An update of the benchmark post-combustion CO2-capture technology

被引:132
作者
Feron, Paul H. M. [1 ]
Cousins, Ashleigh [2 ]
Jiang, Kaiqi [1 ]
Zhai, Rongrong [3 ]
Garcia, Monica [4 ]
机构
[1] CSIRO Energy, Newcastle, NSW, Australia
[2] CSIRO Energy, Brisbane, Qld, Australia
[3] North China Elect Power Univ, Beijing, Peoples R China
[4] IEAGHG, Pure Off, Hatherley Lane, Cheltenham GL51 6SH, Glos, England
关键词
CO2-capture; PCC; Amine; Process design; Techno-economics; CO2 CAPTURE PROCESS; CARBON CAPTURE; FLUE-GAS; OXIDATIVE-DEGRADATION; MEA; SOLVENTS; PLANT; AMP/PZ; CONFIGURATIONS; PROGRAM;
D O I
10.1016/j.fuel.2020.117776
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
This study provides a description of a new benchmark post-combustion CO2 capture (PCC) technology reflecting the publicly reported performances by various technology suppliers. To achieve this several amines and amine formulations have been considered using a process model developed in ProTreat (R). A 40 wt% formulation of PZ (piperazine)/AMP (amino-methyl-propanol) in a 1:2 M ratio was selected as the most representative of the current state of the art. A PCC process configuration with absorber intercooling and rich split flow was selected to reflect the fact that the technology suppliers use a variety of process designs to optimize the process performance. The techno-economic performances were further detailed for the PCC process integrated with an ultra-supercritical coal fired power station and a natural gas fired combined-cycle. The techno-economic evaluation of the PCC process indicated that the costs of capture with respect to 30 wt% MEA for the coal-fired power station were reduced by 22% and for the natural gas fired combined-cycle by 15%.
引用
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页数:11
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