# GE Energy



# Progress Energy

Robinson Unit 1

Furnace Sorbent Injection

Demonstration Project

Final Report, Rev. 02

Appendix A: Coal and Ash Analyses

Contract No. 10023-WA169

GE Job Number 6900

25 February 2009

GE Energy and Environmental Research Corporation

1831 East Carnegie Ave

Santa Ana, CA 92705

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-i 

# GE Energy



# List of Tables

Table Page

A-1. Coal Proximate Analysis .............................................................................................. A-1

A-2. Coal Ultimate Analysis................................................................................................. A-3

A-3. Coal Ash Analysis ........................................................................................................ A-5

A-4. Ash Fusion Temperature............................................................................................... A-7

A-5. Ash Analysis................................................................................................................. A-9

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-1 

# GE Energy

TABLE A-1. COAL PROXIMATE ANALYSIS

Moisture Ash Volatile Fixed

Carbon Sulfur HHV Ash Volatile Fixed

Carbon Sulfur LHV

BTU BTU

07/11/08 6.73 12.50 33.40 47.37 0.99 11884 13.40 35.81 50.79 1.06 12741

07/26/08 6.83 9.96 35.65 47.56 0.85 12333 10.69 38.26 51.05 0 .91 13237

09/17/08 7.54 12.51 33.69 46.26 1.09 11774 13.53 36.44 50.03 1.18 12734

09/18/08 5.48 12.53 33.99 48.00 1.11 12050 13.26 35.96 50.78 1.17 12749

09/18/08 5.27 12.49 35.57 46.67 1.76 12089 13.19 37.55 49.26 1.86 12762

09/19/08 5.02 13.34 33.86 47.78 1.03 11993 14.04 35.65 50.31 1.08 12627

09/19/08 5.88 10.85 34.29 48.98 1.35 12276 11.53 36.43 52.04 1.43 13043

09/24/08 5.93 12.28 34.48 47.31 1.18 12042 13.05 36.65 50.30 1.25 12801

09/24/08 4.97 11.59 35.09 48.35 1.31 12267 12.20 36.93 50.87 1.38 12909

09/24/08 4.94 12.22 35.31 47.53 1.25 12207 12.86 37.15 49.99 1.32 12841

09/25/08 4.03 11.34 36.47 48.16 1.28 12505 11.82 38.00 50.18 1.33 13030

09/25/08 3.71 12.30 35.42 48.57 1.30 12363 12.77 36.78 50.45 1.35 12839

09/29/08 4.83 12.16 34.75 48.26 1.17 12266 12.78 36.51 50.71 1.23 12888

09/29/08 5.02 12.01 33.48 49.49 1.20 12121 12.65 35.25 52.10 1.26 12762

09/29/08 4.91 11.82 33.98 49.29 1.39 12074 12.43 35.73 51.84 1.46 12697

09/29/08 5.62 12.34 33.89 48.15 1.23 12055 13.07 35.91 51.02 1.30 12773

10/01/08 5.41 11.59 33.52 49.48 1.02 12028 12.25 35.44 52.31 1.08 12716

09/30/08 5.58 13.10 33.79 47.53 1.10 11861 13.87 35.79 50.34 1.17 12562

09/30/08 6.22 12.76 34.29 46.73 0.95 11949 13.61 36.56 49.83 1.01 12742

09/30/08 5.56 13.58 34.01 46.85 1.06 11718 14.38 36.01 49.61 1.12 12408

10/02/08 5.03 10.27 34.25 50.45 0.98 12493 10.81 36.06 53.13 1.03 13155

10/02/08 4.49 13.25 33.86 48.40 0.99 12144 13.87 35.45 50.68 1.04 12715

10/03/08 4.83 13.28 33.39 48.50 1.21 12128 13.95 35.08 50.97 1.27 12744

10/03/08 4.50 9.43 35.52 50.55 0.92 12661 9.87 37.19 52.94 0. 96 13258

10/06/08 5.25 11.75 34.09 48.91 1.00 12336 12.40 35.98 51.62 1.06 13020

10/07/08 4.16 12.05 35.59 48.20 1.27 12437 12.57 37.14 50.29 1.32 12977

10/08/08 3.88 11.24 35.44 49.44 1.33 12531 11.69 36.87 51.44 1.38 13037

10/17/08 5.01 11.64 33.72 49.63 1.28 12304 12.25 35.5 52.25 1 .35 12953

10/16/08 4.44 11.05 35.37 49.14 1.37 12525 11.56 37.01 51.43 1.43 13107

10/20/08 3.81 12.25 35.41 48.53 1.16 12352 12.74 36.81 50.45 1.21 12841

10/21/08 4.06 11.39 35.42 49.13 1.38 12541 11.87 36.92 51.21 1.44 13072

10/22/08 3.74 12.22 34.73 49.31 1.19 12390 12.69 36.08 51.23 1.24 12871

10/23/08 5.69 11.16 34.75 48.40 1.42 12289 11.83 36.85 51.32 1.51 13030

10/23/08 5.80 10.54 35.54 48.12 1.63 12391 11.19 37.73 51.08 1.73 13154

10/28/08 5.17 10.48 35.70 48.65 1.70 12537 11.05 37.65 51.30 1.79 13221 Dry Basis

DATE

SAMPLED

% dry % wet As Received

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

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# GE Energy

TABLE A-1. COAL PROXIMATE ANALYSIS (CONT.)

Moisture Ash Volatile Fixed

Carbon BTU Sulfur Ash Volatile Fixed

Carbon BTU Sulfur

10/29/08 5.15 11.88 34.68 48.29 12230 1.59 12.53 36.56 50.91 12894 1.68

10/31/08 5.95 11.93 34.19 47.93 12177 1.52 12.68 36.35 50.97 12947 1.62

10/30/08 5.71 13.17 34.30 46.82 11932 1.54 13.97 36.38 49.65 12655 1.63

11/03/08 5.71 11.86 33.85 48.58 12189 1.48 12.58 35.90 51.52 12927 1.57

11/04/08 4.60 13.97 33.08 48.35 11964 1.38 14.64 34.67 50.69 12541 1.45

11/04/08 5.31 12.93 32.80 48.96 12077 1.36 13.66 34.64 51.70 12754 1.44

11/04/08 4.95 12.43 33.08 49.54 12189 1.40 13.08 34.80 52.12 12824 1.47

11/04/08 4.59 11.09 34.28 50.04 12444 1.62 11.62 35.93 52.45 13043 1.70

11/04/08 4.97 12.62 33.34 49.07 12141 1.38 13.28 35.08 51.64 12776 1.45

11/05/08 6.09 12.00 33.93 47.98 12092 1.33 12.78 36.13 51.09 12876 1.42

11/05/08 4.70 12.37 33.76 49.17 12199 1.54 12.98 35.42 51.60 12801 1.62

11/05/08 6.69 11.54 33.54 48.23 12200 1.25 12.37 35.95 51.68 13075 1.34

11/05/08 7.45 10.92 33.89 47.74 12198 1.17 11.80 36.62 51.58 13180 1.26

11/06/08 6.61 11.63 34.24 47.52 12085 1.10 12.45 36.66 50.89 12940 1.18

11/07/08 5.61 11.14 34.99 48.26 12356 1.26 11.80 37.07 51.13 13090 1.33

11/10/08 5.55 11.88 35.10 47.47 12220 1.20 12.58 37.16 50.26 12938 1.27

11/11/08 3.80 11.04 35.96 49.20 12606 1.30 11.48 37.38 51.14 13104 1.35

11/12/08 4.52 10.89 34.86 49.73 12508 1.31 11.41 36.51 52.08 13100 1.37

11/13/08 5.24 9.75 35.20 49.81 12607 1.35 10.29 37.15 52.56 1 3304 1.42

11/14/08 4.15 10.91 35.23 49.71 12563 1.58 11.38 36.76 51.86 13107 1.65

11/17/08 6.17 10.92 34.08 48.83 12307 1.51 11.64 36.32 52.04 13116 1.61

11/20/08 5.22 11.97 34.59 48.22 12339 1.14 12.63 36.50 50.87 13019 1.20

11/21/08 5.05 11.27 35.72 47.96 12366 1.51 11.87 37.62 50.51 13024 1.59

11/25/08 5.59 11.99 34.48 47.94 12194 1.25 12.70 36.52 50.78 12916 1.32

11/26/08 5.85 11.69 33.75 48.71 12143 1.21 12.42 35.85 51.73 12898 1.28

12/02/08 6.13 10.07 35.32 48.48 12410 1.25 10.73 37.63 51.64 13220 1.33

12/03/08 6.06 11.97 34.39 47.58 12166 1.22 12.74 36.61 50.65 12951 1.30

12/04/08 5.58 11.75 33.86 48.81 12236 1.22 12.44 35.86 51.70 12959 1.29

12/08/08 6.33 10.95 34.13 48.59 12257 1.27 11.69 36.44 51.87 13085 1.36

12/08/08 7.25 10.60 34.32 47.83 12204 1.20 11.43 37.00 51.57 13158 1.29

12/09/08 6.94 11.29 34.06 47.71 12098 1.33 12.13 36.60 51.27 13000 1.43

12/09/08 5.73 11.75 34.25 48.27 12257 1.39 12.46 36.33 51.21 13002 1.47

12/09/08 5.63 12.74 34.10 47.53 12154 1.47 13.50 36.13 50.37 12879 1.56

12/10/08 6.80 11.94 34.20 47.06 12011 1.13 12.81 36.69 50.50 12887 1.21

12/10/08 5.91 11.05 34.59 48.45 12355 1.33 11.74 36.76 51.50 13131 1.41

12/10/08 6.14 11.82 34.43 47.61 12127 1.26 12.59 36.68 50.73 12920 1.34 Dry Basis, % dry As Received, % wet

DATE

SAMPLED

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

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# GE Energy

TABLE A-2. COAL ULTIMATE ANALYSIS

DATE

SAMPLED Carbon Hydrogen Nitrogen Oxygen Carbon Hydrogen Nitrogen Oxygen

07/11/08 67.50 4.36 1.34 6.58 72.37 4.67 1.44 7.06

07/26/08 68.21 4.78 1.42 7.95 73.21 5.13 1.52 8.54

09/17/08 65.73 4.50 1.28 1.09 71.09 4.87 1.38 1.18

09/18/08 67.57 4.60 1.36 7.35 71.49 4.87 1.44 7.77

09/18/08 67.60 4.55 1.32 7.01 71.36 4.80 1.39 7.40

09/19/08 67.07 4.64 1.33 7.57 70.62 4.88 1.40 7.98

09/19/08 68.59 4.74 1.33 7.26 72.88 5.04 1.41 7.71

09/24/08 67.14 4.60 1.19 7.68 71.37 4.89 1.27 8.17

09/24/08 67.98 4.61 1.25 8.29 71.54 4.85 1.32 8.71

09/24/08 67.15 4.91 1.38 8.15 70.64 5.16 1.45 8.57

09/25/08 68.75 5.14 1.46 8.00 71.64 5.36 1.52 8.33

09/25/08 67.87 4.93 1.37 8.52 70.49 5.12 1.42 8.85

09/29/08 68.08 4.54 1.62 7.60 71.53 4.77 1.70 7.99

09/29/08 67.98 4.56 1.61 7.62 71.57 4.80 1.69 8.03

09/29/08 67.38 4.49 1.57 8.44 70.86 4.72 1.65 8.88

09/29/08 67.51 4.50 1.60 7.20 71.53 4.77 1.70 7.63

10/01/08 68.35 4.36 1.30 7.97 72.26 4.61 1.37 8.43

09/30/08 66.78 4.52 1.27 7.65 70.73 4.79 1.34 8.10

09/30/08 66.66 4.56 1.29 7.56 71.08 4.86 1.38 8.06

09/30/08 65.86 4.46 1.25 8.23 69.74 4.72 1.32 8.72

10/02/08 70.48 4.29 1.76 7.19 74.21 4.52 1.85 7.58

10/02/08 68.74 4.28 1.69 6.56 71.97 4.48 1.77 6.87

10/03/08 68.53 4.38 1.70 6.07 72.01 4.60 1.79 6.38

10/03/08 71.74 4.55 1.81 7.05 75.12 4.76 1.90 7.39

10/06/08 68.57 4.64 1.53 7.26 72.37 4.90 1.61 7.66

10/07/08 69.19 4.68 1.32 7.33 72.19 4.88 1.38 7.66

10/08/08 70.01 4.58 1.33 7.63 72.84 4.77 1.38 7.94

10/17/08 68.35 4.48 1.43 7.81 71.95 4.72 1.51 8.22

10/16/08 69.75 4.61 1.41 7.37 72.99 4.82 1.48 7.72

10/20/08 69.03 4.57 1.37 7.81 71.76 4.75 1.42 8.12

10/21/08 68.92 4.68 1.35 8.22 71.84 4.88 1.41 8.56

10/22/08 68.71 4.71 1.39 8.04 71.38 4.89 1.44 8.36

10/23/08 68.20 4.58 1.33 7.62 72.32 4.86 1.41 8.07

10/23/08 68.39 4.66 1.35 7.63 72.60 4.95 1.43 8.10

10/28/08 69.65 4.81 1.27 6.92 73.45 5.07 1.34 7.30

As Received, % wet Dry Basis, % dry

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-4 

# GE Energy

TABLE A-2. COAL ULTIMATE ANALYSIS (CONT.)

DATE

SAMPLED Carbon Hydrogen Nitrogen Oxygen Carbon Hydrogen Nitrogen Oxygen

10/29/08 67.45 4.63 1.29 8.01 71.11 4.88 1.36 8.44

10/31/08 67.44 4.66 1.33 7.17 71.71 4.96 1.41 7.62

10/30/08 66.48 4.64 1.32 7.14 70.51 4.92 1.40 7.57

11/03/08 68.00 4.59 1.32 7.04 72.12 4.87 1.40 7.46

11/04/08 66.68 4.59 0.94 7.84 69.89 4.81 0.99 8.22

11/04/08 67.03 4.57 0.95 7.85 70.79 4.83 1.00 8.28

11/04/08 67.72 4.58 0.92 8.00 71.25 4.82 0.97 8.41

11/04/08 69.03 4.75 1.00 7.92 72.35 4.98 1.05 8.30

11/04/08 67.95 4.64 0.92 7.52 71.50 4.88 0.97 7.92

11/05/08 66.85 4.49 1.37 7.87 71.18 4.78 1.46 8.38

11/05/08 67.93 4.60 1.36 7.50 71.28 4.83 1.43 7.86

11/05/08 66.76 4.63 1.23 7.90 71.55 4.96 1.32 8.46

11/05/08 67.71 4.58 1.37 6.80 73.16 4.95 1.48 7.35

11/06/08 67.46 4.63 1.35 7.22 72.24 4.96 1.45 7.72

11/07/08 68.45 4.77 1.33 7.44 72.52 5.05 1.41 7.89

11/10/08 67.49 4.75 1.46 7.67 71.46 5.03 1.55 8.11

11/11/08 70.46 4.85 1.44 7.11 73.24 5.04 1.50 7.39

11/12/08 69.71 4.67 1.37 7.53 73.01 4.89 1.44 7.88

11/13/08 69.25 4.79 1.56 8.06 73.08 5.05 1.65 8.61

11/14/08 69.99 4.54 1.51 7.32 73.02 4.74 1.58 7.63

11/17/08 67.74 4.64 1.11 7.91 72.19 4.95 1.18 8.63

11/20/08 68.52 4.57 1.44 7.14 72.29 4.82 1.52 7.54

11/21/08 67.88 4.62 1.45 8.22 71.49 4.87 1.53 8.65

11/25/08 67.47 4.81 1.25 7.64 71.47 5.09 1.32 8.10

11/26/08 67.96 4.60 1.38 7.30 72.18 4.90 1.47 7.75

12/02/08 68.50 4.70 1.31 8.04 72.97 5.01 1.40 8.56

12/03/08 67.80 4.71 1.29 6.95 72.17 5.01 1.37 7.41

12/04/08 68.12 4.53 1.39 7.41 72.15 4.80 1.47 7.85

12/08/08 68.21 4.53 1.48 7.23 72.82 4.84 1.58 7.71

12/08/08 68.09 4.54 1.47 6.85 73.41 4.89 1.58 7.40

12/09/08 64.87 5.32 1.49 8.76 69.71 5.72 1.60 9.41

12/09/08 67.99 4.46 1.40 7.28 72.12 4.73 1.49 7.73

12/09/08 65.23 5.18 1.59 8.16 69.12 5.49 1.69 8.64

12/10/08 66.94 4.41 1.32 7.46 71.82 4.73 1.42 8.01

12/10/08 68.48 4.85 1.38 7.00 72.78 5.15 1.47 7.45

12/10/08 66.66 5.02 1.43 7.67 71.02 5.35 1.52 8.18

As Received, % wet Dry Basis, % dry

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-5 

# GE Energy

TABLE A-3. COAL ASH ANALYSIS

DATE

SAMPLED SiO

2 

# Al

2 

# O

3 

# TiO

2 

# Fe 2 

# O

3 

# CaO MgO P 2 

# O 5 

# Na 2 

# O SO

3 

# K 2 

# O SrO BaO MnO

2 

# Undeter

- mined

07/11/08 55.60 29.90 1.63 5.99 1.16 0.99 3.33 0.33 0.11 0.23 0 .11 0.10 0.02 0.50

07/26/08 55.60 28.30 1.32 6.99 1.78 1.01 3.47 0.39 0.32 0.22 0 .14 0.14 0.03 0.29

09/17/08 54.00 30.20 1.53 8.38 1.10 0.99 2.52 0.17 0.10 0.23 0 .09 0.10 0.03 0.56

09/18/08 55.90 29.80 1.47 6.34 1.93 0.91 2.53 0.19 0.10 0.24 0 .08 0.10 0.02 0.39

09/18/08 53.90 28.10 1.45 11.10 1.04 0.88 2.43 0.19 0.10 0.26 0.09 0.10 0.02 0.34

09/19/08 57.50 29.50 1.55 5.94 0.94 0.93 2.69 0.20 0.20 0.17 0 .06 0.08 0.03 0.21

09/19/08 54.70 29.50 1.55 8.71 1.09 0.94 2.61 0.19 0.20 0.18 0 .09 0.10 0.03 0.11

09/24/08 55.30 28.60 1.48 8.48 1.28 0.95 2.59 0.16 0.20 0.40 0 .10 0.12 0.03 0.31

09/24/08 54.40 27.70 1.45 9.97 1.30 1.07 2.56 0.16 0.20 0.43 0 .11 0.13 0.04 0.48

09/24/08 54.50 28.30 1.41 9.61 1.22 0.96 2.80 0.19 0.20 0.25 0 .11 0.12 0.04 0.29

09/25/08 55.80 27.60 1.48 9.02 1.45 1.03 2.29 0.13 0.20 0.32 0 .11 0.11 0.04 0.42

09/25/08 55.60 28.00 1.70 8.63 1.36 0.93 2.27 0.14 0.20 0.21 0 .11 0.12 0.04 0.69

09/29/08 54.50 28.60 1.37 8.74 1.50 1.11 2.90 0.27 0.20 0.30 0 .13 0.16 0.02 0.20

09/29/08 54.90 27.60 1.33 9.41 1.40 1.13 2.94 0.29 0.20 0.27 0 .13 0.17 0.02 0.21

09/29/08 55.10 27.80 1.46 9.65 1.32 0.98 2.49 0.23 0.20 0.31 0 .13 0.14 0.01 0.18

09/29/08 55.10 27.90 1.40 9.29 1.33 1.09 2.69 0.26 0.20 0.32 0 .13 0.16 0.02 0.11

10/01/08 56.00 27.90 1.25 7.81 1.08 1.14 3.58 0.30 0.20 0.18 0 .09 0.15 0.02 0.30

09/30/08 55.90 27.80 1.31 8.31 1.06 1.14 3.34 0.30 0.20 0.21 0 .08 0.12 0.03 0.20

09/30/08 55.80 27.80 1.35 7.90 1.14 1.19 3.48 0.35 0.20 0.23 0 .09 0.13 0.03 0.31

09/30/08 55.70 27.70 1.29 8.60 1.06 1.17 3.44 0.34 0.20 0.14 0 .09 0.15 0.03 0.09

10/02/08 55.70 27.50 1.32 8.41 1.13 1.09 3.27 0.25 0.20 0.08 0 .10 0.14 0.05 0.76

10/02/08 56.90 27.70 1.27 7.31 0.79 1.29 3.44 0.22 0.20 0.09 0 .09 0.11 0.03 0.56

10/03/08 56.60 26.30 1.21 9.43 0.94 1.12 3.03 0.23 0.20 0.20 0 .13 0.13 0.03 0.45

10/03/08 57.10 28.10 1.38 7.34 1.10 1.13 2.88 0.30 0.20 0.09 0 .12 0.13 0.02 0.11

10/06/08 57.30 27.50 1.33 7.66 1.03 1.04 2.76 0.24 0.20 0.18 0 .09 0.11 0.04 0.52

10/07/08 55.90 29.00 1.45 7.72 0.88 0.95 2.54 0.18 0.20 0.16 0 .10 0.11 0.01 0.80

10/08/08 56.60 27.80 1.30 8.88 1.11 0.87 2.39 0.27 0.20 0.13 0 .10 0.09 0.02 0.24

10/17/08 54.50 27.60 1.34 9.66 1.34 1.09 2.84 0.31 0.20 0.21 0 .11 0.15 0.02 0.63

10/16/08 54.90 27.70 1.42 9.92 1.23 0.92 2.35 0.26 0.20 0.18 0 .13 0.14 0.02 0.63

10/20/08 56.40 27.80 1.51 8.27 1.04 0.87 2.37 0.28 0.20 0.21 0 .11 0.12 0.02 0.80

10/21/08 55.10 28.90 1.39 8.97 1.10 0.84 2.27 0.26 0.20 0.19 0 .12 0.13 0.02 0.51

10/22/08 56.20 29.30 1.47 7.53 0.94 0.81 2.36 0.22 0.20 0.27 0 .10 0.10 0.21 0.29

10/23/08 54.50 27.60 1.37 10.30 1.13 0.86 2.72 0.22 0.32 0.18 0.12 0.14 0.03 0.51

10/23/08 53.00 27.10 1.31 12.50 0.98 0.79 2.51 0.20 0.28 0.18 0.11 0.16 0.03 0.85

10/28/08 54.30 26.70 1.41 11.90 1.31 0.77 2.52 0.23 0.20 0.22 0.12 0.12 0.02 0.18

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-6 

# GE Energy

TABLE A-3. COAL ASH ANALYSIS (CONT.)

DATE

SAMPLED SiO

2 

# Al

2 

# O

3 

# TiO

2 

# Fe 2 

# O

3 

# CaO MgO P 2 

# O 5 

# Na 2 

# O SO

3 

# K 2 

# O SrO BaO MnO

2 

# Undeter

- mined

10/29/08 54.90 28.10 1.24 10.20 1.09 0.85 2.25 0.16 0.20 0.24 0.10 0.11 0.02 0.54

10/31/08 55.40 27.10 1.29 10.20 1.28 0.87 2.50 0.27 0.30 0.15 0.09 0.11 0.02 0.42

10/30/08 55.70 26.80 1.28 10.70 1.09 0.84 2.30 0.27 0.25 0.16 0.08 0.09 0.02 0.42

11/03/08 54.20 27.00 1.27 11.40 1.55 0.97 2.32 0.18 0.30 0.21 0.09 0.13 0.02 0.36

11/04/08 56.60 26.90 1.25 8.66 1.50 1.06 2.78 0.23 0.30 0.20 0 .08 0.13 0.02 0.29

11/04/08 56.30 26.60 1.36 9.39 1.59 0.97 2.38 0.19 0.30 0.15 0 .09 0.12 0.02 0.54

11/04/08 56.30 26.60 1.36 9.67 1.46 1.00 2.24 0.17 0.30 0.15 0 .09 0.13 0.02 0.51

11/04/08 54.60 26.10 1.38 11.90 1.54 0.92 2.26 0.20 0.30 0.15 0.10 0.11 0.02 0.42

11/04/08 55.40 26.60 1.32 10.30 1.49 0.97 2.49 0.21 0.30 0.19 0.09 0.12 0.02 0.50

11/05/08 56.90 27.00 1.30 8.75 1.25 0.90 2.52 0.23 0.30 0.25 0 .10 0.14 0.02 0.34

11/05/08 55.80 26.40 1.34 10.40 1.46 0.94 2.42 0.19 0.30 0.24 0.10 0.12 0.02 0.27

11/05/08 56.60 27.10 1.33 8.76 1.29 0.97 2.49 0.21 0.30 0.22 0 .11 0.15 0.02 0.45

11/05/08 56.40 27.50 1.30 8.22 1.36 0.97 2.63 0.27 0.30 0.28 0 .12 0.15 0.02 0.48

11/06/08 54.90 29.80 1.43 7.62 1.47 0.99 2.26 0.23 0.30 0.21 0 .12 0.12 0.05 0.50

11/07/08 55.70 28.80 1.54 8.24 1.35 0.96 2.02 0.20 0.30 0.19 0 .12 0.12 0.04 0.42

11/10/08 55.90 23.70 1.11 12.00 1.79 1.16 2.44 0.50 0.35 0.24 0.12 0.13 0.08 0.48

11/11/08 51.40 26.40 1.19 13.70 1.70 1.16 2.61 0.45 0.35 0.30 0.12 0.14 0.08 0.40

11/12/08 52.80 24.60 1.20 14.30 1.70 1.26 2.43 0.35 0.30 0.39 0.10 0.13 0.10 0.34

11/13/08 52.50 25.60 1.06 13.50 1.45 1.16 2.85 0.37 0.35 0.34 0.10 0.13 0.09 0.50

11/14/08 52.10 26.30 1.26 14.70 0.57 1.19 1.94 0.13 0.51 0.46 0.09 0.10 0.06 0.59

11/17/08 54.40 25.70 1.70 11.70 1.25 1.09 2.49 0.33 0.30 0.32 0.12 0.14 0.02 0.44

11/20/08 57.40 28.50 1.84 7.09 0.88 0.83 2.21 0.17 0.30 0.22 0 .09 0.09 0.03 0.35

11/21/08 55.30 27.40 1.73 9.85 0.73 1.01 2.51 0.28 0.30 0.21 0 .11 0.12 0.02 0.43

11/25/08 57.10 28.30 1.63 7.40 0.77 0.99 2.47 0.24 0.30 0.21 0 .11 0.11 0.02 0.35

11/26/08 56.90 27.80 1.62 7.65 1.44 1.03 2.36 0.23 0.30 0.15 0 .10 0.12 0.02 0.28

12/02/08 57.20 26.60 1.69 9.02 1.12 1.02 2.01 0.18 0.30 0.22 0 .10 0.10 0.05 0.39

12/03/08 56.80 26.20 1.52 8.53 0.91 1.07 3.41 0.36 0.30 0.13 0 .12 0.13 0.02 0.50

12/04/08 56.50 27.00 1.49 8.37 0.94 1.09 3.21 0.29 0.30 0.17 0 .12 0.13 0.02 0.37

12/08/08 53.50 27.30 1.42 10.90 1.06 1.01 3.30 0.40 0.30 0.14 0.12 0.14 0.03 0.38

12/08/08 55.70 26.70 1.45 9.48 1.00 1.04 3.01 0.42 0.30 0.21 0 .13 0.13 0.04 0.39

12/09/08 54.40 27.30 1.48 9.89 1.23 1.10 3.12 0.28 0.30 0.26 0 .12 0.13 0.02 0.37

12/09/08 54.70 26.60 1.42 10.30 0.86 1.09 3.39 0.31 0.30 0.21 0.11 0.13 0.02 0.56

12/09/08 55.20 26.20 1.49 10.70 0.82 1.11 3.15 0.26 0.30 0.19 0.10 0.11 0.02 0.35

12/10/08 55.10 26.40 1.41 10.21 0.98 1.07 3.14 0.24 0.30 0.35 0.11 0.14 0.02 0.53

12/10/08 53.70 26.10 1.46 12.80 0.91 0.95 2.68 0.21 0.30 0.25 0.11 0.10 0.02 0.41

12/10/08 56.00 26.30 1.35 9.26 1.06 1.11 3.34 0.27 0.30 0.26 0 .12 0.13 0.02 0.48

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-7 

# GE Energy

TABLE A-4. ASH FUSION TEMPERATURE

DATE

SAMPLED Initial

Deformation Softening Hemispherical Fluid

07/11/08 2700+ 2700+ 2700+ 2700+

07/26/08 2700+ 2700+ 2700+ 2700+

09/17/08 2700+ 2700+ 2700+ 2700+

09/18/08 2700+ 2700+ 2700+ 2700+

09/18/08 2670 2685 2700+ 2700+

09/19/08 2700+ 2700+ 2700+ 2700+

09/19/08 2700+ 2700+ 2700+ 2700+

09/24/08 2700+ 2700+ 2700+ 2700+

09/24/08 2700+ 2700+ 2700+ 2700+

09/24/08 2700+ 2700+ 2700+ 2700+

09/25/08 2695 2700+ 2700+ 2700+

09/25/08 2691 2700+ 2700+ 2700+

09/29/08 2700+ 2700+ 2700+ 2700+

09/29/08 2695 2700+ 2700+ 2700+

09/29/08 2700+ 2700+ 2700+ 2700+

09/29/08 2693 2700+ 2700+ 2700+

10/01/08 2700+ 2700+ 2700+ 2700+

09/30/08 2700+ 2700+ 2700+ 2700+

09/30/08 2700+ 2700+ 2700+ 2700+

09/30/08 2700+ 2700+ 2700+ 2700+

10/02/08 2700+ 2700+ 2700+ 2700+

10/02/08 2700+ 2700+ 2700+ 2700+

10/03/08 2675 2685 2700+ 2700+

10/03/08 2700+ 2700+ 2700+ 2700+

10/06/08 2700+ 2700+ 2700+ 2700+

10/07/08 2700+ 2700+ 2700+ 2700+

10/08/08 2700+ 2700+ 2700+ 2700+

10/17/08 2680 2700+ 2700+ 2700+

10/16/08 2683 2700+ 2700+ 2700+

10/20/08 2700+ 2700+ 2700+ 2700+

10/21/08 2660 2682 2700+ 2700+

10/22/08 2700+ 2700+ 2700+ 2700+

10/23/08 2700+ 2700+ 2700+ 2700+

10/23/08 2662 2667 2700+ 2700+

10/28/08 2670 2685 2700+ 2700+

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-8 

# GE Energy

TABLE A-4. ASH FUSION TEMPERATURE (CONT.)

DATE

SAMPLED Initial

Deformation Softening Hemispherical Fluid

10/29/08 2645 2697 2700+ 2700+

10/31/08 2700+ 2700+ 2700+ 2700+

10/30/08 2689 2700+ 2700+ 2700+

11/03/08 2685 2700+ 2700+ 2700+

11/04/08 2650 2680 2700+ 2700+

11/04/08 2654 2685 2700+ 2700+

11/04/08 2644 2677 2700+ 2700+

11/04/08 2675 2700+ 2700+ 2700+

11/04/08 2605 2652 2700+ 2700+

11/05/08 2700+ 2700+ 2700+ 2700+

11/05/08 2671 2700+ 2700+ 2700+

11/05/08 2700+ 2700+ 2700+ 2700+

11/05/08 2700+ 2700+ 2700+ 2700+

11/06/08 2700+ 2700+ 2700+ 2700+

11/07/08 2700+ 2700+ 2700+ 2700+

11/10/08 2580 2620 2670 2700+

11/11/08 2485 2515 2608 2684

11/12/08 2650 2691 2700+ 2700+

11/13/08 2450 2560 2600 2649

11/14/08 2475 2495 2590 2635

11/17/08 2581 2619 2659 2700+

11/20/08 2700+ 2700+ 2700+ 2700+

11/21/08 2670 2700+ 2700+ 2700+

11/25/08 2700+ 2700+ 2700+ 2700+

11/26/08 2700+ 2700+ 2700+ 2700+

12/02/08 2700+ 2700+ 2700+ 2700+

12/03/08 2700+ 2700+ 2700+ 2700+

12/04/08 2700+ 2700+ 2700+ 2700+

12/08/08 2640 2655 2664 2700+

12/08/08 2690 2700+ 2700+ 2700+

12/09/08 2667 2700+ 2700+ 2700+

12/09/08 2640 2683 2700+ 2700+

12/09/08 2630 2678 2700+ 2700+

12/10/08 2700+ 2700+ 2700+ 2700+

12/10/08 2639 2670 2700+ 2700+

12/10/08 2675 2700+ 2700+ 2700+

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-9 

# GE Energy

TABLE A-5. ASH ANALYSIS

Moisture As

Received

Sulfur Dry Sulfur Calcium

Oxide Loss On

Ignition

% wet % wet % wet % %

07/11/08 FLYASH-A 0.08 0.17 0.17 1.20 12.73

07/11/08 FLYASH-B 0.02 0.15 0.15 1.17 13.83

09/17/08 FLYASH-BRAVO 0.13 1.40 1.40 12.10 7.60

09/17/08 FLYASH-ALPHA 0.13 1.30 1.30 10.80 8.12

09/18/08 FLYASH B-1 0.40 0.20 0.20 1.13 13.33

09/18/08 FLYASH B-2 0.08 0.12 1.30 1.90 11.91

09/18/08 FLYASH B-3 0.23 1.01 1.01 11.30 4.70

09/18/08 FLYASH B-4 0.06 0.33 0.33 10.20 8.96

09/18/08 FLYASH B-5 0.05 0.10 0.10 11.30 9.21

09/18/08 FLYASH B-6 0.02 0.12 0.12 12.00 8.96

09/19/08 FLYASH A-2 0.20 0.15 0.15 22.10 8.24

09/19/08 FLYASH A-1 0.19 0.04 0.04 1.31 5.26

09/19/08 FLYASH A-3 0.04 0.06 0.06 22.50 6.51

09/19/08 FLYASH B-1 0.38 0.09 0.09 1.16 10.19

09/19/08 FLYASH B-2 0.04 0.03 0.03 23.00 9.05

09/19/08 FLYASH B-3 0.17 0.08 0.08 25.90 8.84

09/24/08 FLYASH A-1 0.18 2.03 2.03 24.00 5.69

09/24/08 FLYASH A-2 0.11 1.91 1.91 15.50 3.56

09/24/08 FLYASH A-3 0.14 1.87 1.87 13.60 5.28

09/24/08 FLYASH B-1 0.18 1.37 1.37 25.10 8.05

09/24/08 FLYASH B-2 0.15 1.51 1.51 14.60 5.17

09/24/08 FLYASH B-3 0.19 2.33 2.33 15.60 5.69

09/25/08 10-R3 A 0.08 2.48 2.48 16.30 6.03

09/25/08 11-R3 A 0.18 2.00 2.00 15.90 7.39

09/25/08 12-R3 A 0.10 0.13 0.13 25.70 7.68

09/25/08 10-R3 B 0.15 0.20 0.20 12.80 7.48

09/25/08 11-R3 B 0.06 0.11 0.11 15.20 5.32

09/25/08 12-R3 B 0.05 0.02 0.02 19.50 3.07

09/29/08 A 4.0 1.50 0.16 0.16 2.51 4.84

09/29/08 A 4.1 0.63 1.24 1.25 11.30 6.90

09/29/08 A 4.2 0.04 1.68 1.68 20.10 6.40

09/29/08 A 4.3 0.56 1.73 1.74 21.70 4.82

09/29/08 B 4.0 0.26 0.22 0.22 3.35 8.96

09/29/08 B 4.1 0.19 0.98 0.98 10.70 7.19

09/29/08 B 4.2 0.14 1.53 1.53 19.90 8.28

10/01/08 B 6.0 0.03 0.27 0.27 2.43 12.37

10/01/08 B 6.3 0.07 1.49 1.49 21.20 8.43

10/01/08 B 6.3-R 0.03 1.78 1.78 23.50 7.83

10/01/08 B 6.2 0.43 1.67 1.68 18.30 7.44

10/01/08 B 6.1 0.04 1.35 1.35 11.90 6.49

IDENTIFICATION DATE

SAMPLED

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-10 

# GE Energy

TABLE A-5. ASH ANALYSIS (CONT.)

DATE

SAMPLED IDENTIFICATION Moisture As

Received

Sulfur Dry Sulfur Calcium

Oxide Loss On

Ignition

% wet % wet % wet % %

10/01/08 A 6.0 0.06 0.27 0.27 2.29 11.47

10/01/08 A 6.3 0.09 1.90 1.90 23.60 8.35

10/01/08 A 6.3-R 0.06 1.81 1.81 23.50 4.78

10/01/08 A 6.2 0.11 1.96 1.96 20.90 4.91

10/01/08 A 6.1 0.12 1.84 1.84 13.90 3.43

09/30/08 A 5.0 0.04 0.29 0.29 3.58 7.70

09/30/08 A 5.1 0.11 1.58 1.58 20.30 7.56

09/30/08 A 5.2 6.43 1.75 1.87 20.60 1.91

09/30/08 A 5.3 0.09 1.77 1.77 19.00 5.16

09/30/08 A 5.4 0.08 1.84 1.84 19.80 8.90

09/30/08 B 5.1 0.08 1.96 1.96 24.40 8.69

09/30/08 B 5.2 0.06 1.79 1.79 20.70 7.95

10/02/08 A 7.0 0.19 0.19 0.19 1.27 17.31

10/02/08 B 7.3 0.12 1.81 1.81 17.50 13.63

10/02/08 B 7.0 0.13 0.19 0.19 1.24 18.53

10/02/08 A 7.3 0.05 1.67 1.67 20.30 14.14

10/03/08 B8.0 0.06 0.19 0.19 1.86 8.48

10/03/08 B8.1 0.03 1.30 1.30 10.40 6.42

10/03/08 B8.3 0.10 1.53 1.53 22.30 7.11

10/03/08 A8.0 0.02 0.23 0.23 2.38 6.98

10/03/08 A8.1 0.04 1.19 1.19 11.50 7.50

10/03/08 A8.2 0.04 2.12 2.12 19.90 7.17

10/03/08 A8.3 0.04 1.72 1.72 20.10 5.19

10/03/08 B8.2 0.03 1.80 1.80 21.10 8.15

10/06/08 A 9.0 0.04 0.13 0.13 1.62 5.99

10/06/08 A 9.1 0.03 2.22 2.22 24.90 6.41

10/06/08 A 9.2 0.32 1.96 1.97 25.30 5.26

10/06/08 B 9.0 0.03 0.02 0.02 1.84 6.35

10/06/08 B 9.1 0.17 1.87 1.87 25.30 6.47

10/06/08 B 9.2 0.04 1.86 1.86 26.50 6.35

10/06/08 B 9.3 0.04 1.53 1.53 25.60 6.29

10/07/08 A 10.0 0.10 1.65 1.65 2.07 2.90

10/07/08 A 10.1 0.05 1.07 1.07 10.30 2.64

10/07/08 A 10.2 0.07 1.64 1.64 14.50 3.07

10/07/08 A 10.3 0.06 1.80 1.80 16.50 3.77

10/07/08 B 10.0 0.06 0.49 0.49 2.72 5.64

10/07/08 B 10.1 0.05 1.18 1.18 10.50 6.67

10/07/08 B 10.2 0.07 1.10 1.10 12.70 6.21

10/07/08 B 10.3 0.03 2.11 2.11 18.70 6.54

10/08/08 B 11.0 0.04 0.17 0.17 1.52 7.42

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-11 

# GE Energy

TABLE A-5. ASH ANALYSIS (CONT.)

DATE

SAMPLED IDENTIFICATION Moisture As

Received

Sulfur Dry Sulfur Calcium

Oxide Loss On

Ignition

% wet % wet % wet % %

10/08/08 B 11.1 0.16 2.42 2.42 24.10 5.85

10/08/08 B 11.2 0.10 1.64 1.64 21.40 4.57

10/08/08 B 11.3 0.05 1.72 1.72 22.70 5.77

10/08/08 A 11.0 0.15 0.09 0.09 1.57 6.48

10/08/08 A 11.1 0.07 2.29 2.29 19.40 3.91

10/08/08 A 11.2 0.07 2.46 2.46 25.00 5.68

10/08/08 A 11.3 0.03 2.10 2.10 23.00 3.23

10/20/08 A1.1 0.03 1.34 1.34 11.20 5.65

10/20/08 A1.0 0.10 1.06 1.06 11.30 2.96

10/20/08 B1.1 0.04 1.59 1.59 14.40 5.82

10/20/08 B1.0 0.04 1.10 1.10 13.40 5.58

10/21/08 A 0.06 1.58 1.58 12.30 5.20

10/21/08 B 0.04 1.94 1.94 15.00 6.76

10/22/08 A 0.04 2.48 2.48 17.10 4.21

10/22/08 B 0.03 2.55 2.55 18.20 5.91

10/23/08 B 0.03 1.51 1.51 18.60 5.55

10/23/08 A 0.02 2.26 2.26 18.50 2.09

10/28/08 A 0.03 0.23 0.23 2.03 9.26

10/28/08 B 0.06 0.20 0.20 1.75 11.12

10/29/08 A 0.08 0.11 0.11 1.06 5.58

10/29/08 B 0.15 0.10 0.10 1.07 7.56

10/31/08 A 0.04 0.98 0.98 9.70 6.15

10/31/08 B 0.03 0.89 0.89 8.26 7.05

10/30/08 A-1 0.04 1.70 1.70 2.11 7.31

10/30/08 A-2 0.11 1.43 1.43 15.70 6.82

10/30/08 B-1 0.06 1.64 1.64 2.38 9.01

10/30/08 B-2 0.05 0.70 0.70 13.30 10.33

11/03/08 A 0.05 1.95 1.95 26.00 4.69

11/03/08 B 0.04 1.78 1.78 16.60 6.47

11/04/08 B 1.04 1.87 1.89 30.60 5.41

11/04/08 A 0.05 1.91 1.91 32.50 5.30

11/04/08 B-2 0.04 2.43 2.43 29.90 6.41

11/04/08 A-2 0.04 2.62 2.62 31.70 6.27

11/05/08 B MID 0.03 2.02 2.02 29.90 8.98

11/05/08 A MID 0.04 2.31 2.31 28.30 6.97

11/05/08 A LOW 0.04 1.92 1.92 31.40 4.96

11/05/08 B LOW 0.03 1.83 1.83 26.10 3.56

11/06/08 A FSI 0.04 2.51 2.51 25.00 4.63

11/06/08 B FSI 0.05 2.13 2.13 22.70 5.00

11/06/08 B NON-FSI 0.03 0.71 0.71 7.39 3.84

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix A, Rev. 02

Contract No. XM10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page A-12 

# GE Energy

TABLE A-5. ASH ANALYSIS (CONT.)

DATE

SAMPLED IDENTIFICATION Moisture As

Received

Sulfur Dry Sulfur Calcium

Oxide Loss On

Ignition

% wet % wet % wet % %

11/06/08 A NON-FSI 0.04 0.85 0.85 8.72 3.54

11/07/08 A 0.03 3.06 3.06 24.50 4.09

11/07/08 B 0.01 3.15 3.15 19.50 4.96

11/10/08 A 0.06 2.78 2.78 25.80 3.27

11/10/08 B 0.03 2.78 2.78 21.20 4.77

11/11/08 A 0.06 1.86 1.86 22.90 4.66

11/11/08 B 0.06 1.75 1.75 24.10 6.59

11/12/08 B 0.04 1.95 1.95 23.00 6.75

11/12/08 A 0.10 2.42 2.42 18.00 4.87

11/13/08 B 0.07 3.56 3.56 24.30 5.77

11/13/08 A 0.06 3.10 3.10 25.20 6.28

11/14/08 A 0.04 2.75 2.75 26.70 3.85

11/14/08 B 0.09 2.16 2.16 28.80 5.28

11/17/08 A 0.12 0.58 0.58 3.11 8.09

11/17/08 B 0.06 0.64 0.64 3.19 9.73

11/21/08 B 0.02 1.76 1.76 22.70 6.16

11/21/08 A 0.06 1.82 1.82 21.20 5.69

11/25/08 B 0.07 2.31 2.31 42.90 7.97

11/25/08 A 0.04 2.15 2.15 26.00 6.30

11/26/08 A 0.03 2.13 2.13 23.20 6.52

11/26/08 B 0.06 1.74 1.74 22.10 7.51

12/02/08 B PET-3 0.06 2.08 2.08 27.60 2.12

12/02/08 A PET-3 0.06 1.92 1.92 29.10 3.20

12/02/08 B PET-1 0.03 1.92 1.92 24.30 1.79

12/02/08 A PET-1 0.07 1.49 1.49 26.60 0.58

12/02/08 A PET-2 0.08 2.53 2.53 23.60 4.40

12/02/08 B PET-2 0.03 1.78 1.78 24.50 1.69

12/03/08 A PET-5 0.05 2.28 2.28 25.90 5.26

12/03/08 B PET-5 0.06 1.76 1.76 27.60 6.93

12/03/08 A PET-4 0.14 0.98 0.98 23.70 4.02

12/03/08 B PET-4 0.06 1.04 1.04 25.90 8.11

12/03/08 A PET-6 0.07 2.50 2.50 24.20 6.24

12/03/08 B PET-6 0.05 1.94 1.94 29.70 7.86

12/05/08 A 0.06 2.32 2.32 20.50 2.74

12/05/08 B 0.06 2.01 2.01 21.50 5.00

12/04/08 A PET-7 0.08 2.10 2.10 28.30 4.11

12/04/08 B PET-7 0.15 1.49 1.49 28.70 2.80

12/04/08 A PET-8 0.06 2.34 2.34 35.60 5.21

12/04/08 B PET-8 0.04 1.90 1.90 29.40 6.75

12/04/08 A PET-9 0.06 2.41 2.41 34.90 4.92

12/04/08 B PET-9 0.07 2.21 2.21 28.80 6.89

# GE Energy



# Progress Energy

Robinson Unit 1

Furnace Sorbent Injection

Demonstration Project

Final Report, Rev. 02

Appendix B: Test Data

Contract No. 10023-WA169

GE Job Number 6900

25 February 2009

GE Energy and Environmental Research Corporation

1831 East Carnegie Ave

Santa Ana, CA 92705

# Progress Energy Robinson Unit 1 Furnace Sorbent Inj ection Demonstration Project Final Report, Appendix B, Rev. 02

Contract No. 10023-WA169, GE JN 6900 25 February 2009

GE Proprietary Information Page B-i 

# GE Energy



# List of Tables

Table Page

B-1. Preliminary Test Data ....................................................................................................... 1

B-2. Parametric Test Data......................................................................................................... 4

B-3. Long-Term Trial Data....................................................................................................... 8Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-1GE EnergyTABLE B-1. PRELIMINARY TEST DATATest DateRunBaselineRun 1BaselineRun 1Run 2Run 3BaselineRun 1BaselineRun 1Test ID2.02.12.22.32.42.52.62.72.82.9Start Time10:0112:0112:0014:0115:0116:017:3111:3010:3112:31Stop Time11:0014:0013:0015:0016:0017:008:3012:3011:3014:20ParametersUnitGross Electrical OutputMWg153.69153.14136.86137.33137.70137.92164.54161.84170.72171.24Net Electrical OutputMWn144.51143.96128.44128.59129.02129.14154.94152.26161.34161.41Exit O2%, wet 3.00 4.21 3.36 4.18 4.16 3.86 2.91 4.18 2.91 4.17Air TemperatureAir Heater Air InletoF90.2295.4677.6777.8777.6377.7170.7774.3877.7583.55Air Heater Air OutletoF478.84497.94462.68475.80480.82481.38472.99487.23476.30492.30Ambient TemperatureoF90.2295.4677.6777.8777.6377.7170.7774.3877.7583.55ESP Exit TemperatureoF264.00274.43243.18246.80251.90255.98247.96258.24255.39268.50Flue Gas TemperatureFlue Gas to AH TemperatureoF575.50586.52567.03569.23570.50571.62580.76587.10586.36591.17Gas Out from AH TemperatureoF266.81287.15247.42261.51264.82263.29253.96270.48261.12278.74Air Heater Differential PressureIN W.C.2.452.832.062.382.332.262.693.032.843.32SorbentSorbent Feed Ratelb/hr07,20005,0005,0005,00003,10003,109Injection Air Flow RateCFM3617,0003217,00017,00017,0003217,0004016,892lb/hr16777,92814477,92877,92877,92814577,92818377,432Injection ConfigurationElevation-UpperUpperUpperUpperUpperUpperUpperUpperUpperUpper# Injectors-121212128812121212Stack - CEMStack Flow Rate kscfm 358.36 384.81 339.04 355.01 352.20346.91 358.63 405.15 393.73 424.38lb/hr 640,665 687,940 606,128 634,679 629,643 620,192 641,138 724,302 703,895 758,698Stack Temperature oF 277.46 293.27 251.11 258.28 266.53 264.99 255.21 270.14 264.83 283.55NOXEmissionlb/MMBTU0.290.320.270.280.280.280.290.320.300.33SO2Emission lb/MMBTU 1.76 0.99 1.79 1.21 1.15 1.39 1.83 1.46 1.71 1.29CO2Emission%12.0911.0811.7610.9610.9811.1412.1411.2812.3511.27Opacity % 16.45 26.83 15.09 17.76 19.40 18.82 18.28 24.71 18.34 27.36Baseline SO2lb/MMBtu1.761.761.791.791.791.791.831.831.711.71Ca/S-N/A2.37N/A1.771.781.78N/A0.92N/A0.94SO2Reduction%N/A43.54N/A32.1335.8922.43N/A20.02N/A24.34Sorbent Utilization%N/A18.34N/A18.1320.1312.57N/A21.88N/A25.909/15/20089/16/20089/17/20089/18/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-2GE EnergyTABLE B-1. PRELIMINARY TEST DATA (CONT.)Test Date9/18/20089/24/2008RunRun 2BaselineRun 1Run 2BaselineRun 1BaselineRun 1Run 2BaselineTest ID2.102.112.122.13Baseline11R1Baseline12R110R1BaselineStart Time15:019:1613:0114:1112:1613:517:409:5512:017:41Stop Time16:3010:1514:0015:1013:1515:408:4011:5014:008:40ParametersUnitGross Electrical OutputMWg171.08138.71138.77138.89153.98154.18123.37144.21164.30133.57Net Electrical OutputMWn161.29129.99129.99129.98144.97144.97115.03135.20154.72124.99Exit O2%, wet 4.15 3.18 4.20 4.19 2.99 4.17 3.58 4.10 4.19 3.09Air TemperatureAir Heater Air InletoF84.4271.0478.0778.7480.5882.7466.5371.4375.3862.71Air Heater Air OutletoF491.95470.68496.64500.47479.16493.15467.79495.74501.64469.42Ambient TemperatureoF84.4271.0478.0778.7480.5882.7466.5371.4375.3862.71ESP Exit TemperatureoF268.04247.32269.06269.54256.26264.79243.53262.20268.93240.56Flue Gas TemperatureFlue Gas to AH TemperatureoF591.85563.57578.07583.63578.59583.23551.39585.16599.31557.65Gas Out from AH TemperatureoF279.11252.82280.47282.75260.97278.30249.50276.42280.53247.64Air Heater Differential PressureIN W.C.3.372.122.412.412.412.791.862.573.121.98SorbentSorbent Feed Ratelb/hr3,10007,0106,91203,11808,9512,5130Injection Air Flow RateCFM16,5463316,16816,2343916,2672415,45717,31330lb/hr75,84715274,11374,41818174,56811170,85679,362136Injection ConfigurationElevation-UpperUpperUpperUpperUpperUpperUpperUpperUpperUpper# Injectors-12121212121212121212Stack - CEMStack Flow Rate kscfm 428.20 341.68 355.27 356.13 359.85384.23 299.04 365.71 405.70 308.97lb/hr 765,511 610,836 635,132 636,676 643,330 686,903 534,609 653,798 725,296 552,364Stack Temperature oF 281.22 253.18 280.51 280.88 263.65 279.14 246.39 273.08 281.75 243.19NOXEmissionlb/MMBTU0.330.290.280.270.260.280.260.280.310.246SO2Emission lb/MMBTU 1.41 1.70 0.86 0.86 1.93 1.51 2.06 0.97 1.56 2.13CO2Emission%11.1712.0111.1811.1412.1911.2811.5311.2311.2512.05Opacity % 32.66 15.72 26.13 29.43 3.61 5.21 4.27 7.74 15.43 3.79Baseline SO2lb/MMBtu1.711.701.701.701.931.932.062.062.062.13Ca/S-0.94N/A2.552.52N/A0.92N/A2.610.66N/ASO2Reduction%17.44N/A49.5149.30N/A21.93N/A53.0824.4N/ASorbent Utilization%18.60N/A19.3919.56N/A23.89N/A20.3737.0N/A9/19/20089/22/20089/23/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-3GE EnergyTABLE B-1. PRELIMINARY TEST DATA (CONT.)Test DateRunRun 1Run 2Run 3Run L1Baseline LowBaselineRun 1Run 2Test ID12R211R210R2LOWBaseline LowBaseline10R311R3Start Time9:3110:5512:0613:2114:018:3111:3112:41Stop Time10:3011:5513:0513:5014:309:3012:3013:00ParametersUnitGross Electrical OutputMWg133.95133.78133.74133.73131.8698.1498.78125.74Net Electrical OutputMWn125.02124.99125.05125.00123.3790.0390.78117.02Exit O2%, wet 4.00 4.12 4.19 4.28 3.34 4.43 4.98 3.98Air TemperatureAir Heater Air InletoF65.5469.2172.1074.0074.1765.2067.1568.33Air Heater Air OutletoF486.06491.75491.96491.68481.36456.46469.11480.72Ambient TemperatureoF65.5469.2172.1074.0074.1765.2067.1568.33ESP Exit TemperatureoF251.19261.25261.76260.44257.85232.96244.13252.95Flue Gas TemperatureFlue Gas to AH TemperatureoF566.88570.46569.19567.60564.68536.12542.39557.71Gas Out from AH TemperatureoF267.29272.63272.43274.49260.51239.05255.95266.64Air Heater Differential PressureIN W.C.2.292.192.212.221.971.461.622.07SorbentSorbent Feed Ratelb/hr9,0033,1002,5793,050002,5643,077Injection Air Flow RateCFM15,66215,71615,75616,137323212,86815,910lb/hr71,79772,04172,22573,97414614758,98772,932Injection ConfigurationElevation-UpperUpperUpperLowerLowerUpperUpperUpper# Injectors-1212121212121212Stack - CEMStack Flow Rate kscfm 342.44 340.74 341.06 342.13 326.29274.24 281.07 329.04lb/hr 612,192 609,163 609,738 611,646 583,322 490,266 502,486 588,236Stack Temperature oF 257.59 267.65 268.25 268.76 264.11 236.33 249.02 259.32NOXEmissionlb/MMBTU0.2510.2470.2490.2550.2590.250.230.22SO2Emission lb/MMBTU 1.09 1.53 1.67 1.68 2.16 2.32 1.70 1.71CO2Emission%11.3111.2511.2311.2111.7210.6410.3711.14Opacity % 5.77 8.32 9.48 10.01 5.08 4.12 1.45 2.76Baseline SO2lb/MMBtu2.132.132.132.162.162.322.322.32Ca/S-2.690.940.780.91N/AN/A0.930.89SO2Reduction%48.8028.0621.7622.10N/AN/A26.8526.54Sorbent Utilization%18.1229.9327.9024.32N/AN/A28.7429.759/24/20089/25/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-4GE EnergyTABLE B-2. PARAMETRIC TEST DATATest DateRunBaselineRun 1Run 2Run 3BaselineRun 1Run 2Run 3Run 4Test ID4.04.14.24.34.44.54.64.74.7.1Start Time8:4110:3112:2513:459:3110:4112:1913:4415:31Stop Time9:4011:3013:2614:4610:0011:4013:1514:4615:55ParametersUnitGross Electrical OutputMWg159.47159.19157.97157.73158.78160.73160.57158.32158.39Net Electrical OutputMWn150.50149.67148.60148.42149.63151.38151.13148.99148.91Exit O2%, wet 2.96 4.16 4.18 4.14 2.94 4.13 4.19 4.15 4.15Air TemperatureAir Heater Air InletoF74.5372.3679.5284.6368.5875.0279.2184.5088.36Air Heater Air OutletoF474.32488.99492.98497.25471.50491.53499.86499.75504.13Ambient TemperatureoF74.5372.3679.5284.6368.5875.0279.2184.5088.36ESP Exit TemperatureoF251.91260.49268.36273.28249.12260.22269.14274.40275.85Flue Gas TemperatureFlue Gas to AH TemperatureoF575.89584.48593.84599.70576.29588.05599.95598.49596.08Gas Out from AH TemperatureoF257.03273.90279.58282.53250.29272.66281.77283.86288.55Air Heater Differential PressureIN W.C.2.522.932.902.942.642.993.022.952.97SorbentSorbent Feed Ratelb/hr02,4986,9048,218457,2046,6776,5666,011Injection Air Flow RateCFM4416,96016,73516,5991,35915,15216,88817,88718,996lb/hr20277,74676,71376,0886,23169,45577,41481,99387,076Injection ConfigurationElevation-UpperUpperUpperUpperUpperUpperUpperUpperUpper# Injectors-121212121212121212Stack - CEMStack Flow Rate kscfm 367.19 391.74 392.23 392.91 369.16397.53 395.50 393.18 392.93lb/hr 1,683,199 1,795,744 1,797,985 1,801,114 1,692,245 1,822,278 1,812,972 1,802,341 1,801,200Stack Temperature oF 260.62 277.31 285.31 288.58 253.35 278.45 288.28 291.62 294.62NOXEmissionlb/MMBTU0.310.290.300.300.260.320.310.300.30SO2Emission lb/MMBTU 1.79 1.41 1.00 0.98 1.60 0.87 0.84 0.80 0.81CO2Emission%12.3111.3111.3011.2812.2411.2611.2511.2611.21Opacity % 5.03 6.91 12.30 16.76 7.65 17.39 24.35 27.06 29.24Baseline SO2lb/MMBtu1.791.791.791.791.601.601.601.601.60Ca/S-N/A0.782.152.55N/A2.482.322.292.11SO2Reduction%N/A21.2544.0345.39N/A45.7747.6949.6949.24Sorbent Utilization%N/A27.3520.5017.77N/A18.4320.5921.7123.399/30/20089/29/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-5GE EnergyTABLE B-2. PARAMETIC TEST DATA (CONT.)Test DateRunBaselineRun 1Run 2Run 3BaselineRun 1Run 2Run 3Run 4Run 5Test ID4.84.94.104.114.164.184.174.18.14.194.19.1Start Time12:3514:0014:4115:415:016:478:219:019:4110:33Stop Time13:3514:3015:3516:476:007:158:409:3010:3011:05ParametersUnitGross Electrical OutputMWg159.05159.30159.24159.2376.1176.5776.3376.5176.3776.29Net Electrical OutputMWn150.00150.08149.99149.9969.9569.9570.0470.0370.0169.99Exit O2%, wet 2.92 4.31 4.26 4.26 5.66 5.80 5.91 5.89 5.90 5.93Air TemperatureAir Heater Air InletoF82.2584.3584.0084.2156.8255.7058.2863.4267.5068.92Air Heater Air OutletoF483.05496.53496.62495.76442.18448.72450.99453.58456.40457.96Ambient TemperatureoF82.2584.3584.0084.2156.8255.7058.2863.4267.5068.92ESP Exit TemperatureoF263.67264.95270.77271.11229.69231.20232.70233.48234.40235.19Flue Gas TemperatureFlue Gas to AH TemperatureoF589.29588.34590.22590.84515.11516.56518.13519.07520.12521.03Gas Out from AH TemperatureoF262.28280.57280.12279.95229.04234.43235.55239.62243.26245.68Air Heater Differential PressureIN W.C.2.542.912.942.941.231.291.231.191.131.14SorbentSorbent Feed Ratelb/hr66,9505,0312,56501,5191,4283,0503,1403,099Injection Air Flow RateCFM9616,63917,09817,416368,61910,02610,42310,81111,050lb/hr44176,27278,37979,83616739,51045,96147,78149,55850,654Injection ConfigurationElevation-LowerLowerLowerLowerN/ALowerLowerLowerLowerLower# Injectors-12121212N/A12Top 681012Stack - CEMStack Flow Rate kscfm 363.72 390.84 389.65 390.23 241.96246.75 277.93 244.69 244.10 244.49lb/hr 6,735,831 1,791,595 1,786,160 1,788,793 110,913 1,131,094 1,274,021 1,121,659 1,118,945 1,120,746Stack Temperature oF 271.35 283.39 285.42 285.71 229.15 233.03 235.33 238.63 241.53 244.62NOXEmissionlb/MMBTU0.270.310.300.300.330.290.290.280.280.28SO2Emissionlb/MMBTU1.51 0.87 0.97 1.20 1.60 1.23 1.30 0.85 0.79 0.76CO2Emission%12.0811.1911.1711.149.869.809.909.899.849.78Opacity % 12.19 28.21 27.45 27.23 1.86 2.00 2.57 4.32 3.83 4.03Baseline SO2lb/MMBtu1.511.511.511.511.601.601.601.601.601.60Ca/S-N/A2.601.890.96N/A0.970.801.942.022.00SO2Reduction%N/A42.3335.7420.42N/A23.3018.8546.7450.8552.31Sorbent Utilization%N/A16.3118.9221.20N/A24.0623.5424.0425.2126.1510/1/200810/2/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-6GE EnergyTABLE B-2. PARAMETIC TEST DATA (CONT.)Test DateRunBaselineRun 1Run 2Run 3BaselineRun 1Run 2Test ID4.124.134.144.154.204.214.22Start Time8:3010:2011:4813:159:3011:0512:25Stop Time9:3011:3013:0014:3010:3012:1413:25ParametersUnitGross Electrical OutputMWg158.25158.56158.68158.57156.85158.69158.67Net Electrical OutputMWn150.04149.97150.01149.99148.69150.01150.03Exit O2%, wet 2.85 3.67 3.68 3.68 2.97 3.63 3.65Air TemperatureAir Heater Air InletoF61.3675.3279.9282.3173.1879.0579.57Air Heater Air OutletoF477.05488.61495.23501.04480.28499.12507.13Ambient TemperatureoF61.3675.3279.9282.3173.1879.0579.57ESP Exit TemperatureoF249.22257.68267.34272.75254.51265.89276.39Flue Gas TemperatureFlue Gas to AH TemperatureoF581.44580.58585.16589.71580.18585.00595.27Gas Out from AH TemperatureoF248.47271.61278.63283.20257.60281.85287.99Air Heater Differential PressureIN W.C.2.342.732.742.752.302.742.71SorbentSorbent Feed Ratelb/hr02,5904,9877,04307,0097,044Injection Air Flow RateCFM3316,74916,64916,5743917,92416,807lb/hr15076,77676,32175,97717782,16677,044Injection ConfigurationElevation-N/AUpperUpperUpperUpperUpperUpper# Injectors-N/A121212121212Stack - CEMStack Flow Ratekscfm 356.58 377.73 379.41 378.99 353.07 377.38 378.07lb/hr 637,471 1,731,493 1,739,201 1,737,282 3,544,411 1,729,916 1,733,068Stack TemperatureoF 247.63 269.40 279.72 284.58 259.05 281.48 288.55NOXEmissionlb/MMBTU0.530.500.500.510.500.500.50SO2Emissionlb/MMBTU 1.64 1.28 1.07 0.94 1.62 0.99 0.89CO2Emission%12.5411.8911.8411.8312.6311.9511.93Opacity % 5.48 11.65 16.78 21.08 5.44 17.77 23.14Baseline SO2lb/MMBtu1.641.641.641.641.621.621.62Ca/S-N/A0.871.672.36N/A2.372.38SO2Reduction%N/A21.8334.9842.46N/A38.8445.08Sorbent Utilization%N/A25.1720.9617.97N/A16.3718.9010/6/200810/3/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-7GE EnergyTABLE B-2. PARAMETIC TEST DATA (CONT.)Test DateRunBaselineRun 1Run 2Run 3Run 4Run 5Run 6Test ID4.244.254.264.274.284.294.30Start Time8:5610:3111:3512:1413:3514:5817:00Stop Time10:0411:0012:0613:0114:2716:2217:35ParametersUnitGross Electrical OutputMWg177.59176.19177.56177.92181.24181.73180.59Net Electrical OutputMWn168.85167.11168.48168.86172.01172.52171.52Exit O2%, wet 2.75 3.67 3.24 3.23 3.28 3.28 3.26Air TemperatureAir Heater Air InletoF66.7969.2771.1572.5074.7375.7176.40Air Heater Air OutletoF479.95486.76489.13491.40493.05494.98496.96Ambient TemperatureoF66.7969.2771.1572.5074.7375.7176.40ESP Exit TemperatureoF254.69259.16261.35262.88265.60268.83272.01Flue Gas TemperatureFlue Gas to AH TemperatureoF589.65591.44592.99594.10596.09598.30599.93Gas Out from AH TemperatureoF257.53270.29271.52273.46275.20277.30279.14Air Heater Differential PressureIN W.C.2.803.283.103.173.253.303.29SorbentSorbent Feed Ratelb/hr001562,5352,5303,8734,985Injection Air Flow RateCFM10415,22115,04714,80914,90716,02915,987lb/hr47569,77268,97567,88668,33573,47573,284Injection ConfigurationElevation-N/AN/AUpperUpperUpperUpperUpper# Injectors-N/AN/A1212121212Stack - CEMStack Flow Rate kscfm 389.56 417.71 410.77 412.13 419.01421.20 419.30lb/hr 3,303,632 1,914,784 1,882,950 1,889,191 1,920,757 1,930,765 1,922,058Stack Temperature oF 2.32 2.28 2.24 1.96 2.11 2.06 1.92NOXEmissionlb/MMBTU0.470.490.460.460.470.470.47SO2Emission lb/MMBTU 2.32 2.28 2.24 1.96 2.11 2.06 1.92CO2Emission%12.8212.0212.3612.3612.3012.2912.31Opacity % 7.65 10.77 9.35 12.47 16.52 20.69 23.46Baseline SO2lb/MMBtu2.322.282.322.322.322.322.32Ca/S-N/AN/A0.030.530.520.801.03SO2Reduction%N/AN/A3.5115.519.2111.2217.14Sorbent Utilization%N/AN/A107.7329.3417.6614.1016.6910/7/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-8GE EnergyTABLE B-3. LONG-TERM TRIAL DATATest DateRunRun 1 Run 2 Run 3 Run 4 Run 1 Run 2 Run 3 Run 1 Run 2 Run 3Start Time1:18 7:00 13:54 15:48 1:12 12:30 15:12 0:06 11:48 15:12Stop Time6:00 12:00 14:54 22:30 6:00 14:54 21:00 6:12 14:48 20:12Parameters UnitGross Electrical OutputMWg64.2664.31147.01181.7562.86183.73183.8970.46183.82184.79Net Electrical OutputMWn59.0659.00139.25172.8257.69174.48175.0765.02174.90175.48Exit O2%, wet 5.52 5.54 3.20 2.82 5.64 3.30 2.78 5.34 2.78 3.66Air TemperatureAir Heater Air InletoF67.0368.0677.0276.7567.2478.7379.0365.9281.6684.51Air Heater Air OutletoF441.80444.84479.16481.80443.15493.95484.10447.72485.11495.74Ambient TemperatureoF67.0368.0677.0276.7567.2478.7379.0365.9281.6684.51ESP Exit TemperatureoF227.16227.86249.82254.43229.65264.73259.78233.48261.31269.51Flue Gas TemperatureFlue Gas to AH TemperatureoF503.96506.61570.02589.39506.13597.58595.47513.69595.03600.48Gas Out from AH TemperatureoF229.67232.85262.30264.21229.89276.20265.38230.36267.68279.16Air Heater Differential PressureIN W.C.0.920.942.192.940.943.272.980.992.973.45SorbentSorbent Feed Ratelb/hr000002,1850002,535Injection Air Flow RateCFM383941383514,98938383713,831lb/hr17218019017616168,71117317416963,400Injection ConfigurationElevation-N/AN/AN/AN/AN/AUpperN/AN/AN/AUpper# Injectors - N/A N/A N/A N/A N/A 12 N/A N/A N/A 12Stack - CEMStack Flow Rate kscfm 206.97 206.45 344.94 401.79 204.45418.94 406.15 214.36 402.58 428.04lb/hr 208,726 946,344 1,581,205 1,841,784 196,809 1,920,421 1,861,803 98,265 1,845,444 1,962,150Stack Temperature oF 231.42 232.16 259.44 266.42 233.02 279.52 270.05 234.85 270.16 285.90NOXEmission lb/MMBTU 0.80 0.81 0.51 0.47 0.85 0.46 0.47 0.77 0.47 0.66SO2Emission lb/MMBTU 2.25 1.85 2.24 2.10 1.43 1.74 1.89 1.53 1.72 1.55CO2Emission % 9.93 9.99 12.37 12.81 9.92 12.36 12.82 10.15 12.88 11.64Opacity % 7.40 6.99 8.35 10.13 7.22 13.80 12.95 7.16 9.85 21.20Baseline SO2lb/MMBtu 2.25 1.85 2.24 2.10 1.43 1.89 1.89 1.53 1.72 1.72Ca/S-N/AN/AN/AN/AN/A0.55N/AN/AN/A0.73SO2Reduction%N/AN/AN/AN/AN/A7.8N/AN/AN/A10.0Sorbent Utilization%N/AN/AN/AN/AN/A14.23N/AN/AN/A13.6810/12/2008 10/13/2008 10/14/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-9GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 1 Run 2 Run 3 Run 4 Run 5 Run 1 Run 2 Run 1 Run 2 Run 3Start Time0:06 7:42 10:54 13:24 16:06 0:06 15:36 0:30 7:00 12:24Stop Time5:30 10:36 13:06 14:36 21:36 5:12 22:18 5:24 9:54 13:06Parameters UnitGross Electrical OutputMWg66.62181.10181.48182.70181.5070.66183.2770.56137.48168.07Net Electrical OutputMWn60.98171.77172.67173.43172.3665.02174.1064.99129.69159.39Exit O2%, wet 6.20 3.71 2.77 3.71 3.72 5.93 3.72 5.88 3.43 2.75Air TemperatureAir Heater Air InletoF63.4170.0284.2989.7484.2564.0884.8073.2374.0484.47Air Heater Air OutletoF462.50492.25484.99493.61491.36461.46495.23463.06482.21482.09Ambient TemperatureoF63.4170.0284.2989.7484.2564.0884.8073.2374.0484.47ESP Exit TemperatureoF245.47261.49263.82267.83266.39245.85271.43249.59258.30263.74Flue Gas TemperatureFlue Gas to AH TemperatureoF522.40602.32599.46599.22598.41524.67600.21525.14571.66580.81Gas Out from AH TemperatureoF243.69269.46267.19280.17275.04243.33279.38248.22261.26266.69Air Heater Differential PressureIN W.C.1.093.372.963.363.331.073.451.162.062.69SorbentSorbent Feed Ratelb/hr2,5182,4529232,5202,5332,9993,01300Injection Air Flow RateCFM12,23013,9373511,7718,82311,49812,02510,1751,60534lb/hr56,06463,88816153,95840,44552,70655,12546,6437,357157Injection ConfigurationElevation-UpperUpperN/AN/AUpperLowerUpperLowerUpperUpper# Injectors - 12 12 N/A N/A 12 12 12 12 12 12Stack - CEMStack Flow Rate kscfm 225.45 409.60 397.79 424.26 421.04232.37 424.27 229.24 325.80 375.41lb/hr 103,345 1,877,591 1,823,455 1,944,815 1,930,028 106,520 1,944,863 147,116 1,493,482 1,720,891Stack Temperature oF 252.76 274.43 271.99 284.10 282.23 252.35 287.03 259.34 263.11 269.64NOXEmission lb/MMBTU 0.79 0.56 0.52 0.48 0.53 0.76 0.53 0.76 0.58 0.46SO2Emission lb/MMBTU 0.77 1.86 1.77 2.01 1.81 1.06 1.76 1.06 1.89 1.87CO2Emission % 9.35 11.46 12.48 10.66 11.82 9.50 11.74 9.48 11.87 12.50Opacity % 9.72 27.50 26.27 37.82 33.54 10.11 29.77 10.10 13.56 18.70Baseline SO2lb/MMBtu 1.53 2.01 1.77 2.01 2.01 1.06 1.89 1.87Ca/S-1.930.64N/AN/A0.62N/AN/AN/AN/AN/ASO2Reduction%49.867.60N/AN/A9.8N/AN/AN/AN/AN/ASorbent Utilization%25.8511.85N/AN/A15.81N/AN/AN/AN/AN/A10/15/2008 10/16/2008 10/17/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-10GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 4 Run 5 Run 1 Run 2 Run 3 Run 4 Run 5 Run 1 Run 2 Run 3Start Time13:30 15:42 0:06 7:42 12:00 18:00 20:24 0:06 2:42 8:12Stop Time15:18 21:48 7:12 10:30 17:54 19:42 22:18 2:18 6:24 10:42Parameters UnitGross Electrical OutputMWg167.60131.8665.33104.4963.2475.0599.7262.3281.49181.38Net Electrical OutputMWn158.93124.1459.9597.2057.8369.5193.7257.0875.91172.36Exit O2%, wet 3.69 3.70 6.01 4.19 6.18 5.56 4.58 5.59 4.66 2.23Air TemperatureAir Heater Air InletoF84.3575.4359.4658.2963.6962.2358.7357.3353.3455.56Air Heater Air OutletoF490.72486.91463.00482.56468.13474.30477.25455.94455.24482.14Ambient TemperatureoF84.3575.4359.4658.2963.6962.2358.7357.3353.3455.56ESP Exit TemperatureoF264.28261.43241.99245.96245.02242.93241.17236.28231.99244.47Flue Gas TemperatureFlue Gas to AH TemperatureoF587.01562.55522.67555.40527.54541.25552.10516.72529.39590.58Gas Out from AH TemperatureoF275.82270.44245.81259.52252.73252.53249.24234.78234.57252.50Air Heater Differential PressureIN W.C.3.052.061.071.571.031.201.410.981.042.70SorbentSorbent Feed Ratelb/hr3,0193,0273,0333,0382,9713,0083,00413200Injection Air Flow RateCFM10,82412,53410,36312,33010,14010,28610,3788603841lb/hr49,61857,45447,50356,52046,48247,15047,5733,940176190Injection ConfigurationElevation-UpperUpperLowerUpperLowerLowerLowerLowerLowerUpper# Injectors - 12 12 12 12 12 12 12 12 12 12Stack - CEMStack Flow Rate kscfm 397.44 327.81 218.03 268.31 215.69233.54 264.90 201.97 231.82 374.00lb/hr 1,821,875 1,502,687 99,946 1,229,935 988,700 1,070,568 1,214,279 92,585 1,062,668 1,714,434Stack Temperature oF 280.86 272.17 245.51 251.31 250.38 248.61 242.23 234.77 227.59 241.88NOXEmission lb/MMBTU 0.49 0.56 0.78 0.61 0.83 0.73 0.58 0.86 0.69 0.46SO2Emission lb/MMBTU 1.63 1.59 1.25 1.30 1.15 1.16 1.40 2.04 2.15 2.06CO2Emission % 11.63 11.26 9.00 10.69 9.17 9.64 10.61 9.66 10.2013.06Opacity % 29.28 17.72 10.05 10.35 10.02 10.09 8.79 8.37 8.19 14.63Baseline SO2lb/MMBtu 1.87 1.89Ca/S-0.861.07N/AN/AN/AN/AN/AN/AN/AN/ASO2Reduction%12.715.8N/AN/AN/AN/AN/AN/AN/AN/ASorbent Utilization%14.6714.75N/AN/AN/AN/AN/AN/AN/AN/A10/17/2008 10/18/2008 10/19/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-11GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 4 Run 5 Run 1 Run 2 Run 3 Run 1 Run 2 Run 1 Run 2 Run 3Start Time13:06 20:30 1:06 9:12 19:42 1:42 7:18 2:00 14:00 20:00Stop Time18:42 21:30 4:06 12:12 22:48 5:24 10:36 4:30 16:30 23:00Parameters UnitGross Electrical OutputMWg124.47182.5865.69178.33167.7870.92168.6466.4867.33109.85Net Electrical OutputMWn116.99173.6560.44169.12159.0765.36159.8361.0561.74102.66Exit O2%, wet 3.62 2.72 5.50 3.67 3.67 6.00 3.64 6.13 6.02 4.24Air TemperatureAir Heater Air InletoF64.2559.4948.6758.7456.6947.3353.4760.2065.3556.93Air Heater Air OutletoF471.56479.09444.56486.18486.04462.97488.97466.21465.06487.65Ambient TemperatureoF64.2559.4948.6758.7456.6947.3353.4760.2065.3556.93ESP Exit TemperatureoF243.98242.93231.95253.30254.74240.60254.05244.21247.74251.08Flue Gas TemperatureFlue Gas to AH TemperatureoF557.58587.87508.00591.25583.45525.41594.26527.91521.61556.56Gas Out from AH TemperatureoF250.32253.11230.84261.39260.51240.30260.54247.12253.26261.75Air Heater Differential PressureIN W.C.1.742.860.933.182.851.162.891.081.051.57SorbentSorbent Feed Ratelb/hr0003,0043,0063,0512,8102,5232,8792,994Injection Air Flow RateCFM37374012,01713,03711,20212,74010,80711,36412,452lb/hr16816918455,08859,76251,34858,40049,54152,09457,080Injection ConfigurationElevation-UpperUpperLowerUpperUpperLowerUpperN/AUpperN/A# Injectors - 12 12 12 12 12 12 12N/A12N/AStack - CEMStack Flow Rate kscfm 304.47 395.72 208.24 413.42 390.74229.81 385.84 221.05 222.64 276.61lb/hr 1,395,683 1,813,972 190,913 1,895,129 1,791,141 273,901 1,768,696 293,860 1,020,575 1,267,994Stack Temperature oF 241.33 247.25 227.84 260.47 260.84 239.68 258.57 1.28 1.30 1.56NOXEmission lb/MMBTU 0.64 0.48 0.85 0.54 0.55 0.81 0.52 0.79 0.69 0.59SO2Emission lb/MMBTU 2.16 2.09 1.97 1.59 1.73 1.13 1.76 1.32 1.29 1.56CO2Emission % 11.73 12.73 9.81 11.89 11.73 9.34 11.77 9.30 9.4011.05Opacity % 10.47 13.15 7.76 19.56 22.55 6.43 17.96 6.15 7.27 5.95Baseline SO2lb/MMBtu Baseline 1.97 1.97 2.31 2.31 1.99 1.99 1.99Ca/S-N/AN/AN/A0.770.821.520.661.521.701.21SO2Reduction%N/AN/AN/A19.512.551.023.633.735.121.6Sorbent Utilization%N/AN/AN/A25.4415.2133.5735.7622.1420.5617.7810/19/2008 10/20/2008 10/21/2008 10/22/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-12GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date10/26/2008RunRun 1 Run 2 Run 3 Run 1 Run 2 Run 3 Run 1 Run 1 Run 2 Run 3Start Time2:30 9:36 14:00 1:00 8:00 19:18 10:00 1:00 14:00 19:00Stop Time4:30 10:42 16:30 4:00 12:30 20:24 16:00 4:00 15:30 22:00Parameters UnitGross Electrical OutputMWg67.92183.43128.1965.59185.03183.5770.4369.57116.61184.05Net Electrical OutputMWn62.52174.28120.3060.45175.99174.5564.9964.19109.35175.16Exit O2%, wet 5.95 3.05 3.49 5.39 2.37 2.29 5.05 5.18 3.82 2.19Air TemperatureAir Heater Air InletoF50.3751.9161.1155.6957.2262.6367.3854.5063.2757.57Air Heater Air OutletoF474.30494.14502.82455.33487.89481.12437.95440.94461.28473.22Ambient TemperatureoF50.3751.9161.1155.6957.2262.6367.3854.5063.2757.57ESP Exit TemperatureoF247.28259.24265.47233.09250.30246.10225.29227.22235.02243.30Flue Gas TemperatureFlue Gas to AH TemperatureoF536.25598.57573.75518.96597.12589.13500.70506.19546.27583.36Gas Out from AH TemperatureoF249.51266.01279.77236.44258.36257.41229.27228.81241.12249.49Air Heater Differential PressureIN W.C.1.123.081.970.962.872.891.031.031.582.77SorbentSorbent Feed Ratelb/hr3,0314,7998,0230000000Injection Air Flow RateCFM11,02011,74114,63731373435354037lb/hr50,51453,82267,097144169156162159183167Injection ConfigurationElevation-N/AUpperN/AN/AUpperN/AN/AN/AN/AN/A# Injectors - N/A 12 N/AN/A12N/AN/AN/AN/AN/AStack - CEMStack Flow Rate kscfm 218.63 357.52 316.04 207.42 395.99374.86 214.76 212.40 295.90 383.66lb/hr 541,184 1,638,856 1,448,720 465,897 1,815,214 1,718,351 1,663,717 477,092 1,356,406 1,758,689Stack Temperature oF 1.25 1.68 1.12 2.06 2.14 2.31 2.34 2.512.41 2.45NOXEmission lb/MMBTU 0.76 0.49 0.49 0.76 0.50 0.49 0.73 0.78 0.57 0.47SO2Emission lb/MMBTU 1.25 1.68 1.12 2.06 2.14 2.31 2.32 2.50 2.42 2.47CO2Emission % 9.53 12.13 11.68 9.95 12.86 12.56 10.15 10.01 12.03 13.30Opacity % 4.04 11.96 15.61 2.49 10.25 8.90 3.65 2.25 4.92 6.60Baseline SO2lb/MMBtu 2.38 2.38 2.38 2.06 2.14 2.31 2.32 2.50 2.42 2.47Ca/S-1.511.152.25N/AN/AN/AN/AN/AN/AN/ASO2Reduction%47.529.353.0N/AN/AN/AN/AN/AN/AN/ASorbent Utilization%31.5125.5723.52N/AN/AN/AN/AN/AN/AN/A10/23/2008 10/24/0810/27/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-13GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 1 Run 2 Run 3 Run 1 Run 2 Run 3 Run 1 Run 2 Run 3 Run 4Start Time7:00 15:36 16:30 0:06 7:42 10:54 0:06 7:42 10:54 13:24Stop Time12:00 16:18 17:06 5:30 10:36 13:06 5:30 10:36 13:06 14:36Parameters UnitGross Electrical OutputMWg185.35183.71183.28183.41182.87182.43119.12184.45183.62181.99Net Electrical OutputMWn176.22174.49173.95174.23173.41173.38111.74175.75174.59172.93Exit O2%, wet 2.25 3.13 3.10 2.72 3.68 2.78 3.92 2.67 3.22 3.43Air TemperatureAir Heater Air InletoF49.3858.9258.2842.0857.0758.4746.7947.3761.9453.25Air Heater Air OutletoF473.20478.60480.15473.98483.15474.89460.19474.25486.00493.04Ambient TemperatureoF49.3858.9258.2842.0857.0758.4746.7947.3761.9453.25ESP Exit TemperatureoF243.59248.52249.65247.04253.95243.83239.47243.22255.48262.61Flue Gas TemperatureFlue Gas to AH TemperatureoF581.26583.33583.43587.07589.07583.94549.93585.14592.09604.09Gas Out from AH TemperatureoF246.01258.32259.66245.85261.23251.85237.78249.87265.38265.51Air Heater Differential PressureIN W.C.2.833.103.092.973.242.891.652.873.073.18SorbentSorbent Feed Ratelb/hr000000004,0613,998Injection Air Flow RateCFM3410,27513,1273612,31237373313,35314,049lb/hr15547,09960,17615556,43916916415461,20964,399Injection ConfigurationElevation-N/AN/AN/AN/AN/AN/AN/AN/AUpperUpper# Injectors - N/A N/A N/A N/A N/A N/A N/A N/A 12 12Stack - CEMStack Flow Rate kscfm 385.38 404.95 401.12 392.06 417.01397.55 291.49 396.77 409.90 415.50lb/hr 2,278,893 1,856,291 1,838,719 1,592,661 1,911,571 1,822,369 187,256 1,818,800 1,879,000 1,904,642Stack Temperature oF 2.43 2.66 2.66 238.38 257.88 245.47 232.00 239.57 260.69 264.51NOXEmission lb/MMBTU 0.45 0.52 0.51 0.48 0.53 0.52 0.64 0.45 0.53 0.54SO2Emission lb/MMBTU 2.64 2.71 2.70 2.88 2.63 2.56 2.44 2.83 2.03 2.03CO2Emission % 12.33 12.33 12.50 11.90 12.00 12.63 11.50 11.66 12.51 12.21Opacity % 6.72 8.79 9.13 12.42 14.87 12.32 7.72 11.29 8.97 15.76Baseline SO2lb/MMBtu 2.64 2.71 2.70 2.88 2.63 2.56 2.44 2.83 2.83 2.83Ca/S-N/AN/AN/AN/AN/AN/AN/AN/A0.690.69SO2Reduction%N/AN/AN/AN/AN/AN/AN/AN/A28.1328.01Sorbent Utilization%N/AN/AN/AN/AN/AN/AN/AN/A40.6740.7110/28/2008 10/29/2008 10/30/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-14GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 1 Run 2 Run 3 Run 4 Run 5 Run 1 Run 2 Run 3 Run 4 Run 5Start Time0:06 7:42 10:54 13:24 16:06 1:24 5:12 7:00 11:06 17:00Stop Time5:30 10:36 13:06 14:36 21:36 4:48 6:24 8:54 12:06 18:06Parameters UnitGross Electrical OutputMWg158.36180.88174.77154.51105.73132.31144.46145.26143.5570.49Net Electrical OutputMWn149.80171.78165.88146.1298.58124.57136.31137.01135.6264.78Exit O2%, wet 3.53 3.17 2.79 3.45 4.46 3.66 3.65 3.64 3.65 5.78Air TemperatureAir Heater Air InletoF43.4747.4962.2765.9760.7744.9544.2443.1765.4972.40Air Heater Air OutletoF491.19488.96481.28486.07484.11495.21498.36502.20500.55475.85Ambient TemperatureoF43.4747.4962.2765.9760.7744.9544.2443.1765.4972.40ESP Exit TemperatureoF255.07255.71252.28253.90256.82254.06253.96255.74260.23259.87Flue Gas TemperatureFlue Gas to AH TemperatureoF592.66597.96588.28577.88558.63590.51601.41608.40594.00540.79Gas Out from AH TemperatureoF258.69257.39256.02264.99262.33256.34260.30261.91268.81264.80Air Heater Differential PressureIN W.C.2.583.022.702.421.572.032.302.322.261.11SorbentSorbent Feed Ratelb/hr7,1412,39905,4736,6508,1668,8019,6184,0333,992Injection Air Flow RateCFM14,1347,6714010,23710,64911,74911,75812,28711,25312,873lb/hr64,79235,16318146,92648,81753,36453,89856,32651,58559,008Injection ConfigurationElevation-UpperUpperN/AN/AUpperUpperUpperUpperUpperLower# Injectors -1212N/AN/A121212121212Stack - CEMStack Flow Rate kscfm 370.54 392.94 386.04 364.68 278.72325.19 347.02 337.67 345.25 227.63lb/hr 169,857 1,801,237 1,769,623 1,671,679 1,277,659 300,078 1,590,754 1,547,879 1,582,605 1,043,433Stack Temperature oF 254.97 254.67 252.34 260.08 259.36 252.28 253.86 255.74 264.81 264.03NOXEmission lb/MMBTU 0.52 0.51 0.49 0.50 0.64 0.52 0.49 0.50 0.51 0.58SO2Emission lb/MMBTU 1.54 1.94 2.31 1.82 1.10 1.05 1.35 0.98 1.60 1.22CO2Emission % 12.08 12.40 12.79 12.14 10.97 11.70 11.00 11.64 11.79 9.74Opacity % 15.46 16.05 14.23 19.68 13.50 12.10 12.90 13.80 14.24 12.01Baseline SO2lb/MMBtu 2.54 2.54 2.54 2.54 2.54 2.54 2.54 2.54 2.54 2.54Ca/S-1.550.48N/A1.202.112.082.242.380.961.75SO2Reduction%39.5423.50N/A28.3056.5858.8146.8061.3636.9651.95Sorbent Utilization%25.5249.13N/A23.5726.7928.2120.9125.8238.4229.7210/31/200811/1/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-15GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date11/1/200811/4/2008RunRun 6 Run 1 Run 2 Run 3 Run 4 Run 1 Run 2 Run 3 Run 4 Run 1Start Time21:00 1:06 8:36 11:06 14:18 0:06 11:18 14:12 17:30 0:06Stop Time22:24 6:24 10:24 12:18 16:24 5:06 12:48 16:06 21:24 4:48Parameters UnitGross Electrical OutputMWg182.6763.62116.5992.6592.6863.28172.79182.03182.3367.76Net Electrical OutputMWn173.5558.06109.1485.8585.9057.98163.98172.89173.7362.39Exit O2%, wet 3.47 6.27 4.08 4.99 4.99 6.24 3.26 3.39 2.67 5.32Air TemperatureAir Heater Air InletoF56.4747.7758.8570.7774.1858.9564.0465.2463.6661.98Air Heater Air OutletoF512.39472.01493.48492.60494.52480.89501.23510.10494.37447.62Ambient TemperatureoF56.4747.7758.8570.7774.1858.9564.0465.2463.6661.98ESP Exit TemperatureoF269.56248.01254.93260.20267.22252.95268.01269.59259.42232.67Flue Gas TemperatureFlue Gas to AH TemperatureoF627.72533.24572.04558.94561.11542.79607.83620.89611.13513.58Gas Out from AH TemperatureoF278.62246.57264.73274.11277.18256.24273.95282.65264.83235.01Air Heater Differential PressureIN W.C.3.351.011.721.441.451.042.933.292.930.99SorbentSorbent Feed Ratelb/hr9,3573,4263,5043,3813,3623,5563,14111,97600Injection Air Flow RateCFM13,77910,94812,83912,83912,99910,15312,80612,44113734lb/hr63,16351,43258,85658,85659,58746,29958,70557,030626153Injection ConfigurationElevation-UpperLowerUpperLowerLowerLowerUpperUpperN/ALower# Injectors -1212121212121212N/A12Stack - CEMStack Flow Rate kscfm 418.38 220.32 279.19 271.65 256.12212.21 391.21 416.74 396.61 208.57lb/hr 1,917,854 272,565 1,279,829 1,245,226 1,174,046 90,316 1,793,289 1,910,313 1,818,072 83,681Stack Temperature oF 277.96 246.47 264.87 272.40 276.00 256.75 271.51 280.48 263.07 232.83NOXEmission lb/MMBTU 0.53 0.78 0.63 0.66 0.75 0.83 0.55 0.54 0.52 0.80SO2Emission lb/MMBTU 1.57 1.19 1.41 1.36 1.30 0.95 1.82 1.29 2.24 2.11CO2Emission % 12.06 9.16 10.82 10.62 10.15 9.24 12.11 12.02 12.64 9.92Opacity % 26.06 8.74 11.89 14.71 15.54 9.02 17.06 26.00 16.025.52Baseline SO2lb/MMBtu 2.54 2.54 2.54 2.54 2.54 2.11 2.24 2.24 2.48 2.11Ca/S-1.801.651.131.141.262.120.732.630.000.00SO2Reduction%38.2353.3344.4746.4848.6954.8518.5442.60N/AN/ASorbent Utilization%21.2332.3539.4940.8538.7525.8625.3916.17N/AN/A11/2/200811/3/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-16GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 2 Run 3 Run 4 Run 5 Run 6 Run 1 Run 2 Run 3 Run 4 Run 5Start Time6:12 8:06 11:06 16:42 20:42 0:42 6:18 8:06 10:42 18:12Stop Time7:00 10:12 15:06 20:00 23:36 4:30 7:24 10:00 17:24 21:24Parameters UnitGross Electrical OutputMWg184.43180.24178.41131.13130.9266.15132.57131.7570.78101.88Net Electrical OutputMWn175.71171.14169.31123.32123.4560.70125.03123.8565.0794.98Exit O2%, wet 2.49 3.23 3.22 3.59 3.48 5.36 3.52 3.70 5.93 4.39Air TemperatureAir Heater Air InletoF62.4863.6765.0265.0164.7163.9263.9064.9569.7262.46Air Heater Air OutletoF483.84505.01516.90511.07490.08451.16467.74489.49488.61493.84Ambient TemperatureoF62.4863.6765.0265.0164.7163.9263.9064.9569.7262.46ESP Exit TemperatureoF247.54264.10274.37266.58252.44233.45237.94249.90256.32258.53Flue Gas TemperatureFlue Gas to AH TemperatureoF596.37614.75631.79604.79589.21518.09567.62582.56558.48576.14Gas Out from AH TemperatureoF258.51277.82286.89278.87256.12237.04246.08263.79267.26261.20Air Heater Differential PressureIN W.C.2.913.183.222.121.910.991.942.041.211.49SorbentSorbent Feed Ratelb/hr012,96412,98510,43600010,2866,9910Injection Air Flow RateCFM1,45813,12112,43113,18032372,24012,83910,35937lb/hr6,68360,14556,98260,41514716810,26758,85547,487168Injection ConfigurationElevation-N/AUpperUpperUpperN/ALowerN/AUpperLowerN/A# Injectors -N/A121212N/A12N/A1212N/AStack - CEMStack Flow Rate kscfm 393.68 409.07 407.46 321.37 313.83207.83 304.97 328.13 231.63 263.92lb/hr 1,804,619 1,875,189 1,867,779 1,473,163 1,438,612 117,527 1,397,967 1,504,125 1,061,809 1,209,829Stack Temperature oF 251.36 274.52 283.93 274.18 254.47 233.78 237.73 257.97 265.85 260.85NOXEmission lb/MMBTU 0.46 0.49 0.49 0.45 0.50 0.73 0.51 0.47 0.69 0.63SO2Emission lb/MMBTU 2.29 1.25 1.16 0.92 2.17 2.08 2.10 0.81 0.59 1.87CO2Emission % 12.84 12.09 12.04 11.37 11.63 9.87 11.73 11.34 9.35 10.76Opacity % 14.81 33.52 3.00 23.38 12.07 5.73 8.36 17.94 16.71 10.88Baseline SO2lb/MMBtu 2.29 2.29 2.29 2.29 2.17 2.08 2.10 2.10 2.08 1.87Ca/S-0.002.822.853.08N/AN/AN/A3.243.83N/ASO2Reduction%N/A45.2949.3459.84N/AN/AN/A61.771.6N/ASorbent Utilization%N/A16.0417.3119.46N/AN/AN/A19.118.7N/A11/4/200811/5/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-17GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date11/8/2008RunRun 1 Run 2 Run 3 Run 4 Run 1 Run 2 Run 3 Run 4 Run 5 Run 1Start Time0:06 11:00 15:42 18:36 0:06 11:24 13:18 14:54 20:18 0:06Stop Time4:54 13:36 17:12 20:54 5:18 13:00 14:36 17:12 23:00 7:36Parameters UnitGross Electrical OutputMWg69.7890.36134.20183.2770.3585.3682.8171.15127.9570.97Net Electrical OutputMWn64.5184.38126.24174.4264.6779.5477.2765.74120.1665.31Exit O2%, wet 5.33 5.18 3.69 2.76 6.07 5.35 5.47 6.00 3.72 5.96Air TemperatureAir Heater Air InletoF56.9876.5481.2266.8857.0176.3979.3879.8967.5064.74Air Heater Air OutletoF461.33484.39517.14497.26472.88480.33480.82480.36490.35470.81Ambient TemperatureoF56.9876.5481.2266.8857.0176.3979.3879.8967.5064.74ESP Exit TemperatureoF235.89250.88279.37264.97245.37257.32259.06261.84259.33246.07Flue Gas TemperatureFlue Gas to AH TemperatureoF529.09556.65606.15611.32538.63546.00548.44545.69566.03533.25Gas Out from AH TemperatureoF240.68264.44293.16267.06250.26263.88265.74268.91267.38251.36Air Heater Differential PressureIN W.C.1.021.372.183.061.151.321.191.191.941.10SorbentSorbent Feed Ratelb/hr05,8418,20103,5413,9943,0063,2573,1743,050Injection Air Flow RateCFM3612,37812,2204211,21311,83312,01112,06110,47610,716lb/hr16256,74056,01419151,26554,24455,05855,28848,02250,473Injection ConfigurationElevation-N/ALowerUpperN/ALowerLowerLowerLowerUpperLower# Injectors - N/A 12 12 N/A 12 12 12 12 12 12Stack - CEMStack Flow Rate kscfm 211.64 255.42 328.51 402.72 228.28248.39 244.07 226.87 315.11 228.36lb/hr 86,630 1,170,855 1,505,901 1,846,053 100,891 1,138,612 1,118,823 1,039,976 1,444,468 145,204Stack Temperature oF 235.28 263.07 289.11 269.63 250.32 263.98 266.60 270.07 265.98 253.53NOXEmission lb/MMBTU 0.78 0.64 0.56 0.49 0.78 0.67 0.68 0.76 0.62 0.75SO2Emission lb/MMBTU 1.96 0.81 0.97 2.11 0.83 0.88 1.08 0.97 1.67 0.95CO2Emission % 10.00 10.05 11.45 12.47 9.29 9.87 9.81 9.34 11.289.08Opacity % 6.09 18.10 31.19 24.27 11.83 14.01 14.60 16.22 19.49 10.34Baseline SO2lb/MMBtu 1.96 1.96 2.11 2.11 1.96 1.96 1.96 1.96 2.11 1.72Ca/S-N/A2.862.55N/A2.102.051.581.931.042.11SO2Reduction%N/A58.4754.05N/A57.4454.9144.9250.6020.9444.76Sorbent Utilization%N/A20.4221.20N/A27.3426.7928.4526.1620.0521.1911/6/200811/7/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-18GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 2 Run 3 Run 4 Run 5 Run 1 Run 2 Run 3 Run 4 Run 1 Run 2Start Time9:06 13:24 17:48 19:54 0:06 12:00 13:30 18:06 0:06 6:54Stop Time11:36 16:54 18:42 0:00 6:24 13:06 17:36 20:12 4:00 11:30Parameters UnitGross Electrical OutputMWg78.7775.6586.0370.7270.80160.26132.95181.5370.81128.47Net Electrical OutputMWn72.9769.9980.5365.0065.01152.02125.29172.9365.32120.67Exit O2%, wet 5.56 5.72 4.77 5.97 5.96 2.87 3.56 2.77 5.25 3.35Air TemperatureAir Heater Air InletoF69.1971.0967.3056.4048.5567.4769.3761.5850.8853.22Air Heater Air OutletoF478.21471.69463.30468.96473.86486.86480.01485.52443.63468.07Ambient TemperatureoF69.1971.0967.3056.4048.5567.4769.3761.5850.8853.22ESP Exit TemperatureoF248.36246.12240.59237.28241.29247.90250.54249.24230.34237.86Flue Gas TemperatureFlue Gas to AH TemperatureoF545.79534.84535.53529.12537.85588.60571.11596.27507.96551.82Gas Out from AH TemperatureoF258.47255.07241.18248.91250.65262.21256.58258.29234.53247.92Air Heater Differential PressureIN W.C.1.231.111.081.091.122.381.942.921.001.78SorbentSorbent Feed Ratelb/hr3,0463,05803,5053,53200000Injection Air Flow RateCFM9,72910,4123910,86811,0733737353738lb/hr44,59947,72817749,81851,357169171161165175Injection ConfigurationElevation-LowerLowerN/ALowerLowerN/AN/AN/AN/AN/A# Injectors - 12 12 N/A 12 12 N/A N/A N/A N/A N/AStack - CEMStack Flow Rate kscfm 237.23 233.09 238.51 229.51 228.31355.98 317.20 397.21 212.65 302.98lb/hr 1,087,483 1,068,479 1,093,330 1,052,083 121,774 1,631,789 1,454,067 1,820,806 71,674 1,388,874Stack Temperature oF 255.54 253.01 236.41 242.86 243.49 250.68 250.92 254.47 226.21 236.20NOXEmission lb/MMBTU 0.70 0.73 0.69 0.78 0.78 0.50 0.60 0.51 0.79 0.56SO2Emission lb/MMBTU 0.75 0.94 1.72 0.87 0.93 2.09 2.09 2.07 1.94 2.22CO2Emission % 9.77 9.70 10.48 9.41 9.09 12.52 11.70 12.54 10.0711.98Opacity % 11.50 13.46 7.75 13.08 13.41 16.92 14.23 23.35 6.3510.06Baseline SO2lb/MMBtu 1.72 1.72 1.72 1.72 1.72 2.09 2.09 2.07 1.94 2.22Ca/S-1.891.94N/A2.332.44N/AN/AN/AN/AN/ASO2Reduction%56.3245.57N/A49.6045.97N/AN/AN/AN/AN/ASorbent Utilization%29.8423.47N/A21.2918.82N/AN/AN/AN/AN/A11/8/200811/9/2008 11/10/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-19GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 3 Run 4 Run 5 Run 6 Run 7 Run 8 Run 1 Run 2 Run 3 Run 4Start Time12:24 13:06 14:06 14:54 19:00 20:24 0:06 7:18 10:36 12:42Stop Time13:00 14:00 14:48 16:48 20:00 21:06 2:24 8:36 12:36 15:00Parameters UnitGross Electrical OutputMWg70.9270.9570.6170.55174.71175.23109.17155.72132.78134.24Net Electrical OutputMWn64.9464.9964.9965.04165.69166.19101.63147.43125.00126.41Exit O2%, wet 5.40 5.92 5.93 6.01 3.53 3.49 4.18 2.69 3.54 3.67Air TemperatureAir Heater Air InletoF61.0562.0362.4963.6455.2651.3746.6549.9558.8862.60Air Heater Air OutletoF449.16454.58456.23461.32494.27493.06481.25454.93463.12470.11Ambient TemperatureoF61.0562.0362.4963.6455.2651.3746.6549.9558.8862.60ESP Exit TemperatureoF237.40237.40237.61241.62256.02255.28250.69241.36244.66248.83Flue Gas TemperatureFlue Gas to AH TemperatureoF511.35515.35520.05527.37603.55599.06551.95553.25546.85551.95Gas Out from AH TemperatureoF237.39242.88243.98247.84265.61262.41256.81243.91252.45259.57Air Heater Differential PressureIN W.C.1.041.071.071.103.173.121.562.171.972.02SorbentSorbent Feed Ratelb/hr002,7693,9844,0714,0343,98605,0046,005Injection Air Flow RateCFM3,3199,8899,91910,19613,40112,27310,7613211,41412,981lb/hr15,21345,33045,46846,73961,42856,26047,39314652,32259,507Injection ConfigurationElevation-N/AN/ALowerLowerUpperUpperLowerN/AUpperUpper# Injectors - N/A N/A 12 12 12 12 12 N/A 12 12Stack - CEMStack Flow Rate kscfm 221.23 230.72 228.04 228.03 409.19407.33 283.92 335.48 325.52 330.79lb/hr 1,014,112 1,057,620 1,045,324 1,045,290 1,875,731 1,867,178 66,479 1,537,834 1,492,201 1,516,330Stack Temperature oF 234.74 237.98 239.76 242.88 263.14 260.88 250.65 232.96 242.34 253.25NOXEmission lb/MMBTU 0.80 0.80 0.81 0.81 0.53 0.52 0.72 0.48 0.59 0.59SO2Emission lb/MMBTU 2.09 2.05 1.34 0.96 1.75 1.72 1.27 1.88 1.21 1.12CO2Emission % 10.00 9.59 9.59 9.51 11.91 11.99 11.00 12.70 11.80 11.68Opacity % 6.83 7.30 9.14 11.66 29.47 26.59 14.85 12.56 15.56 20.00Baseline SO2lb/MMBtu 2.09 2.05 1.94 1.94 2.22 2.22 1.88 1.88 1.88 1.88Ca/S-N/AN/A1.612.340.930.921.67N/A1.712.04SO2Reduction%N/AN/A30.7350.3021.2422.5032.37N/A35.4940.32Sorbent Utilization%N/AN/A19.0921.5422.8624.4919.33N/A20.7519.7611/10/200811/11/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-20GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date11/11/2008RunRun 5 Run 1 Run 2 Run 3 Run 4 Run 5 Run 6 Run 7 Run 1 Run 2Start Time20:54 0:42 6:12 8:24 9:42 10:24 18:12 19:18 0:06 13:42Stop Time22:54 4:12 7:42 9:18 10:18 10:54 18:54 20:06 6:00 14:36Parameters UnitGross Electrical OutputMWg128.5371.92182.21176.82173.55155.88173.90182.7271.5485.66Net Electrical OutputMWn120.7966.24173.69168.04164.56147.42165.01173.8966.1080.07Exit O2%, wet 3.70 5.95 2.16 3.03 3.15 3.38 3.41 3.35 5.99 5.27Air TemperatureAir Heater Air InletoF55.7451.3349.2850.3454.6956.5361.5061.0160.8963.42Air Heater Air OutletoF474.67455.99465.14470.80472.05471.62479.34483.19456.20472.74Ambient TemperatureoF55.7451.3349.2850.3454.6956.5361.5061.0160.8963.42ESP Exit TemperatureoF248.99239.32241.01243.74245.09245.77253.32254.96239.49249.17Flue Gas TemperatureFlue Gas to AH TemperatureoF552.79521.20573.60570.54568.25563.26583.31587.79520.53551.60Gas Out from AH TemperatureoF258.62242.64246.33251.69256.43255.37264.45266.11245.14255.15Air Heater Differential PressureIN W.C.1.901.152.672.872.822.413.033.251.131.37SorbentSorbent Feed Ratelb/hr6,0073,49203,9844,9825,0506,0226,0333,6065,584Injection Air Flow RateCFM12,80911,7173512,40212,78712,95112,98913,00710,75511,870lb/hr58,71752,86716156,85358,61659,36959,54259,62349,68754,412Injection ConfigurationElevation-UpperLowerN/AUpperUpperUpperUpperUpperLowerLower# Injectors - 12 12 N/A 12 12 12 12 12 12 12Stack - CEMStack Flow Rate kscfm 318.10 230.42 369.65 396.87 399.43363.52 403.55 420.00 231.38 248.53lb/hr 1,458,192 138,449 1,694,476 1,819,252 1,830,981 1,666,360 1,849,873 1,925,280 127,387 1,139,262Stack Temperature oF 251.77 237.22 233.68 241.53 248.33 248.45 260.18 262.97 241.52 253.93NOXEmission lb/MMBTU 0.61 0.80 0.44 0.46 0.47 0.52 0.48 0.49 0.77 0.62SO2Emission lb/MMBTU 1.20 0.90 2.10 1.79 1.67 1.53 1.46 1.49 1.09 0.76CO2Emission % 11.50 9.46 13.28 12.41 12.27 12.02 12.06 12.19 9.12 10.22Opacity % 16.20 9.88 12.44 14.81 19.96 17.25 26.38 28.10 8.579.31Baseline SO2lb/MMBtu 1.88 1.94 2.10 2.10 2.10 2.10 2.10 2.10 1.92 1.92Ca/S-2.162.04N/A0.951.191.361.451.382.202.83SO2Reduction%35.9453.87N/A14.7520.5727.2430.4129.0442.8860.25Sorbent Utilization%16.6726.46N/A15.5317.2320.0620.9320.9819.5021.2911/12/200811/13/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-21GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 3 Run 4 Run 5 Run 6 Run 1 Run 2 Run 3 Run 4 Run 1 Run 2Start Time19:00 19:42 20:24 21:48 0:06 5:36 12:30 19:12 0:36 10:30Stop Time19:36 20:12 21:00 22:00 5:12 6:36 13:54 22:06 8:18 12:36Parameters UnitGross Electrical OutputMWg181.86183.19182.80183.0571.3098.84160.24182.8665.36121.89Net Electrical OutputMWn172.75174.09173.73174.0265.7791.79151.78173.6359.89114.41Exit O2%, wet 3.51 3.45 3.47 3.46 6.01 4.56 3.38 3.45 6.18 3.99Air TemperatureAir Heater Air InletoF64.2563.4463.2663.0960.1461.3364.0373.6175.6078.35Air Heater Air OutletoF496.21492.51492.69486.67461.65482.45495.94490.61461.73502.41Ambient TemperatureoF64.2563.4463.2663.0960.1461.3364.0373.6175.6078.35ESP Exit TemperatureoF265.53263.83261.88258.75242.25249.74265.11265.66249.53271.22Flue Gas TemperatureFlue Gas to AH TemperatureoF606.05603.60600.10594.50530.10564.03597.70601.83521.83588.91Gas Out from AH TemperatureoF275.62273.32272.98267.41244.85263.60274.17273.63252.97284.09Air Heater Differential PressureIN W.C.3.383.383.403.311.181.632.823.501.112.01SorbentSorbent Feed Ratelb/hr5,9816,3386,14704,8686,2776,4524,1144,8427,433Injection Air Flow RateCFM13,32614,23215,30313,15710,78512,80113,00112,99910,34713,002lb/hr61,08565,24170,14860,31149,31158,67959,59659,58649,22959,599Injection ConfigurationElevation-UpperUpperUpperN/ALowerLowerUpperUpperLowerUpper# Injectors - 12 12 12 N/A 12 12 12 12 12 12Stack - CEMStack Flow Rate kscfm 418.80 422.28 423.64 420.63 230.24268.85 378.28 426.58 221.06 312.11lb/hr 1,919,779 1,935,747 1,941,979 1,928,183 110,004 1,232,429 1,734,036 1,955,458 169,691 1,430,729Stack Temperature oF 276.43 276.00 274.90 271.47 245.07 255.62 273.54 278.73 259.65 281.68NOXEmission lb/MMBTU 0.50 0.51 0.50 0.49 0.72 0.56 0.48 0.52 0.72 0.57SO2Emission lb/MMBTU 1.42 1.47 1.44 1.92 0.75 1.04 1.30 1.63 0.78 0.87CO2Emission % 12.20 12.22 12.19 12.20 9.63 10.43 11.97 11.89 9.07 11.18Opacity % 30.53 29.77 29.00 23.63 8.32 11.03 22.73 25.76 8.4419.55Baseline SO2lb/MMBtu 1.92 1.92 1.92 1.92 1.92 1.92 1.92 1.92 2.21 2.21Ca/S-1.511.581.53N/A2.832.881.831.042.702.38SO2Reduction%26.0723.3925.00N/A61.0945.5731.9814.7964.8760.84Sorbent Utilization%17.3014.7916.31N/A21.6015.8117.4414.1624.0525.5711/13/200811/14/2008 11/15/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-22GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date11/15/200811/18/2008RunRun 3 Run 1 Run 2 Run 1 Run 2 Run 1 Run 1 Run 2 Run 1 Run 2Start Time21:48 0:00 18:06 0:00 12:06 0:00 11:18 13:48 6:06 17:30Stop Time23:54 7:42 21:24 4:18 16:36 5:24 12:48 20:54 7:54 21:06Parameters UnitGross Electrical OutputMWg68.8668.68173.51119.26129.53125.40181.12181.53177.35179.94Net Electrical OutputMWn63.5163.06164.96111.02121.25116.98172.35172.42168.60170.68Exit O2%, wet 5.34 5.37 2.73 3.92 3.83 3.64 2.21 2.74 2.53 3.36Air TemperatureAir Heater Air InletoF57.5250.0251.9743.4663.6246.3044.7648.9436.4852.52Air Heater Air OutletoF427.57427.89462.28444.29448.62446.01451.80452.96450.71462.77Ambient TemperatureoF57.5250.0251.9743.4663.6246.3044.7648.9436.4852.52ESP Exit TemperatureoF223.65220.18236.58231.33236.36231.27234.32236.00234.88244.44Flue Gas TemperatureFlue Gas to AH TemperatureoF491.07491.72569.14532.43539.02528.97555.52562.14562.39569.09Gas Out from AH TemperatureoF225.66226.61243.97235.92238.52238.15239.01241.77240.13249.95Air Heater Differential PressureIN W.C.0.950.952.661.741.931.832.632.842.693.13SorbentSorbent Feed Ratelb/hr0000000004,125Injection Air Flow RateCFM32363239363634343613,000lb/hr14816914717416616514515816859,592Injection ConfigurationElevation-N/AN/AN/AN/AN/AN/AN/AN/AN/AUpper# Injectors - N/A N/A N/A N/A N/A N/A N/A N/A N/A 12Stack - CEMStack Flow Rate kscfm 212.80 211.84 382.22 307.17 325.06308.19 383.18 397.62 371.45 414.76lb/hr 975,496 136,709 1,752,113 111,023 1,490,079 141,2724,474,428 1,822,688 1,747,906 1,901,245Stack Temperature oF 221.73 218.46 235.61 226.54 232.51 226.17 227.13 232.66 228.22 248.09NOXEmission lb/MMBTU 0.71 0.69 0.47 0.31 0.31 0.27 0.44 0.49 0.48 0.52SO2Emission lb/MMBTU 2.21 2.21 2.18 2.24 2.18 2.41 1.60 1.78 2.17 1.74CO2Emission % 10.19 9.89 12.92 11.58 11.70 11.45 13.31 12.74 12.82 11.96Opacity % 5.71 5.67 14.49 10.73 9.09 7.80 10.24 12.80 11.19 26.69Baseline SO2lb/MMBtu 2.21 2.21 2.18 2.24 2.18 2.41 1.60 1.78 2.17 2.17Ca/S-N/AN/AN/AN/AN/AN/AN/AN/AN/A0.95SO2Reduction%N/AN/AN/AN/AN/AN/AN/AN/AN/A19.86Sorbent Utilization%N/AN/AN/AN/AN/AN/AN/AN/AN/A20.9911/16/2008 11/17/2008 11/19/2008 11/20/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-23GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date11/20/2008RunRun 3 Run 1 Run 2 Run 3 Run 4 Run 1 Run 2 Run 3 Run 1 Run 2Start Time21:30 1:00 7:30 11:42 19:06 0:00 6:24 19:06 0:00 7:24Stop Time23:54 7:12 8:42 13:00 23:54 5:18 9:24 23:54 6:18 10:36Parameters UnitGross Electrical OutputMWg179.38180.66179.25127.39181.67183.57181.66184.47185.08181.16Net Electrical OutputMWn170.22171.68170.12119.47172.62174.41172.43175.10175.82172.23Exit O2%, wet 2.97 2.30 2.38 2.89 2.26 2.26 2.52 2.95 2.91 2.67Air TemperatureAir Heater Air InletoF45.7646.4745.2948.6338.7033.5531.5842.8441.4744.94Air Heater Air OutletoF460.03459.04461.27461.24465.53464.07464.99469.06470.33460.23Ambient TemperatureoF45.7646.4745.2948.6338.7033.5531.5842.8441.4744.94ESP Exit TemperatureoF242.66241.14241.00237.58243.86242.87243.05245.69245.66240.25Flue Gas TemperatureFlue Gas to AH TemperatureoF567.11561.82560.34535.11573.94570.11569.82580.66584.07568.18Gas Out from AH TemperatureoF247.90246.83248.90247.83249.45247.88247.40251.75253.88243.56Air Heater Differential PressureIN W.C.2.972.762.791.742.772.822.873.113.102.84SorbentSorbent Feed Ratelb/hr4,0954,1525,0847,7936,0756,0455,7136,0486,0790Injection Air Flow RateCFM10,48010,48512,20313,00010,75710,76810,75210,76110,75936lb/hr48,03849,19855,94059,59449,30949,29749,28849,32749,901165Injection ConfigurationElevation-UpperUpperUpperUpperUpperUpperUpperUpperUpperN/A# Injectors - 12 12 12 12 12 12 12 12 12 N/AStack - CEMStack Flow Rate kscfm 404.35 388.50 389.33 301.96 389.40393.74 388.54 413.63 413.69 387.87lb/hr 1,853,550 467,861 1,784,692 1,384,204 1,785,028 1,721,899 1,781,047 1,896,064 2,121,083 1,777,995Stack Temperature oF 241.04 235.51 236.78 235.98 235.29 233.63 235.49 242.97 243.20 234.39NOXEmission lb/MMBTU 0.49 0.42 0.42 0.51 0.40 0.40 0.43 0.47 0.45 0.48SO2Emission lb/MMBTU 1.83 1.85 1.77 1.22 1.82 1.83 1.75 1.68 1.59 2.08CO2Emission % 12.30 12.31 12.74 12.29 13.36 13.38 13.06 12.64 12.21 13.11Opacity % 26.02 21.42 21.73 16.93 19.23 19.97 20.39 27.83 26.60 18.80Baseline SO2lb/MMBtu 2.17 2.17 2.17 2.17 2.17 2.17 2.17 2.17 2.08 2.08Ca/S-0.940.991.172.391.331.311.281.321.43N/ASO2Reduction%15.3214.6318.2643.6515.9915.4019.2022.6423.62N/ASorbent Utilization%16.3414.8015.6518.2612.0211.7914.9817.2016.55N/A11/21/2008 11/22/2008 11/23/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-24GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 3 Run 4 Run 5 Run 1 Run 2 Run 3 Run 1 Run 2 Run 3 Run 4Start Time10:48 13:42 18:18 3:06 11:18 17:42 0:54 11:30 17:54 19:30Stop Time12:54 16:18 23:54 10:48 11:42 22:12 5:00 16:06 18:54 20:36Parameters UnitGross Electrical OutputMWg158.9364.72182.73187.54136.96183.8070.71129.01166.70185.45Net Electrical OutputMWn150.3459.27173.73178.39129.10174.6665.04121.01157.95176.15Exit O2%, wet 3.06 5.58 2.64 2.53 3.67 3.19 5.74 4.22 6.12 6.18Air TemperatureAir Heater Air InletoF55.5657.1340.8840.6164.0261.7756.5058.7453.0351.46Air Heater Air OutletoF454.69424.44455.13453.93441.39472.13454.17486.68488.60482.33Ambient TemperatureoF55.5657.1340.8840.6164.0261.7756.5058.7453.0351.46ESP Exit TemperatureoF235.66227.76236.55236.41233.08252.48241.62260.19256.50254.45Flue Gas TemperatureFlue Gas to AH TemperatureoF554.05484.08561.64563.36536.66581.14518.94564.22594.41591.00Gas Out from AH TemperatureoF241.26226.69242.74241.76234.27259.29241.91270.67265.43260.76Air Heater Differential PressureIN W.C.2.340.912.872.932.003.241.111.792.753.22SorbentSorbent Feed Ratelb/hr000004,0994,8887,8124,1064,258Injection Air Flow RateCFM3532333540610,75910,72213,00211,66011,645lb/hr1591461531521,86249,31748,89259,60253,44853,379Injection ConfigurationElevation-N/ALowerN/AN/AN/AUpperLowerUpperUpperUpper# Injectors - N/A 12 N/A N/A N/A 12 12 12 12 12Stack - CEMStack Flow Rate kscfm 365.36 205.68 397.84 400.58 330.93417.72 224.72 291.16 375.78 410.58lb/hr 1,674,806 942,844 1,823,684 1,321,023 1,516,963 1,914,817 45,131 1,334,675 1,722,584 1,882,114Stack Temperature oF 233.22 224.78 232.73 231.99 228.49 257.26 240.74 258.43 259.92 255.43NOXEmission lb/MMBTU 0.54 0.86 0.47 0.45 0.55 0.50 0.73 0.46 0.47 0.47SO2Emission lb/MMBTU 2.19 2.26 2.21 2.10 2.21 1.62 0.63 1.03 1.42 1.58CO2Emission % 12.71 10.10 13.13 12.63 11.85 12.22 9.58 12.75 12.37 12.68Opacity % 16.85 8.43 14.50 13.79 8.45 30.17 11.40 16.84 29.4131.08Baseline SO2lb/MMBtu 2.19 2.26 2.21 2.10 2.21 2.21 2.21 2.21 2.21 2.21Ca/S-N/AN/AN/AN/AN/A0.902.532.350.990.91SO2Reduction%N/AN/AN/AN/AN/A26.5871.3953.2935.6228.55Sorbent Utilization%N/AN/AN/AN/AN/A29.6528.1622.6936.1531.2711/23/2008 11/24/2008 11/25/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-25GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 1 Run 2 Run 1 Run 2 Run 3 Run 1 Run 2 Run 3 Run 1 Run 2Start Time6:36 20:36 12:12 14:12 17:36 0:00 10:06 16:48 0:00 18:12Stop Time9:54 22:06 13:54 17:12 22:42 9:30 15:48 23:54 7:18 19:30Parameters UnitGross Electrical OutputMWg180.95139.3769.9171.4582.2464.3963.5265.0565.41185.85Net Electrical OutputMWn171.93131.2764.2566.1475.6158.8257.8859.6560.05177.15Exit O2%, wet 5.24 3.31 5.63 5.48 5.17 5.66 6.27 5.64 5.57 2.17Air TemperatureAir Heater Air InletoF39.3239.0462.4266.5949.3144.2363.8857.5855.4947.61Air Heater Air OutletoF462.25471.29455.94445.11446.58431.10452.33439.42431.44454.34Ambient TemperatureoF39.3239.0462.4266.5949.3144.2363.8857.5855.4947.61ESP Exit TemperatureoF242.71246.13244.78235.99232.26226.08237.60229.68224.69233.58Flue Gas TemperatureFlue Gas to AH TemperatureoF572.19549.50515.42511.51507.98488.57503.58500.83490.73558.89Gas Out from AH TemperatureoF243.79251.66246.17237.15237.30229.85247.42232.30229.83242.90Air Heater Differential PressureIN W.C.2.852.081.001.031.040.920.970.890.922.72SorbentSorbent Feed Ratelb/hr04,0963,60985004,118000Injection Air Flow RateCFM1,00612,99010,6739893716410,020363739lb/hr4,29059,54645,7794,53216969845,931164176180Injection ConfigurationElevation-N/AUpperLowerN/AN/AN/ALowerN/AN/AN/A# Injectors - N/A 12 12 N/A N/A N/A 12 N/A N/A N/AStack - CEMStack Flow Rate kscfm 383.20 330.28 219.27 213.66 232.54201.73 214.55 205.52 204.80 382.59lb/hr 1,491,249 1,513,981 2,627,886 979,423 1,065,947 143,328 983,505 942,120 125,081 1,753,773Stack Temperature oF 233.71 239.38 249.60 234.93 229.58 221.38 243.01 229.76 225.15 230.15NOXEmission lb/MMBTU 0.46 0.48 0.69 0.71 0.75 0.79 0.83 0.80 0.77 0.41SO2Emission lb/MMBTU 1.89 1.30 0.74 1.40 1.74 1.57 0.51 1.53 1.62 2.09CO2Emission % 12.86 12.09 9.77 10.11 10.39 9.67 9.13 9.88 9.63 13.31Opacity % 19.46 16.43 16.69 10.21 10.27 7.39 15.04 8.19 7.25 15.93Baseline SO2lb/MMBtu 1.89 1.89 1.40 1.40 1.74 1.57 1.57 1.53 1.62 2.09Ca/S-N/A1.342.96N/AN/AN/A3.29N/AN/AN/ASO2Reduction%N/A31.2247.45N/AN/AN/A67.30N/AN/AN/ASorbent Utilization%N/A23.3016.04N/AN/AN/A20.45N/AN/AN/A11/29/200811/26/2008 11/27/2008 11/28/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-26GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date11/29/2008RunRun 3 Run 1 Run 2 Run 1 Run 2 Run 3 Run 1 Run 2 Run 1 Run 2Start Time22:06 0:00 12:24 0:00 7:18 11:30 0:00 19:12 0:00 10:54Stop Time23:54 6:00 17:06 4:48 8:36 16:30 4:36 23:54 7:18 15:12Parameters UnitGross Electrical OutputMWg60.7859.7160.7161.59179.1471.8765.37178.18175.89133.11Net Electrical OutputMWn55.4954.4455.4956.23170.0466.1659.64168.99166.88124.95Exit O2%, wet 5.81 5.74 2.88 2.92 1.47 2.72 3.19 1.61 1.53 1.83Air TemperatureAir Heater Air InletoF46.9546.8563.3849.4249.8251.9241.7939.7935.6656.44Air Heater Air OutletoF420.81416.75419.87421.20454.02418.93444.12476.69468.15481.65Ambient TemperatureoF46.9546.8563.3849.4249.8251.9241.7939.7935.6656.44ESP Exit TemperatureoF223.57218.64219.02221.47234.59221.38234.23249.20244.48253.34Flue Gas TemperatureFlue Gas to AH TemperatureoF473.49471.16477.91481.40558.12485.90505.78589.74576.27565.72Gas Out from AH TemperatureoF224.74226.30224.75225.61243.01223.04238.65253.73247.80263.85Air Heater Differential PressureIN W.C.0.800.790.870.852.780.991.003.012.902.12SorbentSorbent Feed Ratelb/hr0000004,1012,9972,9919,973Injection Air Flow RateCFM36353637343710,60510,46810,46613,008lb/hr16616316617015616848,10647,98649,17159,627Injection ConfigurationElevation-N/AN/AN/AN/AN/AN/ALowerUpperUpperUpper# Injectors - N/A N/A N/A N/A N/A N/A 12 12 12 12Stack - CEMStack Flow Rate kscfm 192.69 190.76 194.46 196.89 368.99214.05 219.58 403.88 395.07 332.83lb/hr 883,289 95,475 891,387 79,097 1,691,431 981,219 84,100 1,851,373 241,287 1,525,670Stack Temperature - CEM oF 221.21 216.62 222.41 218.39 232.98 216.99 229.11 246.11 238.13 254.88NOXEmission lb/MMBTU 0.88 0.85 0.88 0.84 0.48 0.81 0.83 0.47 0.44 0.52SO2Emission lb/MMBTU 2.05 2.25 2.26 2.26 2.10 2.05 0.86 1.63 1.62 0.82CO2Emission % 9.75 9.36 9.43 9.60 12.59 10.09 9.29 12.48 12.15 11.67Opacity % 6.55 5.89 6.03 5.54 11.31 5.99 10.13 23.66 20.78 24.33Baseline SO2lb/MMBtu 2.05 2.25 2.26 2.26 2.10 2.05 2.05 2.05 2.05 2.05Ca/S-N/AN/AN/AN/AN/AN/A2.420.720.753.09SO2Reduction%N/AN/AN/AN/AN/AN/A57.9120.2621.0559.97Sorbent Utilization%N/AN/AN/AN/AN/AN/A23.9028.2728.0419.3811/30/2008 12/1/2008 12/2/2008 12/3/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-27GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date12/6/2008RunRun 3 Run 4 Run 1 Run 2 Run 3 Run 4 Run 1 Run 2 Run 3 Run 1Start Time15:30 22:42 0:48 6:24 9:42 20:30 1:30 9:00 13:00 0:30Stop Time16:00 23:54 4:12 7:48 16:24 22:36 5:18 10:30 16:18 3:54Parameters UnitGross Electrical OutputMWg132.5798.0966.96181.3370.69123.5562.09162.8687.6870.82Net Electrical OutputMWn124.4990.7061.19172.1164.82115.8456.61154.1980.7165.05Exit O2%, wet 1.81 2.48 3.15 1.61 3.05 1.83 3.25 1.62 2.61 2.68Air TemperatureAir Heater Air InletoF60.9937.6236.2836.8261.8956.4155.7553.9355.1542.33Air Heater Air OutletoF487.43458.69450.41478.52466.86474.51456.43482.86472.01449.56Ambient TemperatureoF60.9937.6236.2836.8261.8956.4155.7553.9355.1542.33ESP Exit TemperatureoF260.70242.39239.38245.16246.99250.62241.61249.39249.38237.42Flue Gas TemperatureFlue Gas to AH TemperatureoF575.31530.24512.18588.69532.80548.27516.46583.82541.93509.48Gas Out from AH TemperatureoF270.45245.27242.20255.12254.84257.67244.97261.29257.03241.40Air Heater Differential PressureIN W.C.2.101.471.063.151.171.781.032.661.341.09SorbentSorbent Feed Ratelb/hr8,1843,1953,2243,1877,0373,0643,1545,9895,9803,275Injection Air Flow RateCFM12,98511,42111,41611,41110,71610,93610,94311,87912,10010,948lb/hr59,52252,35451,51052,30749,12250,13250,09654,45255,46649,200Injection ConfigurationElevation-UpperUpperLowerUpperLowerUpperLowerUpperLowerLower# Injectors - 12 12 12 12 12 12 12 12 12 12Stack - CEMStack Flow Rate kscfm 326.33 270.32 222.23 391.21 230.14303.15 213.02 366.58 249.39 217.65lb/hr 1,495,912 1,239,161 141,382 1,793,322 1,054,981 1,389,619 222,483 1,680,380 1,143,223 103,290Stack Temperature - CEM oF 263.73 236.33 232.49 244.55 249.26 253.13 241.92 252.13 250.21 232.48NOXEmission lb/MMBTU 0.50 0.73 0.83 0.47 0.78 0.60 0.88 0.46 0.63 0.62SO2Emission lb/MMBTU 1.00 1.41 1.06 1.69 0.52 1.47 0.90 1.31 0.86 0.95CO2Emission % 11.68 10.52 9.42 12.59 9.49 11.84 9.21 12.41 10.38 10.13Opacity % 28.35 12.83 9.74 21.89 12.85 12.10 8.36 18.68 0.61 1.32Baseline SO2lb/MMBtu 2.05 2.05 2.05 2.05 2.05 2.05 2.05 2.05 2.05 2.05Ca/S-2.591.351.860.783.881.031.941.592.781.79SO2Reduction%51.0130.8648.3317.4074.7928.3755.9035.8957.9853.75Sorbent Utilization%19.7222.7826.0422.3019.2627.5728.8422.6120.8330.0212/3/2008 12/4/2008 12/5/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-28GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test DateRunRun 2 Run 3 Run 4 Run 1 Run 2 Run 3 Run 4 Run 1 Run 2 Run 3Start Time12:12 17:42 20:12 0:00 8:18 11:30 22:12 0:00 7:36 15:24Stop Time16:00 18:36 21:30 5:30 0:54 16:30 23:54 5:30 9:24 19:12Parameters UnitGross Electrical OutputMWg70.81182.18128.4070.7688.1687.78155.94155.82158.25159.66Net Electrical OutputMWn64.90173.10120.4964.9880.8880.64147.65147.39149.61151.19Exit O2%, wet 2.66 1.48 2.05 2.58 2.59 2.52 1.36 1.39 3.34 3.02Air TemperatureAir Heater Air InletoF49.4349.6249.2141.8341.6051.7942.3937.0937.6055.04Air Heater Air OutletoF448.35478.19468.02449.85462.15461.31457.18454.26452.09452.42Ambient TemperatureoF49.4349.6249.2141.8341.6051.7942.3937.0937.6055.04ESP Exit TemperatureoF239.20248.30244.66237.32239.38241.94238.00234.19232.99234.23Flue Gas TemperatureFlue Gas to AH TemperatureoF507.53584.54548.06511.99530.30530.62559.09551.21548.72549.11Gas Out from AH TemperatureoF241.40257.30249.56241.46247.84248.19239.22239.78237.73240.22Air Heater Differential PressureIN W.C.1.063.081.981.011.371.332.162.172.222.30SorbentSorbent Feed Ratelb/hr3,0872,9983,0393,0333,0933,0670000Injection Air Flow RateCFM10,94210,95510,96610,95110,94710,94936343637lb/hr50,15750,21850,26850,26750,18050,189163157167170Injection ConfigurationElevation-LowerUpperUpperLowerLowerLowerN/AN/AN/AN/A# Injectors - 12 12 12 12 12 12 N/A N/A N/A N/AStack - CEMStack Flow Rate kscfm 217.56 401.42 325.25 214.50 247.62246.84 348.14 347.19 350.43 361.41lb/hr 997,279 1,840,109 1,490,946 97,169 1,135,079 1,131,529 1,595,869 157,277 1,606,354 1,656,693Stack Temperature - CEM oF 234.69 248.49 240.61 230.81 236.04 236.68 227.17 225.63 223.84 230.64NOXEmission lb/MMBTU 0.62 0.45 0.51 0.60 0.60 0.59 0.49 0.49 0.48 0.50SO2Emission lb/MMBTU 1.04 1.71 1.53 0.96 1.06 1.10 1.93 1.93 1.90 2.10CO2Emission % 9.98 12.54 11.34 9.76 10.38 10.58 12.87 12.46 12.96 12.65Opacity % 0.72 14.48 7.53 0.59 3.58 3.17 6.07 6.28 6.38 9.26Baseline SO2lb/MMBtu 2.05 2.05 2.05 1.93 1.93 1.93 1.93 1.93 1.93 1.93Ca/S-1.710.720.991.851.541.50N/AN/AN/AN/ASO2Reduction%49.2916.6225.1550.1644.8843.20N/AN/AN/AN/ASorbent Utilization%28.7623.1525.3327.0729.1828.77N/AN/AN/AN/A12/7/2008 12/8/200812/6/2008Progress Energy Robinson Unit 1 Furnace Sorbent Injection Demonstration ProjectFinal Report, Appendix B, Rev. 02Contract No. 10023-WA169, GE JN 690025 February 2009GE Proprietary InformationPage B-29GE EnergyTABLE B-3. LONG-TERM TRIAL DATA (CONT.)Test Date12/8/2008RunRun 4 Run 1 Run 2 Run 3 Run 1 Run 2 Run 3 Run 4Start Time21:36 0:00 12:42 19:12 0:00 15:30 18:48 22:06Stop Time23:54 9:36 17:30 23:54 15:18 17:18 20:00 23:54Parameters UnitGross Electrical OutputMWg157.27157.46159.55159.56159.58159.93129.4069.52Net Electrical OutputMWn148.61148.90151.05151.02151.00151.43121.5463.84Exit O2%, wet 3.31 3.13 3.55 3.62 3.39 3.26 3.61 5.95Air TemperatureAir Heater Air InletoF50.7652.5276.1271.7277.1378.8673.0166.81Air Heater Air OutletoF463.48464.14471.39484.98497.97500.94483.33458.48Ambient TemperatureoF50.7652.5276.1271.7277.1378.8673.0166.81ESP Exit TemperatureoF238.85244.33256.84264.29272.81276.05265.42251.08Flue Gas TemperatureFlue Gas to AH TemperatureoF552.75556.12561.14578.79594.10599.96565.31515.48Gas Out from AH TemperatureoF248.71249.08265.61272.15281.98285.83271.17250.39Air Heater Differential PressureIN W.C.2.452.422.562.662.682.672.011.11SorbentSorbent Feed Ratelb/hr3,6173,6343,6519,4709,3296,0123,9954,174Injection Air Flow RateCFM12,99513,00013,00612,99512,99713,00911,48511,483lb/hr59,56955,42659,61859,56755,85959,63452,64752,638Injection ConfigurationElevation-UpperUpperUpperUpperUpperUpperUpperLower# Injectors - 12 12 12 12 12 12 12 12Stack - CEMStack Flow Rate kscfm 366.03 361.19 367.81 366.91 365.48365.51 321.28 223.29lb/hr 1,677,897 259,192 1,686,042 1,681,936 413,059 1,675,500 1,472,733 1,023,583Stack Temperature - CEM oF 238.82 239.96 264.40 270.73 281.44 286.98 273.91 258.43NOXEmission lb/MMBTU 0.48 0.47 0.49 0.48 0.46 0.46 0.50 0.74SO2Emission lb/MMBTU 1.68 1.51 1.62 1.17 1.03 1.39 1.68 1.34CO2Emission % 12.22 12.06 12.10 12.04 11.79 11.98 11.59 9.53Opacity % 0.00 3.50 11.43 22.52 25.99 25.11 10.78 1.32Baseline SO2lb/MMBtu 1.93 1.93 1.93 1.93 1.93 1.93 1.93 1.93Ca/S-1.031.071.052.742.771.761.372.51SO2Reduction%12.8921.7316.1639.1746.7528.2013.0830.56Sorbent Utilization%12.4620.3715.4114.2916.8916.079.5412.1912/10/200812/9/2008

# GE Energy



# Progress Energy

Robinson Unit 1

Furnace Sorbent Injection

Demonstration Project

Final Report, Rev. 02

Appendix C: Project Environmental, Health, and Safety Plan

Contract No. 10023-WA169

GE Job Number 6900

25 February 2009

GE Energy and Environmental Research Corporation

1831 East Carnegie Ave

Santa Ana, CA 92705

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# Table of Contents

Section Page

1.0 Safety and Environmental Considerations....................................................................C-1

1.1 Objective ...............................................................................................................C-1

1.2 Definitions.............................................................................................................C-1

1.3 Site Safety Program...............................................................................................C-1

1.4 Contractor Site Safety Activities...........................................................................C-5

1.5 Customer Site Safety Guidelines...........................................................................C-6

1.6 References ...........................................................................................................C-11

1.7 Responsibility......................................................................................................C-12

1.8 Interpretation .......................................................................................................C-12

1.9 Sorbent MSDS.....................................................................................................C-12

2.0 Resources ....................................................................................................................C-15

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# List of Figures

Figure Page

C-1. Sorbent MSDS. ............................................................................................................... 13

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# 1.0 Safety and Environmental Considerations

This section summarizes the key safety and environment considerations. For compl ete

guideline, please review PCD Contractor Safety & Environmental Guideline ( SAF-PPDX0001).



# 1.1 Objective

To establish a plan for implementing GE Energy, Environmental Services (ENVS) Health,

Safety and Environmental Manual procedures on all Customer Site Projects, as t hey may

apply to the work scopes and contracts between parties.



# 1.2 Definitions

A. Contractor

– ENVS Subcontractor(s), including their employees and

subcontractors

B. Competent Person - is a person who has adequate knowledge, training and

experience for the task to be preformed. They are also capable of identifyi ng

existing and predictable hazards and reducing too as low as reasonable

practicable.

C. Authorized Person – A person selected, approved or assigned by the employer as

being qualified to perform a specific duty or duties, or to enter specific location( s)

at the workplace.

D. Hazard – Anything, person, material or substance that has the potential to cause

harm, ill health, injury, damage to property, plant, products or the Environment.

E. Risk – Likelihood that an undesired event will occur due to the realization of a

hazard.



# 1.3 Site Safety Program

1.3.1 General

A. The ENVS Site Lead / Manager and ENVS site personnel will assure that

conditions which ENVS personnel are exposed to conform to ENVS Safety

Program requirements.

B. Project Emergency Data Sheet and Project Expat Roster (Non-US/Int ernational)

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• A completed data sheet (Tab 2) shall be provided to ENVS site personnel and

visitors upon their arrival at the site. A roster (Tab 2), listing all ENVS

personnel working at the site shall also be maintained and kept in the site

Safety File.

• The ENVS Site Lead / Manager shall ensure the project data sheet and roster

are maintained current, and copies provided to the responsible ENVS Service

or Installation Manager.

C. Medical

• Upon mobilization, the ENVS Site Manager shall establish medical care

arrangements for ENVS site personnel. Every effort should be made to

identify the most suitable ambulance and medical facilities located near t he

project.

• Emergency contacts and telephone numbers must be posted in the site office

and housing location(s). Suitable first aid kit(s) shall be maintained readily

available in the site office and tool containers.

• Means for communicating with ambulance and medical personnel shall be

established (i.e., phone, interpreter, English speaking physician). Emergency

contacts and telephone numbers must be posted in the site office and housing

location(s).

D. Safety Orientation and Training

• All personnel shall be provided with the training and orientation necessary to

enable them to perform work assignments in a safe manner.

• The ENVS Site Safety Representative shall give project Safety Orie ntations

for ENVS employees. All Project Safety Orientations shall include a revi ew

of ENVS and Progress Energy’s Project Safety Requirements.

• Relevant Safety Talks shall be reviewed with crews during weekly/ daily

toolbox meetings. (See Intranet for Safety Toolbox Talks)

• The Project Emergency Procedures (Notifications, Signals, Access and Egr ess

Routes, Assembly Areas, etc.) shall be communicated to all personnel upon

arrival.

• All significant hazards will be brought to all personals attention.

• All safety orientation and training conducted shall be documented and

maintained in the Site Safety file.

E. Safety Meetings

• Project Safety Meeting - A weekly safety meeting (each shift) s hall be held by

the Site Manager or his/her designee with all ENVS Site Personnel to

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# GE Energy

coordinate related activities and facilitate safety training. Prepared s afety

topics (Toolbox Talks) or related items applicable to current job conditions

should be used.

• Customer Meeting - Safety concerns and related action plans shall be

reviewed during these meetings.

• Meeting Minutes - Documentation showing the following specifics of safety

meetings conducted should be distributed to each attendee and maintained on

file at the site (EHS FORM 5):

o Time and Date of Meeting

o Attendees

o Topics/Comments

o Assignments - Party Responsible/Date (If Applicable)

o Person conducting meeting

Pre job briefs – for any special work, inspections, HVT tests, equip maintenance. Must be

done before task is performed.

F. Program Audits and Inspections

• In addition to daily documented walkarounds, the ENVS Site Safety

Representative should conduct a weekly inspection (each shift) of ENVS

controlled work areas (EHS FORM 4A or 4B).

• Inspection/audit results will be reported to the ENVS Site Manager for

corrective action. Audits / Inspections and related actions will be documented

and maintained on file at the site.

• Upon observance of a safety hazard, the GE Site Manager may, at his/her

discretion, issue a SCAR to the responsible party requiring prompt correction.

• In cases of imminent danger, the GE Site Manager shall immediately prohibit

site personnel from working in the affected area until the hazard has been

corrected.

G. Accident Reports and Record keeping

• All accidents (e.g., injuries, property damage, spills, near misses) shall be

reported and investigated in accordance with ENVS Procedure HS3. Copies

of all injury and illness reports shall be provided to the responsible manager

and Region EHS Manager responsible for the job and the injured employees

Manager within 24 hours.

• Copies of all correspondence related to a serious accident shall be provided to

the Region and HQ EHS Managers immediately.

• Copies of all accident reports should also be provided to the Customer upon

request.

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H. Site Chemical Management (HazCom) Program

• A HazCom program shall be prepared for the site (as applicable to work

scopes) and include an inventory and Material Safety Data Sheet (MSDS) for

hazardous materials used by ENVS on the project. This should be available at

the site.

• All ENVS Personnel shall be provided required training.

• 

# Copies of all MSDS are to be maintained in the Site HazCom Manual located

in the ENVS Site Manager’s office.

I. Regulatory Administrative Requirements

• At project mobilization:

o Post all regulatory required EHS posters

o Post Emergency Response phone numbers.

• Additionally, any regulatory visits / inspection must be

reported immediately to the Region EHS Manager.

J. Site Safety Files

The following items shall be maintained in the site safety files and shall be i ncluded

in the projects archive files at project completion:

• Weekly safety meeting topics and attendees, special safety meetings or talks

(GE lead)

• Weekly safety inspections (GE lead)

• All incident, accident, near miss reports. Both Contractor and GE (include

root cause and corrective action)

• All SCAR's

• All LOTO/Permit to Work documentation.

• All closed permitted hot work, hub compartment entry, confined space

permits.

• Regulator audits, if any

• Pre-op brief form

K. Security Plan

Where deemed necessary by the Service Manager / Project Manager, the ENVS Site

Lead / Manager in conjunction with the GE Energy Security Director shall es tablish a

security plan for ENVS personnel working on the project. All ENVS site personnel

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# GE Energy

shall be briefed on the plan and a copy provided to the Service Manager and EHS

Manger.



# 1.4 Contractor Site Safety Activities

A. The Contractor shall be solely responsible for carrying out all activities safely,

maintaining a safe place of work and ensuring compliance.

B. The Contractor shall regularly inspect its work areas for hazardous conditions and

take required corrective actions immediately.

C. The Contractor shall assign qualified supervision and Competent Persons to

perform work, as required by applicable law and these instructions. The

Contractor shall ensure that each Contractor employee is knowledgeable of

applicable laws and these instructions.

D. Contractor Safety Orientation, Training and staffing

• The Contractor shall provide employees with the training and orientation

necessary to enable them to perform work assignments in a safe manner.

• The Contractor Site Manager will designate a Competent Person as Site

Safety Representative responsible for the proper administration of Contractor

site safety activities. This person shall be named in writing to the GE Site

Lead / Manager.

• All safety orientation and training conducted shall be documented and made

available upon request.

E. Contractor Safety Meetings

• Weekly Contractor Supervisor Safety Meetings shall be held by the

Contractor Site Manager with supervisors to coordinate related activitie s

among each craft/subcontractor and facilitate safety training.

• Weekly / daily Tool Box Safety Meetings shall be held by each Contractor

Supervisor with their crew, using prepared safety topics or related items

applicable to current job conditions.

• Safety meetings should be documented and distributed in accordance with

Section III, Section III, and Paragraph G.

F. Contractor Program Audits and Inspections

• The Contractor Site Safety Representative shall conduct a weekly inspect ion

of the Contractors work areas.

• Audits/Inspections results will be reported to the Contractor Site Manager f or

corrective action.

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G. Accident Reports and Recordkeeping

• All accidents involving personal injury/illness or property damage shall be

immediately reported to the ENVS Site Manager.

• Accidents shall be investigated by both GE and the Contractor and corrective

action implemented to prevent recurrence.

• The Contractor shall maintain accurate documented accident and injury

records. Copies of all correspondence related to an accident / incident shall be

made copied to the ENVS Site Lead / Manager upon request.



# 1.5 Customer Site Safety Guidelines

ENVS and Contractor personnel shall/will follow requirements outlined below:

Note : Where required, Customer EHS Procedures may be used

where a review determines that each Customer Procedure(s)

provides a level of protection equivalent to ENVS requirements

and each Procedure is communicated to all affected personnel

under ENVS scope.

A. Medical/First Aid

Adequate medical/first aid care must be available to anyone who may be injure d

in connection with his or her work. Where Emergency Medical Response

Services are not immediately (Within 15 minutes) available, establish a trai ned;

properly equipped medical response available during work hours to respond to a

medical emergency on the project i.e. qualified first aider

B. Fire Protection

• Maintain proper fire extinguishers readily accessible for use in all work a reas.

Inspect fire extinguishers monthly. Replace and return used fire extinguisher s

promptly for re-charging.

• Keep combustible and flammable materials away from ignition sources.

Protect Scaffold planking etc. from sparks and open flames.

• Ensure that an adequate hot works permit system is in place and implemented.

• Maintain clear access to/of fire apparatus, aisles, traffic lanes and exits. Know

the location of fire exits Prohibit the re-fueling of equipment while it is

running or hot.

C. Housekeeping

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Maintain work areas and walkways clear of obstructions and the accumulation of

tripping hazards and combustible debris.

D. Hot Work and Flame Permit

Use a permit system to safeguard welding, cutting and burning operations.

E. Confined Space Entry Permit

Use a permit system in accordance with HSEM-5.5 to safeguard personnel whil e

working in confined spaces.

F. Personnel Protective Equipment

• Wear approved safety glasses/side shields and hard hats through the project,

except in office areas (Metal hard hats are prohibited). Wear an approved ful l

body harness and two lanyards (100% “Tie-off”) whenever there is a risk of

falling 6ft / 2m or more, are not protected by a standard guardrail or

equivalent. If in doubt, use a full body harness and lanyards attached to a

proper anchorage.

• Designate all areas where approved hearing protection is required. Wear

“Approved” Hearing Protection in “Designated Areas”. When in doubt of

noise levels, hearing protection shall be used.

• Wear other PPE such as Nomex, Gloves, etc. where required.

• Review PGN procedures for lime handling area and activities

G. Appropriate Attire

Wear shirts with sleeves, long pants and work shoes while working in any

construction area.

H. Signs, Signals, and Barricades

• Observe and adhere to all warning signs, signals, and barricades. Post/erect

signs, signals, or barricades necessary to advise personnel of hazardous

conditions in ENVS work areas.

• In order to uniformly identify particular hazards on the project, a barrier tape

identification system will be used. The identification system has been

developed so that any person working on the site, regardless of employer, can

recognize and avoid a hazard when properly marked.

• The following barrier tape identification system shall be used:

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o Yellow Tape (May have black in it) - “Use Caution When

Crossing”. Used for open manholes, trenches, excavations, etc.

o Red Tape (May have black in it) - “Do Not Cross” unless

authorized to do so. Used for open wiring, switchgear, etc.

o Yellow and Magenta (Purple) Tape

- “Do Not Cross” . Used for

possible radiation hazard, x-ray, etc.

• The person erecting the barrier tape shall hang a tag on the tape that indicate s

the hazard, name of Contractor, and name of person erecting the tape. The

barrier tape shall be erected far enough back from the hazard to allow

adequate warning and protection from the hazards. The barrier shall be so

constructed to stand against adverse weather conditions and construction

traffic. The barrier tape shall be maintained as long as the hazard is pres ent.

I. Elevated Work Areas

Provide safe and convenient access such as stairs, ladders, etc. to the working

level. Protect elevated work areas (floors, platforms, walkways, roofs, etc. ) which

are 6’ (h) / 2m or greater or whenever there is an exposure to a hazardous

condition such as working over machinery, implement hazard etc, on all open

sides with standard guardrails or equivalent. Where such protection cannot be

provided, approved full body harness and lanyards attached to a proper anchorage

shall be used.

J. Scaffolding

• Use competent trained scaffold builders to erect scaffolding. Erect all

scaffolding level, plumb and on a firm base. Where required and space

permits, all scaffold platforms must be equipped with a standard guardrail

rigidly secured, standard, mid rail, completely decked, and rigidly secured toe

boards on all open sides. Provide a safe and convenient access to the working

level.

• Some of the test locations have temporary scaffolding

• Have a Competent Person verify, prior to use, that the scaffold has been

properly erected and a “Competent Scaffold”, or “Warning This Scaffold -

Incomplete”, or “Caution - Defective Do Not Use” tag has been attached at

the point of access.

• Prohibit alteration of a scaffold via welding, burning, bending, etc.

• Prohibit riding on mobile scaffolds.

K. Tagging and Lockout

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Safeguard personnel while working on energizable equipment via deenergization, lockout/tagout, checking for “O” potential and grounding.

L. Crane and Motorized Equipment Operation

• Permit only qualified competent operators to operate cranes and motorized

equipment. Contractor supervision shall make available, documentation

establishing operator experience. Permit only Competent Person(s) to rig

loads.

• Operate cranes and motorized within manufacture’s specifications and

limitations.

• Lift plans shall be developed for lifts, which meet any of the following

criteria. Lift plans shall be completed by a Competent Person and submitted

to the Site EHS Representative for review.

o Lifts using more than one crane

o Lifts greater than 75% of the cranes capacity

o Lifts performed during wind speeds between 20 and 30 mph. If

wind speed exceeds 30 mph, do not attempt lift

o Lifting of critical equipment, over critical equipment or at the

discretion of the GE site lead and/or EHS manager.

M. Crane and Motorized Equipment Inspections

Have a Competent certified Person inspect all cranes and motorized equipment at

the beginning of each shift to ensure that all parts, equipment, and accessories that

affect safe operation are properly operating. All defects are to be corre cted prior

to use.

N. Crane Suspended Personnel Baskets

Crane Suspended Personnel Baskets shall only be used to access elevated work

locations where the use of scaffolds, JLG’s, ladders, etc. are more hazardous or

not possible because of structural design or worksite conditions.

O. Tool and Equipment Inspection

In addition to checks prior to use, inspect rigging equipment, ladders, electrical

equipment, welding leads and hoses for defects each quarter. Defective

equipment is to be tagged “Caution - Do Not Use” and removed from service until

it has been repaired or discarded.

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P. Temporary Electrical Power and Ground Fault Protection

• Mark electrical panels to identify the circuit and voltage.

• Properly identify all main disconnects.

• Provide manufactured metal covers or equivalent on any energized panel.

• Protect all temporary wiring or by using Ground Fault Circuit Interrupters

(GFCI). If GFCI is not available, an Assured Equipment Grounding Program

must be implemented for project greater than 1 month in duration.

• Protect temporary electrical wiring, extension cords and leads from dama ge.

Remove from service any damaged wiring, extension cords, and leads.

• Protect temporary lighting via guards or by locating at least 7 feet above the

work level.

Q. Asbestos & Lead Paint

All Suspected Asbestos Containing Materials (ACM’s) and Lead Paint shall be

identified and verified prior to commencement of work. Use, handle and store any

asbestos or material potentially containing asbestos in accordance with t he ENVS

Asbestos Management Procedure.

R. Hazardous Materials Management

• Use, handle, and store hazardous materials in a manner that will prevent harm

to personnel and the environment.

• Deposit any waste generated during the performance of work, to receptacles,

as directed by the Customer’s Facility Representative.

• All chemical containers that are stored and used at the site must be labeled.

Labels must not be removed or defaced.

• Chemicals, fuels and oils received at the Site must be immediately moved to

their designated storage area.

• All storage areas shall be provided with containment and protected by the

elements using a roof, tarp, or approved hazardous material storage cabinet.

S. Spill Prevention

Provisions will be made to prevent the release of hazardous materials to the

environment. These shall include the use of drip pans, oil absorbents and pigs.

All hazardous material deemed to be discarded or abandoned would be

appropriately contained. Oil transfers will be monitored to insure that all hose

connections are in good repair and not leaking. Pipe cutters and threaders will be

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provided with pans or sandboxes as necessary, to maintain housekeeping of chips

and oil.

T. Precautions for Working in the Hub Compartment of an Operating Turbine

• A Permit System shall be used to safeguard Personnel while working in the

turbine compartment of an operating gas turbine. A copy of the permit shall

remain in the work area until the authorized person has verified that all

persons have exited the turbine compartment and it is safe to remove the

permit.

• Additional control measures shall be implemented as required, to protect

personnel against potential work-related hazards not addresses above.

U. Demolition

Prior to the start of demolition operations, obtain an engineering survey of the

structure (performed by a Competent Person/ Structural Engineer) to determ ine

the condition of framing, floors, walls, and the possibility of unplanned collapse

of any portion of the structure. Thereafter, all demolition work shall be

performed in such a sequence and manner as established in accordance with loca l

regulatory requirements.

V. Site Restrictions

• ENVS personnel will be barred or removed from the ENVS site, if found

violating any law, or otherwise engaging in conduct that is likely to cause

personal injury, illness or property damage. Subcontractors shall be solely

responsible for discipline of their employees.

• Additional control measures shall be implemented as required, to protect

personnel against potential work-related hazards not addresses above.



# 1.6 References

A. ENVS Safety Manual

B. ENVS HazCom Program Manual

C. Customer’s Site Safety Policies / Procedures

D. ENVS Contractor Safety Requirements (as required)

E. ENVS Contractor Safety Requirements (as required)

F. ENVS Confined Space Entry Program (as required)

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1.7 Responsibility

A. Site Management - Correct or cause to have corrected, noted or

reported safety deficiencies. Administer and implement the

Project Safety Plan.



# 1.8 Interpretation

A. Contact the Region EHS Manager



# 1.9 Sorbent MSDS

The material safety data sheet (MSDS) in Figure A-5 contains data reg arding the properties

of the hydrated lime sorbent. The sorbent contains mostly calcium hydroxide (>90%) with

traces of magnesium hydroxide, magnesium oxide, calciu carbonate, and silicon diox ide. The

appearance is odorless white or gray powder. It is not combustible. The reactivity is

classified as stable. The sorbent should not be mixed with acid. It may react explos ively with

maleic anhydride. Also, the sorbent may form flammable products when heated wit h

phosporous. It may react with aluminum in presence of water to form hydrogen gas

.

Operators should avoid skin and eye contact to prevent irritation. Contact lenses should not

be worn when working with the sorbent. Inhalation can cause coughing, sneezing, or

breathing problems. The first aid procedure for sorbent contact is to flush the conta minated

area with excess water. For eye contact, the eye should be rinsed with eye w ash solution or

excess water and medical attention should be sought. Any spilled material should be swe pt or

vacuumed, stored in a sealed container, and managed in accordance with plant waste disposal

practices.

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Figure C-1. Sorbent MSDS.

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Figure C-1. Sorbent MSDS (cont.)

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# 2.0 Resources

During the splitter tests, one mechanical technician and one engineer from GE wi ll be on site

to facilitate the test activities. Two additional mechanical technicians a re requested to support

the test activities.