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Investigation of Alternative Strategies for Integrating Post-combustion CO2 Capture to a Natural Gas Combined Cycle Power Plant
被引:9
|作者:
Biliyok, Chechet
[1
]
Canepa, Roberto
[2
]
Hanak, Dawid P.
[1
]
机构:
[1] Cranfield Univ, Combust & CCS Ctr, Bedford MK43 0JN, England
[2] Ansaldo Energia, I-16152 Genoa, Italy
关键词:
TECHNOECONOMIC ANALYSIS;
BENCHMARKING;
OPTIMIZATION;
ABSORPTION;
NGCC;
COAL;
D O I:
10.1021/acs.energyfuels.5b00811
中图分类号:
TE [石油、天然气工业];
TK [能源与动力工程];
学科分类号:
0807 ;
0820 ;
摘要:
With increasing urgency for global action toward climate change mitigation, this study is undertaken to evaluate integration options for post-combustion CO2 capture (PCC) on gas-fired power plants. High-fidelity models of a natural gas combined cycle power plant, a PCC plant, and a CO2 compression train are integrated for a 90% CO2 capture level. Three options to provide steam for solvent regeneration are explored: extracting steam from the intermediate-pressure (IP)/low-pressure (LP) crossover, using a gas-fired package boiler, and extracting steam from the LP drum. The effect of pressure losses because of steam extraction, a factor ignored in previous analyses, is also considered. The integrated plant net efficiency is 47.8, 40.4, and 44.9%, respectively, for the aforementioned scenarios. Next, supplementary firing of gas turbine exhaust is employed to generate an ample amount of steam to preserve plant net output under a sliding pressure scenario and meet solvent regeneration requirements. It is observed that the net plant efficiency converges to a value of 43.5% for the options considered.
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页码:4624 / 4633
页数:10
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