Name: Julie Metts, P.E.

Title: Manager- Air Quality

Company: Santee Cooper

Sign Date: 7/28/2010

Name: Craig McKenzie

Title: Senior Project Manager

Company: GEL, Engineering, LLC

Sign Date: 7/28/2010

Permitted Facility Representative / Date Testing Company Representative / Date

Santee Cooper-Cross Unit #4, ICR Section 114 Testing

Final Test Report 

for

/ /

Based on information and belief formed 

after reasonable inquiry, I certify that the 

statements and information in this test 

report are true, accurate, and complete.

I have reviewed all testing details and 

results in this test report and hereby 

certify that the test report is authentic 

and accurate.

Thursday, February 03, 2011 Page 1 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Facility Information:

Santee Cooper - Cross Generating Station U

553 Cross Station Road

Pineville SC 29468

Contact: Julie Metts, P.E.

Phone: 843-761-8000, ext. 4688

Fax: 843-761-4156

Email: jjmetts@santeecooper.com

Testing Company:

GEL Engineering, LLC

2040 Savage Road

Charleston SC 29407

Contact:Craig McKenzie

Phone: 843-769-7378

Fax: 843-769-7197

Email: cam2@gel.com

Air Permit Number:

0420-0030-B04

Permitted Source ID/Name:

Unit 4 Coal Fire Boiler

Permitted Maximum Process Rate: Max. Normal Operation Process Rate:

5400 MMBtu/hr with steam

Target Process Test Rate

5400 MMBtu/hr with steam

Description of the source (including control equipment). Please see the attachments for source or

 process flow diagram:

Coal-Fired Boiler For Electric Generation, LNB, SCR, ESP, & FGD

Industry/SCC/NAIS 221112

Sampling Location Information:

Test Parameter Information:

AFS #: 4501500030 FRS #: 4911

SCC / Description 10100202 External Combustion Boilers - Electric Generation - Bituminous/Subbituminous 

Coal - Pulverized Coal: Dry Bottom (Bituminous Coal) 

The following state and federal regulations that apply to the proposed testing:

Location

Round

Duct

Diam.

Distance from 

upstream dist.

Distance from

downstream dist.

Number of

Traverse Ports

Equiv. 

Diam

Min.Travers 

Points

Rect. Duct 

Length /Width

stk exhaust 336 0 0 0 2790 1056 4 16

Target

Parameter 

Test

Method

Number of

Test Runs

Test Run

Duration

Sample 

Location Points Comments

stk exhaust Carbon Monoxide Method 10 3 120 0

Total organic compounds 

(TOC) as Propane

stk exhaust Method 25A 3 120 0

stk exhaust Hydrogen Chloride Method 26A 3 180 0

stk exhaust Hydrogen Fluoride Method 26A 3 180 0

stk exhaust Cobalt Method 29 3 240 0

Regulation Description Compound Limit Unit

NA 0

Thursday, February 03, 2011 Page 2 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

The following describes any modifications and/or deviations to the applicable test 

methods. If alternative methods were requested, see the attachments for documentation 

of request AND approval, including dates.

NA

stk exhaust Selenium Method 29 3 240 0

stk exhaust Nickel Method 29 3 240 0

stk exhaust Manganese Method 29 3 240 0

stk exhaust Lead Method 29 3 240 0

stk exhaust Cadmium Method 29 3 240 0

stk exhaust Arsenic Method 29 3 240 0

stk exhaust Chromium Method 29 3 240 0

stk exhaust Antimony Method 29 3 240 0

stk exhaust Beryllium Method 29 3 240 0

stk exhaust O2 Method 3A O2 3 180 0

stk exhaust Co2 Method 3A CO2 3 180 0

Organic Condensible 

Particulate

stk exhaust Method 5/OTM-28 3 240 0

stk exhaust Total Particulate Method 5/OTM-28 3 240 0

Inorganic (Aqueous) 

Condensible Part.

stk exhaust Method 5/OTM-28 3 240 0

Thursday, February 03, 2011 Page 3 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Sampling / Stack Data Results Summary

Location stk exhaust - Method 10

Average

Run Number 1 2 3

Test Date 5/26/2010 5/26/2010 5/26/2010

Run Start Time 7:50:00 AM 11:00:00 

AM

1:16:00 PM

Run Finish Time 10:50:00 AM 1:00:00 PM 3:16:00 PM

Carbon Dioxide, % 13.36 13.35 13.38 13.363

Oxygen, % 5.96 5.85 5.87 5.893

Dry Volumetric Flow Rate, dry scfm 1364766.667 1389183.33

3

1389016.667 1,380,988.88

9

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 15.2 14.3 14.8 14.767

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Location stk exhaust - Method 25A

Average

Run Number 1 2 3

Test Date 5/26/2010 5/26/2010 5/26/2010

Run Start Time 7:50:00 AM 11:00:00 

AM

1:16:00 PM

Run Finish Time 9:50:00 AM 1:00:00 PM 3:16:00 PM

Carbon Dioxide, % 13.36 13.35 13.38 13.363

Oxygen, % 5.96 5.85 5.87 5.893

Dry Volumetric Flow Rate, dry scfm 1364766.667 1389183.33

3

1389016.667 1,380,988.88

9

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 15.2 14.3 14.8 14.767

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 03, 2011 Page 4 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Location stk exhaust - Method 26A

Average

Run Number 1 2 3

Test Date 5/26/2010 5/26/2010 5/26/2010

Run Start Time 8:10:00 AM 11:28:00 

AM

2:48:00 PM

Run Finish Time 11:01:15 AM 2:19:15 PM 5:39:15 PM

Net Run Time, minutes 180 180 180

Dry Gas Meter Volume Sampled, dscf 107.569 115.489 114.418 112.492

Moisture Content of Stack Gas, % 15.66 15.50 15.60 15.587

Moisture Saturation at Stack Gas Temperature, % 13.99 14.23 14.23 14.150

Carbon Dioxide, % 13.43 13.34 13.4 13.390

Oxygen, % 5.49 5.85 5.88 5.740

Average Stack Gas Temperature, °F 127.31 127.94 127.94 127.730

Dry Volumetric Flow Rate, dry scfm 1,390,684.0 1,388,747.2 1,376,457.4 1,385,296.20

0

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,790,730.0 1,795,163.4 1,779,277.0 1,788,390.13

3

Percent Isokinetic of Sampling Rate, % 95.8 103.0 103.0 100.600

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 03, 2011 Page 5 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Location stk exhaust - Method 29

Average

Run Number 1 2 3

Test Date 5/25/2010 5/25/2010 5/25/2010

Run Start Time 8:50:00 AM 1:15:00 PM 5:40:00 PM

Run Finish Time 12:35:00 PM 5:00:00 PM 9:25:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 153.908 152.139 154.590 153.546

Moisture Content of Stack Gas, % 14.87 14.35 14.39 14.537

Moisture Saturation at Stack Gas Temperature, % 14.20 13.97 13.99 14.053

Carbon Dioxide, % 13.51 13.4 13.18 13.363

Oxygen, % 5.99 6.01 5.94 5.980

Average Stack Gas Temperature, °F 127.88 127.25 127.31 127.480

Dry Volumetric Flow Rate, dry scfm 1,390,804.4 1,380,817.1 1,403,882.2 1,391,834.56

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,797,010.6 1,777,429.7 1,807,724.7 1,794,055.00

0

Percent Isokinetic of Sampling Rate, % 102.8 102.4 102.3 102.500

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 03, 2011 Page 6 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Location stk exhaust - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 5/25/2010 5/25/2010 5/25/2010

Run Start Time 8:50:00 AM 1:15:00 PM 5:40:00 PM

Run Finish Time 12:35:00 PM 5:00:00 PM 9:25:00 PM

Net Run Time, minutes 240 240 240

Dry Gas Meter Volume Sampled, dscf 153.075 153.495 152.875 153.148

Moisture Content of Stack Gas, % 14.69 14.47 14.14 14.433

Moisture Saturation at Stack Gas Temperature, % 14.35 13.97 14.01 14.110

Carbon Dioxide, % 13.51 13.4 13.18 13.363

Oxygen, % 5.99 6.01 5.94 5.980

Average Stack Gas Temperature, °F 128.25 127.25 127.38 127.627

Dry Volumetric Flow Rate, dry scfm 1,382,650.3 1,393,158.6 1,390,768.6 1,388,859.16

7

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,790,730.0 1,793,316.1 1,791,468.9 1,791,838.33

3

Percent Isokinetic of Sampling Rate, % 102.9 102.4 102.1 102.467

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 03, 2011 Page 7 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Emissions Summary

Location: stk exhaust - Method 10

Compound: Carbon Monoxide

Average

Run 1 2 3

lb/mmBtuO2 1.42E-02 1.37E-02 1.39E-02 0.014

ppm 1.43E+01 1.39E+01 1.41E+01 14.100

ppm@7%O2 1.33E+01 1.28E+01 1.30E+01 13.033

Location: stk exhaust - Method 25A

Compound: Total organic compounds (TOC) as 

Average

Run 1 2 3

Elb/hr 1.23E+01 9.00E+00 1.31E+01 11.467

lb/mmBtuO2 2.05E-03 1.47E-03 2.13E-03 0.002

ppm 1.31E+00 9.43E-01 1.37E+00 1.208

ppm@7%O2 1.22E+00 8.71E-01 1.27E+00 1.120

Location: stk exhaust - Method 26A

Compound: Hydrogen Chloride

Average

RunNumber 1 2 3

Mass_mg 0.908 0.596 1.089 0.864

Elb/hr 1.55E+00 9.48E-01 1.73E+00 1.409

gr/dscf 1.30E-04 7.96E-05 1.47E-04 0.000

lb/mmBtuO2 2.47E-04 1.55E-04 2.86E-04 0.000

ppm 1.97E-01 1.20E-01 2.22E-01 0.180

ppm@7%O2 1.78E-01 1.11E-01 2.05E-01 0.165

Compound: Hydrogen Fluoride

Average

RunNumber 1 2 3

Mass_mg 0.394 0.383 0.39 0.389

Elb/hr 6.74E-01 6.09E-01 6.21E-01 0.635

gr/dscf 5.65E-05 5.12E-05 5.26E-05 0.000

lb/mmBtuO2 1.07E-04 9.93E-05 1.02E-04 0.000

ppm 1.55E-01 1.41E-01 1.45E-01 0.147

ppm@7%O2 1.40E-01 1.30E-01 1.34E-01 0.135

Location: stk exhaust - Method 29

Compound: Antimony

Average

RunNumber 1 2 3

Mass_mg 0.000675 0.00148 0.000728 0.001

Elb/hr 8.07E-04 1.78E-03 8.75E-04 0.001

gr/dscf 6.77E-08 1.50E-07 7.27E-08 0.000

lb/mmBtuO2 1.33E-07 2.94E-07 1.42E-07 0.000

mg/dscm 1.55E-04 3.44E-04 1.66E-04 0.000

ppm 3.06E-05 6.79E-05 3.29E-05 0.000

ppm@7%O2 2.85E-05 6.34E-05 3.06E-05 0.000

Thursday, February 03, 2011 Page 8 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Compound: Arsenic

Average

RunNumber 1 2 3

Mass_mg 0.01843 0.01502 0.02058 0.018

Elb/hr 2.20E-02 1.80E-02 2.47E-02 0.022

gr/dscf 1.85E-06 1.52E-06 2.05E-06 0.000

lb/mmBtuO2 3.62E-06 2.99E-06 4.01E-06 0.000

mg/dscm 4.23E-03 3.49E-03 4.70E-03 0.004

ppm 1.36E-03 1.12E-03 1.51E-03 0.001

ppm@7%O2 1.27E-03 1.05E-03 1.40E-03 0.001

Compound: Beryllium

Average

RunNumber 1 2 3

Mass_mg 0.000054 0.00005 0.00005 0.000

Elb/hr 6.45E-05 6.00E-05 6.01E-05 0.000

gr/dscf 5.41E-09 5.07E-09 4.99E-09 0.000

lb/mmBtuO2 1.06E-08 9.95E-09 9.74E-09 0.000

mg/dscm 1.24E-05 1.16E-05 1.14E-05 0.000

ppm 3.31E-05 3.10E-05 3.05E-05 0.000

ppm@7%O2 3.09E-05 2.89E-05 2.83E-05 0.000

Compound: Cadmium

Average

RunNumber 1 2 3

Mass_mg 0.00055 0.000307 0.00034 0.000

Elb/hr 6.57E-04 3.69E-04 4.08E-04 0.000

gr/dscf 5.51E-08 3.11E-08 3.39E-08 0.000

lb/mmBtuO2 1.08E-07 6.11E-08 6.62E-08 0.000

mg/dscm 1.26E-04 7.13E-05 7.77E-05 0.000

ppm 2.70E-05 1.52E-05 1.66E-05 0.000

ppm@7%O2 2.52E-05 1.42E-05 1.54E-05 0.000

Compound: Chromium

Average

RunNumber 1 2 3

Mass_mg 0.02375 0.04729 0.03167 0.034

Elb/hr 2.84E-02 5.68E-02 3.80E-02 0.041

gr/dscf 2.38E-06 4.80E-06 3.16E-06 0.000

lb/mmBtuO2 4.66E-06 9.41E-06 6.17E-06 0.000

mg/dscm 5.45E-03 1.10E-02 7.24E-03 0.008

ppm 2.52E-03 5.08E-03 3.35E-03 0.004

ppm@7%O2 2.35E-03 4.74E-03 3.11E-03 0.003

Compound: Cobalt

Average

RunNumber 1 2 3

Mass_mg 0.00141 0.00319 0.000551 0.002

Elb/hr 1.69E-03 3.83E-03 6.62E-04 0.002

gr/dscf 1.41E-07 3.24E-07 5.50E-08 0.000

lb/mmBtuO2 2.77E-07 6.35E-07 1.07E-07 0.000

mg/dscm 3.24E-04 7.41E-04 1.26E-04 0.000

ppm 1.32E-04 3.02E-04 5.14E-05 0.000

Thursday, February 03, 2011 Page 9 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

ppm@7%O2 1.23E-04 2.82E-04 4.78E-05 0.000

Compound: Lead

Average

RunNumber 1 2 3

Mass_mg 0.00483 0.00206 0.00509 0.004

Elb/hr 5.77E-03 2.47E-03 6.11E-03 0.005

gr/dscf 4.84E-07 2.09E-07 5.08E-07 0.000

lb/mmBtuO2 9.48E-07 4.10E-07 9.92E-07 0.000

mg/dscm 1.11E-03 4.78E-04 1.16E-03 0.001

ppm 1.29E-04 5.55E-05 1.35E-04 0.000

ppm@7%O2 1.20E-04 5.18E-05 1.25E-04 0.000

Compound: Manganese

Average

RunNumber 1 2 3

Mass_mg 0.1147 0.01305 0.01337 0.047

Elb/hr 1.37E-01 1.57E-02 1.61E-02 0.056

gr/dscf 1.15E-05 1.32E-06 1.33E-06 0.000

lb/mmBtuO2 2.25E-05 2.60E-06 2.61E-06 0.000

mg/dscm 2.63E-02 3.03E-03 3.05E-03 0.011

ppm 1.15E-02 1.33E-03 1.34E-03 0.005

ppm@7%O2 1.07E-02 1.24E-03 1.25E-03 0.004

Compound: Nickel

Average

RunNumber 1 2 3

Mass_mg 0.02041 0.0169 0.01906 0.019

Elb/hr 2.44E-02 2.03E-02 2.29E-02 0.023

gr/dscf 2.05E-06 1.71E-06 1.90E-06 0.000

lb/mmBtuO2 4.01E-06 3.36E-06 3.71E-06 0.000

mg/dscm 4.68E-03 3.92E-03 4.35E-03 0.004

ppm 1.92E-03 1.61E-03 1.78E-03 0.002

ppm@7%O2 1.79E-03 1.50E-03 1.65E-03 0.002

Compound: Selenium

Average

RunNumber 1 2 3

Mass_mg 0.139 0.136 0.2099 0.162

Elb/hr 1.66E-01 1.63E-01 2.52E-01 0.194

gr/dscf 1.39E-05 1.38E-05 2.10E-05 0.000

lb/mmBtuO2 2.73E-05 2.71E-05 4.09E-05 0.000

mg/dscm 3.19E-02 3.16E-02 4.80E-02 0.037

ppm 9.72E-03 9.62E-03 1.46E-02 0.011

ppm@7%O2 9.06E-03 8.98E-03 1.36E-02 0.011

Location: stk exhaust - Method 5/OTM-28

Compound: Inorganic (Aqueous) Condensible Pa

Average

RunNumber 1 2 3

Mass_mg 85.4 77.8 81.2 81.467

Elb/hr 1.02E+02 9.34E+01 9.77E+01 97.700

gr/dscf 8.61E-03 7.82E-03 8.20E-03 0.008

Thursday, February 03, 2011 Page 10 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Process Run Data

lb/mmBtuO2 1.69E-02 1.53E-02 1.60E-02 0.016

Compound: Organic Condensible Particulate

Average

RunNumber 1 2 3

Mass_mg 8.8 9.4 11.8 10.000

Elb/hr 1.05E+01 1.13E+01 1.42E+01 12.000

gr/dscf 8.87E-04 9.45E-04 1.19E-03 0.001

lb/mmBtuO2 1.74E-03 1.85E-03 2.33E-03 0.002

Compound: Total Particulate

Average

RunNumber 1 2 3

Mass_mg 89.7 73.3 32.8 65.267

Elb/hr 1.07E+02 8.80E+01 3.95E+01 78.167

gr/dscf 9.04E-03 7.37E-03 3.31E-03 0.007

lb/mmBtuO2 1.77E-02 1.45E-02 6.46E-03 0.013

Thursday, February 03, 2011 Page 11 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Process Run Data

Run Name Value UOM Comments

Target

Value

1 Feed Rate 469.17 kpph EPA Methods 10, 

25A, 26A; 

5/26/2010; 8:10-

11:15pm

450

1 Heat Input Million Btus/million BTU using O2 5963.4 EPA Methods 10, 

25A, 26A; 

5/26/2010; 8:10-

11:15pm

5400

1 Steam Output 4297.5 kpph EPA Methods 10, 

25A, 26A; 

5/26/2010; 8:10-

11:15pm

4400

1 Gross Electric Output 654.64 MW EPA Methods 10, 

25A, 26A; 

5/26/2010; 8:10-

11:15pm

625

1 Net Electric Output 617.35 MW EPA Methods 10, 

25A, 26A; 

5/26/2010; 8:10-

11:15pm

590

4 Feed Rate 469.02 kpph EPA Methods 10, 

25A, 26A; 

5/26/2010; 11:28-

2:35pm

450

4 Heat Input Million Btus/million BTU using O2 5961.5 EPA Methods 10, 

25A, 26A; 

5/26/2010; 11:28-

2:35pm

5400

4 Steam Output 4294.9 kpph EPA Methods 10, 

25A, 26A; 

5/26/2010; 11:28-

2:35pm

4400

4 Gross Electric Output 654.77 MW EPA Methods 10, 

25A, 26A; 

5/26/2010; 11:28-

2:35pm

625

4 Net Electric Output 617.24 MW EPA Methods 10, 

25A, 26A; 

5/26/2010; 11:28-

2:35pm

590

5 Feed Rate 470.1 kpph EPA Methods 10, 

25A, 26A; 

5/26/2010; 2:48-

5:55pm

450

Thursday, February 03, 2011 Page 12 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

5 Heat Input Million Btus/million BTU using O2 5975.2 EPA Methods 10, 

25A, 26A; 

5/26/2010; 2:48-

5:55pm

5400

5 Steam Output 4293.9 kpph EPA Methods 10, 

25A, 26A; 

5/26/2010; 2:48-

5:55pm

4400

5 Gross Electric Output 654.93 MW EPA Methods 10, 

25A, 26A; 

5/26/2010; 2:48-

5:55pm

625

5 Net Electric Output 617.68 MW EPA Methods 10, 

25A, 26A; 

5/26/2010; 2:48-

5:55pm

590

6 Feed Rate 466.9 kpph EPA Methods 

5/OTM28, 29; 

5/25/2010; 8:50-

12:57pm

450

6 Heat Input Million Btus/million BTU using O2 5934.6 EPA Methods 

5/OTM28, 29; 

5/25/2010; 8:50-

12:57pm

5400

6 Steam Output 4308.7 kpph EPA Methods 

5/OTM28, 29; 

5/25/2010; 8:50-

12:57pm

4400

6 Gross Electric Output 652.07 MW EPA Methods 

5/OTM28, 29; 

5/25/2010; 8:50-

12:57pm

625

6 Net Electric Output 615.41 MW EPA Methods 

5/OTM28, 29; 

5/25/2010; 8:50-

12:57pm

590

7 Feed Rate 466.92 kpph EPA Methods 

5/OTM28, 29; 

5/25/2010; 1:15-

5:23pm

450

7 Heat Input Million Btus/million BTU using O2 5934.7 EPA Methods 

5/OTM28, 29; 

5/25/2010; 1:15-

5:23pm

5400

7 Steam Output 4297.5 kpph EPA Methods 

5/OTM28, 29; 

5/25/2010; 1:15-

5:23pm

4400

Thursday, February 03, 2011 Page 13 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

APCD Run Data

Process Lab Run Data

7 Gross Electric Output 653.04 MW EPA Methods 

5/OTM28, 29; 

5/25/2010; 1:15-

5:23pm

625

7 Net Electric Output 616.4 MW EPA Methods 

5/OTM28, 29; 

5/25/2010; 1:15-

5:23pm

590

8 Feed Rate 467.96 kpph EPA Methods 

5/OTM28, 29; 

5/25/2010; 5:40-

9:47pm

450

8 Heat Input Million Btus/million BTU using O2 5948 EPA Methods 

5/OTM28, 29; 

5/25/2010; 5:40-

9:47pm

5400

8 Steam Output 4288.5 kpph EPA Methods 

5/OTM28, 29; 

5/25/2010; 5:40-

9:47pm

4400

8 Gross Electric Output 652.93 MW EPA Methods 

5/OTM28, 29; 

5/25/2010; 5:40-

9:47pm

625

8 Net Electric Output 615.85 MW EPA Methods 

5/OTM28, 29; 

5/25/2010; 5:40-

9:47pm

590

Run Name Value UOM Comments

Target

Value

1 Electrostatic Precipitator (ESP) 0 0

1 FGD wet limestone scrubber 0 0

1 Selective catalytic Reduction (SCR) with 

ammonia injection

0 0

Thursday, February 03, 2011 Page 14 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Sampling / Stack Data Results Detail

Location stk exhaust - Method 10

Average

Run Number 1 2 3

Test Date 5/26/2010 5/26/2010 5/26/2010

Run Start Time 7:50:00 AM 11:00:00 AM 1:16:00 PM

Run Finish Time 10:50:00 AM 1:00:00 PM 3:16:00 PM

Carbon Dioxide, % 13.36 13.35 13.38 13.363

Oxygen, % 5.96 5.85 5.87 5.893

Fuel Factor 1.12 1.13 1.12

Dry Volumetric Flow Rate, dry scfm 1364766.667 1389183.333 1389016.667 1,380,988.8

89

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 15.2 14.3 14.8 14.767

Analyzer Make California 

Analytics

Californai 

Analytics

California 

Analytics

Analyzer Model 3300A 3300A 3300A

Analyzer Serial Number N3P125OT N3P125OT N3P125OT

Operating Range 200 200 200 200.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 1 1 1 1.000

Calibration Pre Zero Cylinder ID A4456 A4456 A4456

Calibration Pre Zero Cylinder Instrument Response 0.85 1 0.9 0.917

Calibration Pre Zero Cylinder Bias 1.3 1.6 1.4 1.433

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM041068C ALM041068

C

ALM041068

C

Calibration Pre High Cylinder Instrument Response 49.95 50.5 49.9 50.117

Calibration Pre High Cylinder Bias 0.1 1.2 0 0.433

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID A4456 A4456 A4456

Calibration Post Zero Cylinder Instrument Response 0.9 0.95 0.7 0.850

Calibration Post Zero Cylinder Bias 1.4 1.5 1 1.300

Calibration Post Zero Cylinder Drift 9.9999999999

9999E-02

0.1 0.4 0.200

Calibration Post High Cylinder ID ALM041068C ALM041068

C

ALM041068

C

Calibration Post High Cylinder Instrument Response 50.05 49.95 50.5 50.167

Calibration Post High Cylinder Bias 0.3 0.1 1.2 0.533

Calibration Post High Cylinder Drift 0.2 1.1 1.2 0.833

Cavg 14.9 14.67 14.74 14.770

Cavg Units ppmvd ppmvd ppmvd

Cgas 14.2748 13.9036 14.1093 14.096

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 0 0 0 0.000

Cgasw Units

Thursday, February 03, 2011 Page 15 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Location stk exhaust - Method 25A

Average

Run Number 1 2 3

Test Date 5/26/2010 5/26/2010 5/26/2010

Run Start Time 7:50:00 AM 11:00:00 AM 1:16:00 PM

Run Finish Time 9:50:00 AM 1:00:00 PM 3:16:00 PM

Carbon Dioxide, % 13.36 13.35 13.38 13.363

Oxygen, % 5.96 5.85 5.87 5.893

Fuel Factor 1.12 1.13 1.12

Dry Volumetric Flow Rate, dry scfm 1364766.667 1389183.333 1389016.667 1,380,988.8

89

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Moisture, % 15.2 14.3 14.8 14.767

Analyzer Make JUM JUM JUM

Analyzer Model 109A 109A 109A

Analyzer Serial Number

Operating Range 50 50 50 50.000

Operating Units ppm ppm ppm

No. Readings/Avg. 60 60 60 60.000

Calibration Set 7 7 7 7.000

Calibration Pre Zero Cylinder ID A4456 A4456 A4456

Calibration Pre Zero Cylinder Instrument Response 0.1 0.1 0.1 0.100

Calibration Pre Zero Cylinder Bias 0.9 0.9 0.9 0.900

Calibration Pre Zero Cylinder Drift 0 0 0 0.000

Calibration Pre High Cylinder ID ALM029335 ALM029335 ALM029335

Calibration Pre High Cylinder Instrument Response 9.95 9.98 9.95 9.960

Calibration Pre High Cylinder Bias 0 0.3 0 0.100

Calibration Pre High Cylinder Drift 0 0 0 0.000

Calibration Post Zero Cylinder ID A4456 A4456 A4456

Calibration Post Zero Cylinder Instrument Response 0.1 0.1 0.2 0.133

Calibration Post Zero Cylinder Bias 0.9 0.9 1.9 1.233

Calibration Post Zero Cylinder Drift 0 0 1 0.333

Calibration Post High Cylinder ID ALM029335 ALM029335 ALM029335

Calibration Post High Cylinder Instrument Response 9.98 9.95 9.99 9.973

Calibration Post High Cylinder Bias 0.3 0 0.4 0.233

Calibration Post High Cylinder Drift 0.3 0.3 0.4 0.333

Cavg 1.2 0.9 1.3 1.133

Cavg Units ppmvw ppmvw ppmvw

Cgas 1.311 0.9434 1.3704 1.208

Cgas Units ppmvd ppmvd ppmvd

Fuel Type Coal - 

Bituminous

Coal - 

Bituminous

Coal - 

Bituminous

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Cgasw 1.1117080587

9372

0.808514951

849975

1.167566191

44603

1.029

Cgasw Units ppmvw ppmvw ppmvw

Thursday, February 03, 2011 Page 16 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Location stk exhaust - Method 26A

Average

Run Number 1 2 3

Test Date 5/26/2010 5/26/2010 5/26/2010

Run Start Time 8:10:00 AM 11:28:00 AM 2:48:00 PM

Run Finish Time 11:01:15 AM 2:19:15 PM 5:39:15 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 180 180 180

Nozzle Diameter, inches 0.225 0.225 0.225 0.225

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9806 0.9806 0.9806 0.981

Barometric Pressure, inches of Mercury 30 30 30 30.000

Average Orifice Meter Differential, inches H2O 1.50 1.52 1.49 1.503

Dry Gas Meter Volume Sampled, cubic feet 115.430 125.280 124.072 121.594

Average Dry Gas Meter Temperature, °F 99.13 105.25 105.00 103.127

Dry Gas Meter Volume Sampled, dscf 107.569 115.489 114.418 112.492

Total Moisture Liquid collected, g 424.3 450.2 449.3 441.267

Volume of Water Vapor, standard cubic feet 19.97 21.19 21.15 20.770

Moisture Content of Stack Gas, % 15.66 15.50 15.60 15.587

Moisture Saturation at Stack Gas Temperature, % 13.99 14.23 14.23 14.150

Dry Mole Fraction 0.8601 0.8577 0.8577 0.859

Carbon Dioxide, % 13.43 13.34 13.4 13.390

Oxygen, % 5.49 5.85 5.88 5.740

Carbon Monoxide & Nitrogen, % 81.08 80.81 80.72 80.870

Fuel Factor 1.15 1.13 1.12

Dry Molecular Weight, lb/lb-Mole 30.37 30.37 30.38 30.373

Wet Molecular weight, lb/lb-Mole 28.94 28.84 28.86 28.880

Flue Gas Static Pressure, inches of H2O 0.65 0.65 0.65 0.650

Absolute Flue Gas Pressure, inches of Mercury 30.05 30.05 30.05 30.050

Average Stack Gas Temperature, °F 127.31 127.94 127.94 127.730

Average Velocity Head, inches of H2O 0.6744858245

5552

0.674871077

67214

0.663306256

689921

0.671

Average Stack Gas Velocity, feet/second 48.47 48.59 48.16 48.407

Stack Cross-Sectional Area, square feet 615.752 615.752 615.752 615.752

Dry Volumetric Flow Rate, dry scfm 1,390,684.0 1,388,747.2 1,376,457.4 1,385,296.2

00

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,790,730.0 1,795,163.4 1,779,277.0 1,788,390.1

33

Percent Isokinetic of Sampling Rate, % 95.8 103.0 103.0 100.600

Percent Excess Air, % 34.5 37.8 38.1 36.800

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 336 336 336

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 03, 2011 Page 17 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Location stk exhaust - Method 29

Average

Run Number 1 2 3

Test Date 5/25/2010 5/25/2010 5/25/2010

Run Start Time 8:50:00 AM 1:15:00 PM 5:40:00 PM

Run Finish Time 12:35:00 PM 5:00:00 PM 9:25:00 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.225 0.225 0.225 0.225

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.999 0.999 0.999 0.999

Barometric Pressure, inches of Mercury 30 30 30 30.000

Average Orifice Meter Differential, inches H2O 1.37 1.34 1.39 1.367

Dry Gas Meter Volume Sampled, cubic feet 160.750 159.560 162.367 160.892

Average Dry Gas Meter Temperature, °F 94.25 96.50 97.38 96.043

Dry Gas Meter Volume Sampled, dscf 153.908 152.139 154.590 153.546

Total Moisture Liquid collected, g 571.2 541.5 552.2 554.967

Volume of Water Vapor, standard cubic feet 26.89 25.49 25.99 26.123

Moisture Content of Stack Gas, % 14.87 14.35 14.39 14.537

Moisture Saturation at Stack Gas Temperature, % 14.20 13.97 13.99 14.053

Dry Mole Fraction 0.858 0.8603 0.8601 0.859

Carbon Dioxide, % 13.51 13.4 13.18 13.363

Oxygen, % 5.99 6.01 5.94 5.980

Carbon Monoxide & Nitrogen, % 80.5 80.59 80.88 80.657

Fuel Factor 1.10 1.11 1.14

Dry Molecular Weight, lb/lb-Mole 30.40 30.38 30.35 30.377

Wet Molecular weight, lb/lb-Mole 28.76 28.72 28.69 28.723

Flue Gas Static Pressure, inches of H2O 0.62 0.62 0.65 0.630

Absolute Flue Gas Pressure, inches of Mercury 30.05 30.05 30.05 30.050

Average Stack Gas Temperature, °F 127.88 127.25 127.31 127.480

Average Velocity Head, inches of H2O 0.6743674910

18012

0.659524920

681963

0.681535391

884012

0.672

Average Stack Gas Velocity, feet/second 48.64 48.11 48.93 48.560

Stack Cross-Sectional Area, square feet 615.752 615.752 615.752 615.752

Dry Volumetric Flow Rate, dry scfm 1,390,804.4 1,380,817.1 1,403,882.2 1,391,834.5

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,797,010.6 1,777,429.7 1,807,724.7 1,794,055.0

00

Percent Isokinetic of Sampling Rate, % 102.8 102.4 102.3 102.500

Percent Excess Air, % 39.2 39.4 38.5 39.033

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 336 336 336

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 03, 2011 Page 18 of 19
Santee Cooper-Cross Unit #4, ICR Section 114 Testing

7/28/2010

Location stk exhaust - Method 5/OTM-28

Average

Run Number 1 2 3

Test Date 5/25/2010 5/25/2010 5/25/2010

Run Start Time 8:50:00 AM 1:15:00 PM 5:40:00 PM

Run Finish Time 12:35:00 PM 5:00:00 PM 9:25:00 PM

Net Traversing Points 16 16 16

Net Run Time, minutes 240 240 240

Nozzle Diameter, inches 0.225 0.225 0.225 0.225

Pitot Tube Coefficient 0.84 0.84 0.84 0.840

Dry Gas Meter Calibration Factor 0.9806 0.9806 0.9806 0.981

Barometric Pressure, inches of Mercury 30 30 30 30.000

Average Orifice Meter Differential, inches H2O 1.49 1.51 1.51 1.503

Dry Gas Meter Volume Sampled, cubic feet 164.780 166.530 166.335 165.882

Average Dry Gas Meter Temperature, °F 100.88 105.31 106.94 104.377

Dry Gas Meter Volume Sampled, dscf 153.075 153.495 152.875 153.148

Total Moisture Liquid collected, g 559.8 551.6 534.8 548.733

Volume of Water Vapor, standard cubic feet 26.35 25.96 25.17 25.827

Moisture Content of Stack Gas, % 14.69 14.47 14.14 14.433

Moisture Saturation at Stack Gas Temperature, % 14.35 13.97 14.01 14.110

Dry Mole Fraction 0.8565 0.8603 0.8599 0.859

Carbon Dioxide, % 13.51 13.4 13.18 13.363

Oxygen, % 5.99 6.01 5.94 5.980

Carbon Monoxide & Nitrogen, % 80.5 80.59 80.88 80.657

Fuel Factor 1.10 1.11 1.14

Dry Molecular Weight, lb/lb-Mole 30.40 30.38 30.35 30.377

Wet Molecular weight, lb/lb-Mole 28.68 28.74 28.64 28.687

Flue Gas Static Pressure, inches of H2O 0.62 0.65 0.62 0.630

Absolute Flue Gas Pressure, inches of Mercury 30.05 30.05 30.05 30.050

Average Stack Gas Temperature, °F 128.25 127.25 127.38 127.627

Average Velocity Head, inches of H2O 0.6674720863

77975

0.672057901

942844

0.668068154

853594

0.669

Average Stack Gas Velocity, feet/second 48.47 48.54 48.49 48.500

Stack Cross-Sectional Area, square feet 615.752 615.752 615.752 615.752

Dry Volumetric Flow Rate, dry scfm 1,382,650.3 1,393,158.6 1,390,768.6 1,388,859.1

67

Actual Wet Volumetric Flue Gas Flow Rate, acfm 1,790,730.0 1,793,316.1 1,791,468.9 1,791,838.3

33

Percent Isokinetic of Sampling Rate, % 102.9 102.4 102.1 102.467

Percent Excess Air, % 39.2 39.4 38.5 39.033

F-Factor, dscfm/MMBtu @ %O2 9780 9780 9780 9,780.000

Round Duct Diameter, inches 336 336 336

Rectangular Duct Width, inches 0 0 0

Rectangular Duct Length, inches 0 0 0

Fw 10640 10640 10640 10,640.000

Fc 1800 1800 1800 1,800.000

Thursday, February 03, 2011 Page 19 of 19