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

130 Santee Cooper-CrossUnit #3
Control Device Configuraton

Listed (by boiler) in Question 16 (page 17) of the questionnaire
EIA Facility Code Facility Name Boiler ID

130 Santee Cooper-Cross Unit #3

1 6/17/2010 9:30AM 6/17/2010

2 6/17/2010 1:05 PM 6/17/2010

3 6/17/2010 4:25 PM 6/17/2010

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

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

12:35PM 3.18E-03 Dry U.S. EPA Method 316 BDL

4:10 PM 3.34E-03 Dry U.S. EPA Method 316 BDL

7:30 PM 3.46E-03 Dry U.S. EPA Method 316 BDL

Formaldehyde Emission Test Results

Test End Time
Test Method 

Comments lb/mmBtu ppmdv @ 7% O2

[<14.4] 3.85E-06 2.76E-03 4266.45 5680.75

[<15.9] 4.05E-06 2.90E-03 4269.53 5681.25

[<16.4] 4.17E-06 3.00E-03 4260.63 5687.01

Total Heat Input 

(mmBtu/hr)

Calculated Emission Rate Steam Output (1000 

lb/hr)
Fuel Input 

Rate Fuel Type Units of Measure

14.8 14.48 4.91 1304817 130 444.54 bituminous lb/hour

15 14.37 4.91 1324333 129.9 444.58 bituminous lb/hour

15 14.37 4.85 1321233 130 445.03 bituminous lb/hour

Flue Gas 

Temperature 

(F)

Fuel #1 Flue Gas 

Moisture (%)

Flue Gas 

CO2 (%)

Flue Gas 

O2 (%)

Flue Gas Flow 

Rate (dscfm)
Measurement 

Method

boiler efficiency calculation Fuel Input = Kpph

boiler efficiency calculation Fuel Input = Kpph

boiler efficiency calculation Fuel Input = Kpph

Other Supporting Information
EIA Facility Code Facility Name Boiler ID

130 Santee Cooper-Cross Unit #3

1 6/17/2010 10:00AM

2 6/17/2010 1:25PM

3 6/17/2010 4:00PM

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

6/17/2010 12:00PM 6.5 Dry

6/17/2010 3:25PM 7.6 Dry

6/17/2010 6:00PM 10.1 Dry

Test End Date Test End Time

Methane Emission T
Test Method Used Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments lb/mmBtu

U.S. EPA Method 18 ADL 3.45E-03

U.S. EPA Method 18 ADL 4.04E-03

U.S. EPA Method 18 ADL 5.34E-03

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

5.65 4266.45 5680.75 14.8 14.48 4.91 1304817

6.61 4269.53 5681.25 15 14.37 4.91 1324333

8.75 4260.63 5687.01 15 14.37 4.85 1321233

Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(dscfm)

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

130 444.54 bituminous lb/hour boiler efficiency calculation Fuel input=Kpph

129.9 444.58 bituminous lb/hour boiler efficiency calculation Fuel input=Kpph

130 445.03 bituminous lb/hour boiler efficiency calculation Fuel input=Kpph

Other Supporting 

Information

Flue Gas 

Temperat

ure (F)

Fuel #1
EIA Facility Code Facility Name Boiler ID

130 Santee Cooper-Cross Unit #3

1 6/18/2010 9:45 AM

2 6/18/2010 12:30 PM

3 6/18/2010 2:57 PM

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)

6/18/2010 11:45 AM 0.294 Dry

6/18/2010 2:30 PM 0.287 Dry

6/18/2010 4:57 PM 0.283 Dry

Test End Date Test End Time

Total Vapor Phase Mercury Em
 starting in Column "AI"

Test Method Used Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments (lb/mmBtu)

U.S. EPA Method 30B ADL 2.32E-07 4261.95

U.S. EPA Method 30B ADL 2.32E-07 4283.01

U.S. EPA Method 30B ADL 2.23E-07 4271.97

Total Vapor Phase Mercury Emission Test Results

Steam Output 

(1000 lb/hr)
Fuel Input Rate

5679.74 15.2 14.46 4.93 1334850 129.9 444.46

5694.21 15.1 14.36 4.95 1344500 129.1 445.59

5702.08 14.9 14.38 4.91 1342567 130 446.21

Flue Gas 

Temperature (F)

Flue Gas 

CO2 (%)

Flue Gas 

O2 (%)

Flue Gas 

Flow Rate 

(dscfm)

Flue Gas 

Moisture 

(%)

Total Heat 

Input 

(mmBtu/hr)
 QA/QC Documentation

Fuel Type Units of 

Measure

Measurement 

Method Trap ID Section 1 Mass (ng)

Section 2 

Mass (ng)

bituminous lb/hour boiler efficiency calculation Fuel input=Kpph 73876 85 0.9

bituminous lb/hour boiler efficiency calculation Fuel input=Kpph 73536 85 0.2

bituminous lb/hour boiler efficiency calculation Fuel input=Kpph 73895 86 0.7

Fuel #1

Other Supporting Information
Total 

Mass (ng)

Initial 

Spike 

(ng)

Total NonSpike (ng)

Sample 

Volume 

(dscm)

Volume 

Difference (%)

Volume Diff. 

Limit

Breaktrough 

(%)

85.9 20 65.9 0.22546 0.618291493 1.058823529

85.2 20 65.2 0.23133 0.6920849 0.235294118

86.7 20 66.7 0.233713 0.709417106 0.813953488

#DIV/0!

#DIV/0!

#DIV/0!

≤20% of field 

recovery test

Trap #1
Breaktrough 

Limit

Concentration 

(μg/dscm) Trap ID Section 1 Mass

Section 2 

Mass

Total 

Mass

Initial 

Spike

Total NonSpike

0.292291316 73112 66 0.3 66.3 0 66.3

0.281848442 73132 66 1.1 67.1 0 67.1

0.285392768 70203 65 0 65 0 65

#DIV/0!

#DIV/0!

#DIV/0!

≤ 10% of 

Section 1 Hg 

mass for Hg 

conc. >1 

μg/dscm: or ≤ 

20% of Section 
Sample 

Volume

Volume 

Difference (%)

Volume Diff. 

Limit Breaktrough (%) Breaktrough Limit

Concentration 

(μg/dscm)

0.224066 0.672560493 0.454545455 0.29589496

0.229729 0.672560493 1.666666667 0.292083281

0.232055 0.672560493 0 0.280106009

#DIV/0! #DIV/0!

#DIV/0! #DIV/0!

#DIV/0! #DIV/0!

≤ 10% of Section 

1 Hg mass for 

Hg conc. >1 

μg/dscm: or ≤ 

20% of Section 1 

for Hg conc.≤1 

≤20% of field 

recovery test

Trap #2
Abs. diff. RD (%) Limit Crec

R (%) by 

Run Ravg (%) Limit

0.003604 0.612671 0.003604 95.9

0.010235 1.783285 0.010235 88.2

0.005287 0.934884 -0.00529 106.2

#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 

Average 

Recovery, 

between 85 and 

115%

Measured Spike Recovery ( R )

96.76666667

Paired Trap Agreement (RD)
EIA Facility Code Facility Name Boiler ID

130 Santee Cooper-Cross Unit #3

1 6/17/2010 9:30AM 6/17/2010

2 6/17/2010 1:05 PM 6/17/2010

3 6/17/2010 4:25 PM 6/17/2010

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

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

12:35PM 1.42E-02 Dry U.S. EPA Method 26A-Mod

4:10 PM 7.92E-03 Dry U.S. EPA Method 26A-Mod

7:30 PM 7.92E-03 Dry U.S. EPA Method 26A-Mod

Test End Time

Hydrogen Cyanide Emission Test Results
Data Flag (ADL, 

BDL, DDL)

Test Method 

Comments

BDL [<57.7] 1.50E-05 4266.45 5680.75 15.6 14.48

BDL [<37.7] 9.58E-06 4269.53 5681.25 12.8 14.37

BDL [<37.4] 9.54E-06 4260.63 5687.01 15.3 14.37

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

4.91 1294800 127.3 469.17 bituminous lb/hour boiler efficiency calculation

4.91 1355717 127.9 469.02 bituminous lb/hour boiler efficiency calculation

4.85 1312350 127.9 470.10 bituminous lb/hour boiler efficiency calculation

Flue Gas 

Flow Rate 

(dscfm)

Flue Gas 

Temperature 

(F)

Fuel #1 Flue Gas 

O2 (%)
Fuel Input = Kpph

Fuel Input = Kpph

Fuel Input = Kpph

Other Supporting Information
EIA Facility Code Facility Name Boiler ID

130 Santee Cooper-Cross Unit #3

1 6/18/2010 8:20AM

2 6/18/2010 12:45 PM

3 6/18/2010 5:05PM

Run Number Test Start Date Test Start Time
Total Dissolved Solids 

(mg solids/liter)

Total Suspended Solids 

(mg solids/liter)

6/18/2010 12:25PM 14600 213000

6/18/2010 4:50PM 11300 240000

6/18/2010 9:10PM 28600 7440

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

BDL, DDL)

Standard Methods of the Examination of Water and Wastewater Method 2540BADL

Standard Methods of the Examination of Water and Wastewater Method 2540BADL

Standard Methods of the Examination of Water and Wastewater Method 2540BADL

Constisuent Emission Test Results
Test Method Comments Fuel Input Rate

4261.95 5679.74 1334850 129.9 444.46

4283.01 5694.21 1344500 129.1 445.59

4271.97 5702.08 1342567 130 446.21

Steam Output 

(1000 lb/hr)

Total Heat Input 

(mmBtu/hr)

Flue Gas 

Temperat

ure (F)

Flue Gas 

Flow Rate 

(dscfm)
Fuel Type Units of 

Measure

Measurement 

Method

bituminous lb/hour boiler efficiency calculation Fuel Input = Kpph

bituminous lb/hour boiler efficiency calculation Fuel Input = Kpph

bituminous lb/hour boiler efficiency calculation Fuel Input = Kpph

Other Supporting Information

Fuel #1