## Summary of Impacts - Addition of In-Series Baghouse

Scenario Data sources ACFMInlet TempBag

materialAssumed

Bag lifeBaghouse typeCapital CostAnnualized costEmission

Reduction (tpy)$/tonEmission Reduction (tpy)$/ton Scenario Using Average Emission Factor 1. Add on 1 FF to Main stack onlyMain - averaged over 7 tests1,023,723170Standard2P-J (modular)$7,395,207$1,529,73057.4$26,64928.7$53,245 Main - averaged over 7 tests1,023,723170Standard2P-J (modular)$7,395,207$1,529,730 7/8/9 - 2008 stack test595,888106Standard2P-J (modular)$3,311,576$849,750 P-J (modular)$10,706,784$2,379,48058.8$40,44929.4$80,818
3. Add on 1 FF to Main stack and BHs 7/8/9 combined Main - averaged over 7 tests 7/8/9 - 2008 stack test1,619,611170Standard2P-J (modular)$11,274,855$2,388,65058.8$40,60529.4$81,129

1

### Estimated removal efficiency b ased on standard baghouse performance. 2

### Estimated removal efficience based on reduction due to in-series configuration. 2. Add on 1 FF to Main stack and 1 FF to BHs 7/8/9 combined Total Scenario 2 99.9% RE1 

### 50% RE2

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on BH for main stack only

Main stack
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

2008 575.4

INPUT PARAMETERS: -- Inlet stream flowrate (acfm): 

### 1023723 -- Inlet stream temperature (oF): 170 -- Dust type: Blast furnace dust -- Inlet dust loading (gr/ft3): 

### 0.0018699 Dust mass median diameter (microns): 3.68 -- Filtration time (min): 10 Dust specific resistance (in.H2O/fpm/lb/ft2): 15 -- G/C ratio factors (shaker & reverse-air): A: 

### 2.5 B: 1 C: 

### 1.2 -- G/C ratio factors (pulse-jet only): Material: 10 Application: 0.8 -- Cleaning pressure, psig (pulse-jet only): 100 -- Fraction of bags cleaned (shaker & rev-air): 0 -- Insulation required? ('yes'=1;'no'=0): 1 -- Stainless steel required? ('yes'=1;'no'=0): 0 -- Bag material: Fiberglass w/PTFE Membranes (cost modifier at right)

### 1

-- Fabric effective residual drag (in. H2O/fpm): 1 -- Bag prices ($/ft2): [4] Mechanical shaker: 0 0 0 0 Reverse-air $0.53 $0.69 $0.76 $0.99 Pulse-jet $0.95 $1.08 $1.24 $1.29

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area): Mechanical shaker: 2.7 Reverse-air: 2.7 Pulse-jet: 

### 8.7 -- Net cloth area required (ft2): Mechanical shaker: 

### 379157 Reverse-air: 

### 379157 Pulse-jet: 

### 117682 -- Gross cloth area required (ft2): Mechanical shaker: 

### 394323 Reverse-air: 

### 394323 Pulse-jet: 

### 117682 -- Area per bag/cage (ft2): 13 -- Number of bags/cages (pulse-jet only): 8772 -- Baghouse pressure drop (in. w.c.): Mechanical shaker: 

### 2.97 Reverse-air: 

### 2.97 Pulse-jet: 

### 2.65

Page 2 of 36

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on BH for main stack only

Main stack
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1] CAPITAL COSTS Equipment Costs ($): Item: Cost ($): Shaker Rev-air P-J (mod) P-J (com)

------------------------------------------------------------ Baghouse 

### 0 2,794,245 909,003 663,057 Bags 

### 0 292,785 134,157 134,157 Insulation 

### 0 316,588 247,660 110,990 Stainless 

### 0 0 0 0 Cages 0 0 

### 102,001 102,001

------------------------------------------------------------ Total: 

### 0 3,403,619 1,392,821 1,010,204 PEC($)-base: 

### 0 4,016,270 1,643,528 1,192,041 ' ' -esc.: 

### 0 8,327,916 3,407,930 2,471,749 TCI ($): 

### 0 18,071,577 7,395,207 5,363,696 ($/acfm): 0 

### 18 7 5

============================================================
ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): 

### $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 

### 0.0944 Bag life (years): 5 Capital recovery factor (bags): 

### 0.2439 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0 31,324 31,324 31,324 Supv. labor 

### 0 4,699 4,699 4,699 Maint. labor 

### 0 17,228 17,228 17,228 Maint. matl. 

### 0 17,228 17,228 17,228 Electricity 

### 0 360,179 239,906 239,906 Compr. air 

### 0 0 

### 155,671 155,671 Bag repl. 0 

### 92,012 42,783 42,783 Dust dispos. 0 

### 1,299 1,299 1,299 Overhead 

### 0 42,287 42,287 42,287 Tax,ins.,adm 0 

### 722,863 295,808 214,548 Cap. recov. 0 

### 1,670,218 681,497 489,737

------------------------------------------------ 

### ------------ Total Annual 

### 0 2,959,336 1,529,730 1,256,709

Page 3 of 36

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on BH for main stack only

Main stack
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]ANNUAL COST WEIGHTING FACTORS:

Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0.000 0.011 0.020 0.025 Supv. labor 

### 0.000 0.002 0.003 0.004 Maint. labor 

### 0.000 0.006 0.011 0.014 Maint. matl. 

### 0.000 0.006 0.011 0.014 Overhead 

### 0.000 0.014 0.028 0.034

------------ ----- ----- ----- ----- S/T labor: 

### 0.000 0.038 0.074 0.090 Compr. air 

### 0.000 0.000 0.102 0.124 Bag repl. 

### 0.000 0.031 0.028 0.034 Dust dispos. 

### 0.000 0.000 0.001 0.001 Electricity 

### 0.000 0.122 0.157 0.191 Tax,ins.,adm 

### 0.000 0.244 0.193 0.171 Cap. recov. 

### 0.000 0.564 0.446 0.390

------------ ----- ----- ----- ----- S/T capital: 

### 0.000 0.809 0.639 0.560

------------------------------------------------ 

### ------------ Total: 

### 0.000 1.000 1.000 1.000

============================================================
RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA

Net Cloth Area >/= (ft2): Gross/Net Area Ratio:

------------------------------------------------------------------------1 

### 2.000 4001 

### 1.500 12001 

### 1.250 24001 

### 1.170 36001 

### 1.125 48001 

### 1.110 60001 

### 1.100 72001 

### 1.090 84001 

### 1.080 96001 

### 1.070 108001 

### 1.060 132001 

### 1.050 180001 

### 1.040

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition).
[2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)

Page 4 of 36

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on 2 BHs - Main and 7,8 and 9 combined

BH 7, 8 and 9 combined
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

2008 575.4

INPUT PARAMETERS: -- Inlet stream flowrate (acfm): 

### 595888 -- Inlet stream temperature (oF): 106 -- Dust type: Kettle refinery dust -- Inlet dust loading (gr/ft3): 

### 0.00006906 Dust mass median diameter (microns): 3.68 -- Filtration time (min): 10 Dust specific resistance (in.H2O/fpm/lb/ft2): 15 -- G/C ratio factors (shaker & reverse-air): A: 

### 2.5 B: 1 C: 

### 1.2 -- G/C ratio factors (pulse-jet only): Material: 10 Application: 0.8 -- Cleaning pressure, psig (pulse-jet only): 100 -- Fraction of bags cleaned (shaker & rev-air): 0 -- Insulation required? ('yes'=1;'no'=0): 1 -- Stainless steel required? ('yes'=1;'no'=0): 0

-- Bag material: Fiberglass w/PTFE Membranes (cost modifier at right)

### 1

-- Fabric effective residual drag (in. H2O/fpm): 1 -- Bag prices ($/ft2): [4] Mechanical shaker: 0 0 0 0 Reverse-air $0.53 $0.69 $0.76 $0.99 Pulse-jet $0.95 $1.08 $1.24 $1.29

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area): Mechanical shaker: 2.7 Reverse-air: 2.7 Pulse-jet: 

### 11.9 -- Net cloth area required (ft2): Mechanical shaker: 

### 220699 Reverse-air: 

### 220699 Pulse-jet: 

### 50267 -- Gross cloth area required (ft2): Mechanical shaker: 

### 229527 Reverse-air: 

### 229527 Pulse-jet: 

### 50267 -- Area per bag/cage (ft2): 13 -- Number of bags/cages (pulse-jet only): 3747 -- Baghouse pressure drop (in. w.c.): Mechanical shaker: 

### 2.97 Reverse-air: 

### 2.97 Pulse-jet: 

### 3.61

Page 5 of 36

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on 2 BHs - Main and 7,8 and 9 combined

BH 7, 8 and 9 combined
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]CAPITAL COSTS Equipment Costs ($): Item: Cost ($): Shaker Rev-air P-J (mod) P-J (com)

------------------------------------------------------------ Baghouse 

### 0 1,638,698 415,326 288,771 Bags 

### 0 170,424 57,304 57,304 Insulation 

### 0 184,752 107,505 48,227 Stainless 

### 0 0 0 0 Cages 0 0 

### 43,570 43,570

------------------------------------------------------------ Total: 

### 0 1,993,874 623,706 437,872 PEC($)-base: 

### 0 2,352,771 735,973 516,689 ' ' -esc.: 

### 0 4,878,576 1,526,072 1,071,378 TCI ($): 

### 0 10,586,510 3,311,576 2,324,889 ($/acfm): 0 

### 18 6 4

============================================================
ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): 

### $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 

### 0.0944 Bag life (years): 5 Capital recovery factor (bags): 

### 0.2439 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0 31,324 31,324 31,324 Supv. labor 

### 0 4,699 4,699 4,699 Maint. labor 

### 0 17,228 17,228 17,228 Maint. matl. 

### 0 17,228 17,228 17,228 Electricity 

### 0 209,638 190,090 190,090 Compr. air 

### 0 0 

### 90,613 90,613 Bag repl. 0 

### 51,251 18,275 18,275 Dust dispos. 0 

### 28 28 28 Overhead 

### 0 42,287 42,287 42,287 Tax,ins.,adm 0 

### 423,460 132,463 92,996 Cap. recov. 0 

### 979,456 305,517 212,380

------------------------------------------------ 

### ------------ Total Annual 

### 0 1,776,598 849,750 717,146

Page 6 of 36

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on 2 BHs - Main and 7,8 and 9 combined

BH 7, 8 and 9 combined
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1] ANNUAL COST WEIGHTING FACTORS:

Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0.000 0.018 0.037 0.044 Supv. labor 

### 0.000 0.003 0.006 0.007 Maint. labor 

### 0.000 0.010 0.020 0.024 Maint. matl. 

### 0.000 0.010 0.020 0.024 Overhead 

### 0.000 0.024 0.050 0.059

------------ ----- ----- ----- ----- S/T labor: 

### 0.000 0.063 0.133 0.157 Compr. air 

### 0.000 0.000 0.107 0.126 Bag repl. 

### 0.000 0.029 0.022 0.025 Dust dispos. 

### 0.000 0.000 0.000 0.000 Electricity 

### 0.000 0.118 0.224 0.265 Tax,ins.,adm 

### 0.000 0.238 0.156 0.130 Cap. recov. 

### 0.000 0.551 0.360 0.296

------------ ----- ----- ----- ----- S/T capital: 

### 0.000 0.790 0.515 0.426

------------------------------------------------ 

### ------------ Total: 

### 0.000 1.000 1.000 1.000

============================================================
RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA

Net Cloth Area >/= (ft2): Gross/Net Area Ratio:

------------------------------------------------------------------------1 

### 2.000 4001 

### 1.500 12001 

### 1.250 24001 

### 1.170 36001 

### 1.125 48001 

### 1.110 60001 

### 1.100 72001 

### 1.090 84001 

### 1.080 96001 

### 1.070 108001 

### 1.060 132001 

### 1.050 180001 

### 1.040

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition).
[2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)

Page 7 of 36

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on BH for main combined with 7, 8 and 9

All MACT sources
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

2008 575.4

INPUT PARAMETERS: -- Inlet stream flowrate (acfm): 

### 1619611 -- Inlet stream temperature (oF): 170 -- Dust type: blast furnace/kettel refinery dust -- Inlet dust loading (gr/ft3): 

### 0.0012510 Dust mass median diameter (microns): 3.68 -- Filtration time (min): 10 Dust specific resistance (in.H2O/fpm/lb/ft2): 15 -- G/C ratio factors (shaker & reverse-air): A: 

### 2.5 B: 1 C: 

### 1.2 -- G/C ratio factors (pulse-jet only): Material: 10 Application: 0.8 -- Cleaning pressure, psig (pulse-jet only): 100 -- Fraction of bags cleaned (shaker & rev-air): 0 -- Insulation required? ('yes'=1;'no'=0): 1 -- Stainless steel required? ('yes'=1;'no'=0): 0 -- Bag material: Fiberglass w/PTFE Membranes (cost modifier at right)

### 1

-- Fabric effective residual drag (in. H2O/fpm): 1 -- Bag prices ($/ft2): [4] Mechanical shaker: 0 0 0 0 Reverse-air $0.53 $0.69 $0.76 $0.99 Pulse-jet $0.95 $1.08 $1.24 $1.29

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area): Mechanical shaker: 2.7 Reverse-air: 2.7 Pulse-jet: 

### 8.9 -- Net cloth area required (ft2): Mechanical shaker: 

### 599856 Reverse-air: 

### 599856 Pulse-jet: 

### 181730 -- Gross cloth area required (ft2): Mechanical shaker: 

### 623850 Reverse-air:

### 623850 Pulse-jet: 

### 181730 -- Area per bag/cage (ft2): 13 -- Number of bags/cages (pulse-jet only): 13545 -- Baghouse pressure drop (in. w.c.): Mechanical shaker: 

### 2.97 Reverse-air: 

### 2.97 Pulse-jet: 

### 2.72

Page 8 of 36

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on BH for main combined with 7, 8 and 9

All MACT sources
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]CAPITAL COSTS Equipment Costs ($): Item: Cost ($): ShakerRev-airP-J (mod) P-J (com)

------------------------------------------------------------ Baghouse 

### 0 4,403,6901,378,0281,018,652 Bags 

### 0 463,209 207,172 207,172 Insulation 

### 0 500,210 380,816 170,619 Stainless 

### 0 0 0 0 Cages 0 0 

### 157,501 157,501

------------------------------------------------------------ Total: 

### 0 5,367,1092,123,5171,553,944 PEC($)-base: 

### 0 6,333,1892,505,7501,833,654 ' ' -esc.: 

### 013,132,1515,195,7863,802,163 TCI ($): 

### 028,496,76711,274,8558,250,694 ($/acfm): 0 

### 18 7 5

============================================================
ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): 

### $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 

### 0.0944 Bag life (years): 2 Capital recovery factor (bags): 

### 0.5531 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): Item ShakerReverse-airP-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0 31,324 31,324 31,324 Supv. labor 

### 0 4,699 4,699 4,699 Maint. labor 

### 0 17,228 17,228 17,228 Maint. matl. 

### 0 17,228 17,228 17,228 Electricity 

### 0 569,818 388,708 388,708 Compr. air 

### 0 0 

### 246,285 246,285 Bag repl. 0 

### 328,840 149,826 149,826 Dust dispos. 0 

### 1,375 1,375 1,375 Overhead 

### 0 42,287 42,287 42,287 Tax,ins.,adm 0 

### 1,139,871450,994 330,028 Cap. recov. 0 

### 2,633,7721,038,697 753,237

------------------------------------------------ 

### ------------ Total Annual 

### 0 4,786,4412,388,6501,982,224

Page 9 of 36

### Draft Cost Estimates -Doe Run, Herculaneum Add0on Control Technology - Fabric Filter Based on AVERAGE Stack Flow Rate



### Add-on BH for main combined with 7, 8 and 9

All MACT sources
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1] ANNUAL COST WEIGHTING FACTORS:

Item ShakerReverse-airP-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0.000 0.007 0.013 0.016 Supv. labor 

### 0.000 0.001 0.002 0.002 Maint. labor 

### 0.000 0.004 0.007 0.009 Maint. matl. 

### 0.000 0.004 0.007 0.009 Overhead 

### 0.000 0.009 0.018 0.021

------------ ---------- ----- ----- S/T labor: 

### 0.000 0.024 0.047 0.057 Compr. air 

### 0.000 0.000 0.103 0.124 Bag repl. 

### 0.000 0.069 0.063 0.076 Dust dispos. 

### 0.000 0.000 0.001 0.001 Electricity 

### 0.000 0.119 0.163 0.196 Tax,ins.,adm 

### 0.000 0.238 0.189 0.166 Cap. recov. 

### 0.000 0.550 0.435 0.380

------------ ---------- ----- ----- S/T capital: 

### 0.000 0.788 0.624 0.546

------------------------------------------------ 

### ------------ Total: 

### 0.000 1.000 1.000 1.000

============================================================
RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA

Net Cloth Area >/= (ft2): Gross/Net Area Ratio:

------------------------------------------------------------------------1 

### 2.000 4001 

### 1.500 12001 

### 1.250 24001 

### 1.170 36001 

### 1.125 48001 

### 1.110 60001 

### 1.100 72001 

### 1.090 84001 

### 1.080 96001 

### 1.070 108001 

### 1.060 132001 

### 1.050 180001 

### 1.040

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition).
[2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)

Page 10 of 36Standard Cloth Bags

Baghouse 8
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

2008

INPUT PARAMETERS: -- Inlet stream flowrate (acfm): -- Inlet stream temperature (oF): -- Dust type: -- Inlet dust loading (gr/ft3): Dust mass median diameter (microns): -- Filtration time (min): Dust specific resistance (in.H2O/fpm/lb/ft2): -- G/C ratio factors (shaker & reverse-air): A: B: C: -- G/C ratio factors (pulse-jet only): Material: Application: -- Cleaning pressure, psig (pulse-jet only): -- Fraction of bags cleaned (shaker & rev-air): -- Insulation required? ('yes'=1;'no'=0): -- Stainless steel required? ('yes'=1;'no'=0): -- Bag material:

-- Fabric effective residual drag (in. H2O/fpm): -- Bag prices ($/ft2): [4] Mechanical shaker: 0 0 Reverse-air $0.53 $0.69 Pulse-jet $0.95 $1.08

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area): Mechanical shaker: Reverse-air:Pulse-jet: -- Net cloth area required (ft2): Mechanical shaker: Reverse-air:Pulse-jet: -- Gross cloth area required (ft2): Mechanical shaker:Reverse-air: Pulse-jet: -- Area per bag/cage (ft2): -- Number of bags/cages (pulse-jet only): -- Baghouse pressure drop (in. w.c.): Mechanical shaker:Reverse-air: Pulse-jet:

CAPITAL COSTS Equipment Costs ($): Item: Cost ($): Shaker Rev-air P-J (mod)

------------------------------------------------------------ Baghouse 0 261,014 93,527 Bags 0 24,541 7,209 Insulation 0 27,572 16,146 Stainless 0 0 0 Cages 0 0 5,488

------------------------------------------------------------ Total: 0 313,127 122,370 PEC($)-base: 0 369,490 144,397 ' ' -esc.: 0 766,154 299,414 TCI ($): 0 1,662,553 649,728 ($/acfm): 0 22 9

============================================================Standard Cloth Bags

Baghouse 8
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2] ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 0.0944 Bag life (years): 5 Capital recovery factor (bags): 0.2439 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): Item Shaker Reverse-air P-J (mod)

------------------------------------------------------------ Oper. labor 0 31,324 31,324 Supv. labor 0 4,699 4,699 Maint. labor 0 17,228 17,228 Maint. matl. 0 17,228 17,228 Electricity 0 27,687 24,757 Compr. air 0 0 11,599 Bag repl. 0 7,265 2,299 Dust dispos. 0 3 3 Overhead 0 42,287 42,287 Tax,ins.,adm 0 66,502 25,989 Cap. recov. 0 154,121 60,440

------------------------------------------------ Total Annual 0 368,344 237,852

ANNUAL COST WEIGHTING FACTORS:

Item Shaker Reverse-air P-J (mod)

------------------------------------------------------------ Oper. labor 0.000 0.085 0.132 Supv. labor 0.000 0.013 0.020 Maint. labor 0.000 0.047 0.072 Maint. matl. 0.000 0.047 0.072 Overhead 0.000 0.115 0.178

------------ ----- ----- ----- S/T labor: 0.000 0.306 0.474 Compr. air 0.000 0.000 0.049 Bag repl. 0.000 0.020 0.010 Dust dispos. 0.000 0.000 0.000 Electricity 0.000 0.075 0.104 Tax,ins.,adm 0.000 0.181 0.109 Cap. recov. 0.000 0.418 0.254

------------ ----- ----- ----- S/T capital: 0.000 0.599 0.363

------------------------------------------------ Total: 0.000 1.000 1.000

============================================================
RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA

Net Cloth Area >/= (ft2):

------------------------------------------------------------------------1 4001 12001 24001 36001 48001 60001 72001 84001 96001 108001 132001Standard Cloth Bags

Baghouse 8
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2] 180001

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition). [2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)Standard Cloth Bags

Baghouse 9 (BH 7 will be the same)
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

575.4 2008 575.4

INPUT PARAMETERS:
76274 -- Inlet stream flowrate (acfm): 259807 107 -- Inlet stream temperature (oF): 107 Kettle refinery dust -- Dust type: Refinery bldg dust
0.0000490 -- Inlet dust loading (gr/ft3): 0.00007200 3.68 Dust mass median diameter (microns): 3.68 10 -- Filtration time (min): 10 15 Dust specific resistance (in.H2O/fpm/lb/ft2): 15 -- G/C ratio factors (shaker & reverse-air): 2.5 A: 2.5 1 B: 1 1.2 C: 1.2 -- G/C ratio factors (pulse-jet only): 10 Material: 10 0.8 Application: 0.8 100 -- Cleaning pressure, psig (pulse-jet only): 100 0 -- Fraction of bags cleaned (shaker & rev-air): 0 1 -- Insulation required? ('yes'=1;'no'=0): 1 0 -- Stainless steel required? ('yes'=1;'no'=0): 0 Fiberglass w/PTFE Membranes (cost modifier at right)1 -- Bag material: Fiberglass w/PTFE Membranes (cost modifier at right)1

1 -- Fabric effective residual drag (in. H2O/fpm): 1 -- Bag prices ($/ft2): [4] 0 0 Mechanical shaker: 0 0 0 0 $0.76 $0.99 Reverse-air $0.53 $0.69 $0.76 $0.99 $1.24 $1.29 Pulse-jet $0.95 $1.08 $1.24 $1.29

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area): 2.7 Mechanical shaker: 2.7 2.7 Reverse-air: 2.7 12.1 Pulse-jet: 11.8 -- Net cloth area required (ft2): 28250 Mechanical shaker: 96225 28250 Reverse-air: 96225 6323 Pulse-jet: 22044 -- Gross cloth area required (ft2): 33052 Mechanical shaker: 102961 33052 Reverse-air: 102961 6323 Pulse-jet: 22044

13 -- Area per bag/cage (ft2): 13 472 -- Number of bags/cages (pulse-jet only): 1644 -- Baghouse pressure drop (in. w.c.): 2.97 Mechanical shaker: 2.97 2.97 Reverse-air: 2.97 3.68 Pulse-jet: 3.59

CAPITAL COSTS Equipment Costs ($): Item: Cost ($): P-J (com) Shaker Rev-air P-J (mod) P-J (com)

------------------------------------------------------------ 44,796 Baghouse 0 751,212 208,649 132,077 7,209 Bags 0 76,448 25,130 25,130 7,315 Insulation 0 83,498 48,830 21,951 0 Stainless 0 0 0 0 5,488 Cages 0 0 19,116 19,116

------------------------------------------------------------ 64,808 Total: 0 911,159 301,726 198,275 76,474 PEC($)-base: 0 1,075,168 356,036 233,964 158,572 ' ' -esc.: 0 2,229,408 738,257 485,136 344,101 TCI ($): 0 4,837,816 1,602,018 1,052,744 5 ($/acfm): 0 19 6 4

============================================================Standard Cloth Bags

Baghouse 9 (BH 7 will be the same)
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2] ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 0.0944 Bag life (years): 5 Capital recovery factor (bags): 0.2439 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): P-J (com) Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ 31,324 Oper. labor 0 31,324 31,324 31,324 4,699 Supv. labor 0 4,699 4,699 4,699 17,228 Maint. labor 0 17,228 17,228 17,228 17,228 Maint. matl. 0 17,228 17,228 17,228 24,757 Electricity 0 92,073 82,399 82,399 11,599 Compr. air 0 0 39,507 39,507 2,299 Bag repl. 0 22,928 8,015 8,015 3 Dust dispos. 0 13 13 13 42,287 Overhead 0 42,287 42,287 42,287 13,764 Tax,ins.,adm 0 193,513 64,081 42,110 31,591 Cap. recov. 0 447,782 148,117 96,270

------------ ------------------------------------------------ ------------ 196,778 Total Annual 0 869,073 454,897 381,078

ANNUAL COST WEIGHTING FACTORS: P-J (com) Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ 0.159 Oper. labor 0.000 0.036 0.069 0.082 0.024 Supv. labor 0.000 0.005 0.010 0.012 0.088 Maint. labor 0.000 0.020 0.038 0.045 0.088 Maint. matl. 0.000 0.020 0.038 0.045 0.215 Overhead 0.000 0.049 0.093 0.111

----- ------------ ----- ----- ----- ----- 0.573 S/T labor: 0.000 0.130 0.248 0.296 0.059 Compr. air 0.000 0.000 0.087 0.104 0.012 Bag repl. 0.000 0.026 0.018 0.021 0.000 Dust dispos. 0.000 0.000 0.000 0.000 0.126 Electricity 0.000 0.106 0.181 0.216 0.070 Tax,ins.,adm 0.000 0.223 0.141 0.111 0.161 Cap. recov. 0.000 0.515 0.326 0.253

----- ------------ ----- ----- ----- ----- 0.230 S/T capital: 0.000 0.738 0.466 0.363

------------ ------------------------------------------------ ------------ 1.000 Total: 0.000 1.000 1.000 1.000

============================================================
RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA Gross/Net Area Ratio: Net Cloth Area >/= (ft2): Gross/Net Area Ratio:

------------------------------------------------------------------------ 2.000 1 2.000 1.500 4001 1.500 1.250 12001 1.250 1.170 24001 1.170 1.125 36001 1.125 1.110 48001 1.110 1.100 60001 1.100 1.090 72001 1.090 1.080 84001 1.080 1.070 96001 1.070 1.060 108001 1.060 1.050 132001 1.050Standard Cloth Bags

Baghouse 9 (BH 7 will be the same)
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2] 1.040 180001 1.040

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition). [2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)Membrane Bags

Baghouse 8
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

2008 575.4

INPUT PARAMETERS: -- Inlet stream flowrate (acfm): 76274 -- Inlet stream temperature (oF): 104 -- Dust type: Kettle refinery dust -- Inlet dust loading (gr/ft3): 0.0000490 Dust mass median diameter (microns): 3.68 -- Filtration time (min): 10 Dust specific resistance (in.H2O/fpm/lb/ft2): 15 -- G/C ratio factors (shaker & reverse-air): A: 2.5 B: 1 C: 1.2 -- G/C ratio factors (pulse-jet only): Material: 10 Application: 0.8 -- Cleaning pressure, psig (pulse-jet only): 100 -- Fraction of bags cleaned (shaker & rev-air): 0 -- Insulation required? ('yes'=1;'no'=0): 1 -- Stainless steel required? ('yes'=1;'no'=0): 0 -- Bag material: Fiberglass w/PTFE Membranes (cost modifier at right)3.75

-- Fabric effective residual drag (in. H2O/fpm): 1 -- Bag prices ($/ft2): [4] Mechanical shaker: 0 0 0 0 Reverse-air $1.99 $2.59 $2.85 $3.71 Pulse-jet $3.56 $4.05 $4.65 $4.84

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area): Mechanical shaker: 2.7 Reverse-air: 2.7 Pulse-jet: 12.1 -- Net cloth area required (ft2): Mechanical shaker: 28250 Reverse-air: 28250 Pulse-jet: 6282 -- Gross cloth area required (ft2): Mechanical shaker: 33052 Reverse-air: 33052 Pulse-jet: 6282 -- Area per bag/cage (ft2): 13 -- Number of bags/cages (pulse-jet only): 469 -- Baghouse pressure drop (in. w.c.): Mechanical shaker: 2.97 Reverse-air: 2.97 Pulse-jet: 3.70

CAPITAL COSTS Equipment Costs ($): Item: Cost ($): ShakerRev-airP-J (mod)P-J (com)

------------------------------------------------------------ Baghouse 0 261,014 93,220 44,564 Bags 0 92,029 26,854 26,854 Insulation 0 27,572 16,059 7,276 Stainless 0 0 0 0 Cages 0 0 5,454 5,454

------------------------------------------------------------ Total: 0 380,615 141,587 84,147 PEC($)-base: 0 449,126 167,073 99,294 ' ' -esc.: 0 931,282 346,433 205,890 TCI ($): 0 2,020,883751,760 446,781 ($/acfm): 0 26 10 6

============================================================Membrane Bags

Baghouse 8
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2] ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 0.0944 Bag life (years): 5 Capital recovery factor (bags): 0.2439 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): Item ShakerReverse-airP-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 0 31,324 31,324 31,324 Supv. labor 0 4,699 4,699 4,699 Maint. labor 0 17,228 17,228 17,228 Maint. matl. 0 17,228 17,228 17,228 Electricity 0 27,687 24,922 24,922 Compr. air 0 0 11,599 11,599 Bag repl. 0 25,037 7,471 7,471 Dust dispos. 0 3 3 3 Overhead 0 42,287 42,287 42,287 Tax,ins.,adm 0 80,835 30,070 17,871 Cap. recov. 0 181,067 68,069 39,281

------------------------------------------------ ------------ Total Annual 0 427,394 254,899 213,912

ANNUAL COST WEIGHTING FACTORS:

Item ShakerReverse-airP-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 0.0000.073 0.123 0.146 Supv. labor 0.0000.011 0.018 0.022 Maint. labor 0.0000.040 0.068 0.081 Maint. matl. 0.0000.040 0.068 0.081 Overhead 0.0000.099 0.166 0.198

------------ ---------- ----- ----- S/T labor: 0.0000.264 0.442 0.527 Compr. air 0.0000.000 0.046 0.054 Bag repl. 0.0000.059 0.029 0.035 Dust dispos. 0.0000.000 0.000 0.000 Electricity 0.0000.065 0.098 0.117 Tax,ins.,adm 0.0000.189 0.118 0.084 Cap. recov. 0.0000.424 0.267 0.184

------------ ---------- ----- ----- S/T capital: 0.0000.613 0.385 0.267

------------------------------------------------ ------------ Total: 0.000 1.000 1.000 1.000

============================================================
RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA

Net Cloth Area >/= (ft2): Gross/Net Area Ratio:

------------------------------------------------------------------------1 2.000 4001 1.500 12001 1.250 24001 1.170 36001 1.125 48001 1.110 60001 1.100 72001 1.090 84001 1.080 96001 1.070 108001 1.060 132001 1.050Membrane Bags

Baghouse 8
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2] 180001 1.040

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition). [2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)Membrane Bags

Baghouse 9 (BH 7 will be the same)
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

2008 575.4

INPUT PARAMETERS: -- Inlet stream flowrate (acfm): 259807 -- Inlet stream temperature (oF): 107 -- Dust type: Refinery bldg dust -- Inlet dust loading (gr/ft3): 0.00007200 Dust mass median diameter (microns): 3.68 -- Filtration time (min): 10 Dust specific resistance (in.H2O/fpm/lb/ft2): 15 -- G/C ratio factors (shaker & reverse-air): A: 2.5 B: 1 C: 1.2 -- G/C ratio factors (pulse-jet only): Material: 10 Application: 0.8 -- Cleaning pressure, psig (pulse-jet only): 100 -- Fraction of bags cleaned (shaker & rev-air): 0 -- Insulation required? ('yes'=1;'no'=0): 1 -- Stainless steel required? ('yes'=1;'no'=0): 0

-- Bag material: Fiberglass w/PTFE Membranes (cost modifier at right) 3.75

-- Fabric effective residual drag (in. H2O/fpm): 1 -- Bag prices ($/ft2): [4] Mechanical shaker: 0 0 0 0 Reverse-air $1.99 $2.59 $2.85 $3.71 Pulse-jet $3.56 $4.05 $4.65 $4.84

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area):Mechanical shaker: 2.7 Reverse-air: 2.7 Pulse-jet: 11.8 -- Net cloth area required (ft2): Mechanical shaker: 96225 Reverse-air: 96225 Pulse-jet: 22044 -- Gross cloth area required (ft2):Mechanical shaker: 102961 Reverse-air: 102961 Pulse-jet: 22044 -- Area per bag/cage (ft2): 13 -- Number of bags/cages (pulse-jet only): 1644 -- Baghouse pressure drop (in. w.c.):Mechanical shaker: 2.97 Reverse-air: 2.97 Pulse-jet: 3.59

CAPITAL COSTS Equipment Costs ($): Item: Cost ($):

Shaker Rev-air P-J (mod) P-J (com)

------------------------------------------------------------ Baghouse 0 751,212 208,649 132,077 Bags 0 286,681 94,239 94,239 Insulation 0 83,498 48,830 21,951 Stainless 0 0 0 0 Cages 0 0 19,116 19,116

------------------------------------------------------------ Total: 0 1,121,392 370,834 267,383 PEC($)-base: 0 1,323,242 437,584 315,512 ' ' -esc.: 0 2,743,802 907,351 654,229 TCI ($): 0 5,954,050 1,968,951 1,419,676 ($/acfm): 0 23 8 5

============================================================Membrane Bags

Baghouse 9 (BH 7 will be the same)
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 0.0944 Bag life (years): 5 Capital recovery factor (bags): 0.2439 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 0 31,324 31,324 31,324 Supv. labor 0 4,699 4,699 4,699 Maint. labor 0 17,228 17,228 17,228 Maint. matl. 0 17,228 17,228 17,228 Electricity 0 92,073 82,399 82,399 Compr. air 0 0 39,507 39,507 Bag repl. 0 78,303 26,218 26,218 Dust dispos. 0 13 13 13 Overhead 0 42,287 42,287 42,287 Tax,ins.,adm 0 238,162 78,758 56,787 Cap. recov. 0 531,715 175,708 123,860

------------------------------------------------ ------------ Total Annual 0 1,053,031 515,368 441,549

ANNUAL COST WEIGHTING FACTORS:

Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor0.000 0.030 0.061 0.071 Supv. labor0.000 0.004 0.009 0.011 Maint. labor0.000 0.016 0.033 0.039 Maint. matl.0.000 0.016 0.033 0.039 Overhead 0.000 0.040 0.082 0.096

------------ ----- ----- ----- ----- S/T labor: 0.000 0.107 0.219 0.255 Compr. air 0.000 0.000 0.077 0.089 Bag repl. 0.000 0.074 0.051 0.059 Dust dispos.0.000 0.000 0.000 0.000 Electricity 0.000 0.087 0.160 0.187 Tax,ins.,adm0.000 0.226 0.153 0.129 Cap. recov.0.000 0.505 0.341 0.281

------------ ----- ----- ----- ----- S/T capital:0.000 0.731 0.494 0.409

------------------------------------------------ ------------ Total: 0.000 1.000 1.000 1.000

============================================================
RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA

Net Cloth Area >/= (ft2): Gross/Net Area Ratio:

------------------------------------------------------------------------ 1 2.000 4001 1.500 12001 1.250 24001 1.170 36001 1.125 48001 1.110 60001 1.100 72001 1.090 84001 1.080 96001 1.070 108001 1.060 132001 1.050Membrane Bags

Baghouse 9 (BH 7 will be the same)
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

180001 1.040

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition). [2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)

# Total Cost InvestmentTotal

Annualized Cost2008 Baseline

Pb Emissions (tpy)Emission Reduction

from upgrade* (tpy) CE

($/ton) Furnace area, BH 7 81,548 27,591 1.81 0.95 29,043 Refining, BH 8 102,032 17,048 0.45 0.21 81,179 Refining BH 9 366,932 60,471 2.03 1.3 45,467 *We estimate removal efficiency for membrane bag update to be between 50 and 70 percent.



# Total Cost InvestmentTotal

Annualized Cost2008 Baseline

Pb Emissions (tpy)Emission Reduction

from upgrade* (tpy) CE

($/ton) Main Stack 1,958,851322,823 13.31 8.0 40,424 *We estimate removal efficiency for membrane bag update to be between 50 and 70 percent. 

# Cost of Upgrade to Membrane Bags

Cost of Upgrade to Membrane Bags 

# Table 3.1 - Cost Effectiveness of Upgrading Baghouses to Membrane Bags for Baghouses 7, 8 and 9

Table 3.3 - Cost Effectiveness of Upgrading Baghouses to Membrane Bags for Main Stack Impacts Impacts

# ProcessSourceEmission Reduction Required to Reduce Risks? Control AddedTCI ($)TAC ($)Baseline Emissions (tpy)Emission

Reduction (tpy)Cost

Effectiveness ($/ton) Smelter Main Stack No None 0 013.310 0

BH 7 Yes Membrane bags366,93260,4711.810.9563,654 Refining BH8 Yes Membrane bags102,03217,048

BH 9 Yes Membrane bags366,93260,471 Total refining Yes 468,96477,5192.741.843,066 Total Process 835,897137,99017.862.7550,178 Cost Effectiveness of Additional Controls for Primary Lead Smelting NESHAP

### Main Stack - Standard Bags

Main stack 

### Dec. 20, 2010
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

2008 575.4

INPUT PARAMETERS: -- Inlet stream flowrate (acfm): 

### 1023723 -- Inlet stream temperature (oF): 170 -- Dust type: Blast furnace dust -- Inlet dust loading (gr/ft3): 

### 0.0018699 Dust mass median diameter (microns): 3.68 -- Filtration time (min): 10 Dust specific resistance (in.H2O/fpm/lb/ft2): 15 -- G/C ratio factors (shaker & reverse-air): A: 

### 2.5 B: 1 C: 

### 1.2 -- G/C ratio factors (pulse-jet only): Material: 10 Application: 0.8 -- Cleaning pressure, psig (pulse-jet only): 100 -- Fraction of bags cleaned (shaker & rev-air): 0 -- Insulation required? ('yes'=1;'no'=0): 1 -- Stainless steel required? ('yes'=1;'no'=0): 0 -- Bag material: Fiberglass w/PTFE Membranes (cost modifier at right) 

### 1
-- Fabric effective residual drag (in. H2O/fpm): 1 -- Bag prices ($/ft2): [4] Mechanical shaker: 0 0 0 0 Reverse-air $0.53 $0.69 $0.76 $0.99 Pulse-jet $0.95 $1.08 $1.24 $1.29

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area):Mechanical shaker: 2.7 Reverse-air: 2.7 Pulse-jet: 

### 8.7 -- Net cloth area required (ft2): Mechanical shaker: 

### 379157 Reverse-air: 

### 379157 Pulse-jet: 

### 117682 -- Gross cloth area required (ft2): Mechanical shaker: 

### 394323 Reverse-air: 

### 394323 Pulse-jet: 

### 117682 -- Area per bag/cage (ft2): 13 -- Number of bags/cages (pulse-jet only): 8772 -- Baghouse pressure drop (in. w.c.): Mechanical shaker: 

### 2.97 Reverse-air: 

### 2.97 Pulse-jet: 

### 2.65

### Main Stack - Standard Bags

Main stack 

### Dec. 20, 2010
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2] CAPITAL COSTS Equipment Costs ($): Item: Cost ($): Shaker Rev-air P-J (mod) P-J (com)

------------------------------------------------------------ Baghouse 

### 0 2,794,245 909,003 663,057 Bags 

### 0 292,785 134,157 134,157 Insulation 

### 0 316,588 247,660 110,990 Stainless 

### 0 0 0 0 Cages 0 0 

### 102,001 102,001

------------------------------------------------------------ Total: 

### 0 3,403,619 1,392,821 1,010,204 PEC($)-base: 

### 0 4,016,270 1,643,528 1,192,041 ' ' -esc.: 

### 0 8,327,916 3,407,930 2,471,749 TCI ($): 

### 0 18,071,577 7,395,207 5,363,696 ($/acfm): 0 

### 18 7 5

============================================================
ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): 

### $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 

### 0.0944 Bag life (years): 5 Capital recovery factor (bags): 

### 0.2439 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0 31,324 31,324 31,324 Supv. labor 

### 0 4,699 4,699 4,699 Maint. labor 

### 0 17,228 17,228 17,228 Maint. matl. 

### 0 17,228 17,228 17,228 Electricity 

### 0 360,179 239,906 239,906 Compr. air 

### 0 0 

### 155,671 155,671 Bag repl. 0 

### 92,012 42,783 42,783 Dust dispos. 0 

### 1,299 1,299 1,299 Overhead 

### 0 42,287 42,287 42,287 Tax,ins.,adm 0 

### 722,863 295,808 214,548 Cap. recov. 0 

### 1,670,218 681,497 489,737

------------------------------------------------ 

### ------------ Total Annual 

### 0 2,959,336 1,529,730 1,256,709

### Main Stack - Standard Bags

Main stack 

### Dec. 20, 2010
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]ANNUAL COST WEIGHTING FACTORS:

Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0.000 0.011 0.020 0.025 Supv. labor 

### 0.000 0.002 0.003 0.004 Maint. labor 

### 0.000 0.006 0.011 0.014 Maint. matl. 

### 0.000 0.006 0.011 0.014 Overhead 

### 0.000 0.014 0.028 0.034

------------ ----- ----- ----- ----- S/T labor: 

### 0.000 0.038 0.074 0.090 Compr. air 

### 0.000 0.000 0.102 0.124 Bag repl. 

### 0.000 0.031 0.028 0.034 Dust dispos. 

### 0.000 0.000 0.001 0.001 Electricity 

### 0.000 0.122 0.157 0.191 Tax,ins.,adm 

### 0.000 0.244 0.193 0.171 Cap. recov. 

### 0.000 0.564 0.446 0.390

------------ ----- ----- ----- ----- S/T capital: 

### 0.000 0.809 0.639 0.560

------------------------------------------------ 

### ------------ Total: 

### 0.000 1.000 1.000 1.000

============================================================
RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA

Net Cloth Area >/= (ft2): Gross/Net Area Ratio:

------------------------------------------------------------------------ 1 

### 2.000 4001 

### 1.500 12001 

### 1.250 24001 

### 1.170 36001 

### 1.125 48001 

### 1.110 60001 

### 1.100 72001 

### 1.090 84001 

### 1.080 96001 

### 1.070 108001 

### 1.060 132001 

### 1.050 180001 

### 1.040

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition). [2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)

### Main Stack - Membrane Bags

Main stack
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]

2008 575.4

INPUT PARAMETERS: -- Inlet stream flowrate (acfm): 

### 1023723 -- Inlet stream temperature (oF): 170 -- Dust type: Blast furnace dust -- Inlet dust loading (gr/ft3): 

### 0.0018699 Dust mass median diameter (microns): 3.68 -- Filtration time (min): 10 Dust specific resistance (in.H2O/fpm/lb/ft2): 15 -- G/C ratio factors (shaker & reverse-air): A: 

### 2.5 B: 1 C: 

### 1.2 -- G/C ratio factors (pulse-jet only): Material: 10 Application: 0.8 -- Cleaning pressure, psig (pulse-jet only): 100 -- Fraction of bags cleaned (shaker & rev-air): 0 -- Insulation required? ('yes'=1;'no'=0): 1 -- Stainless steel required? ('yes'=1;'no'=0): 0 -- Bag material: Fiberglass w/PTFE Membranes (cost modifier at right) 

### 3.75
-- Fabric effective residual drag (in. H2O/fpm): 1 -- Bag prices ($/ft2): [4] Mechanical shaker: 0 0 0 0 Reverse-air $1.99 $2.59 $2.85 $3.71 Pulse-jet $3.56 $4.05 $4.65 $4.84

DESIGN PARAMETERS -- Gas-to-cloth ratio (acfm/ft2 cloth area):Mechanical shaker: 2.7 Reverse-air: 2.7 Pulse-jet: 

### 8.7 -- Net cloth area required (ft2): Mechanical shaker: 

### 379157 Reverse-air: 

### 379157 Pulse-jet: 

### 117682 -- Gross cloth area required (ft2): Mechanical shaker: 

### 394323 Reverse-air: 

### 394323 Pulse-jet: 

### 117682 -- Area per bag/cage (ft2): 13 -- Number of bags/cages (pulse-jet only): 8772 -- Baghouse pressure drop (in. w.c.): Mechanical shaker: 

### 2.97 Reverse-air: 

### 2.97 Pulse-jet: 

### 2.65

### Main Stack - Membrane Bags

Main stack
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2] CAPITAL COSTS Equipment Costs ($): Item: Cost ($): Shaker Rev-air P-J (mod) P-J (com)

------------------------------------------------------------ Baghouse 

### 0 2,794,245 909,003 663,057 Bags 

### 0 1,097,943 503,089 503,089 Insulation 

### 0 316,588 247,660 110,990 Stainless 

### 0 0 0 0 Cages 0 0 

### 102,001 102,001

------------------------------------------------------------ Total: 

### 0 4,208,777 1,761,753 1,379,136 PEC($)-base: 

### 0 4,966,356 2,078,868 1,627,380 ' ' -esc.: 

### 0 10,297,963 4,310,626 3,374,446 TCI ($): 

### 0 22,346,579 9,354,058 7,322,548 ($/acfm): 0 

### 22 9 7

============================================================
ANNUAL COST INPUTS: Operating factor (hr/yr): 7920 Operating labor rate ($/hr): $15.82 Maintenance labor rate ($/hr): 

### $17.40 Operating labor factor (hr/sh): 2.00 Maintenance labor factor (hr/sh): 1.00 Electricity price ($/kWhr): 0.062 Compressed air ($/1000 scf): 0.16 Dust disposal ($/ton): 20 Annual interest rate (fraction): 0.07 Control system life (years): 20 Capital recovery factor: 

### 0.0944 Bag life (years): 5 Capital recovery factor (bags): 

### 0.2439 Taxes, insurance, admin. factor: 4% ANNUAL COSTS ($/yr): Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0 31,324 31,324 31,324 Supv. labor 

### 0 4,699 4,699 4,699 Maint. labor 

### 0 17,228 17,228 17,228 Maint. matl. 

### 0 17,228 17,228 17,228 Electricity 

### 0 360,179 239,906 239,906 Compr. air 

### 0 0 

### 155,671 155,671 Bag repl. 0 

### 304,092 139,961 139,961 Dust dispos. 0 

### 1,299 1,299 1,299 Overhead 

### 0 42,287 42,287 42,287 Tax,ins.,adm 0 

### 893,863 374,162 292,902 Cap. recov. 0 

### 1,991,666 828,788 637,028

------------------------------------------------ 

### ------------ Total Annual 

### 0 3,663,865 1,852,553 1,579,532

### Main Stack - Membrane Bags

Main stack
TOTAL ANNUAL COST SPREADSHEET PROGRAM--FABRIC FILTERS [1]
COST BASE DATE: Third Quarter 1986 [2]ANNUAL COST WEIGHTING FACTORS:

Item Shaker Reverse-air P-J (mod) P-J (com)

------------------------------------------------------------ Oper. labor 

### 0.000 0.009 0.017 0.020 Supv. labor 

### 0.000 0.001 0.003 0.003 Maint. labor 

### 0.000 0.005 0.009 0.011 Maint. matl. 

### 0.000 0.005 0.009 0.011 Overhead 

### 0.000 0.012 0.023 0.027

------------ ----- ----- ----- ----- S/T labor: 

### 0.000 0.031 0.061 0.071 Compr. air 

### 0.000 0.000 0.084 0.099 Bag repl. 

### 0.000 0.083 0.076 0.089 Dust dispos. 

### 0.000 0.000 0.001 0.001 Electricity 

### 0.000 0.098 0.130 0.152 Tax,ins.,adm 

### 0.000 0.244 0.202 0.185 Cap. recov. 

### 0.000 0.544 0.447 0.403

------------ ----- ----- ----- ----- S/T capital: 

### 0.000 0.788 0.649 0.589

------------------------------------------------ 

### ------------ Total: 

### 0.000 1.000 1.000 1.000

============================================================

RELATIONSHIP BETWEEN GROSS AND NET CLOTH AREA

Net Cloth Area >/= (ft2): Gross/Net Area Ratio:

------------------------------------------------------------------------ 1 

### 2.000 4001 

### 1.500 12001 

### 1.250 24001 

### 1.170 36001 

### 1.125 48001 

### 1.110 60001 

### 1.100 72001 

### 1.090 84001 

### 1.080 96001 

### 1.070 108001 

### 1.060 132001 

### 1.050 180001 

### 1.040

[1] Parameters and other input data needed for this program can be found in Chapter 5 of the 'OAQPS Control Cost Manual'(4th edition). [2] Base equipment costs reflect this date. [3] VAPCCI = Vatavuk Air Pollution Control Cost Index (for fabric filters) corresponding to year and quarter shown. Base equipment cost, purchased equipment cost, and total capital investment have been escalated to this date via VAPCCI and control equipment vendor data. [4] These prices pertain to the bag material entered above. If this bag material is not available for a baghouse type, enter '0'. (See 'Manual,' Chapter 5, Table 5.7.)

# TCI TAC TCI TAC TCI Main Stack7,395,2071,529,7309,354,0581,852,5531,958,851

Standard Bags Membrane Bags Incremental Cost

Main Stack - Membrane Bag Costs for PJ Modular and Impacts

# TACBaseline Pb Emissions (tpy)Emission

Reduction @ 50% RE (tpy) CE

($/ton) 322,82313.31 6.748,508 Incremental Cost Impacts Main Stack - Membrane Bag Costs for PJ Modular and Impacts

## Doe Run, Herculaneum - Summary of Stack Test Results

Main Stack Test DateMay-99Apr-01Apr-02Jan-03Dec-04Dec-06June, 2008Average Inlet stream flowrate (acfm): 103832810884861088923943784102814396260310157941023723 inlet stream flowrate ((DSCFM) 794047855576838309824628826128809737793078820215 Inlet stream temperature (oF): 181.3186199127164153177170 Inlet dust loading (gr/ft3):per DSCF2.94E-036.44E-043.21E-032.43E-031.00E-035.45E-042.32E-031.87E-03 production rate during test (tonnes/hr) 25.358.0518.01815.88 16.82 production rate during test (ton/hr) 80.98 8.87519.86117.5 31.80 lead emission rate (t/yr) 87.920.7100.8875.6031.116.6469.4057.46 lead emssion rate (lb/hr) 20.074.7223.03217.267.13.815.84513.12 lead emission rate (lb/ton) 0.250.172.600.870.41 0.86 w/o 2.590.42 Baghouse 7/9 stack Test DateJune,2 008

Inlet stream flowrate (acfm): 519614 inlet stream flowrate ((DSCFM) 475165 Inlet stream temperature (oF): 107 Inlet dust loading (gr/ft3):per DSCF0.0000720 production rate during test (tonnes/hr) production rate during test (ton/hr) lead emission rate (t/yr) 1.29 lead emssion rate (lb/hr) 0.2956 Baghouse 8 stack Test DateJune,2 008

Inlet stream flowrate (acfm): 76274 inlet stream flowrate ((DSCFM) 70562 Inlet stream temperature (oF): 104 Inlet dust loading (gr/ft3):per DSCF4.90E-05 production rate during test (tonnes/hr) production rate during test (ton/hr) lead emission rate (t/yr) 0.13 lead emssion rate (lb/hr) 0.0297

Total emissions for all 3 stacks (average scenarios) (TPY)58.89 Total emissions for all 3 stacks (maximum scenarios) (TPY)102.30 Total average emissions for 7,8,9 (TPY) 1.42

These values were not included in the stack test data and were calcualted from the stack test lb/hr value using 8760 hours per year.