TS-10 Heat & Mass Balance Diagrams M701JAC Final
TS-10 Heat & Mass Balance Diagrams M701JAC Final
TS-10 Heat & Mass Balance Diagrams M701JAC Final
90.4 P 687.0 G
0.0 G
565.7 T
TCA Cooler DA EVA Pump
566.8 G
*4 *5
To GT 0.0 G *3
*1 *9
27.8 P 88.2 P 30.9 P
565.2 T 564.6 T 407.8 T HP IP
564.6 G 566.8 G 523.5 G
0.0G 0.0G
*4 661 T
Steam Turbine 3543.7 G
GEN GEN
LP IP HP Comp. Turbine
0.0 G
Condenser Make-Up
Sea Water 32.0 T
30.0 T
Inlet Air Heat Recovery Steam Generator
0.0823 P 0.0 G
47.5 P *2
58.1 G
385.0 T
42.0 T 30.0 G
468.9 G FGH Gas Compressor
HP Process
Fuel
Exhaust Gas Composition
2.2 G 96.16 G
*7 O2(wt.%) : 11.72
*5 LHV : 47704 kJ/kg CO2(wt.%) : 7.32
Condensate H2O(wt.%) : 8.09
*3
Pump N2(wt.%) : 71.59 Singapore / Sakra Repowering
Ar(wt.%) : 1.28 Multi-Shaft 1on1 GTCC
To GT Gross Plant Power Output : 744600 kW
Gross GT Power Output : 542200 kW ×1
Gland Gross ST Power Output : 202400 kW
Steam Gross Heat Rate : 6161 kJ/kWh-LHV
Operating Conditions
Load : 100%
Ambient Temp. : 32.0 deg.C
Gland Steam Cooling Air Relative Humidity : 85 %
Condenser Cooler Barometric Press. : 1010 mbar
Steam Steam Extraction : With Steam Extraction
P : bar (A)
Water Fuel : Natural Gas
Air T : deg.C ORDER No. DWG No Rev.
Note S1-G-100-32-SE
1. All performance values indicated in this diagram are estimated basis. Fuel G : t/h 0
2. Performance values are based on New and Clean condition.
3. ST performance values indicated in this diagram are estimated based on existing heat balance diagram.
This document contains information proprietary to Mitsubishi Hitachi Power Systems Ltd. It is submitted in confidence and is to be used solely for the purpose for which it is furnished and returned upon
request. This document and such information is not to be reproduced, transmitted, disclosed or used otherwise in whole or in part without the written authorization of Mitsubishi Hitachi Power Systems ,Ltd.
For Reference Only
*7 *1
Return Water
HP/IP BFP
75.0 T
160.0 G
8.5 P 20.8 P
502.3 G *9
205.0 T 397.5 T
60.9 G 3.4 G
130.0 G 414.0 G 82.4 G
98.5 G
*2 *8
19.0 P 20.8 P
Deaerator
LP Process 566.0 T 286.4 T *6
461.5 G 36.7 G
31.5 G
*8 *6
68.2 P 584.7 G
26.1 G
566.0 T
TCA Cooler DA EVA Pump
450.9 G
*4 *5
To GT 18.4 G *3
*1 *9
18.5 P 66.6 P 21.3 P
565.4 T 565.1 T 398.2 T HP IP
363.0 G 424.8 G 414.0 G
0.0G 0.0G
*4 674 T
Steam Turbine 2819.9 G
GEN GEN
LP IP HP Comp. Turbine
0.0 G
Condenser Make-Up
Sea Water 32.0 T
30.0 T
Inlet Air Heat Recovery Steam Generator
0.0729 P 10.8 G
47.5 P *2
47.5 G
385.0 T
39.8 T 30.0 G
373.8 G FGH Gas Compressor
HP Process
Fuel
Exhaust Gas Composition
3.9 G 75.71 G
*7 O2(wt.%) : 11.89
*5 LHV : 47704 kJ/kg CO2(wt.%) : 7.21
Condensate H2O(wt.%) : 8.00
*3
Pump N2(wt.%) : 71.62 Singapore / Sakra Repowering
Ar(wt.%) : 1.28 Multi-Shaft 1on1 GTCC
To GT Gross Plant Power Output : 560000 kW
Gross GT Power Output : 408900 kW ×1
Gland Gross ST Power Output : 151100 kW
Steam Gross Heat Rate : 6450 kJ/kWh-LHV
Operating Conditions
Load : 560MW
Ambient Temp. : 32.0 deg.C
Gland Steam Cooling Air Relative Humidity : 85 %
Condenser Cooler Barometric Press. : 1010 mbar
Steam Steam Extraction : With Steam Extraction
P : bar (A)
Water Fuel : Natural Gas
Air T : deg.C ORDER No. DWG No Rev.
Note S1-G-560mw-32-SE
1. All performance values indicated in this diagram are estimated basis. Fuel G : t/h 0
2. Performance values are based on New and Clean condition.
3. ST performance values indicated in this diagram are estimated based on existing heat balance diagram.
This document contains information proprietary to Mitsubishi Hitachi Power Systems Ltd. It is submitted in confidence and is to be used solely for the purpose for which it is furnished and returned upon
request. This document and such information is not to be reproduced, transmitted, disclosed or used otherwise in whole or in part without the written authorization of Mitsubishi Hitachi Power Systems ,Ltd.
For Reference Only
*7 *1
Return Water
HP/IP BFP
0.0 G
32.6 P
625.5 G *9
413.3 T
111.7 G 0.0 G
0.0 G 551.4 G 38.7 G
0.0 G
*2 *8
30.7 P 32.6 P
Deaerator
LP Process 564.0 T 308.4 T *6
590.1 G 38.7 G
0.0 G
*8 *6
92.2 P 664.2 G
0.0 G
565.1 T
TCA Cooler DA EVA Pump
567.6 G
*4 *5
To GT 0.0 G *3
*1 *9
29.9 P 90.0 P 33.1 P
563.3 T 564.0 T 414.0 T HP IP
590.1 G 567.6 G 551.4 G
0.0G 0.0G
*4 661 T
Steam Turbine 3543.7 G
GEN GEN
LP IP HP Comp. Turbine
0.0 G
Condenser Make-Up
Sea Water 32.0 T
30.0 T
Inlet Air Heat Recovery Steam Generator
0.0991 P 0.0 G
*2
57.9 G
45.6 T 0.0 G
606.3 G FGH Gas Compressor
HP Process
Fuel
Exhaust Gas Composition
0.0 G 96.15 G
*7 O2(wt.%) : 11.72
*5 LHV : 47704 kJ/kg CO2(wt.%) : 7.32
Condensate H2O(wt.%) : 8.09
*3
Pump N2(wt.%) : 71.59 Singapore / Sakra Repowering
Ar(wt.%) : 1.28 Multi-Shaft 1on1 GTCC
To GT Gross Plant Power Output : 773300 kW
Gross GT Power Output : 542200 kW ×1
Gland Gross ST Power Output : 231100 kW
Steam Gross Heat Rate : 5932 kJ/kWh-LHV
Operating Conditions
Load : 100%
Ambient Temp. : 32.0 deg.C
Gland Steam Cooling Air Relative Humidity : 85 %
Condenser Cooler Barometric Press. : 1010 mbar
Steam Steam Extraction : No Steam Extraction
P : bar (A)
Water Fuel : Natural Gas
Air T : deg.C ORDER No. DWG No Rev.
Note S1-G-100-32
1. All performance values indicated in this diagram are estimated basis. Fuel G : t/h 0
2. Performance values are based on New and Clean condition.
3. ST performance values indicated in this diagram are estimated based on existing heat balance diagram.
This document contains information proprietary to Mitsubishi Hitachi Power Systems Ltd. It is submitted in confidence and is to be used solely for the purpose for which it is furnished and returned upon
request. This document and such information is not to be reproduced, transmitted, disclosed or used otherwise in whole or in part without the written authorization of Mitsubishi Hitachi Power Systems ,Ltd.
Additional Performance Parameters of The Heat Balance Diagrams
Note;
(*1) The above table shows the additional parameters of the heat balance attached above. The values shown in this table are predicted values, not guaranteed values.
(*2) Refer to "Attachment 1" in this chapter (TS-10) for the numbers shown in this column.
(*3) ST performance values indicated in the above table are estimated based on existing heat balance diagram.
Attachment -1
*7 *1
Return Water
HP/IP BFP
*9
6
23 25
*2 *8
Deaerator
LP Process *6
10 11
18
27 *8 *6
19
24
22 9
TCA Cooler DA EVA Pump
*4 *5
To GT *3
*1 *9
HP IP
13 12 14
*4
Steam Turbine
7
GEN GEN
LP IP HP Comp. Turbine
21
Condenser Make-Up
Sea Water
2
16
Inlet Air 3 Heat Recovery Steam Generator
17
15 *2
20
FGH Gas Compressor
HP Process Fuel
26 1
*7
*5 LHV : - kJ/kg Exhaust Gas Composition
Condensate O2(wt.%) -
*3
Pump CO2(wt.%) - Singapore / Sakra Repowering
H2O(wt.%) - Multi-Shaft 1on1 GTCC
To GT N2(wt.%) - Gross Plant Power Output - kW
Ar(wt.%) - Gross GT Power Output - kW
Gland Gross ST Power Output - kW
Steam Gross Heat Rate - kJ/kWh-LHV
Operating Conditions
Load -
Ambient Temp. - deg.C
Gland Steam Cooling Air Relative Humidity - %
Condenser Cooler Barometric Press. - mbar
Steam Steam Extraction -
Water Fuel -
Air ORDER No. DWG No Rev.
-
Fuel -
This document contains information proprietary to Mitsubishi Hitachi Power Systems Ltd. It is submitted in confidence and is to be used solely for the purpose for which it is furnished and returned upon
request. This document and such information is not to be reproduced, transmitted, disclosed or used otherwise in whole or in part without the written authorization of Mitsubishi Hitachi Power Systems ,Ltd.