Document ID: EPA-HQ-OAR-2010-0871-0022
Agency: epa
Document Type: Supporting & Related Material
Title: 
Posted Date: 2012-03-26T04:00Z

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

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 system provisions do not require monitoring; therefore, costs were not estimated for fuel gas systems. 
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 
IDENTIFICATION OF MONITORING REQUIREMENTS
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 systems. The proposed Subpart M sections for these requirements are listed in Table 1.
Table 1. Monitoring Requirements in Proposed 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 type, 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 systems 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. 
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 typical monitoring requirements in past rules include some provisions for adsorbers, biofilters, and bypasses. Appendix A identifies these specific adsorber, biofilter, and bypass monitoring requirements in the cost note column as a "potential change in impact". 
TCI and TAC for each type of monitoring are also included in Appendix A. The methods used to estimate TCI and TAC are described in Section 3.0 of this memorandum. 
ESTIMATING MONITORING 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 analyzed to identify the type of monitoring equipment sources may use to demonstrate compliance. Cost estimates were developed based on the list of potential equipment types. Costs were also estimated for periodic monitoring and are discussed in detail in section 3.1.2. Table 2 summarizes the different equipment types 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
                 Temperature 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
      
Cost algorithms were developed to estimate the TCI and TAC for the CEMS and CPMS requirements for each standardized monitoring equipment type. Section 3.1 describes the cost parameters contained in each algorithm. 
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. 
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 hourly 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 sector: 2-digit NAICS code 31-33 (http://stats.bls.gov/oes/oes_dl.htm accessed in December 2010).

Hourly requirements for planning were developed using 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
                               Calculation Note
                                  Cost ($/yr)
                                  Engineering
                          36 hours[1] at $83.01/hr[2]
                                     2,988
                                  Management
                          2 hours[1] at $121.38/hr[2]
                                      243
                             Clerical (Purchasing)
                          4 hours[1] at $36.35/hr[2]
                                      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 by 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 estimated the cost of a lock and chain on the bypass 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 year 2010 using the Chemical 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
Temperature Indicator - Gas or Liquid Phase
                                     4,100
                                     9,900
pH Indicator[3]
                                      980
                                     4,900
Relative Humidity Indicator[4]
                                     1,300
                                     5,400
Caustic Strength Monitor[5]
                                      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. 
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). 
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 typically applied to each standardized monitoring equipment type and the hourly 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 Costs
                                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 catalyst bed for catalytic 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 catalyst 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 catalyst on a more frequent 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. 
The monitoring, record keeping, and reporting costs 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 costs (presented in Table 6). 
The monitoring, record keeping, and reporting costs for measuring the concentration of regulated material at the adsorber bed outlet was estimated for monthly, daily, and weekly 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 Costs for Periodic Catalytic Oxidizer Inspection 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 Support[4]
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 costs and ranges provided by MEGTEC representative (Debbie Devroy, personal communication, September 26th, 2011.)

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] ($/hr)
                           Total Annual Cost ($/yr)
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
                                     36.35
                                      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. 

Table 11. Monitoring, Record Keeping, and Reporting Costs 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 Costs 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 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 type. 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 
Temperature Indicator - Gas and Liquid Phase
                                    9,900 
                                    7,600 
pH Indicator[3]
                                    4,900 
                                    6,200 
Caustic Strength Monitor[4]
                                    4,900 
                                    6,200 
Humidity Indicator[3]
                                    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
Continuous Emissions Monitoring Systems (CEMS)
TCI and 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 planning, equipment selection, purchase, installation, support facilities, performance testing, and quality assurance evaluations. The EPA Air Pollution Control Cost Manual method requires an estimate of hourly 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 2010). 
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 separately (refer to Table 6) and are included in the TAC estimate. Appendix B contains further detail regarding the estimate of the TCI and TAC for CEMS. 
Table 14 summarizes the estimates capital and annualized costs for organic CEMS. 
Table 14. Capital and 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
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.

  Chemical Engineering. 2007.  Economic Indicators. <http://www.che.com/business_and_economics/economic_indicators.html>. October. 
 Devroy, D. 2011.  Personal communication 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-Padlock-5UKK1?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 economics for chemical engineers, 5th Ed.  New York, NY: McGraw Hill. 
 PHE-600, 1 (1/2) NPT Differential pH 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.
 PHE-6511 Submersion pH Electrode PVDF (Kynar), 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.  
 U.S. Department of Labor Bureau of Labor Statistics (DOL). 2009. Occupational employment statistics: May 2009 Employment wage estimates. <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 pollution control cost manual, Section 2, Chapter 4.  EPA/45/B-02-001. 

                                       
                                       
                                       
                                       
                                       
                                       
                                       
                                       
                                  APPENDIX A
                                       
            Summary of Subpart M Monitoring Requirements and Costs
                                       
                                       
                                  Device Type
                                Device Section
                                  Monitoring
                 Standardized Monitoring Equipment Identifier
                              Monitoring Section
                                  Conditions
                                     Notes
                         Total 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 differential between inlet and outlet of catalytic incinerator is less than 10 °C
CEMS alternative
                                     9,900
                                     8,400

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

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

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 water
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

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

Potential 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

Potential change in impact

Weekly measurements of adsorber bed outlet VOC or regulated materials concentration over the last 5 minutes of adsorption cycle
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)

Potential change in impact

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

Potential 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)

Potential 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 Month (Plus Engineering/Managerial/Clerical Ratio Time)

Potential 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)

Potential change in impact
Condensers
 
65.746
 
CEMS measuring organic regulated material in exhaust stream
Organic CEMS
65.746(a);
Table 3
If Not Using CPMS
 
                                    180,000
                                    61,000
Assumed Cost of THC CEMS From OAQPS CCM

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
Potential 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
Potential 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

Potential change in impact

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 Phase
65.762(a)
All fabric filters
 
                                     7,900
                                     7,800
Assumes Cost of Differential Pressure Transmitters for Gas Flow Meter System
                                       
                                       
                                       
                                       
                                       
                                       
                                       
                                       
                                       
                                  APPENDIX B
                                       
               Standardized Monitoring Equipment Cost Algorithms
                                       
                                       

 
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

Table B.2 Total Capital Investment and Total Annualized Cost Estimate: Flow Indicator - Gas Phase
                                   Component
                                  Equation[1]
                                   Cost ($)
Capital and Other Initial Costs
 
 
Planning[2, 3]
PL
                                                                          3,377
Flow Indicator[4, 5] ($2002)
PEC
                                                                          1,330
Flow Indicator[4, 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 Reporting[9]
R&R
                                                                          5,950
Taxes, Insurance, Administration[7]
TIA=0.04*TCI10
                                                                            250
Interest Rate[3]
i
                                                                           0.07
Equipment Life[3] (years)
n
                                                                             10
Capital Recovery Factor[7]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[7]
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 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 Costs

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
 
 
Planning[2, 3]
PL
                                                                          3,377
Diff. Pressure Flow Meter[4, 5] ($2002)
PEC
                                                                          2,660
Diff. Pressure Flow Meter[4, 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, Administration[7]
TIA=0.04*TCI10
                                                                            365
Interest Rate[3]
i
                                                                           0.07
Equipment Life[3] (years) 
n
                                                                             10
Capital Recovery Factor[7]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[7]
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

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
 
 
Planning[2, 3]
PL
                                                                          3,377
Magnetic Flow Meter[4, 5] ($2002)
PEC
                                                                          5,250
Magnetic Flow Meter[4, 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, Administration[7]
TIA=0.04*TCI10
                                                                            589
Interest Rate[3]
i
                                                                           0.07
Equipment Life[3] (years) 
n
                                                                             10
Capital Recovery Factor[7]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[7]
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. 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 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 Costs

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
 
 
Planning[2, 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, Administration[7]
TIA=0.04*TCI10
                                                                            317
Interest Rate[3]
i
                                                                           0.07
Equipment Life[3] (years) 
n
                                                                             10
Capital Recovery Factor[7]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[7]
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 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 Costs

Table B.6 Total Capital Investment and Total Annualized Cost Estimate: Pressure Indicator - Gas or Liquid Phase
                                   Component
                                  Equation[1]
                                   Cost ($)
Capital and Other Initial Costs
 
 
Planning[2, 3]
PL
                                                                          3,377
Pressure Transmitter[4] ($2002)
PEC
                                                                          1,376
Pressure Transmitter[4, 5] ($2010)
PEC10=CEPCI (2010)/CEPCI (2002)*PEC
                                                                          1,875
Freight and Sales Tax[6]
F&ST=PEC10*.08
                                                                            150
Install Flow Meter[7]
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, Administration[6]
TIA=0.04*TCI10
                                                                            254
Interest Rate[3]
i
                                                                           0.07
Equipment Life[3] (years) 
n
                                                                             10
Capital Recovery Factor[6]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[6]
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 Costs

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
Temperature Transmitter[4] ($2002)
PEC
                                                                          2,999
Temperature Transmitter[4, 5] ($2010)
PEC10=CEPCI (2010)/CEPCI (2002)*PEC
                                                                          4,087
Freight and Sales Tax[6]
F&ST=PEC10*.08
                                                                            327
Install Flow Meter[7]
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, Administration[6]
TIA=0.04*TCI10
                                                                            395
Interest Rate[3]
i
                                                                           0.07
Equipment Life[3] (years) 
n
                                                                             10
Capital Recovery Factor[6]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[6]
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 Costs

Table B.8 Total Capital Investment and Total Annualized Cost Estimate for pH Transmitter
                                   Component
                                  Equation[1]
                                   Cost ($)
Capital and Other Initial Costs
 
 
Planning[2, 3]
PL
                                                                          3,377
pH Transmitter and Sensor[4] ($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 Reporting[7]
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 Factor[5]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[5]
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 Costs

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 Transmitter[2]
                                                                            662
Eutech Instruments pH 500 1/4 DIN pH/ORP Transmitter[3]
                                                                            349
`+GF+ Signet pH/ORP Transmitter - WU-56560-18 Field Mount[4]
                                                                            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") Diameter[2]
                                                                            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

Table B.11 Total Capital Investment and Total Annualized Cost Estimate for Relative Humidity Transmitter
                                   Component
                                  Equation[1]
                                   Cost ($)
Capital and Other Initial Costs
 
 
Planning[2, 3]
PL
                                                                          3,377
Relative Humidity  Transmitter and Sensor[4] ($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 Reporting[7]
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 Factor[5]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[5]
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 Costs

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 output[2]
                                                                           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

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
 
 
Planning[2, 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 Factor[6]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[6]
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 Costs for Monthly FID Monitoring 

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
 
 
Planning[2, 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 Factor[6]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[6]
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 Costs for Weekly FID Monitoring

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
 
 
Planning[2, 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 Factor[6]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[6]
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 Costs for Daily FID Monitoring

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
1.16.1 1 - Vendor cost information provided by EPA

Table B.17 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 

Table B.18 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 Factor[7]
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

Table B.19 Total Capital Investment and Total Annualized Cost Estimate for Car-Seal
                                   Component
                                  Equation[1]
                                   Cost ($)
Capital and Other Initial Costs
 
 
Lock, Key, Chain[2] ($2011)
PEC11
                                                                             97
Freight and Sales Tax[3] 
F&ST=PEC11*.08
                                                                              8
Installation[4]
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, Administration[3]
TIA=0.04*TCI11
                                                                              6
Interest Rate[6]
i
                                                                           0.07
Equipment Life (years)[6]
n
                                                                             10
Capital Recovery Factor[3]
CRF=(i*(1+i)[n])/((1+i)[n]-1)
                                                                           0.14
Capital Recovery[3]
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. Copyright 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 Costs

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

Table B.20 Cost Data for Car-Seal Equipment

Car-Seal Cost Equipment
                                 Cost ($2011)
Lock - MK Covered Brass 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-Padlock-5UKK1?Pid=search - Accessed 9/23/11
2 - http://www.acehardwaresuperstore.com/3364-tenso-chain/78264.html - Accessed 9/23/11