532 $3,377 $17,773,684 5M257FRESH METHANOL 1.93 4,640 IFR 95 232 0.00 $0 $0 $0 6M257MOTHER LIQUOR 1.93 12,000 IFR 95 600 0.00 $0 $0 $0 7M257MOTHER LIQUOR 1.93 12,000 IFR 95 600 0.00 $0 $0 $0 8M257RECOVERED 1.93 9,560 IFR 95 478 0.00 $0 $0 $0 9M257SEAL FLUSH 1.93 5,200 IFR 95 260 0.00 $0 $0 $0 10M258DRY METHANOL 1.93 11,600 IFR 95 580 0.00 $0 $0 $0 11M258SPENT HEXANE 2.93 27,200 IFR 95 1,360 0.00 $0 $0 $0 12M262HEXANE STORAGE 2.93 156,000 FLARE & CONDENSER 100 468 0.00 $0 $0 $0

13M262HEXANE STORAGE 2.93 9,067 FLARE & CONDENSER 100 27 0.00 $0 $0 $0

14M270HEXANE STORAGE 2.93 8,400 IFR 95 420 0.00 $0 $0 $0 15M270TANK 2.93 2,440 NONE 0 2,440 2,318.00 $9,669 $2,138 $1,845 16M270TANK 2.93 723 NONE 0 723 686.85 $9,769 $2,357 $6,863 17M279"B" PLANT 1.93 2,386 VAPORCONDENSERS 79 492 76.69 $20,357 $5,037 $131,361

18M279CENTRATE AND 1.93 175 NONE 0 175 166.63 $30,354 $7,556 $90,692 19M279INHIBITOR 1.93 433 NONE 0 433 411.73 $11,240 $2,757 $13,392 20M279METHANOL 1.93 883 NONE 0 883 839.04 $25,030 $6,148 $14,655 21M279METHYL ACETATE 1.93 9 VAPORCONDENSERS 77 2 0.40 $18,693 $4,666 $23,179,334

22M279MILLION GAL VAM. 1.61 17,270 VAPORCONDENSERS 82 3,074 393.47 $44,072 $10,737 $54,576

23M279POLYMER TANK 1.93 2,782 VAPORCONDENSERS 89 306 18.36 $16,327 $4,055 $441,721

24M279POLYMER TANK 1.93 7,276 VAPORCONDENSERS 89 800 48.02 $16,327 $4,023 $167,541

25M279SODIUM 1.93 0 NONE 0 0 0.00 $9,720 $2,426 $4,245,782, 26M279VINYL "A" 1.61 8,784 NONE 0 8,784 8,345.18 $30,354 $6,583 $1,578 27M279VINYL "B" 1.61 6,919 NONE 0 6,919 6,572.86 $30,354 $6,794 $2,067 28M279VINYL "C" DAY 1.61 944 NONE 0 944 896.99 $22,551 $5,522 $12,312 29M279VINYL "C" 1.61 8,684 NONE 0 8,684 8,249.42 $30,354 $6,595 $1,599 30M279VINYL ACETATE "A" 1.61 5,765 NONE 0 5,765 5,476.56 $22,551 $4,977 $1,818 31M279VINYL ACETATE "B" 1.61 4,745 NONE 0 4,745 4,507.94 $22,551 $5,092 $2,259 32M279VINYL ACETATE (A 3.54 200 VAPORCONDENSERS 83 34 4.08 $19,498 $4,864 $2,384,314

33M279VINYL ACETATE (B 3.54 358 VAPORCONDENSERS 83 61 7.30 $19,498 $4,862 $1,332,785

34M279WASHWATER 1.93 89 NONE 0 89 84.55 $14,281 $3,554 $84,069 35M280A CRUDE 1.93 3 NONE 0 3 3.23 $14,309 $3,571 $2,211,146 36M280B CRUDE 1.93 22 NONE 0 22 20.52 $14,309 $3,569 $347,856 37M280BIG A CRUDE 1.93 84 NONE 0 84 79.99 $34,823 $8,682 $217,077 38M280BIG B CRUDE 1.93 8 NONE 0 8 7.98 $34,823 $8,691 $2,178,195Att. 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 efficiencyBaseline HAP

emissions (lb/yr) HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton) 39M280CRUDE KA TANK - 1.93 18 NONE 0 18 16.72 $19,920 $4,970 $594,498 40M280E REWORK 1.93 4 NONE 0 4 3.61 $22,578 $5,635 $3,121,884 41M280F CRUDE DCH 1.93 22 NONE 0 22 21.28 $22,578 $5,633 $529,417 42M280HMI STORAGE 1.93 5 NONE 0 5 4.75 $11,279 $2,815 $1,185,263 43M280NO. 2 RECYCLE VA 1.61 18,716 IFR 95 936 0.00 $0 $0 $0 44M280NO. 3 TWKA 1.93 15 NONE 0 15 14.44 $15,221 $3,797 $525,900 45M280NO. 3 TWKA 1.93 2 NONE 0 2 1.52 $33,821 $8,441 $11,106,579 46M280NO. 4 TWKA 1.93 15 NONE 0 15 14.44 $15,221 $3,797 $525,900 47M280RECYCLE AQUA 1.93 0 NONE 0 0 0.19 $9,769 $2,438 $25,663,158 48M280VINYL ACETATE 1.61 18,716 IFR 95 936 0.00 $0 $0 $0 49M280WASTE 1.93 0 NONE 0 0 0.19 $9,720 $2,426 $25,536,842 50M280WASTE ORGANIC 1.93 215 NONE 0 215 204.06 $11,240 $2,781 $27,257 51M281CRUDE NPG 1.93 460 0 460 437.00 $14,701 $3,617 $16,554 52M281FLUX OIL TANK 3.16 1,528 0 1,528 1,451.41 $17,161 $4,111 $5,665 53M281MIX 1.93 38 0 38 36.10 $10,805 $2,693 $149,197 54M281MOLTEN STORAGE 2.93 562 0 562 533.90 $19,467 $4,796 $17,966 55M281MOLTEN STORAGE 2.93 562 VAPOR RECOVERY 0 562 533.90 $19,467 $4,796 $17,966 56M281REJECT 1.93 10 0 10 9.50 $15,559 $3,882 $817,263 57M281STORAGE TANK 13.29 2,300 0 2,300 2,185.00 $25,427 $6,087 $5,572 58M281STORAGE TANK 43 13.29 420 0 420 399.00 $13,899 $3,422 $17,153 59M281STORAGE 2.24 60 0 60 57.00 $10,107 $2,516 $88,281 60M281STORAGE 13.29 60 0 60 57.00 $11,538 $2,873 $100,807 61M281TANK 13.29 240 0 240 228.00 $13,063 $3,233 $28,360 62M283HEXANE STORAGE 2.93 22,000 IFR 95 1,100 0.00 $0 $0 $0 63M283HEXANE STORAGE 2.93 18,000 IFR 95 900 0.00 $0 $0 $0 64M289TANK 2.93 320 IFR 95 16 0.00 $0 $0 $0 65M289TANK 2.93 320 IFR 95 16 0.00 $0 $0 $0 66M289TANK 2.93 320 IFR 95 16 0.00 $0 $0 $0 67M289TANK 2.93 120 IFR 95 6 0.00 $0 $0 $0 68M289TANK 2.93 320 IFR 95 16 0.00 $0 $0 $0 69M293STORAGE 1.68 0 NONE 0 0 0.38 $32,823 $8,192 $43,115,789 70M293STORAGE 1.68 507 NONE 0 507 481.84 $12,066 $2,954 $12,261 71M300TANK 1.93 318 NONE 0 318 302.10 $11,960 $2,949 $19,523 72M300TANK 2.06 81 NONE 0 81 76.95 $14,416 $3,589 $93,281 73M300TANK 2.93 200 IFR 95 10 0.00 $0 $0 $0 74M306TANK/2A/2A 2.93 1,280 NONE 0 1,280 1,216.00 $11,949 $2,838 $4,668 75M306TANK/2B/2B 2.93 1,280 NONE 0 1,280 1,216.00 $11,949 $2,838 $4,668 76M306TANK/3/3 0.71 260 NONE 0 260 247.00 $9,695 $2,391 $19,360 77M330POLY ETHYLENE 2.32 8,868 NONE 0 8,868 8,424.60 $10,520 $1,623 $385 78M343R-1372 1.93 12 NONE 0 12 11.40 $9,669 $2,412 $423,158 79M3582-16,900 GALLON 1.93 7,765 None 0 7,765 7,376.75 $13,585 $2,513 $681 80M3582-9,800 GALLON 1.93 3,882 None 0 3,882 3,687.90 $11,302 $2,382 $1,292 81M3583-150,000 GALLON 1.93 4,500 None 0 4,500 4,275.00 $32,814 $7,682 $3,594 82M358NEW ROSIN TANK, 1.93 3,882 None 0 3,882 3,687.90 $10,520 $2,187 $1,186Att. 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 efficiencyBaseline HAP

emissions (lb/yr) HAP reduction

(lb/yr) TCI ($) TAC ($/yr) CE ($/ton) 83M358RESIN PRODUCT 1.93 3,882 None 0 3,882 3,687.90 $12,866 $2,773 $1,504 84M358RESINATE TANKS, 0.71 6,666 None 0 6,666 6,332.70 $12,045 $2,253 $712 85M358RXN. OIL, HEADS 1.93 4,500 None 0 4,500 4,275.00 $11,317 $2,316 $1,084 86M358ST-26 RESINATE 0.71 2,244 None 0 2,244 2,131.80 $12,739 $2,926 $2,745 87M358TOLUENE TANK 0.71 1,498 None 0 1,498 1,423.10 $12,049 $2,838 $3,988 88M441100 PROCESS 6.93 2,916 NONE 0 2,916 2,770.20 $9,669 $2,084 $1,505 89M441100 PROCESS 1.38 108 NONE 0 108 102.60 $9,669 $2,401 $46,803 90M44T-352,353,&354/FB03 1.93 130 NONE 0 130 123.50 $12,866 $3,197 $51,773 91 M44T-352,353,&354/FB03 1.93 18 PROCESS CHANGE 0 18 17.10 $13,204 $3,294 $385,263 92M44TANK 1.93 113 VAPORCONDENSERS 68 36 9.72 $15,510 $3,868 $795,885

93M44TANK 1.93 14,600 FLARE-WASTE 98 292 0.00 $0 $0 $0 94M44TANKS 360 AND 1.93 7,938 VAPORCONDENSERS 68 2,540 685.80 $27,035 $6,493 $18,936

95M44TANKS 1.68 1,448 NONE 0 1,448 1,375.60 $14,281 $3,401 $4,945 96M44TANKS 1.68 1,450 NONE 0 1,450 1,377.50 $12,100 $2,856 $4,147 97M44TANKS 1.68 5,040 SCRUBBER 0 50 47.88 $12,438 $2,535 $105,890 98M44TANKS 3.62 766 NONE 0 766 727.70 $12,100 $2,934 $8,064 99M44TANKS 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