F4 0.0 kg/s RH HSH HSH HSH G3 519.1 kg/s 1.0433 bar 656.7 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 72.6 kg/s 160.33 bar 586.6 °C 3538.7 kJ/kg To Gas Heater IP admission forced 7.2 kg/s 34.69 bar 353.9 °C 3114.9 kJ/kg LEC G5 kg/s 519.1 1.0131 bar °C 75.6 W11 73.4 kg/s 151.7 °C 650.5 kJ/kg S8 Forced 8.5 kg/s 4.50 bar 313.4 °C 3093.6 kJ/kg W13 15.0 kg/s 149.4 °C 632.4 kJ/kg S5 Forced 71.1 kg/s 34.69 bar 363.8 °C 3138.8 kJ/kg S6 Forced 78.5 kg/s 31.01 bar 585.8 °C 3649.7 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.2 kg/s E Flue gas %mol N2 72.7988 O2 11.4953 Ar 0.8665 H2O 10.7767 CO2 4.0627 To Air Heater W15 73.2 kg/s 151.7 °C 650.5 kJ/kg W10 15.4 kg/s 149.4 °C 632.4 kJ/kg /1 F1 12.146 kg/s °C 15.0 2138.23 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 2138.23 x10^6 kJ/h C W23 0.0 kg/s x1 /1 G2 32.0 °C 62.00 W4 97.0 kg/s 39.5 °C 166.9 kJ/kg S9 8.5 kg/s 4.18 bar 311.4 °C 3090.1 kJ/kg B G1 503.6 kg/s 1.01 bar 32.0 °C E W18 6.9 kg/s 36.7 °C 157.4 kJ/kg F2 (Gas) 12.1 kg/s 207.0 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 71.1 kg/s 35.41 bar 365.3 °C 3140.8 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 6.9 kg/s 239.8 °C 1036.5 kJ/kg S7 78.5 kg/s 29.94 bar 583.8 °C 3646.2 kJ/kg %RH S2 72.6 kg/s 155.66 bar 584.6 °C 3537.7 kJ/kg W2 90.1 kg/s 39.7 °C 167.6 kJ/kg To Condenser W19 0.0 kg/s SSH 128966 kW /1 0.90 Power Factor 0.90 Power Factor 225481 kW S10 88.4 kg/s 0.0693 bar 38.8 °C 2409.6 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10936.0 kg/s 34.9 °C 139.50 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-001_Forced-Rev.1 212777909 20-May-2022 Description: Natural gas, base load. Summer 2100 hrs Degradation, Zero Test Tolerance Ambient: 32.0°C, 62.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 354.45 MW 6032.6 kJ/kWh 59.68 % 344.70 MW 6203.2 kJ/kWh 58.03 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.9 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10936.0 kg/s 30.3 °C 121.36 kJ/kg W1 90.3 kg/s 0.0693 bar 38.8 °C 162.6 kJ/kg E W3 90.3 kg/s 39.0 °C 164.8 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 352.0 kg/s 1.0270 bar 657.2 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 48.6 kg/s 108.96 bar 586.6 °C 3585.0 kJ/kg To Gas Heater IP admission forced 5.9 kg/s 23.93 bar 321.1 °C 3062.8 kJ/kg LEC G5 kg/s 352.0 1.0131 bar °C 71.7 W11 48.2 kg/s 148.0 °C 631.0 kJ/kg S8 Forced 4.6 kg/s 4.23 bar 298.1 °C 3062.5 kJ/kg W13 10.8 kg/s 146.5 °C 618.9 kJ/kg S5 Forced 47.6 kg/s 23.92 bar 370.6 °C 3176.0 kJ/kg S6 Forced 54.2 kg/s 21.45 bar 585.8 °C 3657.6 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.7 kg/s E Flue gas %mol N2 73.1022 O2 12.3839 Ar 0.8701 H2O 9.9863 CO2 3.6575 To Air Heater W15 46.2 kg/s 148.0 °C 631.0 kJ/kg W10 12.5 kg/s 146.5 °C 618.9 kJ/kg /1 F1 7.396 kg/s °C 10.3 1301.97 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 1301.97 x10^6 kJ/h C W23 0.0 kg/s W19 0.0 kg/s x1 /1 G2 32.0 °C 62.00 W4 65.5 kg/s 37.7 °C 158.8 kJ/kg S9 4.6 kg/s 4.14 bar 296.2 °C 3059.0 kJ/kg B G1 352.4 kg/s 1.01 bar 32.0 °C E W18 4.7 kg/s 40.5 °C 172.3 kJ/kg F2 (Gas) 7.4 kg/s 204.4 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 47.6 kg/s 24.41 bar 371.9 °C 3178.0 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 4.7 kg/s 221.1 °C 948.9 kJ/kg S7 54.2 kg/s 20.71 bar 583.9 °C 3654.1 kJ/kg %RH S2 48.6 kg/s 105.80 bar 585.1 °C 3584.0 kJ/kg W2 60.8 kg/s 37.4 °C 157.7 kJ/kg To Condenser SSH IBH is ON 85485 kW /1 0.90 Power Factor 0.90 Power Factor 112742 kW S10 59.8 kg/s 0.0603 bar 36.2 °C 2437.2 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10936.0 kg/s 33.5 °C 133.84 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-002_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Summer 2100 hrs Degradation, Zero Test Tolerance, 50% Load Ambient: 32.0°C, 62.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 198.23 MW 6568.1 kJ/kWh 54.81 % 190.18 MW 6846.0 kJ/kWh 52.59 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.3 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10936.0 kg/s 30.3 °C 121.36 kJ/kg W1 61.2 kg/s 0.0603 bar 36.2 °C 151.8 kJ/kg E W3 61.2 kg/s 36.4 °C 153.5 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 534.5 kg/s 1.0451 bar 655.4 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 74.6 kg/s 163.84 bar 582.6 °C 3524.6 kJ/kg To Gas Heater IP admission forced 7.4 kg/s 35.51 bar 355.5 °C 3117.0 kJ/kg LEC G5 kg/s 534.5 1.0131 bar °C 75.8 W11 75.4 kg/s 152.8 °C 655.3 kJ/kg S8 Forced 8.7 kg/s 4.61 bar 314.6 °C 3095.7 kJ/kg W13 15.4 kg/s 150.4 °C 636.7 kJ/kg S5 Forced 73.0 kg/s 35.51 bar 360.3 °C 3128.5 kJ/kg S6 Forced 80.5 kg/s 31.73 bar 583.1 °C 3643.0 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.1 kg/s E Flue gas %mol N2 73.1575 O2 11.5286 Ar 0.8707 H2O 10.3487 CO2 4.0944 To Air Heater W15 75.2 kg/s 152.8 °C 655.3 kJ/kg W10 15.6 kg/s 150.4 °C 636.7 kJ/kg /1 F1 12.583 kg/s °C 15.0 2215.17 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 2215.17 x10^6 kJ/h C W23 0.0 kg/s x1 /1 G2 24.1 °C 81.00 W4 99.5 kg/s 39.4 °C 166.4 kJ/kg S9 8.7 kg/s 4.29 bar 312.5 °C 3092.2 kJ/kg B G1 518.5 kg/s 1.01 bar 24.1 °C E W18 7.1 kg/s 36.6 °C 157.0 kJ/kg F2 (Gas) 12.6 kg/s 207.0 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 73.0 kg/s 36.25 bar 361.8 °C 3130.5 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 7.1 kg/s 241.0 °C 1042.4 kJ/kg S7 80.5 kg/s 30.64 bar 581.2 °C 3639.5 kJ/kg %RH S2 74.6 kg/s 159.08 bar 580.5 °C 3523.6 kJ/kg W2 92.4 kg/s 39.6 °C 167.2 kJ/kg To Condenser W19 0.0 kg/s SSH 131676 kW /1 0.90 Power Factor 0.90 Power Factor 233491 kW S10 90.7 kg/s 0.0689 bar 38.7 °C 2405.8 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10937.1 kg/s 34.7 °C 138.74 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-003_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Annual Average 2100 hrs Degradation, Zero Test Tolerance Ambient: 24.1°C, 81.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 365.17 MW 6066.2 kJ/kWh 59.35 % 355.28 MW 6235.1 kJ/kWh 57.74 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.8 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10937.1 kg/s 30.0 °C 120.16 kJ/kg W1 92.6 kg/s 0.0689 bar 38.7 °C 162.2 kJ/kg E W3 92.6 kg/s 38.9 °C 164.4 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 351.7 kg/s 1.0270 bar 657.2 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 48.5 kg/s 108.68 bar 586.6 °C 3585.2 kJ/kg To Gas Heater IP admission forced 5.9 kg/s 23.86 bar 320.9 °C 3062.4 kJ/kg LEC G5 kg/s 351.7 1.0131 bar °C 71.3 W11 48.1 kg/s 148.0 °C 630.8 kJ/kg S8 Forced 4.6 kg/s 4.23 bar 297.9 °C 3062.3 kJ/kg W13 10.9 kg/s 146.4 °C 618.8 kJ/kg S5 Forced 47.4 kg/s 23.86 bar 370.7 °C 3176.2 kJ/kg S6 Forced 54.0 kg/s 21.39 bar 585.8 °C 3657.6 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.7 kg/s E Flue gas %mol N2 73.4334 O2 12.3329 Ar 0.8741 H2O 9.6319 CO2 3.7278 To Air Heater W15 46.1 kg/s 148.0 °C 630.8 kJ/kg W10 12.6 kg/s 146.4 °C 618.8 kJ/kg /1 F1 7.519 kg/s °C 10.3 1323.74 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 1323.74 x10^6 kJ/h C W23 0.0 kg/s W19 0.0 kg/s x1 /1 G2 24.1 °C 81.00 W4 65.4 kg/s 37.4 °C 157.6 kJ/kg S9 4.6 kg/s 4.14 bar 296.1 °C 3058.8 kJ/kg B G1 348.9 kg/s 1.01 bar 24.1 °C E W18 4.8 kg/s 40.6 °C 172.4 kJ/kg F2 (Gas) 7.5 kg/s 204.0 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 47.4 kg/s 24.35 bar 372.0 °C 3178.2 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 4.8 kg/s 220.7 °C 946.9 kJ/kg S7 54.0 kg/s 20.65 bar 583.9 °C 3654.1 kJ/kg %RH S2 48.5 kg/s 105.53 bar 585.1 °C 3584.2 kJ/kg W2 60.6 kg/s 37.1 °C 156.4 kJ/kg To Condenser SSH IBH is ON 85336 kW /1 0.90 Power Factor 0.90 Power Factor 116747 kW S10 59.6 kg/s 0.0592 bar 35.9 °C 2435.4 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10937.1 kg/s 33.1 °C 132.59 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-004_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Annual Average 2100 hrs Degradation, Zero Test Tolerance, 50% Load Ambient: 24.1°C, 81.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 202.08 MW 6550.5 kJ/kWh 54.96 % 194.03 MW 6822.4 kJ/kWh 52.77 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.3 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10937.1 kg/s 30.0 °C 120.16 kJ/kg W1 61.0 kg/s 0.0592 bar 35.9 °C 150.5 kJ/kg E W3 61.0 kg/s 36.1 °C 152.2 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 538.7 kg/s 1.0454 bar 646.6 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 73.0 kg/s 160.24 bar 579.0 °C 3518.5 kJ/kg To Gas Heater IP admission forced 7.8 kg/s 34.91 bar 353.0 °C 3112.3 kJ/kg LEC G5 kg/s 538.7 1.0131 bar °C 74.0 W11 73.8 kg/s 152.2 °C 652.6 kJ/kg S8 Forced 8.6 kg/s 4.55 bar 315.1 °C 3096.9 kJ/kg W13 15.9 kg/s 149.9 °C 634.6 kJ/kg S5 Forced 71.5 kg/s 34.91 bar 358.2 °C 3124.9 kJ/kg S6 Forced 79.4 kg/s 31.21 bar 578.4 °C 3632.7 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.1 kg/s E Flue gas %mol N2 73.8791 O2 11.6780 Ar 0.8793 H2O 9.4467 CO2 4.1169 To Air Heater W15 73.6 kg/s 152.2 °C 652.6 kJ/kg W10 16.1 kg/s 149.9 °C 634.6 kJ/kg /1 F1 12.703 kg/s °C 15.0 2236.43 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 2236.43 x10^6 kJ/h C W23 0.0 kg/s x1 /1 G2 15.0 °C 84.00 W4 98.6 kg/s 35.5 °C 150.0 kJ/kg S9 8.6 kg/s 4.22 bar 313.0 °C 3093.4 kJ/kg B G1 522.4 kg/s 1.01 bar 15.0 °C E W18 7.3 kg/s 37.7 °C 161.6 kJ/kg F2 (Gas) 12.7 kg/s 207.0 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 71.5 kg/s 35.63 bar 359.7 °C 3126.9 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 7.3 kg/s 239.6 °C 1035.5 kJ/kg S7 79.4 kg/s 30.14 bar 576.4 °C 3629.2 kJ/kg %RH S2 73.0 kg/s 155.59 bar 577.0 °C 3517.5 kJ/kg W2 91.3 kg/s 35.3 °C 149.1 kJ/kg To Condenser W19 0.0 kg/s SSH 128929 kW /1 0.90 Power Factor 0.90 Power Factor 239197 kW S10 89.5 kg/s 0.0544 bar 34.4 °C 2403.1 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10952.7 kg/s 30.2 °C 120.71 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-005_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Winter 2100 hrs Degradation, Zero Test Tolerance Ambient: 15.0°C, 84.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 368.13 MW 6075.2 kJ/kWh 59.26 % 358.31 MW 6241.6 kJ/kWh 57.68 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.8 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10952.7 kg/s 25.6 °C 102.27 kJ/kg W1 91.3 kg/s 0.0544 bar 34.4 °C 144.1 kJ/kg E W3 91.3 kg/s 34.6 °C 146.3 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 350.5 kg/s 1.0269 bar 657.2 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 48.1 kg/s 107.86 bar 586.6 °C 3586.0 kJ/kg To Gas Heater IP admission forced 5.9 kg/s 23.69 bar 320.2 °C 3061.2 kJ/kg LEC G5 kg/s 350.5 1.0131 bar °C 68.8 W11 47.7 kg/s 147.8 °C 630.3 kJ/kg S8 Forced 4.3 kg/s 4.22 bar 297.8 °C 3062.1 kJ/kg W13 10.9 kg/s 146.3 °C 618.3 kJ/kg S5 Forced 47.1 kg/s 23.69 bar 370.8 °C 3176.8 kJ/kg S6 Forced 53.6 kg/s 21.23 bar 585.8 °C 3657.8 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.6 kg/s E Flue gas %mol N2 74.1250 O2 12.3881 Ar 0.8823 H2O 8.8111 CO2 3.7935 To Air Heater W15 45.7 kg/s 147.8 °C 630.3 kJ/kg W10 12.7 kg/s 146.3 °C 618.3 kJ/kg /1 F1 7.602 kg/s °C 10.3 1338.38 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 1338.38 x10^6 kJ/h C W23 0.0 kg/s W19 0.0 kg/s x1 /1 G2 15.0 °C 84.00 W4 64.9 kg/s 33.2 °C 140.2 kJ/kg S9 4.3 kg/s 4.14 bar 296.0 °C 3058.6 kJ/kg B G1 344.1 kg/s 1.01 bar 15.0 °C E W18 4.9 kg/s 40.5 °C 172.3 kJ/kg F2 (Gas) 7.6 kg/s 203.6 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 47.1 kg/s 24.17 bar 372.1 °C 3178.8 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 4.9 kg/s 220.2 °C 944.8 kJ/kg S7 53.6 kg/s 20.49 bar 583.9 °C 3654.3 kJ/kg %RH S2 48.1 kg/s 104.73 bar 585.1 °C 3585.0 kJ/kg W2 60.0 kg/s 32.6 °C 137.6 kJ/kg To Condenser SSH IBH is ON 86028 kW /1 0.90 Power Factor 0.90 Power Factor 119600 kW S10 58.9 kg/s 0.0460 bar 31.4 °C 2409.7 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10952.7 kg/s 28.6 °C 114.51 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-006_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Winter 2100 hrs Degradation, Zero Test Tolerance, 50% Load Ambient: 15.0°C, 84.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 205.63 MW 6508.8 kJ/kWh 55.31 % 197.57 MW 6774.1 kJ/kWh 53.14 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.5 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10952.7 kg/s 25.6 °C 102.27 kJ/kg W1 60.5 kg/s 0.0460 bar 31.4 °C 131.6 kJ/kg E W3 60.5 kg/s 31.5 °C 133.3 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 540.6 kg/s 1.0455 bar 641.8 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 72.3 kg/s 158.39 bar 576.7 °C 3514.0 kJ/kg To Gas Heater IP admission forced 7.7 kg/s 36.38 bar 352.3 °C 3107.3 kJ/kg LEC G5 kg/s 540.6 1.0131 bar °C 71.4 W11 73.0 kg/s 151.8 °C 650.7 kJ/kg S8 Forced 8.6 kg/s 4.50 bar 315.8 °C 3098.4 kJ/kg W13 16.0 kg/s 149.5 °C 633.0 kJ/kg S5 Forced 70.7 kg/s 34.55 bar 356.6 °C 3121.9 kJ/kg S6 Forced 78.5 kg/s 30.82 bar 575.6 °C 3626.7 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.1 kg/s E Flue gas %mol N2 74.0451 O2 11.7466 Ar 0.8813 H2O 9.2222 CO2 4.1049 To Air Heater W15 72.8 kg/s 151.8 °C 650.7 kJ/kg W10 16.2 kg/s 149.5 °C 633.0 kJ/kg /1 F1 12.701 kg/s °C 15.0 2235.92 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 2235.92 x10^6 kJ/h C W23 0.0 kg/s x1 /1 G2 12.0 °C 87.00 W4 97.7 kg/s 28.9 °C 122.5 kJ/kg S9 8.6 kg/s 4.18 bar 313.7 °C 3094.9 kJ/kg B G1 524.4 kg/s 1.01 bar 12.0 °C E W18 7.1 kg/s 36.3 °C 155.5 kJ/kg F2 (Gas) 12.7 kg/s 207.0 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 70.7 kg/s 35.26 bar 358.1 °C 3123.9 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 7.1 kg/s 241.8 °C 1046.2 kJ/kg S7 78.5 kg/s 29.76 bar 573.7 °C 3623.2 kJ/kg %RH S2 72.3 kg/s 153.79 bar 574.7 °C 3513.0 kJ/kg W2 90.6 kg/s 28.3 °C 119.9 kJ/kg To Condenser W19 0.0 kg/s SSH 126907 kW /1 0.90 Power Factor 0.90 Power Factor 239702 kW S10 88.6 kg/s 0.0365 bar 27.4 °C 2404.3 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10973.8 kg/s 23.2 °C 92.63 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-007_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Minimum Extreme 2100 hrs Degradation, Zero Test Tolerance Ambient: 12.0°C, 87.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 366.61 MW 6098.9 kJ/kWh 59.03 % 356.82 MW 6266.2 kJ/kWh 57.45 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 2.0 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10973.8 kg/s 18.5 °C 74.16 kJ/kg W1 90.6 kg/s 0.0365 bar 27.4 °C 114.8 kJ/kg E W3 90.6 kg/s 27.6 °C 117.1 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 350.3 kg/s 1.0268 bar 657.2 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 48.0 kg/s 107.70 bar 586.6 °C 3586.1 kJ/kg To Gas Heater IP admission forced 6.0 kg/s 23.66 bar 320.0 °C 3060.9 kJ/kg LEC G5 kg/s 350.3 1.0131 bar °C 66.4 W11 47.6 kg/s 147.7 °C 629.7 kJ/kg S8 Forced 4.0 kg/s 4.21 bar 298.1 °C 3062.6 kJ/kg W13 10.9 kg/s 146.2 °C 617.8 kJ/kg S5 Forced 47.0 kg/s 23.66 bar 370.8 °C 3177.0 kJ/kg S6 Forced 53.6 kg/s 21.20 bar 585.8 °C 3657.8 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.6 kg/s E Flue gas %mol N2 74.2714 O2 12.3990 Ar 0.8840 H2O 8.6377 CO2 3.8078 To Air Heater W15 45.6 kg/s 147.7 °C 629.7 kJ/kg W10 12.7 kg/s 146.2 °C 617.8 kJ/kg /1 F1 7.620 kg/s °C 10.3 1341.44 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 1341.44 x10^6 kJ/h C W23 0.0 kg/s W19 0.0 kg/s x1 /1 G2 12.0 °C 87.00 W4 64.6 kg/s 28.3 °C 119.7 kJ/kg S9 4.0 kg/s 4.14 bar 296.3 °C 3059.1 kJ/kg B G1 343.8 kg/s 1.01 bar 12.0 °C E W18 4.9 kg/s 40.4 °C 171.8 kJ/kg F2 (Gas) 7.6 kg/s 203.1 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 47.0 kg/s 24.14 bar 372.1 °C 3179.0 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 4.9 kg/s 219.8 °C 942.8 kJ/kg S7 53.6 kg/s 20.47 bar 583.9 °C 3654.3 kJ/kg %RH S2 48.0 kg/s 104.57 bar 585.1 °C 3585.1 kJ/kg W2 59.8 kg/s 27.3 °C 115.5 kJ/kg To Condenser SSH IBH is ON 85815 kW /1 0.90 Power Factor 0.90 Power Factor 119853 kW S10 58.5 kg/s 0.0339 bar 26.1 °C 2407.9 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10973.8 kg/s 21.6 °C 86.40 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-008_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Minimum Extreme 2100 hrs Degradation, Zero Test Tolerance, 50% Load Ambient: 12.0°C, 87.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 205.67 MW 6522.4 kJ/kWh 55.19 % 197.61 MW 6788.5 kJ/kWh 53.03 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.6 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10973.8 kg/s 18.5 °C 74.16 kJ/kg W1 60.2 kg/s 0.0339 bar 26.1 °C 109.5 kJ/kg E W3 60.2 kg/s 26.2 °C 111.2 kJ/kg F4 0.0 kg/s RH HSH HSH G3 386.5 kg/s 1.0298 bar 657.2 °C HSH HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 52.9 kg/s 118.16 bar 587.0 °C 3577.8 kJ/kg To Gas Heater IP admission forced 0.0 kg/s LEC G5 386.5 kg/s 1.0131 bar 72.6 °C W11 52.9 kg/s 148.7 °C 634.4 kJ/kg S8 Forced 5.6 kg/s 4.28 bar 304.3 °C 3075.2 kJ/kg W13 11.9 kg/s 147.0 °C 621.3 kJ/kg S5 Forced 51.8 kg/s 25.25 bar 366.8 °C 3164.9 kJ/kg S6 Forced 59.9 kg/s 23.73 bar 586.9 °C 3658.3 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 8.1 kg/s E Flue gas %mol N2 73.7454 O2 12.1778 Ar 0.8778 H2O 9.3512 CO2 3.8479 To Air Heater W15 51.0 kg/s 148.7 °C 634.4 kJ/kg W10 13.5 kg/s 147.0 °C 621.3 kJ/kg /1 F1 8.521 kg/s 15.0 °C 1500.05 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 1500.05 x10^6 kJ/h C W23 0.0 kg/s x1 /1 G2 39.0 °C 27.00 W4 72.0 kg/s 39.6 °C 166.7 kJ/kg S9 5.6 kg/s 4.14 bar 302.4 °C 3071.7 kJ/kg B G1 375.5 kg/s 1.01 bar 39.0 °C E W18 5.4 kg/s 44.7 °C 190.0 kJ/kg F2 (Gas) 8.5 kg/s 207.0 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 51.8 kg/s 25.80 bar 368.2 °C 3166.9 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 5.4 kg/s 224.9 °C 966.5 kJ/kg S7 59.9 kg/s 22.91 bar 585.1 °C 3654.8 kJ/kg %RH S2 52.9 kg/s 114.72 bar 585.4 °C 3576.8 kJ/kg W2 66.6 kg/s 39.1 °C 164.8 kJ/kg To Condenser W19 0.0 kg/s SSH 95478 kW /1 0.90 Power Factor 0.90 Power Factor 146942 kW S10 66.5 kg/s 0.0663 bar 38.0 °C 2436.5 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10931.5 kg/s 35.0 °C 140.02 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-009-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Maximum Extreme 2100 hrs Degradation, Zero Test Tolerance Ambient: 39.0°C, 27.0 % RH, 1.013 bar 234.05 MW 6409.0 kJ/kWh 56.17 % '' GENERAL gELECTRIC 1997 Steam Properties C 242.42 MW 6187.8 kJ/kWh 58.18 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 0.0 kg/s E Make-up Water Condenser cooling water inlet 10931.5 kg/s 31.5 °C 126.16 kJ/kg W1 66.6 kg/s 0.0663 bar 38.0 °C 159.2 kJ/kg W3 66.6 kg/s 38.2 °C 161.0 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 348.7 kg/s 1.0267 bar 657.2 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 47.8 kg/s 107.31 bar 586.6 °C 3586.4 kJ/kg To Gas Heater IP admission forced 5.9 kg/s 23.56 bar 319.9 °C 3060.9 kJ/kg LEC G5 kg/s 348.7 1.0131 bar °C 71.6 W11 47.4 kg/s 147.9 °C 630.7 kJ/kg S8 Forced 4.6 kg/s 4.23 bar 297.2 °C 3060.7 kJ/kg W13 10.5 kg/s 146.4 °C 618.8 kJ/kg S5 Forced 46.8 kg/s 23.56 bar 370.8 °C 3177.1 kJ/kg S6 Forced 53.3 kg/s 21.11 bar 585.8 °C 3657.9 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.6 kg/s E Flue gas %mol N2 73.9607 O2 12.8025 Ar 0.8804 H2O 8.7932 CO2 3.5633 To Air Heater W15 45.3 kg/s 147.9 °C 630.7 kJ/kg W10 12.3 kg/s 146.4 °C 618.8 kJ/kg /1 F1 7.104 kg/s °C 10.3 1250.63 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 1250.63 x10^6 kJ/h C W23 0.0 kg/s W19 0.0 kg/s x1 /1 G2 39.0 °C 27.00 W4 64.4 kg/s 38.7 °C 163.1 kJ/kg S9 4.6 kg/s 4.14 bar 295.3 °C 3057.2 kJ/kg B G1 351.6 kg/s 1.01 bar 39.0 °C E W18 4.5 kg/s 40.1 °C 170.4 kJ/kg F2 (Gas) 7.1 kg/s 204.1 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 46.8 kg/s 24.04 bar 372.1 °C 3179.1 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 4.5 kg/s 220.7 °C 947.1 kJ/kg S7 53.3 kg/s 20.38 bar 583.9 °C 3654.4 kJ/kg %RH S2 47.8 kg/s 104.19 bar 585.1 °C 3585.4 kJ/kg W2 59.9 kg/s 38.6 °C 162.6 kJ/kg To Condenser SSH IBH is ON 83519 kW /1 0.90 Power Factor 0.90 Power Factor 104959 kW S10 58.9 kg/s 0.0642 bar 37.4 °C 2447.9 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10931.5 kg/s 34.6 °C 138.49 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-010_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Maximum Extreme 2100 hrs Degradation, Zero Test Tolerance, 50% Load Ambient: 39.0°C, 27.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 188.48 MW 6635.4 kJ/kWh 54.25 % 180.50 MW 6928.7 kJ/kWh 51.96 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.4 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10931.5 kg/s 31.5 °C 126.16 kJ/kg W1 60.4 kg/s 0.0642 bar 37.4 °C 156.7 kJ/kg E W3 60.4 kg/s 37.5 °C 158.4 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 343.8 kg/s 1.0263 bar 657.2 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 47.4 kg/s 106.37 bar 586.6 °C 3587.2 kJ/kg To Gas Heater IP admission forced 5.8 kg/s 23.36 bar 319.2 °C 3059.8 kJ/kg LEC G5 kg/s 343.8 1.0131 bar °C 71.5 W11 47.0 kg/s 147.9 °C 630.2 kJ/kg S8 Forced 4.5 kg/s 4.23 bar 296.8 °C 3060.0 kJ/kg W13 10.4 kg/s 146.4 °C 618.4 kJ/kg S5 Forced 46.4 kg/s 23.36 bar 370.9 °C 3177.7 kJ/kg S6 Forced 52.9 kg/s 20.93 bar 585.8 °C 3658.1 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.6 kg/s E Flue gas %mol N2 73.2051 O2 12.6855 Ar 0.8714 H2O 9.7181 CO2 3.5200 To Air Heater W15 45.0 kg/s 147.9 °C 630.2 kJ/kg W10 12.1 kg/s 146.4 °C 618.4 kJ/kg /1 F1 6.945 kg/s °C 10.3 1222.64 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 1222.64 x10^6 kJ/h C W23 0.0 kg/s W19 0.0 kg/s x1 /1 G2 32.0 °C 62.00 W4 63.7 kg/s 37.5 °C 158.3 kJ/kg S9 4.5 kg/s 4.14 bar 295.0 °C 3056.5 kJ/kg B G1 355.9 kg/s 1.01 bar 32.0 °C E W18 4.4 kg/s 39.8 °C 169.2 kJ/kg F2 (Gas) 6.9 kg/s 203.7 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 46.4 kg/s 23.83 bar 372.2 °C 3179.7 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 4.4 kg/s 220.4 °C 945.6 kJ/kg S7 52.9 kg/s 20.21 bar 584.0 °C 3654.6 kJ/kg %RH S2 47.4 kg/s 103.29 bar 585.1 °C 3586.2 kJ/kg W2 59.3 kg/s 37.3 °C 157.5 kJ/kg To Condenser SSH IBH is ON 83181 kW /1 0.90 Power Factor 0.90 Power Factor 96959 kW S10 58.3 kg/s 0.0600 bar 36.2 °C 2440.1 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10936.0 kg/s 33.4 °C 133.54 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-011_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Summer 2100 hrs Degradation, Zero Test Tolerance, MECL Ambient: 32.0°C, 62.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 180.14 MW 6787.2 kJ/kWh 53.04 % 172.20 MW 7100.3 kJ/kWh 50.70 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.4 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10936.0 kg/s 30.3 °C 121.36 kJ/kg W1 59.7 kg/s 0.0600 bar 36.2 °C 151.5 kJ/kg E W3 59.7 kg/s 36.3 °C 153.2 kJ/kg F4 0.0 kg/s RH HSH HSH HSH G3 344.2 kg/s 1.0264 bar 657.2 °C HSH RH HEC HEV LSH HEC IEC IEV HEC IEC HEC S1 Forced 47.4 kg/s 106.26 bar 586.6 °C 3587.3 kJ/kg To Gas Heater IP admission forced 5.8 kg/s 23.35 bar 319.1 °C 3059.6 kJ/kg LEC G5 kg/s 344.2 1.0131 bar °C 71.1 W11 46.9 kg/s 147.9 °C 630.2 kJ/kg S8 Forced 4.4 kg/s 4.22 bar 296.8 °C 3060.0 kJ/kg W13 10.5 kg/s 146.4 °C 618.4 kJ/kg S5 Forced 46.3 kg/s 23.35 bar 371.0 °C 3177.9 kJ/kg S6 Forced 52.9 kg/s 20.95 bar 585.8 °C 3658.0 kJ/kg LEV To HP Attemperator To RH Attemperator Reheat atemperator forced 0.7 kg/s E Flue gas %mol N2 73.5426 O2 12.6512 Ar 0.8754 H2O 9.3481 CO2 3.5827 To Air Heater W15 44.9 kg/s 147.9 °C 630.2 kJ/kg W10 12.2 kg/s 146.4 °C 618.4 kJ/kg /1 F1 7.066 kg/s °C 10.3 1243.99 x10^6 kJ/h ISH Heat Consumption 0.00 x10^6 kJ/h A1 Heat Consumption 1243.99 x10^6 kJ/h C W23 0.0 kg/s W19 0.0 kg/s x1 /1 G2 24.1 °C 81.00 W4 63.8 kg/s 37.3 °C 157.2 kJ/kg S9 4.4 kg/s 4.14 bar 295.0 °C 3056.5 kJ/kg B G1 356.2 kg/s 1.01 bar 24.1 °C E W18 4.5 kg/s 39.9 °C 169.6 kJ/kg F2 (Gas) 7.1 kg/s 203.5 °C x1 To Condensate Line B F2 (Oil) 0.000 kg/s 15.6 °C 42565.8 kJ/kg LHV S3 46.3 kg/s 23.82 bar 372.3 °C 3179.9 kJ/kg x1 Fuel HX TfuelN 207.000 °C S15 0.0 kg/s /1 /1 Mole Fractions CH4 0.969049 C2H6 0.019114 N2 0.010897 CO2 0.000940 ------------------Sulfur 0.0 ppm,w LHV 48902.4 kJ/kg HHV/LHV 1.109013 x1 Gas Fuel W17_Forced 4.5 kg/s 220.2 °C 944.7 kJ/kg S7 52.9 kg/s 20.23 bar 584.0 °C 3654.5 kJ/kg %RH S2 47.4 kg/s 103.17 bar 585.1 °C 3586.3 kJ/kg W2 59.3 kg/s 37.0 °C 156.2 kJ/kg To Condenser SSH IBH is ON 83334 kW /1 0.90 Power Factor 0.90 Power Factor 100403 kW S10 58.3 kg/s 0.0590 bar 35.9 °C 2437.8 kJ/kg 0.0 kg/s Evap Cooler water to each GT 1 4 GSC 2 3 W25 Condenser cooling water exit 10937.1 kg/s 33.1 °C 132.34 kJ/kg CFE Gross Power Gross Heat Rate (LHV) Gross Efficiency (LHV) Project: Site: CC Manzanillo III Colima, Mexico Net Plant Power 1x1 7F.05 Net Plant Heat Rate (LHV) Heat Balance: By: Date: Net Plant Efficiency (LHV) 1604653-A-012_Forced-Rev.1 212777909 14-May-2022 Description: Natural gas, base load. Annual Average 2100 hrs Degradation, Zero Test Tolerance, MECL Ambient: 24.1°C, 81.0 % RH, 1.013 bar GENERAL gELECTRIC 1997 Steam Properties C 183.74 MW 6770.5 kJ/kWh 53.17 % 175.79 MW 7076.7 kJ/kWh 50.87 % GE Company Proprietary This document contains proprietary information to the GE Company and may not be used or disclosed to others except with written permission of GE Company. W22 1.3 kg/s 1.03 bar 15.0 °C 63.1 kJ/kg Make-up Water Condenser cooling water inlet 10937.1 kg/s 30.0 °C 120.16 kJ/kg W1 59.7 kg/s 0.0590 bar 35.9 °C 150.3 kJ/kg E W3 59.7 kg/s 36.0 °C 151.9 kJ/kg
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