Development of pilot WGS/multi-layer membrane for CO2 capture

被引:19
|
作者
Lee, See Hoon [2 ]
Kim, Jung Nam [1 ]
Eom, Won Hyun [1 ]
Ryi, Shin-Kun [3 ]
Park, Jong-Soo [3 ]
Baek, Ii Hyun [1 ]
机构
[1] Korea Inst Energy Res, High Efficiency & Clean Energy Res Div, Taejon 305343, South Korea
[2] Chonbuk Natl Univ, Dept Resources & Energy Engn, Taejon 305343, South Korea
[3] Korea Inst Energy Res, Energy Mat & Convergence Res Dept, Taejon 305343, South Korea
关键词
Water gas shift (WGS); Membrane; CO2; capture; Gasification; GAS; SIMULATION; HYDROGEN;
D O I
10.1016/j.cej.2012.07.013
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
For pre-combustion CO2 capture processes, a 1 Nm(3)/h water gas shift (WGS)/multi-layer membrane system has been developed. Simulated syngas (H-2: 25-35, CO: 60-65, CO2: 5-15 vol.%) was used in these experiments. The 1 Nm(3)/h WGS/multi-layer membrane system consisted of mass flow controllers, water gas shift reactors, gas/steam separators, five layer Pd-Cu membrane module, back pressure regulator, gas chromatograph (GC) analyzers and nondispersive infrared (ND-IR) gas analyzers. The operation conditions of WGS/multi-layer membrane system were 200-400 degrees C, 10-20 bar and steam/carbon ratios in WGS were between 2.0 and 5.0. In the experiments of WGS/multi-layer membrane system, the average gas concentration before membrane module was H-2: 57-58, CO2: 42-43, CO: 0.2-0.3 vol.%. The CO2 concentration of retentate flow reached up to 80 vol.% and the H-2 concentration of permeate flow was over 99 vol.%. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:521 / 525
页数:5
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