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Pressure swing adsorption/membrane hybrid processes for hydrogen purification with a high recovery

发表时间:2019-03-13
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论文类型:
期刊论文
第一作者:
Li, Baojun
通讯作者:
He, GH (reprint author), Dalian Univ Technol, Sch Chem Engn, R&D Ctr Membrane Sci & Technol, State Key Lab Fine Chem, Dalian 116012, Peoples R China.
合写作者:
He, Gaohong,Jiang, Xiaobin,Dai, Yan,Ruan, Xuehua
发表时间:
2016-06-01
发表刊物:
FRONTIERS OF CHEMICAL SCIENCE AND ENGINEERING
收录刊物:
SCIE、EI、ISTIC、CSCD
文献类型:
J
卷号:
10
期号:
2
页面范围:
255-264
ISSN号:
2095-0179
关键字:
hydrogen purification; PSA; membrane separation; hybrid process
摘要:
Hydrogen was recovered and purified from coal gasification-produced syngas using two kinds of hybrid processes: a pressure swing adsorption (PSA)-membrane system (a PSA unit followed by a membrane separation unit) and a membrane-PSA system (a membrane separation unit followed by a PSA unit). The PSA operational parameters were adjusted to control the product purity and the membrane operational parameters were adjusted to control the hydrogen recovery so that both a pure hydrogen product (>99.9%) and a high recovery (>90%) were obtained simultaneously. The hybrid hydrogen purification processes were simulated using HYSYS and the processes were evaluated in terms of hydrogen product purity and hydrogen recovery. For comparison, a PSA process and a membrane separation process were also used individually for hydrogen purification. Neither process alone produced high purity hydrogen with a high recovery. The PSA-membrane hybrid process produced hydrogen that was 99.98% pure with a recovery of 91.71%, whereas the membrane-PSA hybrid process produced hydrogen that was 99.99% pure with a recovery of 91.71%. The PSA-membrane hybrid process achieved higher total H-2 recoveries than the membrane-PSA hybrid process under the same H-2 recovery of membrane separation unit. Meanwhile, the membrane-PSA hybrid process achieved a higher total H-2 recovery (97.06%) than PSA-membrane hybrid process (94.35%) at the same H-2 concentration of PSA feed gas (62.57%).
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