IGCC process intensification for simultaneous power generation and CO2 capture

被引:29
作者
Ahmed, Usama [1 ]
Zahid, Umer [3 ]
Jeong, Yeong Su [1 ]
Lee, Chul-Jin [2 ]
Han, Chonghun [1 ]
机构
[1] Seoul Natl Univ, Sch Chem & Biol Engn, Seoul 151744, South Korea
[2] Seoul Natl Univ, Engn Dev Res Ctr, Bldg 311,Room 324 1, Seoul 151744, South Korea
[3] King Fahd Univ Petr & Minerals, Dept Chem Engn, Dhahran 31261, Saudi Arabia
关键词
IGCC; Process intensification; CO2; capture; Power generation; GASIFICATION COMBINED-CYCLE; CARBON CAPTURE; TECHNOLOGY; PERFORMANCE; ELECTRICITY; HYDROGEN; STORAGE; PLANTS; COAL;
D O I
10.1016/j.cep.2015.12.012
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
In this study IGCC process which is a commercial example of pre-combustion technique has been developed in order to analyze the overall plant output with CO2 capture while discussing the process economics. Three different schemes with consistent and transparent methodology have been proposed in order to ensure fair evaluation of analysis. First two cases use water gas shift (WGS) reactions scheme with sour shift catalysis process. The resulted syngas rich of CO2 is treated by CO2 capture unit producing a syngas almost free of CO2 which can be either combusted by air or O-2. The first case uses air as an oxidant for burning H-2 and the combustor temperature is controlled by air as well. In the second case, O-2 is used as an oxidizing agent for H-2 combustion and combustion temperature is controlled by recycling the captured CO2. In the third case, WGS reactor and CO2 capture units are removed. The syngas composed of CO and H-2 is sent directly for combustion with high purity O-2 making it similar to an oxy-fuel combustion process and CO2 is recovered while condensing steam from the flue gas. All the results are compared in terms of both power plant efficiencies and economics. (C) 2016 Published by Elsevier B.V.
引用
收藏
页码:72 / 86
页数:15
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