Carbon Capture from Natural Gas Combined Cycle Power Plants: Solvent Performance Comparison at an Industrial Scale

被引:11
|
作者
Sharifzadeh, Mahdi [1 ]
Shah, Nilay [1 ]
机构
[1] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn, CPSE, London SW7 2AZ, England
关键词
CO2; carbon capture; natural gas combined cycle (NGCC) power plant; energy efficiency; integrated process design and control; GCCmax; POSTCOMBUSTION CO2 CAPTURE; STRIPPER CONFIGURATIONS; INTEGRATED DESIGN; OPTIMIZATION; DIOXIDE;
D O I
10.1002/aic.15072
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Natural gas is an important source of energy. This article addresses the problem of integrating an existing natural gas combined cycle (NGCC) power plant with a carbon capture process using various solvents. The power plant and capture process have mutual interactions in terms of the flue gas flow rate and composition vs. the extracted steam required for solvent regeneration. Therefore, evaluating solvent performance at a single (nominal) operating point is not indicative and solvent performance should be considered subject to the overall process operability and over a wide range of operating conditions. In the present research, a novel optimization framework was developed in which design and operation of the capture process are optimized simultaneously and their interactions with the upstream power plant are fully captured. The developed framework was applied for solvent comparison which demonstrated that GCCmax, a newly developed solvent, features superior performances compared to the monoethanolamine baseline solvent. (C) 2015 American Institute of Chemical Engineers
引用
收藏
页码:166 / 179
页数:14
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