### Pollutant Control Annual Cost to Comply Annual Reductions (TPY)* Hg ACI/FF $3,137,815 0.00190 Shown is the cost effectiveness for applying ACI/FF combination to all units to reduce emissions to the reference method detection level (RMDL) of 0.00034 mg/dscm for Hg. *From BTF_EmissionReductions File

### Cost Effectiveness ($/ton) $1,653,131,275 Shown is the cost effectiveness for applying ACI/FF combination to all units to reduce emissions to the reference method detection level (RMDL) of 0.00034 mg/dscm for Hg.

### Secondary Impacts of ERU-Liquid **Secondary Emissions from ERU-Liquid FF**  **SNCR Total**  **CO2 elec (Mw)**  5,572 66 5,637 7,494,062 **water (gal/yr)** 21,303,000 21,303,000 **AC I (lb/yr)**  0 **Dust (tpy)** 308 308 **Natural Gas (Mmscf/yr)** 0 0 lbs/yr 7,494,062 tons/yr 3,747.0

**Emission Factors Electrcity** **a** 

### Pollutant **(lb/Mw-hr) (lb/10** **6**

### scf) **lb/ft3 ton/ft3**  **CO2** 1,329 120,000 0.12 0.00006 **CO**

- 84 0.000084 0.000000042 **NOx** 1.9366 100 0.0001 0.00000005 **SO2** 5.2589

- - - a. National em ission factors from Egrid for EGUs b. Natural gas emission factors from AP 42 **Natural Gas b** 

### Secondary Emissions from ERU-Liquid

**CO SO2**  **NOx**

29,646 10,917

0 0 0 29,646 10,917 0.0 14.8 5.5

### Summary of MACT Compliance Costs for Energy Recovery Units

**Total Capital Investment**  **($) Total Annual** 

**Cost ($/yr)**  **Total Capital**

**Investment ($)**  **Total Annual**

**Cost ($/yr)**  **Total Capital**

**Investment ($)**  **Total Annual Cost**

**($/yr)**

LADeltech HB-507 Flue Gas Recirculation CO oxidation catalyst, fabric filter $2,111,113 $533,006 $123,896 $89,587 $2,235,009 $622,593 LADeltech HB-512 Flue Gas Recirculation CO oxidation catalyst, fabric filter $5,384,706 $1,237,710 $123,896 $89,587 $5,508,602 $1,327,297 MDSeverstalSparrows 1BLR No Equipment CO oxidation catalyst, fabric filter, SNCR $18,264,374 $3,949,452 $249,050 $134,227 $18,513,424 $4,083,679
MEPioneerPlastics Boiler #5/Thermal Oxidizer No Equipment CO oxidation catalyst, fabric filter, SNCR $5,787,718 $1,354,042 $134,196 $92,787 $5,921,914 $1,446,829
WAEmeraldKalama U-2 Collectors, Settling Chambers, Separators - General none $0 $0 $98,396 $79,887 $98,396 $79,887
WAEmeraldKalama U-7 Collectors, Settling Chambers, Separators - General none $0 $0 $98,396 $79,887 $98,396 $79,887 **$32,375,741 $7,640,173**  **Control Costs Monitoring, Reporting, and**  **Recordkeeping Costs Total MACT Floor Control, Monitoring,**  **Reporting, and Recordkeeping Costs FacilityID**  **UnitID Existing Control Device**  **Consolidated MACT Controls**

1 of 1Table 2A. Energy Recovery Units - Liquid/Gas: Costs to Meet MACT Floor (1 of 4)

**Dust Elec**  **Elec Water**  TCI ($) TCI

($/dscfm) TAC

($/yr) TAC

($/yr/dscfm) tpy Mw TCI ($) TCI

($/dscfm) TAC

($/yr) TAC

($/yr/dscfm) Mw gal/yr TCI ($) TCI

($/dscfm) TAC

($/yr)

LADeltech HB-507 Flue Gas Recirculation CO oxidation catalyst, fabric filter $1,658,936 $187.49 $337,822 $38.18 4.99 108 $452,177 $56.21 $195,184
LADeltech HB-512 Flue Gas Recirculation CO oxidation catalyst, fabric filter $4,435,287 $129.19 $852,254 $24.82 19.37 403 $949,419 $30.42 $385,456 MDSeverstalSparrows 1BLR No Equipment CO oxidation catalyst, fabric filter, SNCR $13,170,514 $120.23 $2,761,553 $25.21 197.42 4,075 $3,383,226 $30.88 $378,598 $3.46 62.1 11,178,000 $1,710,634 $18.68 $809,301
MEPioneerPlastics Boiler #5/Thermal Oxidizer No Equipment CO oxidation catalyst, fabric filter, SNCR $3,843,694 $132.91 $869,267 $30.06 86.67 986 $1,034,806 $35.78 $117,366 $4.06 3.4 10,125,000 $909,218 $31.53 $367,408

WAEmeraldKalama U-2 Collectors, Settling Chambers, Separators - General none

WAEmeraldKalama U-7 Collectors, Settling Chambers, Separators - General none

308.45 5,572 65.5 21,303,000 **SNCR CO Oxidation Catalyst**  **FacilityID UnitID**  **ControlDevice Consolidated MACT**  **Controls**
**Add Fabric Filter**Table 2A. Energy Recovery Units - Liquid/Gas: Costs to Meet MACT Floor (2 of 4)

LADeltech HB-507 Flue Gas Recirculation CO oxidation catalyst, fabric filter
LADeltech HB-512 Flue Gas Recirculation CO oxidation catalyst, fabric filter MDSeverstalSparrows 1BLR No Equipment CO oxidation catalyst, fabric filter, SNCR
MEPioneerPlastics Boiler #5/Thermal Oxidizer No Equipment CO oxidation catalyst, fabric filter, SNCR

WAEmeraldKalama U-2 Collectors, Settling Chambers, Separators - General none

WAEmeraldKalama U-7 Collectors, Settling Chambers, Separators - General none **FacilityID UnitID**  **ControlDevice Consolidated MACT**  **Controls**

TAC ($/yr/dscfm)
$24.26 $12.35 $8.84 $12.74Table 2A. Energy Recovery Units - Liquid/Gas: Costs to Meet MACT Floor (3 of 4)

LADeltech HB-507 Flue Gas Recirculation CO oxidation catalyst, fabric filter
LADeltech HB-512 Flue Gas Recirculation CO oxidation catalyst, fabric filter MDSeverstalSparrows 1BLR No Equipment CO oxidation catalyst, fabric filter, SNCR
MEPioneerPlastics Boiler #5/Thermal Oxidizer No Equipment CO oxidation catalyst, fabric filter, SNCR

WAEmeraldKalama U-2 Collectors, Settling Chambers, Separators - General none

WAEmeraldKalama U-7 Collectors, Settling Chambers, Separators - General none **FacilityID UnitID**  **ControlDevice Consolidated MACT**  **Controls Annual Stack**  **Test TCI**  **($) TCI** 

**($/dscfm) TA** **C**

**($/yr) TA** **C**

**($/yr/dscfm)** TCI

($) TAC

($/yr) TAC

($/yr) TCI

($) TAC

($/yr) TCI

($) TAC

($/yr) TCI

($) TAC

($/yr) TCI

($) TAC

($/yr)
$2,111,113 $244 $533,006 $62 $55,000 $6,039 $55,000 $25,500 $9,700 $43,146 $14,660 $5,384,706 $160 $1,237,710 $37 $55,000 $6,039 $55,000 $25,500 $9,700 $43,146 $14,660 $18,264,374 $170 $3,949,452 $38 $55,000 $6,039 $55,000 $158,000 $56,100 $25,500 $9,700 $10,300 $3,200 $5,787,718 $200 $1,354,042 $47 $55,000 $6,039 $55,000 $25,500 $9,700 $10,300 $3,200 $43,146 $14,660

$0 $0 $0 $0 $55,000 $6,039 $55,000 $43,146 $14,660

$0 $0 $0 $0 $55,000 $6,039 $55,000 $43,146 $14,660

**Controls Subtotals Initial Stack Test**  **Bag Leak Detection System**  **SNCR Monitoring System Add CPMS or PM CEMS**  **Opacity Monitoring System** Table 2A. Energy Recovery Units - Liquid/Gas: Costs to Meet MACT Floor (4 of 4)

LADeltech HB-507 Flue Gas Recirculation CO oxidation catalyst, fabric filter
LADeltech HB-512 Flue Gas Recirculation CO oxidation catalyst, fabric filter MDSeverstalSparrows 1BLR No Equipment CO oxidation catalyst, fabric filter, SNCR
MEPioneerPlastics Boiler #5/Thermal Oxidizer No Equipment CO oxidation catalyst, fabric filter, SNCR

WAEmeraldKalama U-2 Collectors, Settling Chambers, Separators - General none

WAEmeraldKalama U-7 Collectors, Settling Chambers, Separators - General none **FacilityID UnitID**  **ControlDevice Consolidated MACT**  **Controls Annual Control**  **Device Inspection**  **Reporting and Recordkeeping**  **Requirements** TAC ($/yr) TCI

($) TAC

($/yr) TAC

($/yr) **TCI**

**($) TA** **C**

**($/yr) TCI** 

**($) TA** **C**

**($/yr)**
$1,000 $250 $200 $2,989 $123,896 $89,587 $2,235,009 $622,593 $1,000 $250 $200 $2,989 $123,896 $89,587 $5,508,602 $1,327,297 $1,000 $250 $200 $2,989 $249,050 $134,227 $18,513,424 $4,083,679 $1,000 $250 $200 $2,989 $134,196 $92,787 $5,921,914 $1,446,829

$1,000 $250 $200 $2,989 $98,396 $79,887 $98,396 $79,887

$1,000 $250 $200 $2,989 $98,396 $79,887 $98,396 $79,887 $32,375,741 $7,640,173 **Total MACT Floor Control, Monitoring, Reporting, and**  **Recordkeeping Cost Testing, Monitoring, and**  **Recordkeeping Subtotals Annual Visual Emissions**  **Test of Ash Handling**Table 2A. Energy Recovery Units - Liquid/Gas: Costs to Meet MACT Floor (1 of 2)

TCI ($) TCI

($/dscfm) TAC

($/yr) TAC

($/yr/dscfm) TCI

($) TCI

($/dscfm) TAC

($/yr) TAC

($/yr/dscfm)

LADeltech HB-507 Flue Gas Recirculation CO oxidation catalyst, fabric filter ACI $21,142 $2.39 $42,098 $4.76
LADeltech HB-512 Flue Gas Recirculation CO oxidation catalyst, fabric filter ACI $47,691 $1.39 $135,398 $3.94 MDSeverstalSparrows 1BLR No Equipment CO oxidation catalyst, fabric filter, SNCR ACI $95,670 $0.87 $1,174,198 $10.72
MEPioneerPlastics Boiler #5/Thermal Oxidizer No Equipment CO oxidation catalyst, fabric filter, SNCR ACI $43,025 $1.49 $299,453 $10.36

WAEmeraldKalama U-2 Collectors, Settling Chambers, Separators - General none ACI/FF $2,006,522 $166 $546,759 $45 $24,975 $2.14 $179,622 $15.38

WAEmeraldKalama U-7 Collectors, Settling Chambers, Separators - General none ACI/FF $1,884,734 $172 $522,488 $48 $24,797 $2.15 $177,799 $15.40 $1,069,247 2,008,567.34 **FacilityID UnitID**  **ControlDevice Consolidated MACT**  **Controls**
**Add Fabric Filter Beyond the Floor**  **Control Options**
**ACI**Table 2A. Energy Recovery Units - Liquid/Gas: Costs to Meet MACT Floor (2 of 2)

LADeltech HB-507 Flue Gas Recirculation CO oxidation catalyst, fabric filter
LADeltech HB-512 Flue Gas Recirculation CO oxidation catalyst, fabric filter MDSeverstalSparrows 1BLR No Equipment CO oxidation catalyst, fabric filter, SNCR
MEPioneerPlastics Boiler #5/Thermal Oxidizer No Equipment CO oxidation catalyst, fabric filter, SNCR

WAEmeraldKalama U-2 Collectors, Settling Chambers, Separators - General none

WAEmeraldKalama U-7 Collectors, Settling Chambers, Separators - General none **FacilityID UnitID**  **ControlDevice Consolidated MACT**  **Controls ACI**  **Monitoring TCI**  **($) TCI** 

**($/dscfm) TA** **C**

**($/yr) TA** **C**

**($/yr/dscfm)** TCI

($) TAC

($/yr) TAC

($/yr) **TCI**

**($) TA** **C**

**($/yr) TCI** 

**($) TA** **C**

**($/yr)**
$21,142 $2 $42,098 $5 $2,600 $250 $6,789 $21,392 $48,886 $47,691 $1 $135,398 $4 $2,600 $250 $6,789 $47,941 $142,187 $95,670 $1 $1,174,198 $11 $8,000 $250 $12,189 $95,920 $1,186,387 $43,025 $1 $299,453 $10 $7,200 $250 $11,389 $43,275 $310,841

$2,031,497 $168 $726,381 $61 $25,500 $9,700 $10,100 $25,750 $23,989 $2,057,247 $750,369

$1,909,531 $175 $700,287 $63 $25,500 $9,700 $10,100 $25,750 $23,989 $1,935,281 $724,276 $19,400 $40,600 $4,201,056 $3,162,946 **Bag Leak Detection System**  **Controls Subtotals Total MACT Floor Control,**  **Monitoring, Reporting, and Recordkeeping Cost**  **Testing, Monitoring, and Recordkeeping Subtotals** LADeltech HB-507 Energy recovery unit - Liquid/Gas 2160 50
LADeltech HB-512 Energy recovery unit - Liquid/Gas 2160 194 MDSeverstalSparrows 1BLR Energy recovery unit - Liquid/Gas 6900 650
MEPioneerPlastics Boiler #5/Thermal Oxidizer Energy recovery unit - Liquid/Gas 6250 39.5
WAEmeraldKalama U-2 Energy recovery unit - Liquid/Gas 8688 53
WAEmeraldKalama U-7 Energy recovery unit - Liquid/Gas 8688 53 **Facility ID**  **UnitID Subcategory**  **Operating Hours (hr/y** **r) Design** 

**Capacity**million Btu/hr 5.467936508 8848.235555 8848.235555 13103.11044 400

million Btu/hr 5.467936508 6.216666667 34331.15395 36265.88325 50840.06853 400
million Btu/hr 5.467936508 109543.8653 109543.8653 140463.8268 350
million Btu/hr 4.691666667 17.25333333 28920.08333 7587.18733 44243.41495 350
million Btu/hr 6.1 12.1 12075 7644.604317 17298.00345 400
million Btu/hr 5.612142857 10.36785714 10927.85714 8280.126083 17092.45205 400 **Stack Gas Flow Rate (dscfm)**  **dscfm @ 7% O2 Stack Gas Flow**  **Rate (acfm) Stack Gas Temp**  **(°F) Design**  **Capacity**

**Units Av** **erage Moisture (%)**  **Av erage O2 (%)** **PM Filt HCl**  gr/dscf ppmvd

0.56 0.060942787 4.439581776
0.56 0.060942787 4.439581776
1 0.060942787 4.439581776
0.76 0.111885782 4.439581776
0.56 0.009999792 4.439581776
0.56 0.009999792 4.439581776 **Fraction PM that is PM 2.5** 

### MACT

Floor Em ission lim it (mg/dscm ) MACT Floor Em ission limit (gr/dscf) Meets limit? Facility Name 9.20 0.00 

### No LADeltech 9.20 0.00 

### No LADeltech 9.20 0.00 

### No MDSeverstalSparrows 9.20 0.00 

### No MEPioneerPlastics 9.20 0.00 

### No WAEmeraldKalama 9.20 0.00 

### No WAEmeraldKalama

### Combustor ID Design Capacity (mmbtu/hr) Annual

operating hours, hr/yr (H) Exhaust gas flow rate,

dscfm (Q) HB-507 50 2160 8848.235555 HB-512 194 2160 34331.15395 1BLR 650 6900 109543.8653 Boiler #5/Thermal Oxidizer 39.5 6250 28920.08333 U-2 53 8688 12075 U-7 53 8688 10927.85714 

### Input Parameters

### Actual gas flow into fabric

filter, acfm (AQ) PM concentration, gr/dscf (PM) a.

lb/m in b. scfm Operating

labor rate, $/hr (LR) Electricity

cost, $/kW h (EC) Compress

ed air cost, $/1,000 ft3 (CAC) Dust

disposal cost, $/ton (DDC) 13103.11044 0.060942787 

### 47.32082 1012.14 51.26 0.069981 0.31 42.14111 50840.06853 0.060942787 

### 183.6048 3927.103 51.26 0.069981 0.31 42.14111 140463.8268 0.060942787 

### 585.8463 12530.6 51.26 0.069981 0.31 42.14111 44243.41495 0.111885782 

### 154.6661 3308.136 51.26 0.069981 0.31 42.14111 17298.00345 0.009999792 

### 64.57773 1381.246 51.26 0.069981 0.31 42.14111 17092.45205 0.009999792 

### 58.44275 1250.025 51.26 0.069981 0.31 42.14111 Water vapor in gas from incinerator (7.1% by weight)

### a. Bag

CRF, 2-yr life, 7% interest b.

Cage CRF, 4-yr life, 7% interest c.

Equipm en t CRF, 20- yr life, 7% interest a. 2008 b. 1989 **TCI $**  $/dscfm Electricity Operating labor 0.553092 0.295228 0.094393 575.4 357.5 $1,658,936.16 187.4877934 7544.782 13840.47 0.553092 0.295228 0.094393 575.4 357.5 $4,435,286.78 129.1913108 28234.52 13840.47 0.553092 0.295228 0.094393 575.4 357.5 $13,170,514.33 120.2305058 285264.4 44212.61 0.553092 0.295228 0.094393 575.4 357.5 $3,843,693.85 132.9074264 68985.05 40047.66 0.553092 0.295228 0.094393 575.4 357.5 $2,006,521.90 166.1715859 40884.33 55669.45 0.553092 0.295228 0.094393 575.4 357.5 $1,884,734.22 172.4706128 37138.14 55669.45 Cost Index Capital recovery

factors Total Capital Investment

### Supervisory

labor Maintenance

labor Maintenance

materials Compressed

air Dust

disposal a. Bag

cost b. Bag replaceme nt labor cost c. Bag replaceme nt cost 2076.0705 7612.2585 33178.72319 1055.87363 210.3594 18324.54 1599.235 11019.68 2076.0705 7612.2585 88705.73559 4096.78969 816.1944 71099.21 6205.03 42756.34 6631.89188 24316.93688 263410.2867 36157.4153 8319.335 196436.9 17143.61 118129.6 6007.14844 22026.21094 76873.87696 10316.0265 3652.444 61873.87 5399.909 37208.58 8350.4169 30618.1953 40130.43799 5606.60013 189.4642 24191.05 2111.221 14547.57 8350.4169 30618.1953 37694.68436 5539.97715 171.4648 23903.58 2086.134 14374.7 Direct Annual Operating Costs, $/yr

Bag replacement

### a.

Number of bags b.

Cage replaceme nt labor cost c.

Cage replaceme nt cost Overhead Property taxes, insurance, and adm inistra tion Capital

recovery **TA C** 

**$/yr** ($/yr) /

dscfm **Number of**

**Ductlines** 

### 207.9859 1599.235 1348.746 34024.51 66357.45 155424.3 337,822 38.17957 1 

### 806.9852 6205.03 5233.136 67340.72 177411.5 414129.8 852,254 24.82449 1 

### 2229.585 17143.61 14458.4 203143 526820.6 1230688 2,761,553 25.20956 1 

### 702.2764 5399.909 4554.12 86972.94 153747.8 358875.4 869,267 30.05756 1 

### 274.5715 2111.221 1780.54 80861.1 80260.88 187860.2 546,759 45.28026 1 

### 271.3088 2086.134 1759.382 79399.65 75389.37 176382.6 522,488 47.81249 1 

### Total Annual Cost Indirect Annual Costs, $/yr Cage replacement**TA C - Duct**  TCI - Duct - FRP TCI - Duct -

SS TCI - Duct -

CS Duct

Diameter CRF-DUCT elec (Mw) 

### Dust disposal cost ($/yr) 4,129 79,778 30,720 26,335 2.3574 0.09439293 1.08E+02 210 14,552 355,106 108,282 76,460 4.6436 0.09439293 4.03E+02 816 118,003 3,753,410 878,048 487,665 7.7185 0.09439293 4.08E+03 8,319 12,062 285,253 89,753 65,107 4.3318 0.09439293 9.86E+02 3,652 4,915 98,387 36,573 30,478 2.7086 0.09439293 5.84E+02 189 4,875 97,425 36,274 30,269 2.6925 0.09439293 5.31E+02 171

### Dust disposal unit cost ($/ton) Dust amount (tpy) 42 

### 4.991786 42 

### 19.36813 42 

### 197.4161 42 

### 86.67177 42 

### 4.495946 42 

### 4.068825

# Energy

**Recovery**

**Unit Selective Noncataly tic Reduction Costs** 

Facility Name Combustion Equipment Unit Heat Input Capacity (HI) Annual operating

hours (H) Exhaust gas

flow rate (Q) NOX


### MMBtu/hr hr/yr dscfm lb/MMBtu

LADeltech HB-507 50 2160 8848.235555 0.28 LADeltech HB-512 194 2160 34331.15395 0.28 MDSeverstalSparrows 1BLR 650 6900 109543.8653 0.28 MEPioneerPlastics Boiler #5/Thermal Oxidizer 39.5 6250 28920.08333 0.28 WAEmeraldKalama U-2 53 8688 12075 0.28 WAEmeraldKalama U-7 53 8688 10927.85714 0.28



### Facility/Unit ID

### Urea solution

cost (U) Electricity

cost (EC) Water

cost (WC) Capital recovery factor, 20-yr equipm ent life, 7% interest (CRF) Cost Index - 2008 Cost Index -

1998 $/gal $/kW h $/1000 gal = [i x (1 + i)a

### ] / [(1 + i)a 

### - 1], where i = interest rate, a = equipment life $0.85 $0.07 $0.20 0.09439 575.4 390.6 $0.85 $0.07 $0.20 0.09439 575.4 390.6 $0.85 $0.07 $0.20 0.09439 575.4 390.6 $0.85 $0.07 $0.20 0.09439 575.4 390.6 $0.85 $0.07 $0.20 0.09439 575.4 390.6 $0.85 $0.07 $0.20 0.09439 575.4 390.6



### Parameters

### Total Direct Capital Cost (DC) Indirect Installation Costs (IC) Other Capital

Costs (OC) $ $ $ = [$950/(MMBtu/hr)] x (HI) x [2,375 MMBtu/hr / HI] 0.577

### x (0.66 + 0.85 x 45% NOX



### removal efficiency) x (1.2 retrofit factor) x (575.4/390.6) = 0.2 x DC = [0.173 x (DC + IC)] + (119.3 gal x U) $812,158 $162,432 $168,705 $1,441,175 $288,235 $299,289 $2,403,470 $480,694 $499,062 $735,084 $147,017 $152,705 $832,425 $166,485 $172,913 $832,425 $166,485 $172,913 

### Total Capital Investment (TCI)

### Total Capital

Investment Total Capital

Investment/dscfm Maintenance Reagent Electricity
$ $/dscfm $/yr $/yr $/yr

= DC + IC + OC = $ / Q = 0.015 x TCI = (0.36 gal/hr) x H x U = kW[0.47 x NOX 

### x HI / 106

### ] / 9.5 x H x EC $1,143,296 $129.21 $17,149 $661 $100 $2,028,699 $59.09 $30,430 $661 $388 $3,383,226 $30.88 $50,748 $2,111 $4,150 $1,034,806 $35.78 $15,522 $1,913 $228 $1,171,823 $97.05 $17,577 $2,659 $426 $1,171,823 $107.23 $17,577 $2,659 $426 

### Direct A**nnual Costs**

### Indirect Capital Costs

Water Capital recovery $/yr $/yr $/yr ($/yr) / dscfm = (1.62 gal/hr) x H x WC = CRF x TCI = Direct Annual Costs + Indirect Annual Costs = ($/yr) / Q
$700 $107,919 $126,529 $14.30 $700 $191,495 $223,674 $6.52 $2,236 $319,353 $378,598 $3.46 $2,025 $97,678 $117,366 $4.06 $2,815 $110,612 $134,089 $11.10 $2,815 $110,612 $134,089 $12.27 

### Total A**nnual Costs**
Total cost

### Elec Water

Mw gal/yr

1.50E+00 3,499,200.00 

### Sources: 5.80E+00 3,499,200.00 

### 1. Cost equations, urea solution cost: OAQPS Control Cost Manual. Section 4.2: NO
6.21E+01 11,178,000.00 

### 2. Hospital/Medical/Infectious Waste Incinerators (HMIW I) [EPA-HQ-OAR-2006-0534] Heating value: Process Description Report (II-A-110). 3.42E+00 10,125,000.00 

### 3. Electricity cost: Energy

Information Administration. Average Industrial Retail Price of Electricity: October 2009. 6.38E+00 14,074,560.00 

### 4. Water cost: Air Compliance Advisor, version 7.5. 6.38E+00 14,074,560.00 

### 5. NOX 

### removal efficiency: Clean Air Technology Center. EPA Technical Bulletin: Nitrogen Oxides (NO 8.56E+01 5.65E+07

### 1. Cost equations, urea solution cost: OAQPS Control Cost Manual. Section 4.2: NOX 

### Post-Combustion, Chapter 1: Selective Noncataly tic Reduction. 2. Hospital/Medical/Infectious Waste Incinerators (HMIW I) [EPA-HQ-OAR-2006-0534] Heating value: Process Description Report (II-A-110). 3. Electricity

cost: Energy

Information Administration. Average Industrial Retail Price of Electricity: October 2009. 4. Water cost: Air Compliance Advisor, version 7.5. removal efficiency: Clean Air Technology Center. EPA Technical Bulletin: Nitrogen Oxides (NOX

### )--W hy and How They

Are Controlled. 456/F-99-006R.

### Post-Combustion, Chapter 1: Selective Noncataly

tic Reduction. 2. Hospital/Medical/Infectious Waste Incinerators (HMIW I) [EPA-HQ-OAR-2006-0534] Heating value: Process Description Report (II-A-110).

)--W hy and How They

Are Controlled. 456/F-99-006R.

## Monitoring Costs

**Parameters/Costs Equation**  **FF WS**  **SNCR Bag leak**  **detector CO** 

**CEMS HCl** 

**CEMS PM CEMS**  **Hg CEMS**  **Multi**

**metal CEMS**  **Dioxin or Hg**

**sorbent trap biweekly**  **monitoring**
A. Parameters 1. Recording lime/carbonflow, min/4-hr period 2. Annual operating hours, hr/yr (H) 3. Cost index a. 2008 575.4 575.4 575.4 575.4 575.4 575.4 575.4 575.4 575.4 575.4 b. 2006 499.6 499.6 499.6 499.6 499.6 499.6 499.6 499.6 499.6 499.6 c. 1997 386.5 386.5 386.5 386.5 386.5 386.5 386.5 386.5 386.5 386.5 d. 1993 359.2 359.2 359.2 359.2 359.2 359.2 359.2 359.2 359.2 359.2 e. 1992 358.2 358.2 358.2 358.2 358.2 358.2 358.2 358.2 358.2 358.2 4. Operating labor wage rate, $/hr (LR) $34.60 $34.60 $34.60 $34.60 $34.60 $34.60 $34.60 $34.60 $34.60 $34.60 5. Capital recovery factor, 20-yr equipment life, 7% interest (CRF) = [i x (1 + i)a] / [(1 + i)a - 1], where i = interest rate, a = equipment life 0.09439 0.09439 0.09439 0.09439 0.09439 0.09439 0.09439 0.09439 0.09439 0.09439
B. Total Capital Investment, $ (TCI) 1. Planning $700 $700 $700 $800 $4,000 $3,300 $900 $3,300 2. Select type of equipment $400 $400 $400 $4,500 $10,000 $16,100 $12,200 $16,100 3. Provide support facilities $1,500 $1,500 $1,500 $500 $20,600 $20,600 $500 $20,600 4. Purchased equipment cost (PEC) $13,000 $19,300 $5,300 $14,100 $48,400 $51,900 $73,500 $109,900 5. Install and check equipment $1,000 $1,000 $1,000 $4,800 $18,200 $19,300 $19,500 $21,500 6. Perf. spec. tests (certif.) $700 $700 $700 $0 $15,700 $12,800 $35,500 $42,300 7. Prepare QA/QC plan $700 $700 $700 $800 $17,500 $17,500 $15,400 $17,500 8. Total capital cost = Planning + selecting equipment + support facilities + PEC + installation + perf. spec. tests + QA/QC plan $18,000 $24,300 $10,300 $25,500 $134,000 $142,000 $158,000 $231,000 $230,000 $115,000

C. Annual Costs, $/yr 1. Operating labor = (5 min to record lime/carbon flow/4-hr period) x (1 hr/60 min) x H x LR 2. Maintenance materials = 0.02 x TCI $400 $500 $200 3. Operation & maintenance = Day-to-day activities + annual RATA + CGA + annual QA + O&M review and update $6,000 $27,600 $24,600 $27,300 $78,100

4. Recordkeeping and reporting = $1,000 x (525.4/386.5) $1,500 $1,500 $1,500 $200 $1,200 $1,600 $6,300 $1,600 5. Overhead = 0.6 x (labor + maintenance materials) $200 $300 $100 6. Property taxes, insurance, and administration = 0.04 x TCI $700 $1,000 $400 7. Capital recovery = CRF x TCI $1,700 $2,300 $1,000 $3,500 $12,600 $20,200 $22,500 $32,900 8. Total annual cost = Operating labor + maintenance materials + recordkeeping and reporting + overhead + property taxes, insurance, and administration + capital recovery $4,500 $5,600 $3,200 $9,700 $41,400 $46,400 $56,100 $112,600 $63,300 $41,500 **Al l model sizes** Notes: 1. Monitoring costs have been rounded to the nearest $100 to be consistent with level of rounding in original costs. 2. Costs to be replaced include: (a) bag leak detector replacing opacity test; (b) CO CEMS replacing CO test and secondary chamber temperature monitor; (c) HCl CEMS replacing HCl test, HCl sorbent monitor (dry scrubbers) and scrubber liquor pH monitor (wet scrubbers); (d) PM CEMS replacing PM and opacity tests and and pressure drop monitor (wet scrubbers); (e) multi-metal/Hg CEMS replacing flue gas temperature monitor (wet scrubbers); (f) dioxin sorbent trap biweekly monitoring replacing fabric filter inlet temperature monitor; and (g) Hg sorbent trap biweekly monitoring replacing flue gas temperature monitor (wet scrubbers).
Sources: 1. Hospital/Medical/Infectious Waste Incinerators (HMIW I) [EPA-HQ-OAR-2006-0534] Testing and Monitoring Options and Costs Memo (IV-B-66). 2. E-mail and attachment from Peter Westlin, EPA, to Mary Johnson, EPA. August 19, 2008. Monitoring Options for SNCR on Medical Waste Incinerators. 3. E-mail from Dan Bivins, EPA, to Mary Johnson, EPA. September 27, 2006. Cost of CO CEMS. 4. E-mail from Dan Bivins, EPA, to Mary Johnson, EPA. July 28, 2006. Some Preliminary Thoughts on the HW I Monitoring.

## Monitoring Costs

**Parameters/Costs**
A. Parameters 1. Recording lime/carbonflow, min/4-hr period 2. Annual operating hours, hr/yr (H) 3. Cost index a. 2008 b. 2006 c. 1997 d. 1993 e. 1992 4. Operating labor wage rate, $/hr (LR) 5. Capital recovery factor, 20-yr equipment life, 7% interest (CRF) B. Total Capital Investment, $ (TCI) 1. Planning 2. Select type of equipment 3. Provide support facilities 4. Purchased equipment cost (PEC) 5. Install and check equipment 6. Perf. spec. tests (certif.) 7. Prepare QA/QC plan 8. Total capital cost

C. Annual Costs, $/yr 1. Operating labor
2. Maintenance materials 3. Operation & maintenance

4. Recordkeeping and reporting 5. Overhead 6. Property taxes, insurance, and administration 7. Capital recovery 8. Total annual cost **AC I**  LADeltechLADeltech MDSeverstalSparrows MEPioneerPlastics

WAEmeraldKalama

WAEeraldKalama HB-507 HB-512 1BLR Boiler #5/Thermal Oxidizer U-2 U-7 5 5 5 5 5 5 2,160 2,160 6,900 6,250 8,688 8,688
575.4 575.4 575.4 575.4 575.4 575.4 499.6 499.6 499.6 499.6 499.6 499.6 386.5 386.5 386.5 386.5 386.5 386.5 359.2 359.2 359.2 359.2 359.2 359.2 358.2 358.2 358.2 358.2 358.2 358.2 $34.60 $34.60 $34.60 $34.60 $34.60 $34.60 0.09439 0.09439 0.09439 0.09439 0.09439 0.09439

$1,600 $1,600 $5,000 $4,500 $6,300 $6,300

$1,000 $1,000 $3,000 $2,700 $3,800 $3,800

$2,600 $2,600 $8,000 $7,200 $10,100 $10,100Notes: 1. Monitoring costs have been rounded to the nearest $100 to be consistent with level of rounding in original costs. 2. Costs to be replaced include: (a) bag leak detector replacing opacity test; (b) CO CEMS replacing CO test and secondary chamber temperature monitor; (c) HCl CEMS replacing HCl test, HCl sorbent monitor (dry scrubbers) and scrubber liquor pH monitor (wet scrubbers); (d) PM CEMS replacing PM and opacity tests and and pressure drop monitor (wet scrubbers); (e) multi-metal/Hg CEMS replacing flue gas temperature monitor (wet scrubbers); (f) dioxin sorbent trap biweekly monitoring replacing fabric filter inlet temperature monitor; and (g) Hg sorbent trap biweekly monitoring replacing flue gas temperature monitor (wet scrubbers).
Sources: 1. Hospital/Medical/Infectious Waste Incinerators (HMIW I) [EPA-HQ-OAR-2006-0534] Testing and Monitoring Options and Costs Memo (IV-B-66). 2. E-mail and attachment from Peter Westlin, EPA, to Mary Johnson, EPA. August 19, 2008. Monitoring Options for SNCR on Medical Waste Incinerators. 3. E-mail from Dan Bivins, EPA, to Mary Johnson, EPA. September 27, 2006. Cost of CO CEMS. 4. E-mail from Dan Bivins, EPA, to Mary Johnson, EPA. July 28, 2006. Some Preliminary Thoughts on the HW I Monitoring.

# Ac**tivated Carbon Injection Model Costs**

Unit-specific field Unit-specific field Unit-specific field

Facility name Combustion equipment Annual operating hours (H) hr/yr

LADeltech HB-507 2160 LADeltech HB-512 2160 MDSeverstalSparrows 1BLR 6900 MEPioneerPlastics Boiler #5/Thermal Oxidizer 6250 WAEmeraldKalama U-2 8688 WAEmeraldKalama U-7 8688 

### Facility/Unit ID

### Unit-specific field

Exhaust gas flow rate (Q) Operating labor

rate (LR) Activated carbon

cost (ACC) Dust disposal cost (DDC) dscfm $/hr $/lb $/ton

8848.235555 

### $34.60 $1.38 $42.29 34331.15395 

### $34.60 $1.38 $43.29 109543.8653 

### $34.60 $1.38 $47.29 28917.33333 

### $34.60 $1.38 $51.29 11680.95238 

### $34.60 $1.38 $66.29 11542.14815 

### $34.60 $1.38 $67.29

### Unit-specific field

Capital recovery

factor, 20-yr equipm ent life, 7% interest (CRF) Cost Index 2008 Cost Index

1990 ACI Adjustment

Factor (AF)
= [i x (1 + i)a

### ] / [(1 + i)a 

### - 1], where i = interest rate, a = equipment life 0.09439 575.4 361.3 0.83 

### 0.09439 575.4 361.3 0.83 

### 0.09439 575.4 361.3 0.83 

### 0.09439 575.4 361.3 0.83 

### 0.09439 575.4 361.3 0.83 

### 0.09439 575.4 361.3 0.83

### Total Unit cost Operating labor Supervisory labor Maintenance $ $/dscfm $/yr $/yr $/yr = 4,500 x (Q/1,976)0.6

### x (1.2 retrofit factor) x (575.4/361.3) = $ / Q = (0.25 hr/8-hr shift) x H x LR = 0.15 x

(operating labor) = 0.2 x TCI $21,142 $2.39 $2,336 $350 $4,228 $47,691 $1.39 $2,336 $350 $9,538 $95,670 $0.87 $7,461 $1,119 $19,134 $43,025 $1.49 $6,758 $1,014 $8,605 $24,975 $2.14 $9,394 $1,409 $4,995 $24,797 $2.15 $9,394 $1,409 $4,959 **Capital Investment Direct A** **nnual Costs**

### Activated carbon Dust disposal Overhead Property taxes, insurance, and adm inistration $/yr $/yr $/yr $/yr = 0.00127 x Q x H x ACC x AF = 0.00127 x Q x (1 ton/2,000 lb) x H x DDC x AF = 0.6 x (labor + maintenance materials) = 0.04 x TCI $27,768 $425 $4,148 $846 $107,741 $1,690 $7,334 $1,908 $1,098,182 $18,816 $16,628 $3,827 $262,588 $4,880 $9,826 $1,721 $147,447 $3,541 $9,479 $999 $145,695 $3,552 $9,457 $992 **Indirect A nnual Costs**  **Direct A nnual Costs** 

### Capital recovery $/yr $/yr ($/yr) / dscfm Elec Water ACI
= CRF x TCI = Direct Annual Costs +

Indirect Annual Costs = ($/yr) / Q lb/yr $1,996 $42,098 $4.76 20,122 $4,502 $135,398 $3.94 78,073 $9,031 $1,174,198 $10.72 795,784 $4,061 $299,453 $10.36 190,281 $2,357 $179,622 $15.38 106,846 $2,341 $177,799 $15.40 105,576 1,296,682 Total cost **Total A nnual Cost** 

### Dust

ton/yr 10.06 3. Activated carbon cost: The Innovation Group. Chemical Profiles: Carbon, Activated. 2002. Assumed 20% price increase based on online 39.04 information from Norit, an activated carbon vendor. 397.89 95.14 53.42 52.79

### 3. Activated carbon cost: The Innovation Group. Chemical Profiles: Carbon, Activated. 2002. Assumed 20% price increase based on online

### FACName Unit ID Exhaust gas flow (acfm) Temperat

ure (F) Actual

Exhaust Flow rate (scfm) Unit Input

Flow (scfm) Equipm en

t Cost ($) Additional

Purchase Equipm ent Cost(Instruments, taxes, freight) LADeltech HB-507 13103.1104 400 

### 8044.7 8446.935 151379.4 52982.78389 LADeltech HB-512 50840.0685 400 

### 31213.44 32774.11 317845.9 111246.0529 MDSeverstalSparrow s 1BLR 140463.827 350 

### 91561.61 96139.69 572684.8 200439.6905

MEPioneerPlastics Boiler

#5/Thermal Oxidizer 44243.415 350 

### 28840.15 30282.16 304387.6 106535.6547 WAEmeraldKalama U-2 17298.0034 400 

### 10620.17 11151.18 176221.5 61677.51095 WAEmeraldKalama U-7 17092.4521 400 

### 10493.97 11018.67 175072.7 61275.45005

### Direct Installation

Costs Indirect

Installation Costs TCI $ $/scfm a. Catalyst CRF, 2-yr life, 7% interest c.

Equipm en t CRF, 20- yr life, 7% interest Power of fan 57630.13094 44959.67662 $452,176.56 $56.21 0.553092 0.094393 9.8829144 121003.921 94400.22206 $949,418.93 $30.42 0.553092 0.094393 38.3457079 218021.1148 170087.3945 $1,710,633.60 $18.68 0.553092 0.094393 112.4834325

115880.3535 90403.11267 $909,218.48 $31.53 0.553092 0.094393 35.4301267 67087.50976 52337.77357 $526,380.89 $49.56 0.553092 0.094393 13.0468783 66650.18238 51996.59618 $522,949.54 $49.83 0.553092 0.094393 12.8918428

### Electricity

Cost $/yr Operating

Labor $/yr Superviso

ry Labor Maintenan

ce labor Maintenan

ce Materials Catalyst

replacement Volum e Catalyst

Replacem ent Cost Capital

Recovery Overhead 5809.583 18165 2724.75 18165 18165 42.2 22407.7 40397.94 51262.19 22541.18 18165 2724.75 18165 18165 163.9 86941.7 80755.22 100021.6 66122.38 18165 2724.75 18165 18165 480.7 255035.1 135472.3 227026.3

20827.28 18165 2724.75 18165 18165 151.4 80331.2 77634.48 95026.92 7669.491 18165 2724.75 18165 18165 55.8 29581.3 46670.98 56682.35 7578.355 18165 2724.75 18165 18165 55.1 29229.8 46382.92 56416.76

### Adm in/Prope

rty Taxes/Insura nce Total Annual

costs $/yr $/scfm $18,087.06 $195,184 24.26 $37,976.76 $385,456 12.35 $68,425.34 $809,301 8.84
$36,368.74 $367,408 12.74 $21,055.24 $218,879 20.61 $20,917.98 $217,746 20.75

# Energy

**Recovery**

**Unit Incremental Control Model Costs**

Facility name Combustion

equipm ent Annual

operating hours (H) Exhaust gas

flow rate to FF (Qff) Exhaust gas

flow rate (Q) Unc. HCl

concentration (HClu)* hr/yr acfm dscfm ppmvd

Used for bag replacement only
LADeltech HB-507 2160 13103.11044 8848.235555 11.03226245 LADeltech HB-512 2160 50840.06853 34331.15395 11.03226245 MDSeverstalSparro ws 1BLR 6900 140463.8268 109543.8653 11.03226245
MEPioneerPlastics Boiler #5/Thermal

Oxidizer 6250 44243.41495 28920.08333 11.03226245
WAEmeraldKalama U-2 8688 17298.00345 12075 11.03226245
WAEmeraldKalama U-7 8688 17092.45205 10927.85714 11.03226245



### Facility/Unit ID

### Cont. HCl

concentration (HClc)** Operating

labor rate (LR) Wastewater (blowdown) flow (B) Caustic

cost (CC) Sewage

disposal cost (SDC) Water cost

(WC) Lim e cost

(LC) Sodium bicarbonate cost (SBC) ppmvd $/hr gpm $/ton $/1,000 gal $/1,000 gal $/ton $/ton

0.5 $34.60 0.018 $357 $3.80 $0.20 $95 $440 

### 0.5 $34.60 0.069 $357 $3.80 $0.20 $95 $440 

### 0.5 $34.60 0.219 $357 $3.80 $0.20 $95 $440 

### 0.5 $34.60 0.058 $357 $3.80 $0.20 $95 $440 

### 0.5 $34.60 0.024 $357 $3.80 $0.20 $95 $440 

### 0.5 $34.60 0.022 $357 $3.80 $0.20 $95 $440

### Dust disposal

cost (DDC) Activated

carbon cost (ACC) Natural gas

cost (NGC) Electricity

cost (EC) Total bag cost
$/ton $/lb $/1,000 ft3 $/kW h Bag CRF, 2-yr life, 7% interest Cage CRF, 4-yr life, 7% interest $/yr

$42.14 $1.38 $9.58 $0.07 0.55309 0.29523 $18,325 $42.14 $1.38 $9.58 $0.07 0.55309 0.29523 $71,099 $42.14 $1.38 $9.58 $0.07 0.55309 0.29523 $196,437 $42.14 $1.38 $9.58 $0.07 0.55309 0.29523 $61,874 $42.14 $1.38 $9.58 $0.07 0.55309 0.29523 $24,191 $42.14 $1.38 $9.58 $0.07 0.55309 0.29523 $23,904 

### = [i x (1 + i)a

### ] / [(1 + i)a 

### - 1], where i = interest rate, a = equipment life Capital recovery

factors

### Bag replacement

labor cost Total cage

cost Cage replacement labor cost Urea solution

cost (U) Caustic Sewage disposal Makeup

water $/yr $/yr $/yr $/gal = HCl x (3.117E

9) x Q x H x CC = B x (60

mi n/hr) x H x SDC = B x (60

mi n/hr) x H x WC $1,079 $1,195 $1,079 $0.85 $11 $9 $0 $4,188 $4,638 $4,188 $0.85 $41 $34 $2 $11,572 $12,813 $11,572 $0.85 $420 $345 $18 $3,645 $4,036 $3,645 $0.85 $100 $83 $4 $1,425 $1,578 $1,425 $0.85 $58 $48 $3 $1,408 $1,559 $1,408 $0.85 $53 $43 $2 

### Increase Caustic Flow

### Makeup lime Dust disposal

$/yr ($/yr) / dscfm $/yr = Caustic + Sewage disposal + Makeup water = ($/yr) / Q = (2.4E-7 lb/dscf) x HCl x Q x (1 ton/2000 lb) x (60 mi n/hr) x H x LC = HCl x Q x (60 min/hr) x (2.86E-7 lb/dscf) x (1 ton/2,000 lb) x H x DDC = Makeup lime + Dust disposal
$20 $0.00 $144 $76 $220 $77 $0.002 $560 $296 $855 $783 $0.007 $5,704 $3,015 $8,719 $187 $0.006 $1,364 $721 $2,085 $109 $0.01 $792 $418 $1,210 $98 $0.009 $716 $379 $1,095 

### Total cost **Increase Lime Flow**
Total cost Increase Caustic Flow

### Makeup NaHCO3 

### Dust disposal

($/yr) / dscfm $/yr
= ($/yr) / Q = (2.73E-7 lb/dscf x HCl x Q) x

(1 ton/2000 lb) x (60 min/hr) x H

x SBC = [(HCl x Q x 60 min/hr x 2.10E-7

lb/dscf)] x (1 ton/2,000 lb) x H x

DDC = Makeup NaHCO3 + Dust disposal
$0.02 $760 $56 $816 $0.02 $2,948 $217 $3,165 $0.08 $30,050 $2,214 $32,263 $0.07 $7,186 $529 $7,715 $0.10 $4,171 $307 $4,478 $0.10 $3,774 $278 $4,053 

### Total cost **Increase NaHCO3 Flow**
Total Cost

### Activated carbon Dust disposal

($/yr) / dscfm $/yr ($/yr) / dscfm = ($/yr) / Q = (1.27E-3) x Q x

H x ACC = (1.27E-3) x Q x (1

ton/2,000 lb) x H x DDC = Activated carbon + Dust disposal = ($/yr) /

Q
$0.09 $33,496 $511 $34,007 $3.84 $0.09 $129,965 $1,984 $131,949 $3.84 $0.29 $1,324,707 $20,226 $1,344,933 $12.28 $0.27 $316,783 $4,837 $321,620 $11.12 $0.37 $183,861 $2,807 $186,668 $15.46 $0.37 $166,394 $2,541 $168,935 $15.46 

### Total cost **Increase Carbon Flow**
Total Cost

### Fan electricity $/yr ($/yr) / dscfm = (0.32 Btu/lb/°F) x (28.5 lb/lbmole) x (100° F) x (lbmole/385 ft3

### ) x (ft3

### /1,000 Btu) x (Q/0.9) x (60 min/hr) x H x NGC = ($/yr) / Q = 0.746 x (0.0205 x Q) x H x EC
$28,915 $3.27 $19,524 $112,189 $3.27 $75,755 $1,143,525 $10.44 $772,158 $273,456 $9.46 $184,650 $158,714 $13.14 $107,171 $143,636 $13.14 $96,989 

### Natural gas **Increase Natural Gas**

### Pum p electricity Bag replacement $/yr ($/yr) /

dscfm =0.746 x (0.00267 x Q + 4.554) x H x EC = Fan electricity + pum p electricity = ($/yr) / Q = Bag CRF x [(total bag cost) + (bag

replacement labor cost)]
$3,033 $22,558 $2.55 $10,732 $10,357 $86,112 $2.51 $41,641 $102,135 $874,293 $7.98 $115,048 $25,468 $210,118 $7.27 $36,238 $15,930 $123,101 $10.19 $14,168 $14,604 $111,593 $10.21 $14,000 

### Increase Scrubber Horsepower
Total cost

### Cage replacement $/yr ($/yr) / dscfm $/yr ($/yr)/dscfm

= Cage CRF x [(total cage cost) + (cage replacement labor cost)] = Bag replacement + Cage replacement = ($/yr) / Q = (0.36 gal/hr) x H x U = ($/yr) / Q

$672 $11,404 $1.29 $661 $0.07 $2,606 $44,247 $1.29 $661 $0.02 $7,199 $122,247 $1.12 $2,111 $0.02 $2,268 $38,505 $1.33 $1,913 $0.07 $887 $15,055 $1.25 $2,659 $0.22 $876 $14,876 $1.36 $2,659 $0.24 

### Increase NOX Reagent Reagent **Improve FF Performance**
Total cost

### Secondary IMPACTS

6. Electricity

cost: Energy

Information Administration. Average Industrial Retail Price of Electricity: October 2009. 7. Water cost, sewage disposal cost: Air Compliance Advisor, version 7.5. * Actual HCl concentration in this row

### 6. Electricity cost: Energy

Information Administration. Average Industrial Retail Price of Electricity: October 2009.

# Maintenance and Inspection Costs **Parameters/Costs Equation**  **Values**
A. Parameters 1. Cost index a. 2008 575.4 d. 1992 358.2 B. Maintenance/Inspection Cost, $/yr (rounded) 1. Company

A = $500 x (575.4/358.2) $800 2. Company

B = $350 x (575.4/358.2) $600 3. Company

C = $800 x (575.4/358.2) $1,300 4. Company

D = $750 x (575.4/358.2) $1,200 5. Average = ∑(Companies A-D) / 4 $1,000
Note: Maintenance/inspection costs have been rounded to the nearest $100 to be consistent with level of rounding in original costs.
Source: Hospital/Medical/Infectious Waste Incinerators (HMIW I) [EPA-HQ-OAR-2006-0534] Maintenance/Inspection Programs Memorandum (II-B-88).

# Stack Testing Costs **Parameters/Costs Equation**  **Values**
A. Parameters 1. Cost index a. 2008 575.4 d. 1992 358.2 B. Testing Costs, $ **An nual PM, HCl, opacity;**  1. Method 5 (PM) = $8,000 x (575.4/358.2) $12,000 **An nual everything except CO:**  2. Method 9 (opacity) = $1,000 x (575.4/358.2) + $1,500 $2,500 **An nual PM, HCl, CO, Nox, SO2, opacity:**  3. Method 10 (CO) = $4,000 x (575.4/358.2) + $1,000 $7,000 4. Method 26 (HCl) = $5,000 x (575.4/358.2) $7,000 **An nual everything:**  5. Method 29 (metals) = $8,000 x (575.4/358.2) + $2,000 $14,000 6. Method 23 (CDD/CDF) = $21,000 x (575.4/358.2) - $5,000 $26,000 7. Method 7E (NOX

### ) = $5,000 x (575.4/358.2) $7,000 8. Method 6C (SO2

### ) = $5,000 x (575.4/358.2) $7,000
Note: 1. Initial testing costs to be annualized over 15 years at 7% interest. 2. Testing costs have been rounded to the nearest $1,000 (except for opacity) to be consistent with level of rounding in original costs; costs also adjusted based on additional information from EPA. 3. Multiple test costs adjusted by 2/3 in nationwide cost estimates to account for travel, accommodations, methods/sampling trains, etc. common to the tests.
Sources: 1. Memorandum from R. Segall, EPA/EMB, to R. Copland, EPA/SDB. October 14, 1992. Medical Waste Incinerator Study: Emission Measurement and Continuous Monitoring. (II-B-89) 2. E-mail from Jason Dewees, EPA, to Peter Westlin, EPA. August 20, 2008. Monitoring Options for SNCR & Test Cost Questions. 3. E-mail from Jason Dewees, EPA, to Mary Johnson, EPA. August 20, 2008. Re: Monitoring Options for SNCR & Test Cost Questions.

**CRF (15 yr, 7%): 0.109795** 

### Initial Test annualized (TAC)

**$14,333 $50,333**  **$28,333 $55,000**  $6,039

# Visible Emissions Testing Costs **Parameters/Costs Equation**  **Values**
A. Parameters 1. Operating labor rate, $/hr (LR) $34.60 2. Capital recovery

factor, 5-yr equipment life, 7% interest (CRF) = [i x (1 + i)a

### ] / [(1 + i)a 

### - 1], where i = interest rate, a = equipment life 0.24389
B. Total Capital Investment, $ (TCI) = Com bination light m eter/anemometer ($200) + digital stopwatches (2 each at $25) $250
C. Direct Annual Costs, $/yr 1. Operating labor = (1 hr/reading) x (3 readings/test) x (1 test/yr) x LR $104 D. Indirect Annual Costs, $/yr 1. Overhead = 0.6 x (operating labor) $62 2. Property

taxes, insurance, and adm inistration = 0.04 x TCI $10 3. Capital recovery = CRF x TCI $61 E. Total Annual Cost, $/yr (rounded) = Direct Annual Costs + Indirect Annual Costs $200
Sources: 1. Professional Equipment. 2008. Light Meters Industrial and Professional: Digital Light Meter. Website: http://www.professionalequipment.com. Accessed July

24, 2008. 2. Cole-Parmer. 2008. Digital Stopwatches -Cole Parmer Instrument Catalog. Website: http://www.coleparm er.com. Accessed July 24, 2008.

# Recordkeeping and Reporting Costs **(A) (B)**  **(C) (D)**  **(E) (F)**  **(G)**

**Burden item Person**  **hours per occurrence**  **Number of**

**occurrences per year**  **Technical**

**person-hours per year (C = A**  **x B) Management** 

**person-hours per year (D = C**  **x 0.05) Clerical** 

**person-hours per year (E =**  **C x 0.1) Total person** 

**hours per year (F = C +**  **D + E) Cost, $**  A. Applications N/A B. Surveys and Studies N/A C. Reporting Requirements 1. Read instructions 1.0 1 1.0 0.05 0.1 1.2 $41 2. Required activities a. Perf. spec. tests (certif.) for CMS 17 1 17 0.9 1.7 20 $696 3. Write report a. Notification of initial performance test i. Pollutants, fugitive ash emissions 2.0 1 2.0 0.1 0.2 2.3 $82 ii. Fugitive ash emissions 1.0 1 1.0 0.05 0.1 1.2 $41 b. Notification of initial CMS demonstration 2.0 1 2.0 0.1 0.2 2.3 $82 c. Report of initial performance test i. Pollutants, fugitive ash emissions 8.0 1 8.0 0.4 0.8 9.2 $328 ii. Fugitive ash emissions 2.0 1 2.0 0.1 0.2 2.3 $82 d. Report of initial CMS demonstration Incl. in C2 e. Annual report i. Results of performance tests conducted during the year 40 1 40 2.0 4.0 46 $1,638 D. Recordkeeping Requirements 1. Read instructions Incl. in C1 2. Plan activities N/A 3. Implement activities N/A 4. Develop record system N/A 5. Time to enter information a. Records of initial performance test Incl. in C3 b. Records of annual and any subsequent compliance tests Incl. in C3
E. Total Labor Burden and Cost 73 3.7 7.3 84 $2,989
Notes: 1. Industry costs are based on the following hourly rates: technical at $34.60, management at $82.23, and clerical at $22.32 (see table below). The composite hourly labor rate is ($34.60/hr) + (0.05 x $82.23/hr) + (0.1 x $22.32/hr) = $40.94/hr. Labor rates were increased by 60% to account for overhead. 2. Person-hours per occurrence for CMS performance specification costs are based on the performance specification costs to certify CMS ($700) divided by the composite hourly labor rate ($40.94/hr). 3. Control device inspection cost already accounted for under monitoring costs. 4. Assume 8 hours for each facility to review the report of the initial performance test for pollutants and fugitive ash. 5. Assume 2 hours for each facility to review the report of the initial performance test for fugitive ash. 6. Assume 40 hours to review report of annual PM, CO, and HCl compliance reports. 7. The average recurrent burden and cost in the first 3 years after promulgation for the sources with recurrent burden are equal to the person-hours added down each column for technical, management, and clerical and the sum of the cost column.

# Recordkeeping and Reporting Costs **(A) (B)**  **(C) (D)**  **(E) (F)**  **(G)**

**Burden item Person**  **hours per occurrence**  **Number of**

**occurrences per year**  **Technical**

**person-hours per year (C = A**  **x B) Management** 

**person-hours per year (D = C**  **x 0.05) Clerical** 

**person-hours per year (E =**  **C x 0.1) Total person** 

**hours per year (F = C +**  **D + E) Cost, $** 
Sources: 1. Bureau of Labor Statistics, Occupational Employment Statistics, May 2008 National Industry-Specific Occupational Employment and W age Estimates. 2. Hospital/Medical/Infectious Waste Incinerators (HMIW I) [EPA-HQ-OAR2006-0534] Testing and Monitoring Options and Costs Memo (IV-B-66).

Labor Rates:

**Parameter Pulp, Paper**  **and Paperboard**  **Mills Pipeline** 

**Transportation Cement and** 

**Concrete Product**  **Manufacturing Pharma** 

**ceutical & Medicine** **Manufac turing**  **Total Loaded** 

1. Technical - Stationary Engineers & Boiler Operators $19.14 $21.11 $18.88 $27.36 $21.62 $34.60 2. Management - Engineering Managers $41.41 $58.22 $43.90 $62.05 $51.40 $82.23 3. Clerical - Office Clerks, General $14.21 $14.15 $12.58 $14.85 $13.95 $22.32 4. Composite labor rate $40.94

### Cost Factor (in 2008$) **Reference/Note Year of Costs** 



### Advanced Combustion Controls (Linkageless Boiler Management System) -- cost is per boiler - TCI LBMS costs are based on a 2008 quote provided to the U.S. Department of Energy. The installed cost for a LBMS on a 20 mmBtu/hr unit was are $19,127. The DOE noted that costs are relatively fixed, regardless of the size of the unit. Assumed to represent $2008, since that was the year the quote was obtained.

**Activated Carbon Injection** Received spreadsheet of HMIWI model costs from Tom Holloway of RTI International. Originally $2004 Received spreadsheet of HMIWI model costs from Tom Holloway of RTI International. Originally $2004 **Packed Scrubber**
Received spreadsheet of HMIWI model costs from Tom Holloway of RTI International. Originally $2004 **Secondary Chamber/Afterburner Retrofit**
Received spreadsheet of HMIWI model costs from Tom Holloway of RTI International. Originally $2004 **Selective Non-Catalytic Reduction** Received spreadsheet of HMIWI model costs from Tom Holloway of RTI International. Originally $2004 **Catalytic Oxidizer** Used catalytic oxidizer costing for all sizes,though some fell outside the appropriate sizerange for the equation. Originally $2004Hospital/Medical/Infectious Waste Incinerators (HMIWI). [EPAHQ-OAR-2006-0534] 19,127 $

**Fabric Filter**

Hospital/Medical/Infectious Waste Incinerators (HMIWI). [EPAHQ-OAR-2006-0534]

EPA Air Pollution Control Cost Manual, Sixth Edition EPA 452/B-02- 001Hospital/Medical/Infectious Waste Incinerators (HMIWI). [EPAHQ-OAR-2006-0534]

Hospital/Medical/Infectious Waste Incinerators (HMIWI). [EPAHQ-OAR-2006-0534]Hospital/Medical/Infectious Waste Incinerators (HMIWI). [EPAHQ-OAR-2006-0534]