Instructions for filling in the Emission Test Template

This Information Collection Request (ICR) spreadsheet is intended to collect information about emission data fro

fuel burning power plants and which test methods were used to do so for cases where the test methods are not 

supported by the Electronic Reporting Tool (ERT). This spreadsheet should only be used if the method is not in t

if you do not have access to a lab which performs methods that are in the ERT. You must complete at least 3 se

runs or sampling events for each of the requested constituents. This spreadsheet is intended to be used for one 

one facility. Data for multiple boilers should be handled by using separate copies of this spreadsheet.

yellow are required. All cells that are shaded in green are populated using drop-down lists. You do not need to 

cells shaded in gray, as they are automatically populated from the Boiler Information worksheet. 

resulting spreadsheet with the following naming convention: [FacilityID]_Unit_[BoilerID]_EmisTestMethods.xls 

(example: 8100_Unit_2_EmisTestMethods.xls).

Please refer to the following steps when using these spreadsheets.

Boiler Information Worksheet

1. Please enter the EIA Facility Code, Facility Name and Boiler ID of your boiler on the Boiler Information worksh

2. Please enter the control device configuration.

Emission Data Worksheets

The emission data worksheets are provided for each constituent or constituent family required for this analysis. 

spreadsheet, you must enter boiler operating information during sampling, fuel input information, and emission 

results. There are generally 1 to 3 emission test results records to be entered depending on the constituent or c

family. For example, CO only requires 1 record with 3 sample events, while Mercury requires that you enter bot

Hg+2, or if the Ontario-Hydro Method was used, you would need to enter Hg0, HgP, and Hg

Volatile Organic HAP and Speciated Semi-Volatile Organic HAP worksheets allow you to use a drop

Constituent field to define as many records as needed to record each HAP that you have results for. General ins

follow for these worksheets:

Boiler Operation Information

1. Please provide the values of all requested parameters for each of test run/sample.

2. Please provide any other supporting information or comments in the Other Supporting Information field.

Fuel Information

1. Please enter what types of fuel are being used in your boiler using the drop-downs in the Fuel Type Selection 

You may enter up to 4 fuel types. If you are not burning one or more of the fuel types entered in one or more sa

then enter an input rate of zero. 

2. Please enter the unit of measure using the drop down provided.

3. Please enter the test method used to determine the fuel input rate.

4. Please provide any other information that you feel may be important in the Other Supporting Information fie

Emission Data
1. Some constituents ask for the emission rate results of each run in two different units of measure, while other

If emission rate results are requested in two different units of measure (ex. lb/MMBtu (Pounds per million BTU) 

ppmvd @ 7% O2(parts per million by volume dry basis at 7 percent oxygen)), you are required to provide both.

2. Please provide the test method used. This may or may not match the example given in the Test Method Used 

Please ensure that the name includes the owning organization of the test method (ex. U.S. EPA Method 0010).

3. Please provide any other information that you feel may be important in the Other Supporting Information fie

4. If data sheets and QA/QC documentation tables are provided for the test method you are entering data for p

enter these data.
nformation about emission data from fossil 

ses where the test methods are not currently 

nly be used if the method is not in the ERT or 

T. You must complete at least 3 separate 

sheet is intended to be used for one boiler of 

copies of this spreadsheet. Fields shaded in 

down lists. You do not need to populate 

rmation worksheet. Please name each 

nit_[BoilerID]_EmisTestMethods.xls 

ler on the Boiler Information worksheet. 

ent family required for this analysis. On each 

fuel input information, and emission test 

d depending on the constituent or constituent 

Mercury requires that you enter both Hg0 and 

, HgP, and Hg+2. However, both the Speciated 

low you to use a drop-down provided in the 

at you have results for. General instructions 

er Supporting Information field.

downs in the Fuel Type Selection field. 

fuel types entered in one or more samples, 

he Other Supporting Information field.
erent units of measure, while others do not. 

b/MMBtu (Pounds per million BTU) and 

, you are required to provide both.

mple given in the Test Method Used field. 

ethod (ex. U.S. EPA Method 0010).

he Other Supporting Information field.

 method you are entering data for please also 
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB
Control Device Configuraton

Listed (by boiler) in the Configuration Order Section of the Facility Unit Configurations Section of the Electronic ICR
lectronic ICR
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

CO data provided in CEM spreadsheet

Run Number Test Start Date Test Start Time
Measured Value (ppm)

Test End Date Test End Time
Basis (Wet or Dry) Test Method Used Data Flag (ADL, BDL, DDL)

CO Emission Test Results
Test Method Comments lb/mmBtu ppmdv @ 7% O2

Calculated Emission Rate
Steam Output (1000 lb/hr) Total Heat Input 

(mmBtu/hr) Flue Gas Moisture (%)
Flue Gas CO2

 (%) Flue Gas O2 (%) Flue Gas Flow Rate (scfm)
Fuel Input Rate Fuel Type

Flue Gas Temperature (F)

Fuel #1
Units of Measure Measurement Method Fuel Input Rate

Fuel #1
Fuel Type Units of Measure Measurement Method

Fuel #2
Fuel Input Rate Fuel Type Units of Measure

Fuel #3
Measurement Method Fuel Input Rate Fuel Type

Fuel #4
Units of Measure Measurement Method

Fuel #4

Other Supporting 

Information
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

1 5/11/2010 8:53 5/11/2010

2 5/11/2010 12:22 5/11/2010

3 5/11/2010 15:33 5/11/2010

Run Number Test Start Date Test Start Time Test End Date
Measured Value (ug) Basis (Wet or Dry) Test Method Used 

10:53 9.9 Wet U.S. EPA Method 0011

14:22 8.9 Wet U.S. EPA Method 0011

17:28 9.8 Wet U.S. EPA Method 0011

Test End Time

Formaldehyde Emission Test Results
Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments lb/mmBtu ppmdv @ 7% O2

BDL 0.000002 0.6214 780

BDL 0.000002 0.5463 804

BDL 0.000002 0.5891 802

sion Test Results Calculated Emission Rate Steam Output (1000 

lb/hr)
Fuel Input 

Rate

1060 8.2 13.3 5.4 245870 314 86000

1004 9 13.5 5.2 242223 309 88000

1068 8.1 13.4 5.2 240510 322 87100

Total Heat Input 

(mmBtu/hr)

Flue Gas 

Moisture (%)

Flue Gas 

CO2 (%)

Flue Gas 

O2 (%)

Flue Gas Flow 

Rate (scfm)

Flue Gas 

Temperature 

(F)
Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate

bituminous lb/hour Other

bituminous lb/hour Other

bituminous lb/hour Other

Fuel #1 Fuel #2
Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #3 Fuel #4
Other Supporting Information
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

1 5/11/2010 11:15

2 5/11/2010 13:30

3 5/11/2010 15:45

Run Number Test Start Date Test Start Time
Measured Value (ppm) Basis (Wet or Dry)

5/11/2010 13:15 1.1 Wet

5/11/2010 15:30 1.1 Wet

5/11/2010 17:45 1.1 Wet

Methane Emission T

Test End Date Test End Time
Test Method Used Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments lb/mmBtu

U.S. EPA Method 18 BDL 0.001615

U.S. EPA Method 18 BDL 0.001605

U.S. EPA Method 18 BDL 0.001595

Methane Emission Test Results Calculated Emission Rate
ppmdv @ 7% O2

0.9616 801 1008.2 13.5 5.27 16846330

0.9556 803 1073.9 13.5 5.15 16873780

0.9497 802 1070.3 13.4 5.19 16823670

Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(dscfh)

lated Emission Rate

Steam Output 

(1000 lb/hr)

Total Heat 

Input 

(mmBtu/hr)

Flue Gas 

Moisture 

(%)

Flue Gas 

CO2 (%)
Fuel 

Input 

Rate

Fuel Type Units of 

Measure

Measurement 

Method

Fuel 

Input 

Rate

Fuel Type Units of 

Measure

322 88200 bituminous lb/hour

323 87800 bituminous lb/hour

322 87300 bituminous lb/hour

Flue Gas 

Temperat

ure (F)

Fuel #1 Fuel #2
Measurement 

Method

Fuel 

Input 

Rate

Fuel Type Units of 

Measure

Measurement 

Method

Fuel 

Input 

Rate

Fuel Type Units of 

Measure

Fuel #3 Fuel #4
Measurement 

Method

Other Supporting 

Information
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

SO2 data provided in CEM spreadsheet 

Run Number Test Start Date Test Start Time Test End Date
Measured Value 

(ppm) Basis (Wet or Dry) Test Method Used 

SO2 Emission Test Results

Test End Time
Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments lb/mmBtu ppmdv @ 7% O

2

Calculated Emission Rate Steam Output 

(1000 lb/hr)
Fuel Input 

Rate Fuel Type

Flue Gas 

Temperature 

(F)

Fuel #1 Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(scfm)

Total Heat 

Input 

(mmBtu/hr)

Flue Gas 

Moisture 

(%)

Flue Gas 

CO2 (%)
Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type

Fuel #1 Fuel #2 Fuel #3
Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #3 Fuel #4
Other Supporting Information
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

1 5/12/2010 12:00

2 5/12/2010 15:15

3 5/13/2010 10:09

Run Number Test Start Date Test Start Time
Please note QA/QC documentation starting in Column "AI"

Measured Value 

(μg/dscm) Basis (Wet or Dry)

5/12/2010 14:00 Wet

5/12/2010 17:15 Wet

5/13/2010 12:09 Wet

Test End Date Test End Time

Total Vapor Phase Mercury Em
 starting in Column "AI"

Test Method Used Data Flag (ADL, 

BDL, DDL)

lbs/mmBtu 

Sample A

(lb/mmBtu) 

Sample B

U.S. EPA Method 30B ADL 1.82507E-08 1.83492E-08 801

U.S. EPA Method 30B ADL 1.92735E-08 2.1897E-08 803

U.S. EPA Method 30B ADL 1.47747E-08 2.16411E-08 791

Steam Output 

(1000 lb/hr)

Total Vapor Phase Mercury Emission Test Results
Fuel Input Rate

1086 13.6 16536730 324 88700

1093 13.7 16629820 324 89200

1070 13.8 16171890 318 87400

Total Heat 

Input 

(mmBtu/hr)

Flue Gas 

CO2 (%)

Flue Gas 

Moisture 

(%)

Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(dscfh)

Flue Gas 

Temperature (F)
Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate

bituminous lb/hour Other

bituminous lb/hour Other

anthracite lb/hour Other

Fuel #1 Fuel #2
Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #3 Fuel #4
 QA/QC Documentation

Trap ID Section 1 

Mass (ng)

Section 2 

Mass (ng)

Total 

Mass (ng)

Initial 

Spike 

(ng)

Total NonSpike (ng)

65900 6.955 0.6 7.554 0 7.554

65852 8.085 0.515 8.6 0 8.6

65897 5.757 0.793 6.55 0 6.55

Other Supporting Information
Sample 

Volume 

(dscm)

Volume 

Difference (%)

Volume Diff. 

Limit

Breaktrough 

(%)

Breaktrough 

Limit

Concentration 

(μg/dscm) Trap ID

252.174 0.823 8.626887132 2.99555E-05 65727

271.857 0.045 6.369820656 3.16343E-05 65734

270.101 1.832 13.77453535 2.42502E-05 65589

#DIV/0! #DIV/0!

#DIV/0! #DIV/0!

#DIV/0! #DIV/0!

≤20% of field 

recovery test

≤ 10% of 

Section 1 Hg 

mass for Hg 

conc. >1 

μg/dscm: or ≤ 

20% of Section 

Trap #1
Section 1 

Mass

Section 2 

Mass

Total 

Mass

Initial 

Spike

Total NonSpikeSample 

Volume

Volume 

Difference (%)

Volume Diff. 

Limit

56.887 0.683 57.57 50 7.57 251.351 0.823

59.29 0.479 59.769 50 9.769 271.812 0.045

58.722 0.807 59.529 50 9.529 268.269 1.832 ≤20% of field 

recovery test

Trap #2
Breaktrough (%) Breaktrough 

Limit

Concentration 

(μg/dscm) Abs. diff. RD (%) Limit Crec

1.200625802 3.01172E-05 1.62E-07 0.269239 50

0.807893405 3.59403E-05 4.31E-06 6.372226 51.1

1.374271993 3.55203E-05 1.13E-05 18.85567 53

#DIV/0! #DIV/0! #DIV/0! #DIV/0!

#DIV/0! #DIV/0! #DIV/0! #DIV/0!

#DIV/0! #DIV/0! #DIV/0! #DIV/0!

≥10 % RD mass 

for Hg conc. >1 

μg/dscm: or 

≤20% RD or ≤0.2 

μg/dscm abs.diff. 

for Hg conc. ≤1 

≤ 10% of Section 

1 Hg mass for 

Hg conc. >1 

μg/dscm: or ≤ 

20% of Section 1 

for Hg conc.≤1 

Paired Trap Agreement (RD) Measured Spik
R (%) by 

Run Ravg (%) Limit

100

102.3

106

Average 

Recovery, 

between 85 and 

115%

Measured Spike Recovery ( R )

102.7666667
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

Run Number Test Start Date Test Start Time
Measured Hg

0

 Value 

(μg/dscm)

Measured Hg+2 Value 

(μg/dscm)

Test End Date Test End Time
Measured HgP

 Value 

(μg/dscm)

Basis (Wet or Dry) Test Method Used Data Flag (ADL, BDL, DDL)

Total Vapor Phase Mercury Emission Test Results
Test Method 

Comments

Total Mercury 

(lb/mmBtu)

Flue Gas 

CO

2

 (%)

Steam Output 

(1000 lb/hr)

Total Heat 

Input 

(mmBtu/hr)

Flue Gas 

Moisture (%)
Fuel Input Rate Fuel Type Units of 

Measure

Measurement 

Method

Fuel #1 Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(scfm)

Flue Gas 

Temperature 

(F)
Fuel Input Rate Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #2 Fuel #3
Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Other Supporting Information

Fuel #4
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

Speciated Volatile Organic HAP Emission Data

Carbon disulfide 1 5/1/2010

Carbon disulfide 1 5/1/2010

Carbon disulfide 1 5/1/2010

Carbon disulfide 2 5/1/2010

Carbon disulfide 2 5/1/2010

Carbon disulfide 2 5/1/2010

Carbon disulfide 3 5/2/2010

Carbon disulfide 3 5/2/2010

Carbon disulfide 3 5/2/2010

Compound 

(use drop down to define for as many 

rows as needed)

Run Number Test Start Date







NOT REQUIRED

Note: Each run should include a value for each fraction and the total for each pollutant.

Fraction Measured Value 

(ppm)

10:00 AM 5/1/2010 12:00 PM Front Half*

10:00 AM 5/1/2010 12:00 PM Back Half**

10:00 AM 5/1/2010 12:00 PM Total

2:00 PM 5/1/2010 5:00 PM Front Half*

2:00 PM 5/1/2010 5:00 PM Back Half**

2:00 PM 5/1/2010 5:00 PM Total

10:00 AM 5/2/2010 12:00 PM Front Half*

10:00 AM 5/2/2010 12:00 PM Back Half**

10:00 AM 5/2/2010 12:00 PM Total

Front Half*

Back Half**

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Test Start Time Test End Date Test End Time
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Total

Front Half*

Back Half**

Total
Footnotes:

* Front half fraction contains filter, cyclone, and cartridge

** Back half fraction contains condensate, solvent, impingers

Basis Test Method Used Data Flag (ADL, BDL, DDL)

Volatile Organic HAP Emission Test Results







Test Method 

Comments lb/mmBtu ppmdv @ 7% O2

Calculated Emission Rate Steam Output 

(1000 lb/hr)

Total Heat 

Input 

(mmBtu/hr)







Fuel Input 

Rate Fuel Type

Flue Gas 

Temperature (F)

Fuel #1 Flue Gas 

Moisture (%)

Flue Gas 

CO2 (%)

Flue Gas 

O2 (%)

Flue Gas Flow 

Rate (scfm)







Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type

Fuel #1 Fuel #2 Fuel #3







Units of 

Measure

Measurement 

Method Fuel Input Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #3 Fuel #4







Other Supporting Information







EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

Speciated Semi-Volatile Organic HAP Emission Data

Acenaphthene 1 5/1/2010

Acenaphthene 1 5/1/2010

Acenaphthene 1 5/1/2010

Acenaphthene 1 5/1/2010

Acenaphthene 2 5/1/2010

Acenaphthene 2 5/1/2010

Acenaphthene 2 5/1/2010

Acenaphthene 3 5/1/2010

Acenaphthene 3 5/2/2010

Acenaphthene 3 5/2/2010

Acenaphthene 3 5/2/2010

Compound 

(use drop down to define for as 

many rows as needed)

Run Number Test Start Date







NOT REQUIRED

Note: Each run should include a value for each fraction and the total for each pollutant.

10:00 AM 5/1/2010 12:00 PM

10:00 AM 5/1/2010 12:00 PM

10:00 AM 5/1/2010 12:00 PM

10:00 AM 5/1/2010 12:00 PM

2:00 PM 5/1/2010 5:00 PM

2:00 PM 5/1/2010 5:00 PM

2:00 PM 5/1/2010 5:00 PM

2:00 PM 5/1/2010 5:00 PM

10:00 AM 5/2/2010 12:00 PM

10:00 AM 5/2/2010 12:00 PM

10:00 AM 5/2/2010 12:00 PM

Test Start Time Test End Date Test End Time







Footnotes:

* Front Half Composite contains particulate filter, front half of t

** Back Half Composite contains XAD-2 resin tube, back half o

*** Condensate Composite contains condensate and Impinger c

Fraction Measured Value (ppm) Basis (Wet or Dry)

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**
Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*
Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite
Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***
Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**
Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*
Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite
Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite

Front Half Composite*

Back Half Composite**

Condensate Composite***

Total Composite
osite contains particulate filter, front half of the filter holder, and probe solvent rinses

osite contains XAD-2 resin tube, back half of the filter holder, and coil condenser solvent rinses

posite contains condensate and Impinger contents and the glassware solvent rinses

Test Method Used Data Flag (ADL, BDL, DDL)

Semi-Volatile Organic HAP Emission Test Results







Test Method 

Comments lb/mmBtu ppmdv @ 7% O

2

Calculated Emission Rate Steam Output 

(1000 lb/hr)

Total Heat 

Input 

(mmBtu/hr)







Fuel Input 

Rate Fuel Type Units of Measure

Fuel #1 Flue Gas 

CO2 (%)

Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(scfm)

Flue Gas 

Temperature 

(F)

Flue Gas 

Moisture 

(%)







Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Fuel #2 Fuel #3







Measurement 

Method Fuel Input Rate Fuel Type Units of Measure

Measurement 

Method

Other Supporting Information

Fuel #4







EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

1 5/11/2010 8:51 5/11/2010

2 5/11/2010 12:22 5/11/2010

3 5/11/2010 15:45 5/11/2010

Run Number Test Start Date Test Start Time Test End Date
Measured Value (ug) Basis (Wet or Dry)

11:43 55 Wet

15:14 57 Wet

18:37 59.7 Wet

Test End Time
Test Method Used Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments

U.S. EPA Conditional Test Method 033 (CTM-033) BDL 0.000009

U.S. EPA Conditional Test Method 033 (CTM-033) BDL 0.000009

U.S. EPA Conditional Test Method 033 (CTM-033) BDL 0.000009

Calculated 

Emission Rate 

(lb/mmBtu)

Hydrogen Cyanide Emission Test Results
Fuel Input 

Rate

782 1064 9.67 13.4 5.24 243429 312.8 86900

804 1026 9.3 13.5 5.17 238673 318.8 87900

805 1075 9.46 13.5 5.17 252861 318.4 87700

Flue Gas 

Temperature 

(F)

Flue Gas 

Moisture 

(%)

Flue Gas 

CO2 (%)

Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(dscfm)

Steam Output 

(1000 lb/hr)

Total Heat 

Input 

(mmBtu/hr)
Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method Fuel Input Rate

bituminous lb/hour Other

bituminous lb/hour Other

bituminous lb/hour Other

Fuel #1 Fuel #2
Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #3 Fuel #4
dedicated weight belt for coal 

Other Supporting Information
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

1 5/11/2010 8:51 5/11/2010

2 5/11/2010 12:22 5/11/2010

3 5/11/2010 15:45 5/11/2010

Run Number Test Start Date Test Start Time Test End Date
Measured Value (ug) Basis (Wet or Dry) Test Method Used 

11:43 312613 Wet U.S. EPA Method 26A-Mod

15:14 238567 Wet U.S. EPA Method 26A-Mod

18:37 367184 Wet U.S. EPA Method 26A-Mod

Test End Time

Hydrogen Chloride Emission Test Results
Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments

ADL 0.050479 782 1064 9.67 13.4

ADL 0.039739 804 1026 9.3 13.5

ADL 0.057522 805 1075 9.46 13.5

 Test Results

Steam Output 

(1000 lb/hr)

Total Heat 

Input 

(mmBtu/hr)

Calculated 

Emission Rate 

(lb/mmBtu)

Flue Gas 

Moisture 

(%)

Flue Gas 

CO2 (%)
Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate

5.24 243429 312.8 86900 bituminous lb/hour Other

5.17 238673 318.8 87900 bituminous lb/hour Other

5.17 252861 318.4 87700 bituminous lb/hour Other

Flue Gas 

Flow Rate 

(scfm)

Flue Gas 

Temperature 

(F)

Fuel #1 Flue Gas 

O2 (%)
Fuel Type Units of 

Measure

Measurement 

Method Fuel Input Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate

Fuel #2 Fuel #3
Fuel Type Units of 

Measure

Measurement 

Method

Fuel #4

Other Supporting Information
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

1 5/11/2010 8:51 5/11/2010

2 5/11/2010 12:22 5/11/2010

3 5/11/2010 15:45 5/11/2010

Run Number Test Start Date Test Start Time Test End Date
Measured Value (ug) Basis (Wet or Dry) Test Method Used 

11:43 324 Wet U.S. EPA Method 26A-Mod

15:14 336 Wet U.S. EPA Method 26A-Mod

18:37 352 Wet U.S. EPA Method 26A-Mod

Hydrogen Flouride Emission Test Results

Test End Time
Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments

BDL 0.000052 782 1064 9.67

BDL 0.000056 804 1026 9.3

BDL 0.000055 805 1075 9.46

Calculated 

Emission Rate 

(lb/mmBtu)

Flue Gas 

Moisture (%)

Test Results

Steam Output 

(1000 lb/hr)

Total Heat 

Input 

(mmBtu/hr)
Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

13.4 5.24 243429 312.8 86900 bituminous lb/hour Other

13.5 5.17 238673 318.8 87900 bituminous lb/hour Other

13.5 5.17 252861 318.4 87700 bituminous lb/hour Other

Flue Gas 

Temperature 

(F)

Fuel #1 Flue Gas 

CO2 (%)

Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(scfm)
Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method Fuel Input Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #2 Fuel #3
Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #4

Other Supporting Information
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

NOX data provided in CEM spreadsheet

Run Number Test Start Date Test Start Time
Measured NO (ppm) Test End Date Test End Time
Measured NO2

 (ppm) Basis (Wet or Dry) Test Method Used 

NOX Emission Test Results
Data Flag (ADL, BDL, DDL) Test Method Comments (lb/mmBtu)

Total NOX Calculated Emission Rate
ppmdv @ 7% O2

Flue Gas 

O2 (%)

 Calculated Emission Rate Steam Output 

(1000 lb/hr)

Total Heat Input 

(mmBtu/hr)

Flue Gas 

Moisture (%)

Flue Gas 

CO2 (%)
Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate

Flue Gas 

Temperature 

(F)

Flue Gas Fuel #1

Flow Rate 

(scfm)
Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel Input 

Rate

Fuel #2 Fuel #3
Fuel Type Units of 

Measure

Measurement 

Method

Fuel #4

Other Supporting Information
EIA Facility Code Facility Name Boiler ID

10672 Cedar Bay CBB

Run Number Test Start Date Test Start Time
Not applicable 

Total Dissolved Solids 

(mg solids/liter)

Total Suspended Solids 

(mg solids/liter)

Test End Date Test End Time
Test Method Used Data Flag (ADL, 

BDL, DDL)

Constisuent Emission Test Results
Test Method Comments Fuel Input Rate

Flue Gas 

Temperat

ure (F)

Flue Gas 

Flow Rate 

(scfm)

Steam Output 

(1000 lb/hr)

Total Heat Input 

(mmBtu/hr)
Fuel Type Units of 

Measure

Measurement 

Method Fuel Input Rate Fuel Type Units of Measure

Measurement 

Method Fuel Input Rate

Fuel #1 Fuel #2
Fuel Type Units of 

Measure

Measurement 

Method

Fuel Input 

Rate Fuel Type Units of Measure

Measurement 

Method

Fuel #3 Fuel #4
Other Supporting Information
EIA Facility 

Code Facility Name Boiler ID

10672 Cedar Bay CBB

Measured 

Value 

(ppm)

Basis 

(Wet or 

Dry)

1 5/11/2010 11:15 5/11/2010 13:15 0.74 Wet

2 5/11/2010 13:30 5/11/2010 15:30 0.69 Wet

3 5/11/2010 15:45 5/11/2010 17:45 1.01 Wet

Run Number Test Start Date Test Start Time Test End Date Test End Time

Methane Emission Tes
Test Method Used 

Data 

Flag 

(ADL, 

BDL, 

DDL)

Test 

Method 

Comments

lb/mmBtu ppmdv 

@ 7% O2

BDL Method 25A 0.001087 0.6469 801

BDL Method 25A 0.001007 0.5994 803

BDL Method 25A 0.001465 0.872 802

Calculated Emission 

Steam Output (1000 lb/hr)

Methane Emission Test Results
1008.2 13.5 5.27 16846330

1073.9 13.5 5.15 16873780

1070.3 13.4 5.19 16823670

Total Heat Input (mmBtu/hr) Flue Gas Moisture (%) Flue Gas Flow Rate (dscfh) Flue Gas 

CO2 (%)

Flue Gas 

O2 (%)
Fuel 

Input 

Rate

Fuel Type Units of 

Measure

Measure

ment 

Method

Fuel 

Input 

Rate

Fuel 

Type

Units of 

Measure

Measure

ment 

Method

Fuel 

Input 

Rate

322 88200 bituminous lb/hour

323 87800 bituminous lb/hour

322 87300 bituminous lb/hour

Flue Gas Temperature (F)

Fuel #1 Fuel #2
Fuel 

Type

Units of 

Measure

Measure

ment 

Method

Fuel 

Input 

Rate

Fuel 

Type

Units of 

Measure

Measure

ment 

Method

Other Supporting Information

Fuel #3 Fuel #4