Natural gas upgrading through hydrogen selective membranes: Application in Carbon Free Combined Cycles

被引:10
作者
Atsonios, K. A. [1 ,2 ]
Panopoulos, K. D. [1 ]
Doukelis, A. F. [2 ]
Koumanakos, A. K. [2 ]
Morud, J. [3 ]
Kakaras, E. [1 ,2 ]
机构
[1] Ctr Res & Technol Hellas, Chem Proc & Energy Resources Inst CERTH CPERI, 4th Km NR Ptolemais Kozani, Ptolemais 50200, Greece
[2] Natl Tech Univ Athens, Lab Steam Boilers & Thermal Plants, Athens 15780, Greece
[3] SINTEF, Mat & Chem, NO-7465 Trondheim, Norway
来源
GHGT-11 | 2013年 / 37卷
关键词
Combined Cycle; Autothermal Reforming; Water Gas Shift; Pd Membranes; CO2; capture;
D O I
10.1016/j.egypro.2013.05.186
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 work examines the integration of Pd membrane-based CO2 capture technology in a hydrogen-fired Combined Cycle power plant. Four alternative configurations were investigated and sensitivity analyses were performed on the overall plant efficiency by varying parameters such as the steam to carbon ratio at the reformer and the Hydrogen Recovery Factor. The cost implications of the examined cases are presented and a comparison with an MDEA state-of-the-art case is performed. The Pd membrane technology results in a lower energy penalty than MDEA, while the avoidance cost of CO2 is strongly dependent on membrane module cost. (C) 2013 The Authors. Published by Elsevier Ltd. Open access under CC BY-NC-ND license. Selection and/or peer-review under responsibility of GHGT
引用
收藏
页码:914 / 923
页数:10
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