## - 

# .. Docket No. A-92-45 Item IXc-B-l MEMORANDUM TO: Group IV Polymers and Resins Docket A-92-45 FROM: Keith Barnett, EPAJOAQPSIESDIOCG 

### DATE: December 2000 SUBJECT: Final Analysis of Equipment Leak 

### Program for PET Facilities Subject 10 

### the Group IV Polymers and Resins NESHAP Based on comments received on the June 8, 1999, proposed denial of petitions for reconsideration on the Group IV equipment leak provisions as they apply to PET facilities, a final equipment leak analysis (hereafter referred to as the December 2000 analysis) has been developed. This memo presents the results of the December 2000 analysis and summarizes the changes that have been made to the previous analysis entitled "Equipment Leak Analysis for PET Facilities Subject to the Group IV Polymers and Resins NESHAP," October 26, 1998, which may be found in Docket A-92-45 as Item VIc-B-l (hereafter referred to as the October 1998 analysis). Table 1 summarizes the changes made to the October 1998 analysis. 

### RESULTS Table 2 presents the results of the December 2000 analysis by subcategory and compares the results with those presented in the October 1998 analysis (i.e., Docket Item Vlc-B-I). As seen in Table 2, the October 1998 analysis cost effectiveness ratios range from $1,400 to $2,300 per Mg of HAP emission reduction. The cost effecti veness ratios of the equipment leak program under the December 2000 analysis range from $1,800 to $3,600 per Mg of HAP emission reduction. Appendix A presents the cost effectiveness values for each of the individual facilities by subcategory. Appendix B presents the facility specific cost spreadsheets for the December 2000 analysis. Appendix C presents the facility specific emissions and emission reduction spreadsheets for the December 2000 analysis. 

### DISCUSSION The following paragraphs discuss the changes made to the October 1998 analysis.
1

### TABLE 1. SUMMARY OF CHANGES MADE TO OCTOBER 1998 ANALYSIS

ITEM DESCRIPTION OF CHANGE Monitoring Costs Increased initial monitoring costs for pumps. valves. and connectors in gas/vapor or light liquid service. Eastman Kodak. Rochester Incorporated compliance with 6 NYCRR Part 236 into baseline. Tennessee Eastman and Carolina Incorporated new data on leak frequencies and emission factors for Eastman components subject to Method 21 monitoring. DuPont conneclors in gas/vapor Incorporated new data on emission factors for conneClors in gas/vapor or or light liquid service light liquid service for DuPont. Monitoring periods Decreased expected monitoring frequency for (I) connectors at all facilities. (2) valves in gas/vapor service at Carolina Eastman. and (3) valves in light liquid service at ICI-Fayetteville. In-House vs Subcontraclor Applied the 500 or fewer components subject to Method 21 rule for using personnel in-house personnel to those facilities in which during anyone month 500 or fewer components subject to Method 21 would be monitored. Facilities that did not provide Estimated leak frequencies and emission factors for components subject to company- or facility-specific data Method 21 at facilities for which company- or facility-specific data were not for components subject to provided using company- or facility-specific data provided by other Method 21 monitoring companies.



### TABLE 2 SUMMARY OF COST EFFECrIVENESS RESULTS 

### ($/Mg of emission' reduction) Subcategory October 1998 Analysis December 2000 Analysis DMT-Balch 2.291 3.600 DMT-Continuous 1,401 2,991 TPA-Conlinuous 1.769 1.821 TPA-Batch 1,812 1.812



### 2

### Initial Monitoring Cost Changes Table 3 summarizes the changes made to the initial monitoring costs for pumps in light liquid service, valves in gas or light liquid service, and connectors in gas or light liquid service. As seen in Table 3, the cost per component for initial monitoring for these components were increased from $4.65 to $17.70 per component when using a subcontractor and from either $0.75 or $3.75 to $16.50 per component when using in-house personnel. No changes were made to any of the other cost components. TABLE 3. INITIAL MONITORING COST CHANGES ($ 

### per component) October 1998 Analysis December 2000 Analysis Component Subcontractor In-House Subcontractor In-House Personnel Personnel Personnel Personnel Pumps, light liquid service 4.65 3.75 Valves, gas service Valves, light liquid service 17.70 16.50 4.65 0.75 Connectors, gas service Connectors, light liquid service


### Eastman Kodak
- Rochester. New York Based on comments from Eastman Kodak, their Rochester, New York, facility is subject to 6 NYCRR Part 236
- Synthetic Organic Chemical Manufacturing Facility Component Leaks (see Appendix D). The cost for c,!mplying with Part 236 was calcqlated and the incremental cost for complying with the Group IV equipment leak program was then calculated.

TABLE4.**mCREMENTALCOST~CTIVENESSFOR** 

### EASTMAN KODAK'S ROCHESTER FACILITY
Annual Costs ($) Annual Emission Cost Effectiveness ($JMg of Rule Requirement Reduction (Mglyr) emission reduction) Part 236 8,079 2.47 3,271 Group IV Resins 12,675 3.02 4,197 Increments 4,596 0.55 8,356 

### 3

### Tennessee Eastman and Carolina Eastman Facilities Based on comments and data supplied by Tennessee Eastman and Carolina Eastman, the revised analysis incorporates new emission factors and leak frequencies for their facilities. Table 5 presents these new emission factors and leak**f~uencies.** 

### The following paragraphs discuss the derivation of these factors and leak frequencies. Uncontrolled Emission Leak Factors: These values were taken or derived from spreadsheets submi.tted**b~ Eastm~n**  

### .. N?te that**Eastmans'su~m~ttal** 

### showed a rate of 0.00143 for pumps in light liqUid service, which IS 

### Incorrect based on their Excel spreadsheet. The correct value is 0.01433 lbs/hr/component. Total Number of Components: These were determined based on the Excel spreadsheets provided by Eastman. Number of Components Leaking Above the nON Definition: For valves and connectors, 500 ppm is the leak definition used. For pumps, 5,000 ppm is the leak definition used for polymerizing monomers, which would be applicable to PET 

### facilities. The 1,000 ppm is shown for comparison. The number of leakers were determined from**th~** 

### Excel spreadsheets by sorting from low to high on the screening values and then counting the number of components at or above the leak definition level. Percent Leakers: This is simply the number of components leaking divided by the total number of components. Subsequent Leak Rate: For those components whose initial percent leak rate is less than the subsequent leak rate attributable to the HON program, the subsequent leak 'rate was assumed to be the same as the initial leak rate. For Valves, light liquid service at Tennessee Eastman and for pumps, light liquid service at Carolina Eastman, the initial leak rates were higher than the HON's subsequent leak rate. For valves, light liquid service, the HON's subsequent leak rate of 2% was used. For pumps, light liquid service at Carolina Eastman, an extrapolation was used. The HON reports initial and subsequent leak rates of 17.1 % 

### and 8.04% with a leak definition of 1,000 ppm. Since the relevant leak definition for PET 

### facilities is 5,000 ppm, the subsequent leak frequency was extrapolated as follows: 8.93% x (8.04/17.1) 

## = 4.2%. Subsequent Emission }'actor: For those components whose subsequent leak rate was assumed to be the same as the initial leak rate, the following assumptions were made: (1) the same percentage of components found to be not leaking continued to be non-leaking and emitting at the same rate for the entire monitoring period and for the entire year, (2) the same percentage of components found leaking at the start were found leaking each monitoring period for the year, and (3) the leaking components would increase linearly during each monitoring period, resulting in emissions occurring over the year at one-half the uncontrolled leaker emission factor. 

### 4

## TABLE 5. EASTMAN EMISSION FACTORS AND LEAK FREQUENCIES UncontroJled Emission Factor Number of Percent Subsequent Non-Leak Components Leakers Subsequent (Ibslhr/component) 

### Total and Leak Rates (%) Component Number of Leaking (0/0) Emission aboveHON Rate (lbslhrl AU Non-Iekaing Leaking Components Leak Non- Leakers component) Components Components Components Definition Initial leakers 

### Tennessee Eastman Pumps. light liquid 0.00385 0.0023053 0.308644 198 1 at 5,000 0.51 99.49 0.51 0.00308 ppm Valves, gas/vapor 0.00030 0.00008985 0.01444 538 8 1.49 98.51 1.49 0.000196 Valves. light liquid 0.00082 0.00030118 0.02176 

### 3,893 

### 94 2.415 98.00 2.00 0.000513 Connectors (gas/vapor 0.00038 0.00022085 0.036043 14,138 63 0.44 99.56 0.44 0.000299 and light liquid)


### Carolina Eastman 9 at 1,000 16.1 

### at 

### 5.000 Pumps. light liquid 0.01433 0.00313 0.1287 56 

### ppm 

### ppm: at 5.000 0.00570 5 at 5.000 8.93 95.8 

### ppm: 4.2 ppm Valves. gas/vapor 0.000026 0.00002 0.00168466 300 1 0.33 99.67 0.33**0.ססOO227** Valves, light liquid 0.00013 0.00006454 0.00418874 1,318 20 1.52 98.48 1.52 0.0000954 Connectors (gas/vapor 0.000047 

### O.OOOOtS86 0.011634 and light liquid) 

### 4.906 13 0.265 99.735 0.265 0.0000312



### 5

### For valves, light liquid service at Tennessee Eastman, 98% of the valves were assumed to be non-leaking each monitoring period at the average leak rate for those valves found to be not leaking at the initial monitoring and 2% of the valves were assumed to be leaking each monitoring period at one-half the average leak rate for those valves found to be 

### leaking at the initial monitoring. (The one-half assumption is equivalent to leaking at the full average leak rate for leakers starting at the mid-way point in each monitoring period or for 4,380 hours per year.) For pumps, light liquid service at Carolina Eastman. 95.8% of the pumps were assumed to be non-leaking each monitoring at the average leak rate for those pumps found to be 

### not leaking at the initial monitoring and 4.2% of the pumps were assumed to be leaking each monitoring period at one-half the average leak rate for those pumps found to be 

### leaking at the initial monitoring. (The one-half assumption is equivalent to leaking at the full average leak rate for leakers starting at the mid-way point in each monitoring period or for 4,380 hours per year.) The subsequent emission factors arc calculated using the following equation: (% 

### non-leakers x non-Ieaker emission factor) 

## + (% 

### leakers x leaker emission factor x 0.5) DuPont Connectors in Gas/Vapor Service or Light Liquid Service DuPont identified an average emission factor of 0.00022 Ibs/hr/component for connectors in gaslvapor or light liquid service. DuPont noted that according to their data the was no statistical difference between initial and subsequent leak frequencies for these connectors. As for components at Eastman facilities that showed the same initial and subsequent leak frequencies, an average emission factor was developed to estimate emissions that would occur between subsequent monitoring event. The average emission factor developed is 0.00014 Ibs/hr/component. This factor was derived as follows: 1. An initial leak frequency of 0.52 percent was assigned to these connectors. This leak frequency is the average of the reported leak frequencies for these connectors from Tennessee Eastman, Carolina Eastman. and ICI-Fayetteville [(0.265 

## + 0.44 

## + 0.86)/3 

# = 0.52). 2. Subsequent leak frequency was assumed to be 0.5 percent, which is the expected subsequent leak frequency for these components under the rule. This subsequent leak frequency is essentially identical to DuPont's assertion that they found no statistical difference between initial and subsequent leak frequencies. 3. Non-Ieaker and leaker emission factors that correspond to the initial leak rate of 0.00022 Ibs/hr/component were calculated by first assuming the ratio of the leakers' leak rate to the non-Ieakers' leak rate is the same as the average ratio found at Tennessee Eastman and Carolina Eastman. The ratios at these two companies are 163.2 for Carolina Eastman and 733.55 for Tennessee Eastman, yielding an average ratio of 448.37. Next, the following equation was solved to deterinine the leak rate for each non-leaking connector:


### 6

### Non-leaker emission rate 

# = 0.00022 

# =0.00006596 lbslhr/component 0.99478 

## + (0.00522 x 448.37) The leaker emission rate 

# = 0.00006596 x 448.37 

# =0.02958 lbslhr/component 4. The average emission factor was then calculated as follows: (0.OOO06596 x 0.99478) 

### + (0.02958 x 0.005 x 0.5) 

# =0.0001396lbs/hr/component These initial emission and subsequent average emission factors and leak frequencies were applied to all DuPont facilities in the December 2000 analysis. In-House versus Subcontractor Personnel In the December 2000 analysis. the detennination of whether a facility would use inhouse personnel or subcontractor personnel is based on the estimated number of components that would be monitored in anyone month. If this number is equal to or less than 500 components. the facility is assumed to use in-house personnel. If this number is greater than 500 components. the facility is assumed to use subcontractor personnel. Table 6 summarizes the estimated maximum number of components that would be subject to Method 21 monitoring in anyone month period. In calculating this number of components. the monitoring period for connectors in , gas/vapor or light liquid service was estimated to be once every four years. Thus. one quarter of the total number of connectors in gas/vapor or light liquid service would be monitored each year. Within each year. it was assumed that one quarter of these components would be monitored each quarter. For example, if a facility has 800 connectors in gas/vapor or light liqUid service, 200 of these connectors would be monitored each year over four years. Within each year, 50 connectors would be monitored in each of four months (to correspond to the quarterly mOnitoring of valves). Leak Frequencies and Emission Factors for "Other Facilities" In 

### the December 2000 analysis, uncontro]]ed emission factors and initial leak frequencies identified by specific companies for specific components subject to Method 21 monitoring were extended to the other facilities that did not identify leak frequencies and emission factors specific to their facilities or to components not addressed by companies that did submit company- or facility-specific infonnation. In general, initial leak frequencies, subsequent leak frequencies. and uncontrolled emission rates were calculated as averages of reported initial leak frequencies, subsequent leak frequencies. and uncontrolled emission rates. Then, ratios of leaker emission factors to non-Ieaker emission factors were calculated based on Carolina Eastman and Tennessee Eastman 

### data. Lastly, the subsequent average emission factor was calculated using the same equation shown earlier for DuPont connectors. Controlled emission factors for several Hoechsl Celanese and ICI-Fayetteville components were also re-estimated using this procedure. Appendix E presents a spreadsheet showing these calculations.



### 7

## TABLE 6. ESTIMAnON OF MAXnvruM: NUMBER 

## OF COfvlPONENTS TO MONITOR 

## IN ONE MONTH Total Number of Personnel to be Valves. light Connectors. Components to 

### Used to Conduct Pumps, gas/vapor and Company Location Process light liquid Valves, gas 

### liquid Monitor in One Method 21 light liquid Month MonitorinR 

### 3M Decatur DMT-B 4 

### 66 18 14.3 

### 162 In-House 

### 3M Greenville DMT-B 

### 2 

### 34 40 7.4 83 In-House BASF 

### Lowland DMT-B 8 

### 135 160 

### 29.4 332 In-House Eastman Kodak Rochester DMT-B 4 

### 75 89 

### 16.4 184 In-House Hoechst Shelby DMT-B 

### 0 

### 37 146 30.8 214 

### In-House Celanese DMT-B 

### 4 431 116 21.3 572 Hoechsl Spartanburg DMT-C 

### 14 204 250 142.1 610 Celanese TPA.c 0 8 0 

### 0.0 8 

### Totals 

### 18 643 366 163.3 1190 

### Subcontractor 

### leI Fayetteville DMT-B 

### 24 0 350 80.3 454 In-House leI Hopewell DMT-B 3 

### 59 70 12.8 145 In-House DMT-B 1 

### 25 30 5.4 61 Shell Pt. 

### Pleasant TPA-C 

### 32 20 46 7.4 

### 105 TPA-B 0 0 

### 0 0.0 0 Totals 

### 33 45 76 12.8 167 In-House DMT-B 

### 16 0 

### 167 0.0 183 Tennessee Kingsport DMT-C 

### 34 16 808 242.1 1100

Eastman TPA-C 

### 2 14 

### 86 29.4 131 Totals 

### 52 30 1061 271.4 1414 Subcontractor DMT-C 20 

### 68 511 118.4 717 Carolina Eastman Columbia TPA-C 0 

### 153 0 

### 21.6 175 Totals 

### 20 221 

### 511 140 892 Subcontractor DuPont Brevard DMT-C 

### 2 10 57 17.8 

### 87 In-House DMT-C 

### 39 158 

### 886 278.1 1361


# - DuPont Cape Fear TPA-C 

### 22 13 

### 32 . 4.9 72 Totals 

### 61 171 918 283 1433 . Subcontractor DuPont Circleville DMT-C 

### 10 42 234 73.3 

### 359 In-House 

### 8 

# L

# ( TABLE 6. ESTIMATION OF MAXIMUM NUMBER OF COMPONENTS TO MONITOR IN ONE MONTH (concluded) 

## (



# \ Connectors t 

### Total Number of Personnel to 

### be Company Location Process Pumps. Valves. gas Valves, light gas/vapor and Components to Used to Conduct light liquid liquid Monitor in One Method 21 

### light liquid Month Monitorin2 DMT-C 9 

### 36 202 

### 63.4 

### 310 DuPont Cooper Ri ver TPA-C 

### 31 19 45 7.1 

### 102 Totals 40 

### S5 247 70.5 

### 413 In-House DuPont Florence DMT-C 

### 19 77 

### 434 136.1 

### 666 Subcontractor DMT-C 13 

### 54 304 95.3 466 

### DuPont Kinston 

### lPA-C 28 17 

### 41 6.4 92 

### Totals 

### 41 71 345 101.75 559 

### Subcontractor DuPont Old Hickory DMT-C 12 50**~80** 88.0 

### Hoechst 

### 430 In·House Celanese Greer 

### TPA.c 0 

### 4 0 2.2 6 

### In-House Hoechst Salisbury Celanese 

### TPA-C S6 112 

### O. 17.5 186 

### In-House Wellman 

### TPA-C 0 5 0 

### 0.0 5 

### In-House

YKK TPA-C 

### 8 0 8 1.0 17 

### In-House



### 9

### Table 7 presents the initial and subsequent leak frequencies used for components subject to Method 21 at all facilities in the current revised analysis and compares them to those used in the October 1998 analysis. Table 8 presents the uncontrolled and controlled emission factors used for components subject to Method 21 at 

# an facilities in the current revised analysis and compares them to those used in the October 1998 analysis. Monitoring PeriodUnder the rule, if the leak frequency for valves in gas/vapor service is less than or equal to 1.0 percent but greater than 0.5 percent, the monitoring period is twice per year. Based on data submitted, a leak frequency of 0.91 percent for these components were calculated for the "other facilities." Therefore, for the "other facilities" the December 2000 analysis uses a monitoring frequency of twice per year for these components. Under the rule, if the leak frequency for valves in gas/vapor service is less than or equal to 0.5 percent but greater than 0.25 percent, the monitoring period is once per year. Based on data submitted, Carolina Eastman reports a leak frequency of 0.33 percent for these components. Therefore, for Carolina Eastman the December 2000 analysis uses a monitoring frequency of once per year for these components. Under the rule, if the leak frequency for valves in light liquid service is less than or equal to 1 percent, the monitoring period is twice per year. Based on data submitted, ICI-FayetteviJIe 

# ..I reports a leak frequency of 0.86 percent for these components. Therefore, for ICI-Fayetteville the December 2000 analysis uses a monitoring frequency of twice per year for these components. Under the rule, if the leak frequency for connectors in**~as/vapor** 

### or light liquid service is less than or equal to 0.5 percent, the monitoring period can be once every four years. 

### In the December 2000 analysis, this once every four year period for monitoring has been used for all facilities.

10

### TABLE 7. SUMMARY OF LEAK FREQUENCIES (%) Initial Subsequent Component CompanylFacility October 1998 December October 1998 December Analysis 2000 Analysis 2000 Analysis Analysis Valves. gas/vapor HC facilities 2.35 2.35 2.00 2.00 Eastman
- Kingsport 1.6 1.49 2.00 1.49 Carolina Eastman 0 0.33 0 0.33 All Others 13.6 1.39 2.00 0.91 Valves. light liquid HC facilities 2.5 2.5 2.00 2.00 Eastman
- Kingsport 1.7 2.415 2.00 2.00 Carolina Eastman 0 1.52 0 1.52 ICI-Fayetteville 0.86 0.86 Q.86 0.86 All Others 8.5 1.824 2.00 1.46 Pumps. light liquid HC facilities 8.68 8.68 8.04 4.2 Eastman
- Kingsport 3.65 0.51 3.65 0.51 Carolina Eastman 8.73 8.93 8.04 4.2 ICI-Fayetteville 16.7 16.7 8.04 8.04 All Others 17.1 8.71 8.04 4.2 Connectors. HC facilities 0.86 0.86 0.5 0.5 gas/vapor and light Eastman
- Kingsport 0.47 0.44 0.5 0.44 liquid Carolina Eastman 0.33 0.265· 0.5 0.265 DuPont 3.9 0.52 0.5 0.5 ICI-Fayetteville 0.86 0.86 0.5 0.5 All Others 3.9 0.61 0.5 0.5

II

### TABLE 8. SUMMARY OF EMISSION FACTORS (Ibs/hr/component) Uncontrolled Controlled (Ibslhrlcomponent) (Ibslhr/component) Component CompanylFaciJity October 1998 December December October 1998 Analysis 2000 Analysis 2000 Analysis Analysis Valves, gas/vapor HC facilities 0.002303 0.002303 0.001 0.0013385 Eastman
- Kingsport 0.00158 0.00030 0.001 0.000196 Carolina Eastman 0 0.000026. 0**0.ססOO227** All Others 0.0131 0.000876 0.001 0.000516 Valves. light liquid HC facilities 0.00266 0.00266 0.0011 0.0011266 Eastman
- Kingsport 0.001835 0.00082 0.0011 0.000513 Carolina Eastman 0 0.00013 0 0.0000954 ICI-Fayetteville 0.000955 0.000955 0.000955 0.0005285 All Others 0.00887 0.001141 0.0011 0.0004931 Pumps, light liquid HC facilities 0.022685 0.022685 0.011 0.0074535 Eastman
- Kingsport 0.01013 0.00385 0.01013 0.00308 Carolina Eastman 0.022792 0.01433 0.011 0.00571 ICI-Fayetteville 0.04269 0.04269 0.011 . 0.01226 All Others 0.0438 0.020889 0.011 0.0068948 Connectors, HC facilities 0.000923 0.000923 0.000286 0.0004029 gas/vapor and light Eastman
- Kingsport 0.000523 0.00038 0.000286 0:000299 liquid Carolina Eastman 0.000164 0.000041 0.000164 0.0000312 DuPont 0.00403 0.00022 0.000286 0.0001396 ICI-Fayetteville 0.000926 0.000926 0.000286 0.0004042 All Others 0.00403 0.0005 0.000286 0.0002837



### 12

### APPENDIX A DETAll.ED COST EFFECTIVENESS SUMMARIES BY FACILITY AND SUBCATEGORYDECEMBER 2000 COST EFFECTIVENESS SUMMARY Annual Emission Cost Cost Company Location Costs Reduction Effectivness Effectiveness from October 

## .,.) DMT- Batch 2000 Analysis 3M Decatur $12,262 2.91 $4,214 3M Greenville $9,324 1.53 $6,094 BASF Lowland $18,425 5.76 $3,199 EK Rochester $4,596 0.55 $8,356 Hoeschst Celanese Shelby $10,218 2.19 $4,666 Hoeschst Celanese Spartanburg $30,136 14.67 $2,054 ICI Fayetteville $31,125 6.16 $5,053 ICI Hopewell $11,609 2.78 $4,176 Shell PI. Pleasant $4,328 1.37 $3,159 Tennessee Eastman Kingsport $10,015 1.53 $6,545 TOTALS $142,037 39.45 $3,600 $2,291
DMT Continuous Carolina Eastman Columbia $n,366 31.71 $2,440 DuPont Brevard $11,212 2.63 $4,263 DuPont Cape Fear $113,794 39.96 $2,848 DuPont Circleville $27,356 10.62 $2,576 DuPont Cooper River $24,030 9.20 $2,612 DuPont Florence $71,352 19.80 $3,604 DuPont Kinston $54,947 13.45 $4,085 DuPont Old Hickory $30,887 12.14 $2,544 Hoeschst Celanese Spartanburg $50,658 15.20 $3,333 Tennessee Eastman Kingsport $93,740 30.94 $3,030 

# -..I TOTALS $555,342 185.65 $2,991 $1,401
TPA Continuous Carolina Eastman Columbia $14,928 66.99 $223 DuPont Cape Fear $17,603 4.92 $3,578 DuPont Cooper River $28,065 7.24 $3,876 DuPont Kinston $24,447 6.84 $3,574 Hoechst Celanese Greer $10,441 1.47 $7,102 Hoechst-Celanese Salisbury $55,640 8.97 $6,203 Hoeschst Celanese Spartanburg $1,089 0.03 $36,307 Shell PI. Pleasant $28,751 7.40 $3,885 Tennessee Eastman Kingsport $9,413 5.85 $1,609 Wellman $31,252 15.83 $1,974 YKK $11,038 2.20 $5,017 TOTALS $232,667 127.74 $1,821 $1,769 TPA Batch Shell PI. Pleasant $4,911 2.71 $1,812 $1,812

J 

# ...., CosUnl.xls

### APPENDIXB 

### FACll..ITY SPECIFIC COST SPREADSHEETS FOR DECEMBER 2000 ANALYSIS

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