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### V

GMF1 6OM1 1 MC1 10 P1 6EM1 OP1 0.5ACSS 20000 GMF2 1 OM2 2 MC2 1 P2 EM2 1 OP2 1 BCSS 20000 GMF3 4OM3 10 MC3 8 P3 EM3 4 OP3 2 DAS 4000 GMF4 8OM4 5 MC4 2.5 P412EM4 12 OP4 25 M6 28,000 GMF5 16OM5 20 MC5 100 P512EM5 20 OP5 5V11 30 GMF6 40OM6 16 MC6 2 EM6 OP6 250 V12 0.6 GMF7 20OM7 6 MC7 4 EM7 OP7 10 V13 200 GMF8 30OM8 50 MC8 EM8 365 OP8 3V14 100 GMF9 OM9 MC9 200 EM9 700 OP9 4 V15 0 GMF10 2OM10 MC10 5 EM101200 OP10 V21 18 GMF11 3OM11 4 MC11 24 EM11 300 OP11 500 V22 0.6 GMF12 80 MC12 500 EM124000 OP12 100 V23 200 GMF13 10 MC13 6 EM13 OP13 40 V24 75 GMF14 75 MC14 50 EM14 200 OP14 50 V25 0 GMF15 5 MC15 20 EM151000 OP15 6V41 27 GMF16 48 MC162,800 EM16 3 OP16 20 V42 2 GMF17 60 MC17 EM17 OP17 0.25V43 600 GMF18 1.5 MC18 12 OP18 15V44 125 GMF19 15 MC19 25 OP19 16V45 0.15 GMF20 12 MC20 OP20 V51 21 MC21 OP21 0.05V52 2 MC22 OP22 12 V53 50 MC23 3.5 OP23 8V54 110 MC24 30 OP24 2.5V55 0.15 MC25 0.4 OP25 200 W10 10440 MC26 0.2 OP260.3811 W11 12390 OP27 24 W12 7890 MC28 8 OP28 3500 W13 18000 MC29 75 OP29 1.5W7 25000 MC30 32 OP30 3.5W8 8490 MC31 40 OP31 W9 12500 OP32 600 W16 5860 MC33 125 OP33 1000 W20 MC34 OP34 0.25 W18 10200 MC3515000 OP35 32 M9 MC36 850 OP36 15000 PM (beta) 56000

Page 1F

FF1P 0.8 FF1CC FF1PS FF1QA FF1E 1.2 FF1SF 2 FFOP1 0 FF2P FF2CC 0 FF2PS FF2QA 0 FF2E 0.933 FF2SF FFOP2 0.8 FF3P 0 FF3CC FF3PS 1 FF3QA 0.85 FF3E FF3SF 0.75 FFOP3 FF4P FF4CC 1 FF4PS 1 FF4QA 0.925 FF4E FF4SF FFOP4 0 FF5P 0.88 FF5CC 1 FF5PS FF5QA FF5E FF5SF FFOP5 0 FF6P 1 FF6CC 0 FF6PS 0.85 FF6QA FF6E 0.96 FF6SF 0 FFOP6 FF7P 1 FF7CC 0 FF7PS FF7QA FF7E FF7SF 1 FFOP7 0.6 FF8P 1.2 FF8CC 0.6 FF8PS FF8QA FF8E FF8SF FFOP8 0.75 FF9P FF9CC FF9PS 0 FF9QA 0.85 FF9E FFOP9 FF10P 1.3 FF10CC 0.9 FF10PS 0 FF10QA FF10E 0.82 FF10SF 0 FFOP10 1 FF11P 0 FF11CC 0 FF11PS FF11QA 0.8 FF11E 0 FF11SF 0 FFOP11 0.8 FF12P FF12CC 0 FF12PS 0.76 FF12QA FF12E FFOP12 0.9 FF13P 0.84 FF13CC 0.95 FF13PS 0.5 FF13QA FF13E 0 FFOP13 0.85 FF14CC 0 FF14PS 1.9 FF14QA FF14E FF14SF 1 FFOP14 1 FF15CC FF15PS FF15QA FF15E FF15SF 1 FFOP15 FF16CC FF16PS 2 FF16E FF16SF 1 FFOP16 0.8 FF17CC 0.8 FF17PS 0 FF17E FF17SF FFOP17 FF18CC FF18PS FF18E FFOP18 FF19CC 0 FF19PS 0.7 FF19E 1.2 FFOP19 2.7 FF20CC FF20PS FF20E 20390 FFOP20 2.25 FF21CC 0 FF21PS FF21E FF-2BL FFOP21 1.95 FF22CC FF22PS 0.75 FF22E FF-1BL 0 FFOP22 2.1 FF24CC 0.9 FF23PS 0.8 FF23E 1 FF0BL 0.00 FFOP23 FF25CC 0 FFEP1 0.76 FF1BL 0 FFOP24 160 Y19 1 FF40E 1.2 FF2BL 0 FFOP25 0 Y18 -0.6667 Z18 1 FF41E FF3BL 0 FFOP26 6 Y17 -0.6 Z17 1 FF4BL FFOP27 0 Y16 -0.5 Z16 1 Z16a 1.000 Z16b 1 FF50E 0 FF5BL FFOP28 6 Y15 -0.5 Z15 1 FF51E FF6BL FFOP29 2 Y7a (all monitors) -1 Z7a 0 FF7BL 0.70 FFOP30 0 Y7b (monitors and BLD) -1 Z7b 0 FF60E 0 FF8BL 0.800 FFOP31 2 Y19 (gas analyzers and PM) -0.75 Z19 1 For FAT: -0.75 -1 FF70E 0 FF9BL FFOP32 4 Y22 opacity and flow -1 Z22 0 1 0 FF80E 0 FF10BL FFOP33 0 Y21 gas & PM extractives 0 Z21 0 FF81E 0 FF11BL 0.7 FFOP34 Y21a -0.5 Z21a 1 FF12BL 1 FFOP35 Y20 -1 Z20 0 FF90E 1 FF13BL 0 FFOP36 0 Y31 gas after control and PM 0 FF91E 0.1 FF14BL 1 FFOP37 0 FF15BL FFOP38 0 Q8 0 Z100 1 1 FF100E 1.05 FF16BL FFOP39 Q9 1 Z101 0 1.15 FF17BL FFOP40 0.7 Q10 0 FFOP41 0 Q11 0 FFOP42 Q15 0 Z115 0 0 FFOP43 1 Q12 1 FFOP44 0.5 Q16 0 FFOP45 2.25 Q18 0 FFOP46 0.6 FFOP47 0 F24 2 F25 0 FFOP48 0 F25 after w/o Hg 0 Y25 -1 Z25 0 Z25a -0.5 1 FFOP49 0.85 F24 before w/o Hg 2 Z24 1 1 1 0.8 FFOP50 0.4 FFOP51 Q7 0 Z33 0 Z34 0 FFOP52 Q13 0 Z13 0 FFOP53 Q6a (beta) 0 Z54 0 FFOP54 Q6b (ls, insitu) 0 FFOP55 0.9 Q6c (ls, ext) 0 Z40 0 Z56 0 FFOP56 1.9 FFOP7A 0.6

Page 1Costs

Labor Test ODC Planning Review regulations 230 Resolve questions 442 288 Review drawing 240 Inspect source 278 76 Define constraints 691 Write engineering report 1,248

Subtotal 3,130 0 364

Select Equipment Decide on approach 346 Write specifications 1,907 Identify potential bidders 288 Write RFP's 1,382 Copy and mail RFP's 168 80 Respond to bidders 403 50 Review and evaluate proposals 2,861 320 Select winner(s) and negotiate contract(s) 720 Management 3,302 2,624

Subtotal 11,378 0 3,074

Support Facilities Sampling ports 365 Utilities 0 Platforms and ladders 0 Instrument room/shelter 21,000

Subtotal 0 0 21,365

Purchase equipment Opacity monitor 0 PM Monitor 0 non-Hg GAS CEM analyzer(s) 20,390 Sampling system(s) 24,000 PLC 6,800 DAS, including software 2,800 Flow monitors 0 Hg CEMS equipment (analyzer, sampling 0 line, data acquisition, software, etc) Bag leak detection system 0 Taxes and shipping 3,239

Subtotal 57,229

Install Install equipment 2,592 0 Startup equipment 461 6,353 Training 2,212 4,729

Subtotal 5,265 0 11,081

Performance test Select test contractor 768 50 Pretest meeting 363 391 0 Drift tests 108 150 Analyzer RATA or PM ICT 948 9,773 90 Write PST test report 1,268 Review report 161

Subtotal 2,349 11,432 290

Page 1Costs

Labor Test ODC QA/QC plan (O&M plan for BLD) Review needs 173 Hire consultant 653 50 On-site meeting 609 2,790 293 Write draft plan 0 6,019 Review draft plan 369 Write final plan 0 1,699 Get Agency approval 146 Kick-off meeting 792 2,502 364

Subtotal 2,741 13,010 707

Total first costs 24,861 24,442 94,110

Grand total first costs 143,413

Operation, Maintenance, and Repairs Daily checks of COMS/PM/BLD 0 Daily checks of CEMS 3,686 Weekly checks of Beta PM monitors 0 Weekly check of CEMS 2,056 Monthly check of Beta PM/BLD 0 Monthly check of CEMS 1,037 Quarterly check of monitors 0 0 Consumables 1,500

Subtotal 6,780 0 1,500

Annual RATA for gas analyzers Pretest preparation 346 Hire testing team 96 Notify Agency 48 Do RATA 547 9,773 Take corrective action 37 188 Retest 35 214 Write report 869 Certify report and send 96

Subtotal 1,205 11,043 0

PM Monitor RCA (every 3 years) Pretest preparation 0 Hire testing team 0 Notify agency 0 Conduct RCA 0 0 Recalibration calculations 0 0 Write test report 0 0 Certify and send report to agency 0

Subtotal 0 0 0

PM Monitor RRA (annually) Pretest preparation 0 Hire testing team 0 Notify agency 0 Conduct RRA 0 0 Write test report 0 0 Certify and send report to agency 0

Subtotal 0 0 0

Page 2Costs

Labor Test ODC Cylinder Gas Audits (ACA/SVA for PM) Notify Agency 0 Do CGA's and/or ACA/SVA 311 1,125 Take corrective action 225 Retest 121 113 Write, certify, and send report 622 45

Subtotal 1,279 0 1,283

Recordkeeping and reporting Daily data reduction 1,152 Monthly reduction and review 979 Quarterly (semiannual) emissions report 350 160

Subtotal 2,482 0 160

Annual QA & O&M review and update Meeting with plant technicians 1,047 260 Update QA plan (O&M plan) 576 50 Update equipment inventory and repairs 276 2,039 Phone support 438

Subtotal 2,337 0 2,349

Capital recovery (10 years; 7% interest rate) 3,540 3,481 13,401

Annual costs 17,622 14,524 18,693

Total annual costs 50,839

Summary table

First Costs Labor Test ODCs Total Planning 3,130 0 364 3,494 Select Equipment 11,378 0 3,074 14,451 Support Facilities 0 0 21,365 21,365 Purchase CEMS Hardware 0 0 57,229 57,229 Install and Check CEMS 5,265 0 11,081 16,346 Performance Specification Tests 2,349 11,432 290 14,071 QA/QC Plan 2,741 13,010 707 16,457 24,861 24,442 94,110 143,413

Annual Costs Day-to-Day Activities 6,780 0 1,500 8,280 Annual RATA 1,205 11,043 0 12,248 PM Monitor RCA 0 0 0 0 PM Monitor RRA 0 0 0 0 Cylinder Gas Audits (ACA/SVA for PM) 1,279 0 1,283 2,561 Recordkeeping and Reporting 2,482 0 160 2,642 Annual QA & O&M Review and Update 2,337 0 2,349 4,686 Capital Recovery 3,540 3,481 13,401 20,422

Total w/o capital recovery 14,082 11,043 5,292 30,417 Total with capital recovery 17,622 14,524 18,693 50,839

Page 3

### Consultant Description of activities gas PM gas PM gas PM simplecomplex simplecomplex I. Planning A. Review regulations The CEE will determine the applicability of the regulation to the source, review monitoring and reporting requirements stipulated in the regulation, and determine what continuous emission monitoring is needed. 6 1 1 1

B. Resolve questions The CEE begins to deal with the practical application of continuous emission monitoring to the source. Additional discussions with other plant personnel and possibly with the applicable regulatory agency regarding requirements and options are conducted. If the CEE is not located onsite, travel to the site (also related to inspecting the source, noted below) is usually also included. 4 1 1 2

C. Review drawings The CEE will determine what monitoring locations are available and if those locations meet the monitoring location specifications. Access to possible monitoring locations is also evaluated at this time.c 

### 5 5 5 >5

D. Inspect source The CEE and/or a plant technician physically inspect an existing source to verify information from the drawings, determine where sampling lines could run, and identify other issues.c 

### 4 0 0 >4 3 3 3 >3

E. Define specific constraints The CEE will define exhaust gas characteristics that will affect the CEMS (e.g., temperature, moisture, velocity, dirtiness), define stack power requirements, and determine if additional electrical power is needed, determine exact sample port locations, and define any other specific constraints that will affect the monitoring program (e.g., safety

designation). 12 4 2 4

F. Write engineering report The CEE will document findings from the above activities for management and to provide a record trail of the decisions made. 20 4 4 6

II. Select Equipment A. Decide on approach Estimated base-case labor effort for existing sourcesa



### BLDb 

### CEE BLDb 

### Plant technician

### Consultant Description of activities gas PM gas PM gas PM simplecomplex simplecomplex Estimated base-case labor effort for existing sourcesa



### BLDb 

### CEE BLDb 

### Plant technician

The CEE will decide which type of monitor or monitoring system will best meet the goals of the monitoring program. The CEE will need to research and evaluate the advantages and disadvantages of different options and how those advantages and disadvantages apply to the specific source. 6 2 2 2

B. Write specification The CEE will write the specification for the CEMS, and a plant technician will review it. The equipment specification will likely consist of the CEMS technical specifications and sketches and photographs of the monitoring location(s). 40 10 10 20 4 1 1 2

C. Identify

potential bidders The CEE will investigate, perhaps using the internet, to identify vendors and develop a bidders list. 6 4 4 4

D. Write RFPs and guarantees

The CEE will draft instructions to bidders, bid terms and conditions, payment terms, pricing instructions, warranty, and milestones the vendor is expected to meet. 30 10 10 20

E. Copy and mail RFPs The CEE will prepare transmittal letters and have the RFP packages prepared for mailing (either by

regular mail or e-mail). 4.5 3 3 3

F. Respond to bidder's questions The CEE will receive and answer several questions from each of the bidders. 10 6 3 6

G. Review and evaluate proposals The CEE will review the vendor's proposals to detemine which best meets the intent ofthe bid specification and which vendor will likely provide the best and most costeffective CEMS. Issues for negotiation will also be identified. 40 30 20 30

As a default option, the CEE and 2 plant technicians would hold best and final meetings with two vendors 8 8 8 8 16 16 16 16

H. Select winner and negotiate contract

### Consultant Description of activities gas PM gas PM gas PM simplecomplex simplecomplex Estimated base-case labor effort for existing sourcesa



### BLDb 

### CEE BLDb 

### Plant technician

Based on evaluation of the proposal and best and final meetings, the CEE will select the winner. The CEE will also call the winner (and the other bidders). The CEE may also need to finalize various contractual issues such as payment schedules and cancellation charges. 15 12 12 12

I. Management during manufacture and installation As the CEMS is being constructed, the CEE and a plant technician would review and approve vendor drawings, contact the vendor during system development, and provide oversight of installation of support facilities and the CEMS. 40 28 8 8 10 7 4 4

For CEMS consisting of gas analyzers and/or extractive PM monitors, a default option is for the CEE and plant technician to conduct a factory acceptance test at the vendor's facility. 20 20 20 20

V. Installation (existing source) A. Install equipment 150e 

### 32 1 1f 

### B. Startup equipment 32 4 3.2 0.4g 

### C. Training 96h 

### 64i



### VII. QA/QC plan (O&M plan for BLD) A. Review needs 3 1 2 2 B. Hire consultant 15.2 12.8 C. On-site meeting 3.68 2.72 7.365.44 11.048.16 D. Write draft plan 10 10 80 50 E. Review draft plan 6 2 d d 3 2 F. Write final plan 5 5 20 5 G. Get Agency

approval 3.68 2.72 H. Kick-off meeting 7.52 6.08 3 3 7.528.08 4 4 5.644.56

VIII. Operation, maintenance, and repairs A. Daily checks of COMS/PM/BLD, hr/d 0.05 0.25 0.25 B. Daily checks of CEMS, hr/dj 

### 0.5 C. Weekly

checks of Beta PM monitors, hr/wk 0.25 D. Weekly

check of CEMS, hr/wkk 

### 2 E. Monthly check of Beta PM/BLD, hr/monthl 

### 2 1.5 1.5 F. Monthly check of CEMS, hr/monthm 

### 5 G. Quarterly

check of monitors, hr/quarter i

### Consultant Description of activities gas PM gas PM gas PM simplecomplex simplecomplex Estimated base-case labor effort for existing sourcesa



### BLDb 

### CEE BLDb 

### Plant technician

H. Consumables

XIII. Recordkeeping and Reporting A. Daily data reduction, hr/d 0.25 0.5 B. Monthly reduction and review, hr/monthn 

### 1 0.25 4 1 0.25 0.25 C. Quarterly

emissions report, hr/quarter 1 0.5 4 2 C. Semiannual emissions report, hr/six-months 0.5 0.5 1 1

XIV. Annual QA & O&M review and update A. Meeting with plant technicians 5 2 16 4 B. Update QA plan (O&M plan) 15 5 2 2 C. Update equipment inventory and repairs 16 4 2 2 D. Telephone support 18 14 8 8

b

### A simple BLD system has only one sensor. A complex BLD system has multiple sensors.

c

### For a complex BLD system, each additional sensor after the first adds 15 minutes.
d

### Assume cost of management and plant technician review equals 20 percent of the cost for the CEE to prepare the draft plan.

e

### Add 180 hr for a Hg analyzer. f 

### Add 1 hr for each additional sensor.

g

### Labor is for each additional sensor.
h

### Based on 3 days for four technicians.
i

### Based on 2 days for four technicians. j

### Add 0.5 hr/d for a Hg analyzer, regardless of the number of other gas analyzers. k 

### Add 2 hr/wk for a Hg analyzer, regardless of the number of other gas analyzers. l

### Labor for BLD systems is per sensor.

m

### Add 8 hr/month for a Hg analyzer, regardless of the number of other gas analyzers.

n

### 2 hr/quarter for beta gauge PM monitors, and 5 hr/quarter for light scattering PM monitors a

### Base cases for the purposes of this summary are CEMS that consist of either 4 gas analyzers, 1 PM monitor, or a bag leak detection system (except for some annual activities, where the level of effort for a bag leak detection system is per sensor). Travel time is not included in these labor hours. Fractions of an hour (other than 0.05, 0.25, and 0.5) result when the actual baseline scenario used in the model consists of gas analyzers and a PM monitor.

### Summary

of CEMS

Analy zers BEFORE AFTER CO 0 0 SO2 1 0 NOX 0 0 HCl 0 0 Mercury

(and CO2/O2) 0 0 CO2 1 0 O2 0 0 THC 0 0

Monitors OPACITY 0 0 FLOW 0 0 PM (beta gauge) 0 0 PM (light scattering; insitu) 0 0 PM (light scattering; extractive) 0 0

Bag leak detector Number of fabric filters to be monitored= 0 0 Number of sensors= 0 0

Summary

of Costs

First Costs Labor Test ODCs Total Planning 3,130 0 364 3,494 Select Equipment 11,378 0 3,074 14,451 Support Facilities 0 0 21,365 21,365 Purchase CEMS Hardware 0 0 57,229 57,229 Install and Check CEMS 5,265 0 11,081 16,346 Performance Specification Tests 2,349 11,432 290 14,071 QA/QC Plan 2,741 13,010 707 16,457 24,861 24,442 94,110 143,413

Annual Costs Day-to-Day

Activities 6,780 0 1,500 8,280 Annual RATA 1,205 11,043 0 12,248 PM Monitor RCA 0 0 0 0 PM Monitor RRA 0 0 0 0 Cylinder Gas Audits (ACA/SVA for PM) 1,279 0 1,283 2,561 Recordkeeping and Reporting 2,482 0 160 2,642 Annual QA & O&M Review and Update 2,337 0 2,349 4,686 Capital Recovery 3,540 3,481 13,401 20,422

Total w/o capital recovery 14,082 11,043 5,292 30,417 Total with capital recovery 17,622 14,524 18,693 50,839