期刊
FUEL
卷 87, 期 1, 页码 14-24出版社
ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2007.03.042
关键词
membrane; power; IGCC; CO2; capture
Published data for an operating power plant, the ELCOGAS 315 N[We Puertollano plant, has been used as a basis for the simulation of an integrated gasification combined cycle process with CO2, capture. This incorporated a fixed site carrier polyvinylamine membrane to separate the CO2 from a CO-shifted syngas stream. It appears that the modified process, using a sour shift catalyst prior to sulphur removal, could achieve greater than 85% CO2 recovery at 95 vol% purity. The efficiency penalty for such a process would be approximately 10% points, including CO2 compression. A modified plant with CO2 capture and compression was calculated to cost (sic)2320/kW, producing electricity at a cost of 7.6 (sic) cents/kWh and a CO2 avoidance cost of about (sic)40/tonne CO2. (c) 2007 Elsevier Ltd. All rights reserved.
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