### 1

**MEMORANDUM TO**  : Andrew Bouchard and Brenda Shine, EPA **FROM** : Graham Gibson, Jason Renzaglia, Mae Thomas, and Philip Crawford, ERG **DATE** : January

20, 2012 **SUBJECT** : Development of Monitoring Cost Estimates for the Proposed Part 65 Uniform

Standards for Control Devices

– Subpart M **1.0 INTRODUCTION**  This memorandum describes the methods and procedures used to estimate monitoring costs for the proposed Part 65 Uniform Standards for Control Devices (Subpart M) . The total capital investment (TCI) and total annualized costs (TAC) were estimated for continuous emissions monitoring systems (CEMS), continuous parametric monitoring systems (CPMS), and periodic monitoring required in the proposed subpart . The proposed Subpart M includes monitoring requirements for 11 specific control devices, as well as requirements for other controls not specified in the regulation, and closed vent systems . Monitoring costs were estimated for closed vent systems and 10 of the 11 specific control devices, including small boilers and process heaters, incinerators (thermal and catalytic oxidizers), absorbers (wet scrubbers), regenerative and non-regenerative carbon adsorbers, condensers, biofilters, sorbent injection, and fabric filters . The fuel gas s ystem provisions do not require monitoring; therefore, costs were not estimated for fuel gas s ystems . This memorandum is organized as follows: 1.0 Introduction 2.0 Identification of Monitoring Requirements 3.0 Estimating Monitoring Costs 4.0 References Appendix A: Summary

of Subpart M Monitoring Requirements and Costs Appendix B: Cost Algorithms for Selected Monitoring Equipment

### 2

**2.0 IDENTIFICATION OF MO**  **NITORING REQUIREMENT S**  The proposed Subpart M regulation includes monitoring requirements for 11 specific control devices, as well as requirements for other controls not specified in the regulation and closed vent s ystems . The proposed Subpart M sections for these requirements are listed in Table 1. **Table 1**  **. Monitoring Requirements in Propose**  **d Subpart M Control Device**  **Proposed Subpart M Section Reference**  Small Boilers and Process Heaters 40 CFR 65.724 Incinerators

– Thermal 40 CFR 65.726 Incinerators

– Catalytic 40 CFR 65.728 Fuel Gas Systems 40 CFR 65.732 Absorbers 40 CFR 65.740 Adsorbers

– Regenerative 40 CFR 65.742 Adsorbers

– Non-Regenerative 40 CFR 65.744 Condensers 40 CFR 65.746 Biofilters 40 CFR 65.748 Sorbent Injection 40 CFR 65.760 Fabric Filters 40 CFR 65.762 Other Control Devices 40 CFR 65.800 Closed Vent Systems 40 CFR 65.720 

### The monitoring requirements for subpart M are summarized in an Excel spreadsheet (see Appendix A) containing the control device typ e, the specific monitoring requirements, the corresponding rule reference, standardized monitoring equipment, special conditions (e.g., if intermittent, if scrubbing liquid is not a reactant, etc.), and any additional necessary notes . Fuel gas s ystems do not require monitoring and therefore, are not included in Appendix A . Other control devices are also not included in Appendix A because it is unknown what type of monitoring will be selected .

### 3

Many of the requirements in the Uniform Standards are the same or are similar to previous rules and do not represent changes that will translate into a cost increase from existing rules applicable to the chemical industry . Although the Uniform Standards are intended to reduce the overall burden for facilities, some of the proposed changes could cause an increase in costs . The proposed monitoring requirements in Subpart M that may result in a change in impacts from the ty pical monitoring requirements in past rule s include some provisions for adsorbers, biofilters, and by

passes . Appendix A identifies the se specific adsorber, biofilter, and by pass monitoring requirements in the c ost note column as a “potential change in impact” . TCIand TAC for each type of monitoring are also included in Appendix A . The methods used to estimate TCIand TAC are described in Section 3.0 of this memorandum . **3.0 ESTIMATING MONITORIN**  **G COSTS** The proposed regulation contains CEMS requirements for each control device specified in Table 1, with the exception of closed vent systems . CPMS requirements are also provided as alternatives to the CEMS requirements for each control device . Requirements for each control device were anal yz ed to identify the typ e of monitoring equipment sources may use to demonstrate compliance . Cost estimates were developed based on the list of potential equipment ty pes . Costs were also estimated for periodic monitoring and are discuss ed in detail in section 3.1.2 . Table 2 summarizes the different equipment ty pes for which cost estimates were developed . **Table 2. Standardized Monitoring Equipment Types Standardized Monitoring Equipment**  Flow Indicator

– Gas Phase Differential Pressure Flow Meter

– Gas Phase Magnetic Flow Meter

– Liquid Phase Differential Pressure Indicator

– Gas Phase Fabric Filter Bag Leak Detection System Pressure Indicator

– Gas or Liquid Phase Tem perature Indicator

– Gas or Liquid Phase

pH Indicator Relative Humidity Indicator Caustic Strength Indicator Portable Flame Ionization Detector Car- Seal Lock, Key, and Chain Organic CEMS

### 4

Cost algorithms were developed to estimate the TCI and TAC for the CEMS and CPMS requirements for each standardized monitoring equipment ty pe . Section 3.1 describes the cost parameters contained in each algorithm . **3.1 Cost Parameters**  **for CPMS** Each CPMS cost algorithm includes common parameters for TCI and TAC . The calculation for TCI consists of planning, purchased equipment costs, freight and sales tax, and equipment installation . TAC consists of operation and maintenance, monitoring, record keeping, reporting, taxes, insurance, administration costs, and annualized capital costs (i.e., capital recovery) . Each cost component and method of calculation are described below . Periodic monitoring costs are discussed in section 3.1.2 . **3.1.1 Capital**  **Cost Parameters for CPMS**  **Planning Costs**  Planning costs were estimated using standardized labor rates and hourly requirements . Labor rates were based on U.S. Department of Labor, Bureau of Labor Statistics labor rates (DOL, 2009) . A fringe benefit loading rate of 1.5 and an overhead and profit rate of 1.4 were multiplied by

each hourly

rate to obtain loaded rates . Calculated hourl y labor rates are presented in Table 3. **Table 3. Summary of 2009 Hourly Labor Rates**

**Labor Class (A)**  **Mean hourly labor rate**  **1** 

### ($/hr) **(B)**

**Fringe benefit**  **loading rate (C)** 

**Overhead and profit**  **rate (D=AxBxC)** 

**Loaded wage rate**  **($/hr)** Professional Specialty and Technical (SOC Code: 17 -2081) 39.53 1.5 1.4 83.01 Executive, Administrative and Managerial (SOC Code: 11 - 9041) 57.8 1.5 1.4 121.38 Administrative Support, Including Clerical (SOC Code: 43 - 0000) 17.31 1.5 1.4 36.35 Installation, Maintenance, and Repair (SOC Code: 49 - 0000) 22.08 1.5 1.4 46.37 Plant and System Operators, All (SOC Code: 51 - 8099) 22.72 1.5 1.4 47.71 1 - Labor rates as reported by U.S. Department of Labor, Bureau of Labor Statistics (U.S. DOL, 2010) . Labor rates for May 2009 for general manufacturing industry s ector: 2 - digit NAICS code 31 - 33 (http://stats.bls.gov/oes/oes_dl.htm accessed in December 2010 ).

### 5

Hourly requirements for planning were developed us ing estimates presented in EPA’s Air Pollution Control Cost Manual, Sixth Edition (U.S. EPA, 2002) . The total planning cost used in each CPMS cost algorithm is presented in Table 4 .

**Table 4. Summary of Planning Labor Cost Calculation for CPMS Component**  **Ca lculation Note**  **Cost ($/yr)** Engineering 36 hours 1 

### at $83.01/hr2 

### 2,988 Management 2 hours 1 

### at $121.38/hr2 

### 243 Clerical (Purchasing) 4 hours 1 

### at $36.35/hr2 

### 145 **Total Planning Labor Cost ($2010) 3,377**  1 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4 . October 2000 . EPA/452/B - 02 - 001 . Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 2 - Refer to Table 3 for labor rate information 

### Purchased Equipment Costs Purchased equipment costs were estimated b y the following methods and sources:

 For flow meters for gas and liquid phase, pressure and differential pressure indicators, and temperature indicators, ERG used instrumentation cost data presented in “Plant Design and Economics for Chemical Engineers” (Peters, Timmerhaus, and West, 2003).  For a flow indicator for gas phase, ERG assumed the cost to be one half of the purchased equipment cost of the gas phase flow meter.  For a fabric filter bag leak detection system, ERG assumed the cost was equal to the cost of the differential pressure indicators .  For a pH indicator and relative humidity indicator, ERG used online pricing information . Refer to Tables B.9, B.10, and B.12 in Appendix B for specific references to cost source material .  For a caustic strength indicator, ERG assumed the cost was equal to the cost of the pH indicator .  For a portable flame ionization detector (FID), ERG used quotes provided by vendors (supplied by

EPA) . Refer to Table B.16 in Appendix B for specific cost source material .  For a car- seal lock, key and chain, ERG e stimated the cost of a lock and chain on the by pass valve . Refer to Table B.20 in Appendix B for specific cost source material .  Table 5 summarizes the purchased equipment cost for each equipment type . Purchased equipment costs were normalized to ye ar 2010 using the Chemical

### 6 Engineering Plant Cost Index (June 2010) except for equipment types noted in Table 5 . Additional details, including references, are provided in the cost algorithms of Appendix B. **Table 5. Summary of CPMS Monitoring Purchased Equipment Costs**  **1** 

### Standardized Monitoring Equipment **Estimated Purchased Equipment Cost ($2010)**  **TCI ($2010)** Flow Indicator - Gas Phase 2 

### 1,800 6,300 Differential Pressure Flow Meter - Gas Phase 3,600 9,100 Magnetic Flow Meter - Liquid Phase 7,200 15,000 Differential Pressure Indicator - Gas Phase 2,900 7,900 Fabric Filter Bag Leak Detection System 2 

### 2,900 7,900 Pressure Indicator - Gas or Liquid Phase 1,900 6,400 Tem perature Indicator - Gas or Liquid Phase 4,100 9,900 pH Indicator3 

### 980 4,900 Relative Humidity Indicator4 

### 1,300 5,400 Caustic Strength Monitor5 

### 980 4,900 Portable Flame Ionization Detector 5,400 9,200 Car- Seal 97 150 1 - Costs have been rounded to two significant figures 2 - Purchased equipment cost (PEC) assumed to be half of differential pressure flow meter - gas phase 3 - PEC assumed to be equal to differential pressure indicator - gas phase 4 - Cost year 2011 5 - PEC assumed to be equal to pH indicator 

### Freight, Sales Tax, and Installation Freight, sales tax, and installation costs were estimated using standard percentages . Freight and sales tax were estimated at 8 percent of the purchased equipment cost (U.S. EPA, 2000) . Equipment installation was estimated at 47 percent of the purchased equipment cost, freight, and sales tax (Peters, Timmerhaus, and West, 2003) . Appendix B provides the detailed calculations using the capital cost components in this section to calculate total capital costs for each standardized monitoring equipment type . **3.1.2 Annualized**  **Cost Parameters for CPMS**  TAC estimates include operation and maintenance, monitoring, record keeping and reporting, taxes, insurance, administration, and annualized capital (i.e., capital recovery costs) .

### 7

**Operation and Maintenance Costs** Operation and maintenance costs were estimated to be 10 percent (U.S. EPA, 2000) of the sum of the purchased equipment cost and installation costs . Taxes, insurance, and administration fees were estimated at 4 percent (U.S. EPA, 2000) of TCI . **Monitoring, Record Keeping and Reporting** Continuous monitoring and associated record keeping and reporting costs were estimated using standard labor requirements ty pically applied to each standardized monitoring equipment ty pe and the hourl y rates shown in Table 3. The standard monitoring, record keeping, and reporting cost calculations are presented in Table 6.

**Table 6. Standard Monitoring, Record Keeping, and Reporting Cost s**  **Labor Category Calculation Note**  **Level of Effort**  **1** 

### (hr/yr) **Labor**

**Rate ($/hr)**  **Total**

**Annual Cost ($/yr)**  **Monitoring Labor** Operator Time 5 min/shift, 3 shifts/day, 365 days/yr 91.3 47.71 4,354 **Record Keeping and Reporting** Engineering Review 2.5% of Operator Time 2.28 83.01 189 Manager Review 2.5% of Operator Time 2.28 121.38 277 Clerical 10% of Operator Time 9.13 36.35 332 **Total Record Keeping and Reporting 798**  **Total Monitoring, Record Keeping, and Reporting Cost 5,950**  1 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4 . October 2000 . EPA/452/B - 02 - 001 . Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 2 - Refer to Table 3 for labor rate information 

### In addition to continuous monitoring, the proposed Subpart M contains provisions that require some periodic monitoring . The cost estimate for periodic monitoring requirements included specialized costs and assumptions as follows:

 For the annual internal inspection of the catal yst bed for catal ytic oxidizers, ERG assumed a three day

shutdown period . ERG also assumed that additional operator and engineering support would be required . ERG reasoned that sampling and analysis of the catal yst would occur during the annual internal inspection; therefore, no additional cost to shutdown the oxidizer for sample collection was estimated . Sources may be required to sample and analyze their catal yst on a more freq uent basis; however, these costs were not included . Table 7 presents estimated costs for the annual internal inspection and Table 8 presents an estimated cost of catalyst analysis .

### 8

 The monitoring, record keeping, and reporting cost s for adsorber regeneration frequency and duration, and to ensure proper operation, including valve sequencing and cycle time, were each assumed to be equal to the standard monitoring, record keeping, and reporting cost s (presented in Table 6) .  The monitoring, record keeping, and reporting cost s for measuring the concentration of regulated material at the adsorber bed outlet was estimated for monthly, daily, and weekl y frequencies . Refer to Table 9 through Table 11 for the specific cost calculations .  The monitoring, record keeping, and reporting cost for car- seal inspection was estimated using 10 minutes per month of operator time . Refer to Table 12 for the specific cost calculations . **Table 7. Monitoring, Record Keeping, and Reporting Cost s**  **for Periodic Catalytic Oxidizer Inspec** **tion and Catalyst Analysis Labor Category**  **Calculation Note Level of**  **Effort (hr/yr)**  **Labor**

**Rate 1**  

### ($/hr) **Total**

**Annual Cost ($/yr)**  **Monitoring Labor** Operator Time 2 

### 3 days 72 47.71 3,435 Operator Time 3 

### 1 day Overtime 24 71.57 1,718 Engineering Support4 

### 25% of Operator Time 18 83.01 1,494 **Record Keeping and Reporting 5**  

### Engineering Review 2.5% of Operator Time 1.80 83.01 149 Manager Review 2.5% of Operator Time 1.80 121.38 218 Clerical 10% of Operator Time 7.20 36.35 262 **Total Record Keeping and Reporting**  **630 Total Monitoring, Record Keeping, and Reporting Cost**  **7,906** 1 - Refer to Table 3 for labor rate information 2 - Operator for 1 day shutdown, 1 day inspection, 1 day startup . 3 - Operator on overtime for 1 day to assist with shutdown and startup . Regular operator hourly rate multiplied by 1.5 for overtime rate . 4 - Engineering support for shutdown, inspection, and startup. 5 - Hourly percentage requirements from EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4 . October 2000 . EPA/452/B - 02 - 001 . Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 

### Table 8. Catalytic Oxidizer Catalyst Analysis Costs **Catalyst Test Cost ($2011)**  Performance Analysis 1 

### 700 - 1,000 Contamination Analysis 1 

### 300 **Total Average Cost**  **1,150** 1 - Approximate cost s and range s provided by MEGTEC representative (Debbie Devroy, personal communication, September 26th, 2011 . )

### 9

**Table 9. Monitoring, Record Keeping, and Reporting Costs for Monthly FID Monitoring Labor Category**  **Calculation Note**  **Level of Effort**  **1** 

### (hr/yr) **Labor**

**Rate 2**  

### ($/hr) **Total**

**Annual Cost ($/** **y r)**  **Monitoring Labor** Operator Time 3 

### 30 minutes/month, 12 months/yr 6 47.71 286 **Record Keeping and Reporting** Engineering Review 2.5% of Operator Time 0 .15 83.01 12 Manager Review 2.5% of Operator Time 0 .15 121.38 18 Clerical 10% of Operator Time 0.6 3 6.35 22 **Total Record Keeping and Reporting 52**  **Total Monitoring,**  **Record Keeping ,**  **and Reporting Cost 339**  1

– EPA Air Pollution Control Cost Manual , Section 2, Chapter 4 . October 2000 . EPA/452/B - 02 - 001 . Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 2

– Refer to Table 3 for labor rate information 3

– Operator time estimated for monthly monitoring . Engineering, manager, and clerical time are calculated using percentages from EPA’s Air Pollution Control Cost Manual . 

### Table 10. Monitoring, Record Keeping, and Reporting Costs for Weekly FID Monitoring **Labor Category Calculation Note**  **Level of Effort**  **1** 

### (hr/yr) **Labor**

**Rate ($/hr)**  **Total**

**Annual Cost ($/yr)**  **Monitoring Labor** Operator Time 3 

### 30 min/week, 52 weeks/yr 26 47.71 1,241 **Record Keeping and Reporting** Engineering Review 2.5% of Operator Time 0.65 83.01 54 Manager Review 2.5% of Operator Time 0.65 121.38 79 Clerical 10% of Operator Time 2.6 36.35 95 **Total Record Keeping and Reporting**  **227 Total Monitoring, Record Keeping, and Reporting Cost**  **1,468** 1 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4 . October 2000 . EPA/452/B - 02 - 001 . Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 2 - Refer to Table 3 for labor rate information 3

– Operator time estimated for weekly monitoring . Engineering, manager, and clerical time are calculated using percentages from EPA’s Air Pollution Control Cost Manual .

### 10

**Table 11. Monitoring, Record Keeping, and Repo rting Cost**  **s for Daily FID Monitoring**  **Labor Category Calculation Note**  **Level of Effort**  **1** 

### (hr/yr) **Labor**

**Rate ($/hr)**  **Total**

**Annual Cost ($/yr)**  **Monitoring Labor** Operator Time 3 

### 30 min/day 365 days/yr 182.5 47.71 8,707 **Record Keeping and Reporting** Engineering Review 2.5% of Operator Time 4.56 83.01 379 Manager Review 2.5% of Operator Time 4.56 121.38 554 Clerical 10% of Operator Time 18.25 36.35 663 **Total Record Keeping and Reporting 1,596**  **Total Monitoring, Record Keeping, and Reporting Cost 10,303**  1 - EPA Air Pollution Control Cost Manual Section 2 Chapter 4 . October 2000 . EPA/452/B - 02 - 001 . Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 2 - Refer to Table 3 for labor rate information 3

– Operator time estimated for daily monitoring . Engineering, manager, and clerical time are calculated using percentages from EPA’s Air Pollution Control Cost Manual. 

### Table 12. Monitoring, Record Keeping, and Reporting Cost **s for Monthly Car** **- Seal Inspection**  **Labor Category Calculation Note**  **Level of Effort**  **1** 

### (hr/yr) **Labor**

**Rate ($/hr)**  **Total**

**Annual Cost ($/yr)**  **Monitoring Labor** Operator Time 3 

### 10 minutes/month, 12 months/yr 2 47.71 95 **Record Keeping and Reporting** Engineering Review 2.5% of Operator Time 0.05 83.01 4 Manager Review 2.5% of Operator Time 0.05 121.38 6 Clerical 10% of Operator Time 0.2 36.35 7 **Total Record Keeping and Reporting 17**  **Total Monitoring, Record Keeping, and Reporting Cost 113**  1 - EPA Air Pollution Control Cost Manual Section 2 Chapter 4 . October 2000 . EPA/452/B - 02 - 001 . Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 2 - Refer to Table 3 for labor rate information 

### Capital Recovery Annualized capital costs were estimated using formulas provided in EPA’s Air Pollution Control Cost Manual (U.S. EPA, 2002 ) . A capital recovery factor (CRF) was determined based on an assumed equipment life of 10 years and an interest rate of 7 percent . EPA’s Air Pollution Control Cost manual assumes an equipment life of 10 years and an interest rate of 7 percent for CEMS; therefore, the same equipment life and interest rate were assumed for all standardized

### 11

monitoring equipment types . The annualized capital cost was determined by multiplying the CRF by the TCI . Equation 1 presents the calculation ERG used to determine the CRF.Equation 1 Where: CRF = Capital Recovery Factor i = Interest Rate n = Equipment Life Table 13 provides a summary of the TCI and TAC for each standardized monitoring equipment ty

pe . Refer to Appendix A for application of monitoring equipment and costs to control equipment . Refer to Appendix B for detailed monitoring cost algorithms . Note that some of the cost items listed for each control device in Appendix A are alternative monitoring . Therefore, the costs should not be totaled for a given control device .

**Table 13. Summary of CPMS Monitoring Equipment Costs 1**  

### Equipment **TCI ($2010) TAC ($/yr)**  Flow Indicator - Gas Phase 6,300 6,600 Differential Pressure Flow Meter - Gas Phase 9,100 7,400 Magnetic Flow Meter - Liquid Phase 15,000 8,900 Differential Pressure Indicator - Gas Phase 7,900 7,000 Fabric Filter Bag Leak Detection System 2 

### 7,900 7,000 Pressure Indicator - Gas and Liquid Phase 6,400 6,600 Tem perature Indicator - Gas and Liquid Phase 9,900 7,600 pH Indicator3 

### 4,900 6,200 Caustic Strength Monitor4 

### 4,900 6,200 Humidity Indicator3 

### 5,400 6,300 Portable Flame Ionization Detector (monthly) 9,200 2,600 Portable Flame Ionization Detector (weekly) 9,200 3,700 Portable Flame Ionization Detector (daily) 9,200 13,000 Car- Seal Lock, Key, and Chain 150 160 1 - Costs have been rounded to two significant figures 2 - TCI and TAC assumed to be equal to differential pressure indicator - gas phase 3 - Cost year 2011 4 - TCI and TAC assumed to be equal to pH indicator

### 12

**3.2 Continuous Emissions Monitoring Systems (CEMS)**  TCIand TAC were estimated for organic CEMS using methods from EPA’s Air Pollution Control Cost Manual (EPA, 2003) . The TCI estimate includes the CEMS sampling system cost, monitor cost, data acquisition system cost, auxiliary equipment costs, and direct and indirect installation costs . The estimate also includes pl anning, equipment selection, purchase, installation, support facilities, performance testing, and quality assurance evaluations . The EPA Air Pollution Control Cost Manual method requires an estimate of hourl y labor rates for personnel involved in the installation, and default costs are provided . For the most current estimation, default labor values were replaced with the labor rates presented in Table 3 . Purchased equipment costs were also updated using the Chemical Engineering Plant Cost Index (June 2 010) . The TAC estimate includes the purchase of calibration gas, water, and electrical power or other consumables required by the CEMS . Operating and supervisory labor cost, maintenance costs, equipment replacement cost, property taxes, insurance, administrative charges, and overhead are also included . Annualized capital costs (i.e., capital recovery) were also included (refer to Equation 1 for further details regarding annualized capital costs) . Monitoring, record keeping, and reporting were calculated separatel y (refer to Table 6) and are included in the TAC estimate . Appendix B contains further detail regarding the estimate of the TCIand TAC for CEMS . Table 14 summarizes the estimates capital and annualized costs for organic CEMS .

**Table 14. Capital an d Annualized Costs for CEMS**  **1** 

### CEMS Configuration **Total Capital Investment ($)**  **Total Annualized**  **Costs ($/yr)** Organic CEMS 2 

### 180,000 61,000 1

– Costs rounded to two significant figures 2

– Assumed equal cost of THC CEMS 

### 4.0 **REFERENCES** Chain

– Campbell Tenso Chain Trade Size 2/0. 2011. <http://www.acehardwaresuperstore.com/3364 - tenso - chain/78264.html>. September 23 , 2011. Chemical Engineering. 2010. Economic Indicators. <http://www.che.com/business_and_economics/economic_indicators.html>. June.

### 13

Chemical Engineering. 2007. Economic Indicators. <http://www.che.com/business_and_economics/economic_indicators.html> . October. Devro y, D . 2011 . Personal c ommunication from MEGTEC . ( September) . Eutech Instruments pH 500 1⁄4 DIN pH/ORP Transmitter. 2011 . Retrieved September 20, 2011, from http://www.coleparmer.com/catalog/product_view.asp?sku=5671720 . +GF+ Signet pH/ORP Transmitter

– WU - 56560 - 18 Field Mount. 2011. <http ://www.coleparmer.com/catalog/product_view.asp?sku=5656018 > . September 20. Hanna Instruments HI504910 Digital Transmitter. 2011. <http://www.opentip.com/Tools -Auto Industrial/Hanna- Instruments - Hi - Digital - Transmitter-p - 2167364.html?source=googleps > . September 20. HX15 - D Duct Mounted RH Temp Transmitter (8.5” Probe). 2011. <http://www.omega.com/ppt/pptsc.asp?ref=HX15&Nav=temhu04 > . September 20 . Isolated 4 - 20 mA pH transmitter with integral display NEMA 4x enclosure. 2011. <http://www.omega.com/googlebase/product.html?pm=PHTX - 11 > . September 20. Lock

– MK Covered Brass Padlock with SS Shackle. 2011. <http://www.grainger.com/Grainger/ABUS -Vinyl - Covered- Brass - Padlock5UKK1?Pid=search> . September 20. ORE - 600 1 1⁄2 NPT differential ORP electrode, CPVC sensor body 180mm (7.1”) long 55mm (2.14”) Diameter. 2011 . <http://www.omega.com/ppt/pptsc.asp?ref=PHUCN600&Nav=gredd05 > . September 20. Peters, T . , and West. 2003. Plant design and e conomics for chemical engineers , 5th Ed. New York, NY: McGraw Hill. PHE - 600, 1 1⁄2 NPT Differential pH electrode, CPVC sensor body 18 0mm (7.1”) long 55mm (2.14”) diameter. 2011. <http://www.omega.com/ppt/pptsc.asp?ref=PHUCN600&Nav=gredd05 > . September 20. PHE - 6511 Submersion pH Electrode PVDF (Ky nar), Max Temp with “ -ACRYL” option 100C (212F). 2011. <http://www.omega.com/ppt/pptsc.asp?ref=PHE - 6510&Nav=gredd07 > . RHCM - 20 - 1 - 140F Duct mount dew point transmitter with 4 - 20mA and 24 Vdc power supply ouput. 2011. <http://www.omega.com/ppt/pptsc.asp?ref=RHCM&Nav=temhu04 > . September 20. RHCM - 20 - 4 - PT100 Duct mount dew point transmitter with 100 Ohm RTD and 230 VAC power supply output. 2011. <http://www.omega.com/ppt/pptsc.asp?ref=RHCM&Nav=temhu04 > . September 20.

### 14

U.S. Department of Labor Bureau of Labor Statistics (DOL). 2009. Occupational employ ment statistics: May

2009 Employ

ment wage e stimates. <http://stats.bls.gov/oes/current/oessrci.htm>. November. U.S. EPA. 2002. Air pollution control cost manual, 6 th 

### ed. EPA/452/B - 02 - 001 . 

### U.S. EPA. 2000. EPA Air p ollution c ontrol c ost manual, Section 2 , Chapter 4. EPA/45/B - 02 - 001.

## APPENDIX A **Summary of Subpart M Monitoring Requirements and Costs**

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 1 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes**  All Control Devices Flow indicator at inlet or outlet of control device Flow Indicator -

Gas Phase If intermittent 6,300 7,400 Assumed 1/2 Purchased Equipment Cost of Gas Flow Meter

Boilers and Process Heaters 65.724 CEMS measuring organic regulated material in exhaust stream Organic CEMS 65.724(a); Table 3 If Not Using

CPMS 180,000 61,000 Assumed Cost of THC CEMS From OAQPS CCM Temperature monitoring device in fire box Temperature

Indicator - Gas and Liquid Phase 65.724(a);

Table 4 All boilers and

process heaters CEMS

alternative 9,900 8,400

Incinerators 65.726 &

65.728 CEMS

measuring organic regulated material in exhaust stream Organic CEMS 65.726(a); Table 3 If Not Using

CPMS 180,000 61,000 Assumed Cost of THC CEMS From OAQPS CCM Temperature monitoring device in fire box or in ductwork immediately downstream of fire box Temperature

Indicator - Gas and Liquid Phase 65.726(a);

Table 4 If thermal

incinerator is used CEMS

alternative 9,900 8,400 Temperature monitoring devices in gas stream immediately before and after catalyst bed Temperature

Indicator - Gas and Liquid Phase 65.726(a);

Table 4 If catalytic

incinerator is used CEMS

alternative 9,900 8,400

Temperature monitoring device at inlet Temperature

Indicator - Gas and Liquid Phase 65.726(a);

Table 4 If catalytic

incinerator is used and temperature CEMS

alternative 9,900 8,400

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 2 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes**  differential between inlet and outlet of catalytic incinerator is less than 10 °C Periodic Catalyst Checks Catalyst Testing 65.728(a)(1) If catalytic incinerator is used and monitoring inlet temperature is used CEMS

alternative 1,150 Assumed annual sampling and analysis during internal inspection shutdown. Actual sampling and analysis may be more frequent Annual internal inspections of the catalyst bed to check for fouling, plugging, mechanical breakdown, channeling, abrasion, and settling Monitoring,

Record Keeping, and Reporting 65.728(a)(2) If catalytic incinerator is used and monitoring inlet temperature is used CEMS

alternative 7,906

Absorbers 65.740 Flow meter to monitor absorber influent liquid flow Magnetic Flow

Meter - Liquid Phase 65.740(a);

Table 4 All absorbers CEMS alternative 15,000 9,700 Flow meter to monitor liquid to - gas ratio based on absorber influent liquid flow and gas stream flow Differential

Pressure Flow Meter - Gas Phase 65.740(a);

Table 4 All absorbers CEMS alternative 9,100 8,200

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 3 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes** 

Pressure gauges at inlet and outlet of absorber to monitor pressure drop Differential

Pressure Indicator - Gas Phase 65.740(a);

Table 4 Acid gas

absorbers & absorbers controlling particulate and/or metal regulated materials; If pressure drop through absorber is greater than 5 inches of water CEMS

alternative 7,900 7,800

Temperature monitoring device at scrubber gas stream exit Temperature

Indicator - Gas and Liquid Phase 65.740(a);

Table 4 Absorbers

controlling particulate and/or metal regulated materials; If temperature differential between inlet gas stream and inlet liquid stream is greater than 100 °F CEMS

alternative 9,900 8,400

pH monitoring device to monitor scrubber liquid effluent pH pH Indicator 65.740(a); Table 4 Acid gas

scrubbers; If scrubbing liquid is a reactant CEMS

alternative 4,900 7,000 Caustic strength monitoring device to monitor scrubber liquid effluent caustic strength Caustic

Strength Monitor 65.740(a);

Table 4 Absorbers not

controlling acid gas, particulates, and metal regulated materials; If scrubbing liquid is a reactant CEMS

alternative 4,900 7,000 Assume Cost Equal to pH Monitor

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 4 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes** 

Temperature monitoring device Temperature

Indicator - Gas and Liquid Phase 65.740(a);

Table 4 Absorbers not

controlling acid gas, particulates, and meta regulated materials; If scrubbing liquid is not a reactant; If pressure drop through absorber is greater than 5 inches of wate r CEMS

alternative 9,900 8,400

Adsorbers – Regenerative 65.742 CEMS measuring organic regulated material in exhaust stream Organic CEMS 65.742(b); Table 3 If Not Using

CPMS 180,000 61,000 Assumed Cost of THC CEMS From OAQPS CCM Integrating regeneration stream flow device to monitor total regeneration stream flow Differential

Pressure Flow Meter - Gas Phase 65.742(b);

Table 4 If non - vacuum

regeneration system CEMS

alternative 9,100 8,200 Assume Cost Equal to Gas Flow Meter

Adsorber bed temperature monitoring device to monitor adsorber bed temperature during temperature regulation portion of the regeneration cycle Temperature

Indicator - Gas and Liquid Phase 65.742(b);

Table 4 If non - vacuum

regeneration system CEMS

alternative 9,900 8,400

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 5 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes**  Adsorber bed temperature monitoring device to monitor adsorber bed temperature during non temperature regulation portion of the regeneration cycle Temperature

Indicator - Gas and Liquid Phase 65.742(b);

Table 4 If non - vacuum

regeneration system CEMS

alternative 9,900 8,400

Pressure transmitter to monitor vacuum level during regeneration Pressure

Indicator - Gas and Liquid Phase 65.742(b);

Table 4 If vacuum

regeneration system CEMS

alternative 6,400 7,400

Monitor regeneration frequency and duration Monitoring,

Record Keeping, and Reporting 65.742(b);

Table 4 All

regenerative absorbers CEMS

alternative 5,950 Assume Monitoring, Record Keeping, and Reporting Costs Only - No capital required P otential change in impact Daily verification of adsorber operation including proper valve sequencing and cycle time Monitoring,

Record Keeping, and Reporting 65.742(b)(1) All regenerative absorbers CEMS

alternative 5,950 Assume Monitoring, Record Keeping, and Reporting Costs Only - No capital required P otential change in impact Weekly measurements of adsorber bed outlet VOC or regulated materials concentration over the last 5 minutes of adsorption Portable FID

(Weekly) 65.742(b)(2) All regenerative absorbers CEMS

alternative 9,200 3,700 Capital Cost of Portable Monitor and Basis of 30 Minutes of Operator Time per Week (Plus Engineering/Managerial/Clerical Ratio Time) P otential change in impact

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 6 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes**  cycle Develop corrective action plan Corrective

Action Plan 65.742(b)(2) All regenerative absorbers CEMS

alternative 3,377 Assume planning cost used for CPMS equipment P otential change in impact

Adsorbers – Non Regenerative 65.744 CEMS measuring organic regulated material in exhaust stream Organic CEMS 65.744(a); Table 3 If Not Using

CPMS 180,000 61,000 Assumed Cost of THC CEMS From OAQPS CCM Daily monitoring of adsorber bed outlet VOC or regulated materials concentration Portable FID

(Daily) 65.744(a)(2);

Table 4 All non regenerative absorbers CEMS

alternative 9,200 13,000 Capital Cost of Portable Monitor and Basis of 30 Minutes of Operator Time per Day (Plus Engineering/Managerial/Clerical Ratio Time) P otential change in impact Monthly monitoring of adsorber bed outlet VOC or regulated materials concentration Portable FID

(Monthly) 65.744(a)(2)(i) if adsorber has more than 2 months of life remaining CEMS

alternative 9,200 2,600 Capital Cost of Portable Monitor and Basis of 30 Minutes of Operator Time per Mont h (Plus Engineering/Managerial/Clerical Ratio Time) P otential change in impact Weekly monitoring of adsorber bed outlet VOC or regulated materials concentration Portable FID

(Weekly) 65.744(a)(2)(ii) if adsorber has more than 2 weeks of life remaining CEMS

alternative 9,200 3,700 Capital Cost of Portable Monitor and Basis of 30 Minutes of Operator Time per Week (Plus Engineering/Managerial/Clerical Ratio Time) P otential change in impact Condensers 65.746 CEMS measuring organic regulated material in exhaust Organic CEMS 65.746(a); Table 3 If Not Using

CPMS 180,000 61,000 Assumed Cost of THC CEMS From OAQPS CCM

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 7 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes**  stream Temperature monitoring device at outlet of condenser Temperature

Indicator - Gas and Liquid Phase 65.746(a);

Table 4 All condensers CEMS alternative 9,900 8,400

Biofilters 65.748 CEMS measuring organic regulated material in exhaust stream Organic CEMS 65.748(a); Table 3 If Not Using

CPMS 180,000 61,000 Assumed Cost of THC CEMS From OAQPS CCM Biofilter bed temperature monitoring device(s) Temperature

Indicator - Gas and Liquid Phase 65.748(a);

Table 4 All biofilters CEMS alternative 9,900 8,400 Biofilter bed moisture content monitoring device(s) Relative

Humidity Indicator 65.748(a);

Table 4 All biofilters CEMS alternative 5,400 7,100 P otential change in impact Pressure gauges at inlet and outlet of absorber to monitor pressure drop Pressure

Indicator - Gas and Liquid Phase 65.748(a);

Table 4 All biofilters CEMS alternative 6,400 7,400 P otential change in impact

Closed Vent Systems 65.720 Flow indicator at entrance to any bypass line which also sounds an alarm when flow is detected Flow Indicator -

Gas Phase 65.720(c)(1) If not using car seal or a lock and - key type configuration 6,300 7,400 Assumed 1/2 Purchased Equipment Cost of Gas Flow Meter P otential change in impact

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 8 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes**  Secure the bypass line valve in the non - diverting position with a car- seal or a lock - and - key type configuration - visually inspect the seal at least once a month Car- Seal 65.720(c)(2) If not using a flow indicator 150 160

Sorbent Injection 65.760 Monitor the sorbent injection rate Monitoring,

Record Keeping, and Reporting 65.760(b) All sorbent injection systems CEMS

alternative 5,950 Assume monitoring of sorbent screw feed. Assume Monitoring, Record Keeping, and Reporting Costs Only - No capital required Flow meter to monitor the sorbent injection system carrier gas flow rate Differential

Pressure Flow Meter - Gas Phase 65.760(b) All sorbent injection systems CEMS

alternative 9,100 8,200 Temperature monitoring device immediately downstream of combustion device fire box Temperature

Indicator - Gas and Liquid Phase 65.760(b) If operating a combustion device upstream of sorbent injection system CEMS

alternative 9,900 8,400 Temperature monitoring device in ductwork immediately downstream of particulate matter control device Temperature

Indicator - Gas and Liquid Phase 65.760(b) If using particulate matter control device upstream of adsorbent injection system CEMS

alternative 9,900 8,400

Fabric Filters 65.762 Bag leak detection system Differential

Pressure Indicator - Gas 65.762(a) All fabric filters 7,900 7,800 Assumes Cost of Differential Pressure Transmitters for Gas Flow Meter System

### Appendix A: Summary of Subpart M Monitoring Requirements and Costs

A - 9 **Device Type Device** 

**Section Monitoring**  **Standardized Mo**  **nitoring Equipment**  **Identifier Monitoring** 

**Section Conditions**  **Note s**  **T o**  **t al Capital**  **Investment ($)**  **Total**

**Annualized Costs**  **($/yr) Cost Notes**  Phase

## APPENDIX **B Standardized Monitoring Equipment Cost Algorithms** 

### B - 1

**Table B.1 Abbreviations used in Cost Algorithms Abbreviation**  **Definition** PL Planning Cost PEC Purchased Equipment Cost - Year of Source Material PEC10 Purchased Equipment Cost - Year 2010 Dollars PEC11 Purchased Equipment Cost - Year 2011 Dollars CEPCI(YEAR) Chemical Engineering Plant Cost Index for Specified Year F&ST Freight and Sales Tax INST Installation of Equipment Cost TCI10 Total Capital Investment - Year 2010 Dollars TCI11 Total Capital Investment - Year 2011 Dollars O&M Annual Operation and Maintenance Costs TIA Annual Taxes, Insurance, and Administration Costs CRF Capital Recovery Factor i Interest Rate n Equipment Life (Years) CR Annualized Capital Cost (Capital Recovery) TAC10 Total Annual Cost, Year 2010 Dollars TAC11 Total Annual Cost, Year 2011 Dollars

### B - 2

**Table B.2 Total Capital Investment and Total Annualized Cost Estimate: Flow Indicator -**  **Gas Phase**  **Component Equation**  **1** 

### Cost **($) Capital and Other Initial**  **Costs** Planning2, 3 

### PL 3,377 Flow Indicator4, 5 

### ($2002) PEC 1,330 Flow Indicator4, 5, 6 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 1,812 Freight and Sales Tax 7 

### F&ST=PEC10*.08 145 Install Flow Meter 8 

### INST=(PEC10+F&ST)*0.47 920 **Total Capital Investment ($2010)**  TCI10=PEC10+F&ST+INST+PL **6,254 Annualized Costs**  Operation and Maintenance 7 

### O&M=.10(PEC10)+.10(INST) 273 Monitoring, Record Keeping, and Reporting9 

### R&R 5,950 Taxes, Insurance, Administration7 

### TIA=0.04*TCI10 250 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor7 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery7 

### CR=CFR*TCI10 890 **Total Annualized Costs ($/yr) ($2010)** TAC10=O&M+R&R+TIA+CR **7,363** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual Section 2 Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Assumes half the cost of Gas Flow Meter - Refer to Table B.3 Total Capital Investment and Total Annualized Cost Estimate: Differential Pressure Flow Meter - Gas Phase 5 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 896 Figure B - 12 "Purchased Cost of Flow Indicators." 6 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 7 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2 002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 8 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 9 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost s

### B - 3

**Table B.3 Total Capital Investment and Total Annualized Cost Estimate for Differential Pressure**  **Flow Meter -**  **Gas Phase**

**Component Equation**  **1** 

### Cost **($) Capital and Other Initial Costs**  Planning2, 3 

### PL 3,377 Diff. Pressure Flow Meter4, 5 

### ($2002) PEC 2,660 Diff. Pressure Flow Meter4, 5, 6 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 3,625 Freight and Sales Tax 7 

### F&ST=PEC10*.08 290 Install Flow Meter 8 

### INST=(PEC10+F&ST)*0.47 1,840 **Total Capital Investment ($2010)** TCI10=PEC10+F&ST+INST+PL **9,131 Annualized Costs**  Operation and Maintenance 7 

### O&M=.10(PEC10)+.10(INST) 546 Monitoring, Record Keeping and Reporting 9 

### R&R 5,950 Taxes, Insurance, Administration7 

### TIA=0.04*TCI10 365 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor7 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery7 

### CR=CFR*TCI10 1,300 **Total Annualized Costs ($/yr) ($2010)**  TAC10=O&M+R&R+TIA+CR **8,162** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Differential Pressure, Explosion Proof, Stainless Steel Pressure Transmitters ($2100) + 2070 kPa Carbon Steel Weld-Neck Flange, 6 Inch Line ($450) + Orifice Plate 0.003175 m Thick 316 Stainless Steel, 6 Inch Line ($110) 5 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill , New York, NY. Pg. 896 Figure B - 12 "Purchased Cost of Flow Indicators." 6 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 7 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 8 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 9 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost

### B - 4

**Table B.4 Total Capital Investment and Total Annualized Cost Estimate: Magnetic Flow Meter -**  **Liquid Phase Component**  **Equation 1**  

### Cost ($) **Capital and Other Initial Costs** Planning2, 3 

### PL 3,377 Magnetic Flow Meter4, 5 

### ($2002) PEC 5,250 Magnetic Flow Meter4, 5, 6 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 7,154 Freight and Sales Tax 7 

### F&ST=PEC10*.08 572 Install Flow Meter 8 

### INST=(PEC10+F&ST)*0.47 3,632 **Total Capital Investment ($2010)** TCI10=PEC10+F&ST+INST+PL **14,735 Annualized Costs**  Operation and Maintenance 7 

### O&M=.10(PEC10)+.10(INST) 1,079 Monitoring, Record Keeping and Reporting 9 

### R&R 5,950 Taxes, Insurance, Administration7 

### TIA=0.04*TCI10 589 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor7 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery7 

### CR=CFR*TCI10 2,098 **Total Annualized Costs ($/yr) ($2010)** TAC10=O&M+R&R+TIA+CR **9,716** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - 304 Stainless Steel, 1035 -kPa flanged pipe, 315 Stainless - Steel Electrodes, Teflon Lining, 6 Inch Line 5 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copy right 2003. McGraw- Hill, New York, NY. Pg. 896 Figure B - 12 "Purchased Cost of Flow Indicators." 6 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 7 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 8 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 9 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost s

### B - 5

**Table B.5 Total Capital Investment and Total Annualized Cost Estimate: Differential Pressure**  **Indicator -**  **Gas Phase**

**Component Equation**  **1** 

### Cost **($) Capital and Other Initial Costs**  Planning2, 3 

### PL 3,377 Diff. Pressure Transmitters 4, 5 

### ($2002) PEC 2,100 Diff. Pressure Transmitters 2, 5, 6 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 2,862 Freight and Sales Tax 7 

### F&ST=PEC10*.08 229 Install Flow Meter 8 

### INST=(PEC10+F&ST)*0.47 1,453 **Total Capital Investment ($2010)** TCI10=PEC10+F&ST+INST+PL **7,920 Annualized Costs**  Operation and Maintenance 7 

### O&M=.10(PEC10)+.10(INST) 431 Monitoring, Record Keeping and Reporting 9 

### R&R 5,950 Taxes, Insurance, Administration7 

### TIA=0.04*TCI10 317 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor7 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery7 

### CR=CFR*TCI10 1,128 **Total Annualized Costs ($/yr) ($2010)** TAC10=O&M+R&R+TIA+CR **7,826** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Differential Pressure, Explosion Proof, Stainless Steel Pressure Transmitters ($2100) 5 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 896 Figure B - 12 "Purchased Cost of Flow Indicators." 6 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 7 - EPA Air Pol lution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 8 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 9 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost s

### B - 6

**Table B.6 Total Capital Inve stment and Total Annualized Cost Estima** **te: Pressure Indicator -**  **Gas or**  **Liquid Phase Component**  **Equation 1**  

### Cost **($) Capital and Other Initial Costs**  Planning2, 3 

### PL 3,377 Pressure Transmitter4 

### ($2002) PEC 1,376 Pressure Transmitter4, 5 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 1,875 Freight and Sales Tax 6 

### F&ST=PEC10*.08 150 Install Flow Meter7 

### INST=(PEC10+F&ST)*0.47 952 **Total Capital Investment ($2010)** TCI10=PEC10+F&ST+INST+PL **6,354 Annualized Costs**  Operation and Maintenance 6 

### O&M=.10(PEC10)+.10(INST) 283 Monitoring, Record Keeping and Reporting 8 

### R&R 5,950 Taxes, Insurance, Administration6 

### TIA=0.04*TCI10 254 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor6 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery6 

### CR=CFR*TCI10 905 **Total Annualized Costs ($/yr) ($2010)** TAC10=O&M+R&R+TIA+CR **7,391** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 897 Figure B - 14 "Purchased Cost of Pressure Indicators." 5 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 6 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 7 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 8 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost s

### B - 7

**Table B.7 Total Capital Investment and Total Annualized Cost Estimate : Temperature Indicator**  **- Gas or**  **Liquid Phase**

**Component Equation**  **8** 

### Cost **($) Capital and Other Initial Costs**  Planning2, 3 

### PL 3,377 Tem perature Transmitter4 

### ($2002) PEC 2,999 Tem perature Transmitter4, 5 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 4,087 Freight and Sales Tax 6 

### F&ST=PEC10*.08 327 Install Flow Meter7 

### INST=(PEC10+F&ST)*0.47 2,074 **Total Capital Investment ($2010)** TCI10=PEC10+F&ST+INST+PL **9,865 Annualized Costs**  Operation and Maintenance 6 

### O&M=.10(PEC10)+.10(INST) 616 Monitoring, Record Keeping and Reporting 8 

### R&R 5,950 Taxes, Insurance, Administration6 

### TIA=0.04*TCI10 395 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor6 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery6 

### CR=CFR*TCI10 1,405 **Total Annualized Costs ($/yr) ($2010)**  TAC10=O&M+R&R+TIA+CR **8,365** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 897 Figure B - 13 "Purchased Cost of Temperature Recorders and Indicators." 5 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 6 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 7 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 8 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost s

### B - 8

**Table B.8 Total Capital Investment and Total Annualized Cost Estimate for pH Transmitter**

**Component Equation**  **1** 

### Cost ($) **Capital and Other Initial Costs** Planning2, 3 

### PL 3,377 pH Transmitter and Sensor4 

### ($2011) PEC11 976 Freight and Sales Tax 5 

### F&ST=PEC11*.08 78 Installation 6 

### INST=(PEC11+F&ST)*0.47 496 **Total Capital Investment ($2011)** TCI11=PEC11+F &ST+INST+PL **4,927 Annualized Costs**  Operation and Maintenance 5 

### O&M=.10(PEC11)+.10(INST) 147 Monitoring Record Keeping and Reporting7 

### R&R 5,950 Taxes, Insurance, Administration 5 

### TIA=0.04*TCI11 197 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor5 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery5 

### CR=CFR*TCI11 701 **Total Annualized Costs ($/yr) ($2011)** TAC11=O&M+R&R+TIA+CR **6,995** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Average of online price quotes, refer to Table B.9 and Table B.10 5 - EPA Air Pollution Control Cost Manual Section 1 Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 6 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 7 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost s

### B - 9

**Table B.9 Cost Data for pH Transmitter**  **pH Transmitter Description Cost**  **($2011)** Isolated 4 -20 mA pH transmitter with integral display NEMA 4x enclosure 1 

### 430 Hanna Instruments HI504910 Digital Transmitter2 

### 662 Eutech Instruments pH 500 1/4 DIN pH/ORP Transmitter3 

### 349 `+GF+ Signet pH/ORP Transmitter - WU - 56560 - 18 Field Mount4 

### 578 **Average Cost 505**  1 - http://www.omega.com/googlebase/product.html?pm=PHTX - 11 - Accessed 9/20/11 2 - http://www.opentip.com/Tools - Auto - Industrial/Hanna - Instruments - Hi - Digital - Transmitter-p 2167364.html?source=googleps - Accessed 9/20/11 3 - http://www.coleparmer.com/catalog/product_view.asp?sku=5671720 - Accessed 9/20/11 4 - http://www.coleparmer.com/catalog/product_view.asp?sku=5656018 - Accessed 9/20/11 

### Table B.10 Cost Data for pH Electrode **pH Electrode Description Cost**  **($2011)** PHE - 600, 1 1/2 NPT differential pH electrode, CPVC sensor body 180mm (7.1") long 55mm (2.14") diameter 1 

### 575 ORE - 600 1 1/2 NPT differential ORP electrode, CPVC sensor body 180 mm (7.1") long 55mm (2.14") Diameter2 

### 575 PHE - 6511 Submersion pH Electrode PVDF (Kynar), Max Temp with " -ACRYL" option 100C (212F) 3 

### 265 **Average Cost 472**  1 - http://www.omega.com/ppt/pptsc.asp?ref=PHUCN600&Nav=gredd05 - Accessed 9/20/11 2 - http://www.omega.com/ppt/pptsc.asp?ref=PHUCN600&Nav=gredd05 - Accessed 9/20/11 3 - http://www.omega.com/ppt/pptsc.asp?ref=PHE - 6510&Nav=gredd07 - Accessed 9/20/11

### B - 10

**Table B.11 Total Capital Investment and Total Annualized Cost Estimate for Relative Humidity Transmitter**  **Component Equation**  **1** 

### Cost **($) Capital and Other Initial Costs**  Planning2, 3 

### PL 3,377 Relative Humidity Transmitter and Sensor4 

### ($2011) PEC11 1,250 Freight and Sales Tax 5 

### F&ST=PEC11*.08 100 Installation 6 

### INST=(PEC11+F&ST)*0.47 635 **Total Capital Investment ($2011)** TCI11=PEC11+F&ST+INST+PL **5,361 Annualized Costs**  Operation and Maintenance 5 

### O&M=.10(PEC11)+.10(INST) 188 Monitoring, Record Keeping and Reporting7 

### R&R 5,950 Taxes, Insurance, Administration 5 

### TIA=0.04*TCI11 214 Interest Rate 3 

### i 0.07 Equipment Life (years) 3 

### n 10 Capital Recovery Factor5 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery5 

### CR=CFR*TCI11 763 **Total Annualized Costs ($/yr) ($2011)**  TAC11=O&M+R&R+TIA+CR **7,116** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Average of online price quotes, refer to Table B.12 5 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 6 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copyright 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 7 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost s

### B - 11

**Table B.12 Cost Data for Relative Humidity Sensor and Transmitter Relative Humidity Sensor and Transmitter Description**  **Cost ($2011)**  RHCM -20 - 1 - 140F Duct mount dewpoint transmitter with 4 -20mA and 24 Vdc power supply output 1 

### 1588 RHCM -20 -4 -PT100 Duct mount dewpoint transmitter with 100 Ohm RTD and 230 VAC power supply output2 

### 1603 HX15 -D Duct Mounted RH/Temp Transmitter (8.5" Probe) 3 

### 559 **Average Cost 1250**  1 - http://www.omega.com/ppt/pptsc.asp?ref=RHCM&Nav=temhu04 - Accessed 9/20/11 2 - http://www.omega.com/ppt/pptsc.asp?ref=RHCM&Nav=temhu04 - Accessed 9/20/11 3 - http://www.omega.com/ppt/pptsc.asp?ref=HX15&Nav=temhu04 - Accessed 9/20/11

### B - 12

**Table B.13 Total Capital Investment and Total Annualized Cost Estimate: Monthly Monitoring with Portable Flame Ionization Detector** 

**Component Equation**  **1** 

### Cost ($) **Capital and Other Initial Costs** Planning2, 3 

### PL 3,377 Portable FID 4 

### ($2008) PEC 5,779 Portable FID 4, 5 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 5,415 Freight and Sales Tax 6 

### F&ST=PEC10*.08 433 **Total Capital Investment ($2010)** TCI10=PEC10+F&ST+PL **9,224 Annualized Costs**  Operation and Maintenance 3 

### O&M=.10(PEC10) 541 Monitoring, Record Keeping and Reporting 7 

### R&R 339 Taxes, Insurance, Administration 6 

### TIA=0.04*TCI10 369 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor6 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery6 

### CR=CFR*TCI10 1,313 **Total Annualized Costs ($/yr) ($2010)** TAC10=O&M+R&R+TIA+CR **2,563** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Average of 3 vendor costs, provided by EPA 5 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 6 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 7 - Refer to Table 7 Monitoring, Record Keeping and Reporting Cost s for Monthly FID Monitoring

### B - 13

**Table B.14 Total Capital Investment and Total Annualized Cost Estimate: Weekly Monitoring with Portable Flame Ionization Detector** 

**Component Equation**  **1** 

### Cost ($) **Capital and Other Initial Costs**  Planning2, 3 

### PL 3,377 Portable FID 4 

### ($2008) PEC 5,779 Portable FID 4, 5 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 5,415 Freight and Sales Tax 6 

### F&ST=PEC10*.08 433 **Total Capital Investment ($2010)** TCI10=PEC10+F&ST+PL **9,224 Annualized**  **Costs** Operation and Maintenance 3 

### O&M=.10(PEC10) 541 Monitoring, Record Keeping and Reporting 7 

### R&R 1,468 Taxes, Insurance, Administration 6 

### TIA=0.04*TCI10 369 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor6 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery6 

### CR=CFR*TCI10 1,313 **Total Annualized Costs ($/yr) ($2010)** TAC10=O&M+R&R+TIA+CR **3,692** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Average of 3 vendor costs, provided by EPA 5 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 6 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 7 - Refer to Table 8 Monitoring, Record Keeping and Reporting Cost s for Weekly FID Monitoring

### B - 14

**Table B.15 Total Capital Investment and Total Annualized Cost Estimate for Daily Monitoring with Portable FID** 

**Component Equation**  **1** 

### Cost ($) **Capital and Other Initial Costs** Planning2, 3 

### PL 3,377 Portable FID 4 

### ($2008) PEC 5,779 Portable FID 4, 5 

### ($2010) PEC10=CEPCI (2010)/CEPCI (2002)*PEC 5,415 Freight and Sales Tax 6 

### F&ST=PEC10*.08 433 **Total Capital Investment ($2010)** TCI10=PEC10+F&ST+PL **9,224 Annualized Costs**  Operation and Maintenance 3 

### O&M=.10(PEC10) 541 Monitoring, Record Keeping and Reporting 7 

### R&R 10,303 Taxes, Insurance, Administration 6 

### TIA=0.04*TCI10 369 Interest Rate 3 

### i 0.07 Equipment Life 3 

### (years) n 10 Capital Recovery Factor6 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery6 

### CR=CFR*TCI10 1,313 **Total Annualized Costs ($/yr) ($2010)** TAC10=O&M+R&R+TIA+CR **12,527** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 4 Summary of Planning Labor Cost Calculation for CPMS 3 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 4 - Average of 3 vendor costs, provided by EPA 5 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 6 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 7 - Refer to Table 9 Monitoring, Record Keeping and Reporting Cost s for Daily FID Monitoring

### B - 15

**Table B.16: Costs for Portable Flame Ionization Detector**  **1** 

### Company **Description Cost**  **($2008)** Sleuth Portable FID (for hydrocarbon measurements) 5,720 Perkins -Elmer Portable FID 4,262 REPSS.com Photovac MicroFID (includes FID, charger, filters, Teflon probe,

carrying trap) 7 ,356 **Average Cost 5,779**  4.1.1 1 - Vendor cost information provided by EPA

### B - 16

**Table B.1 7**  **Regression Constants 1**  

### and Hourly Rates for Organic CEMS **Calculation Component**  **Factor or Cost** k1 ($1999) 85,354 k2 (hours) 343 k3 (hours) 168 k4 (hours) 0 k5 (hours) 110 k6 (hours) 93 k7 **2** 

### 1 k8 ($1999) 4,060 k9 (hours) 44 k10 (hours) 391 k11 (hours) 0 k12 (hours) 2 k13 (hours) 79 k14 2 

### 0 A (Corporate Environmental Engineer hourly cost) 3 

### 48 B (Plant Technician hourly cost) 4 

### 36 C (Plant Technician II hourly cost) 5 

### 46 D (CEMS Consultant hourly cost) 6 

### 121 E (Test Crew hourly cost) 7 

### 83 F 1 

### (Cost of Equipment) ($1999) 10,200 1 - All "k" regression constants and "F" factor are from EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 2 - Unit less 3 - Corporate Environmental Engineer hourly rate assumed equal to "Plant and System Operators, All" From Table 3.1: Summary of 2009 Hourly Labor Rates 4 - Plant Technician hourly rate assumed equal to "Administrative Support, Including Clerical" from Table 3.1: Summary of 2009 Hourly Labor Rates 5 - Plant Technician II hourly rate assumed equal to "Installation, Maintenance, and Repair" from Table 3.1: Summary of 2009 Hourly Labor Rates 6 - CEMS Consultant hourly rate assumed equal to "Executive, Administrative and Managerial" From Table 3.1: Summary of 2009 Hourly Labor Rates 7 - Test Crew

hourly rate assumed equal to "Professional Specialty and Technical" From Table 3.1: Summary of 2009 Hourly Labor Rates

### B - 17

**Table B.1 8**  **Total Capital Investment and Total Annualized Cost Estimate: Organic CEMS**  **1** 

### Component **Equation 2**  

### Cost ($) **Capital and Other Initial**  **Costs** k12010 3, 4 

### ($2010) k12010=k1*CEPCI(2010)/CEPCI(1999) 117,804 PEC10 3, 4 

### (Cost of Equipment) ($2010) PEC10=F*CEPCI(2010)/CEPCI(1999) 14,078 **Total Capital Investment 8**  

### ($2010) TCI=k12010+(k2xA)+(k3xB)+(k4xC)+(k5xD)+(k6xE)+ (k7xPEC10)+PL **175,432 Annualized Costs**  Monitoring, Record Keeping, and Reporting 5 

### R&R 5,950 Interest Rate 6 

### i 0.07 Equipment Life 6 

### (years) n 10 Capital Recovery Factor7 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 k82010 3, 4 

### ($2010) k82010=k8*CEPCI(2010)/CEPCI(1999) 5,604 **Total Annualized Costs 4, 8**  

### ($/yr) ($2010) TAC10=k82010+(k9xA)+(k10xB)+(k11xC)+(k12xD)+ (k13xE)+(k14xPEC10)+(CRFxTCI)+R&R **61,009** 1 - Assumed cost of THC CEMS EPA Air Pollution Control Cost Manual 2 - Refer to Table B.1 for abbreviation definitions 3 - "Economic Indicators." Chemical Engineering. June 2010. Web. <http://www.che.com>. 4 - Refer to Table B.12 for "k" regression constants, "A,B,C,D,E," and "F" Factors, and "F10 Factors" 5 - Refer to Table 4 Monitoring, Record Keeping, and Reporting Cost for Daily FID Monitoring 6 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf 7 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 8 - Monitoring, Record Keeping, and Reporting added to Total Annualized Costs

### B - 18

**Table B.19 Total Capital Investment and Total Annualized Cost Estimat e for Car** **- Seal** 

**Component Equation**  **1** 

### Cost ($) **Capital and Other Initial Costs** Lock, Key, Chain2 

### ($2011) PEC11 97 Freight and Sales Tax 3 

### F&ST=PEC11*.08 8 Installation4 

### INST=(PEC11+F&ST)*0.47 49 **Total Capital Investment ($2011)** TCI11=PEC11+F& ST+INST+PL **154 Annualized Costs**  Operation and Maintenance 3 

### O&M=.10(PEC11)+.10(INST) 15 Monitoring, Record Keeping and Reporting 5 

### R&R 113 Taxes, Insurance, Administration3 

### TIA=0.04*TCI11 6 Interest Rate 6 

### i 0.07 Equipment Life (years) 6 

### n 10 Capital Recovery Factor3 

### CRF=(i*(1+i) n

### )/((1+i) n

### - 1) 0.14 Capital Recovery3 

### CR=CFR*TCI11 22 **Total Annualized Costs ($/yr) ($2011)** TAC11=O&M+R&R+TIA+CR **156** 1 - Refer to Table B.1 for abbreviation definitions 2 - Refer to Table 19 Cost Data for Car- Seal Equipment 3 - EPA Air Pollution Control Cost Manual , Section 1 , Chapter 2. January 2002. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs1ch2.pdf 4 - Peters, Timmerhaus, and West. "Plant Design and Economics for Chemical Engineers." Fifth Edition. Copy right 2003. McGraw- Hill, New York, NY. Pg. 251 Table 6 - 9 "Ratio factors for estimating capital investment items based on delivered equipment cost." 5 - Refer to Table 6 Standard Monitoring, Record Keeping, and Reporting Cost s 6 - EPA Air Pollution Control Cost Manual , Section 2 , Chapter 4. October 2000. EPA/452/B - 02 - 001. Available at: http://www.epa.gov/ttn/catc/dir1/cs2ch4.pdf

### B - 19

**Table B.20 Cost Data for Car -**  **Seal Equipment Car** **- Seal Cost Equipment**  **Cost ($2011)** Lock - MK Covered Bra ss Padlock with SS Shackle 1 

### 23 Chain - Campbell Tenso Chain Trade Size 2/0 2 

### 74 **Total Cost 97**  1 - http://www.grainger.com/Grainger/ABUS - Vinyl - Covered- Brass - Padlock5UKK1?Pid=search - Accessed 9/23/11 2 - http://www.acehardwaresuperstore.com/3364 -tenso - chain/78264.html - Accessed 9/23/11