Modelling and simulation of two-bed PSA process for separating H<sub>2</sub> from methane steam reforming

Huiru Li; Zuwei Liao; Jingyuan Sun; Binbo Jiang; Jingdai Wang; Yongrong Yang

doi:10.1016/j.cjche.2018.11.022

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Modelling and simulation of two-bed PSA process for separating H₂ from methane steam reforming

Process Systems Engineering and Process Safety | Updated：2026-01-06

- Modelling and simulation of two-bed PSA process for separating H₂ from methane steam reforming
- Modelling and simulation of two-bed PSA process for separating H₂ from methane steam reforming
- 中国化学工程学报（英文版） 2019年27卷第8期页码：1870-1878
- Affiliations：
  
  1. Zhejiang Provincial Key Laboratory of Advanced Chemical Engineering Manufacture Technology, College of Chemical and Biological Engineering, Zhejiang University,Hangzhou,China,310027
  2. State Key Laboratory of Chemical Engineering, College of Chemical and Biological Engineering, Zhejiang University,Hangzhou,China,310027
- Author bio：
- Funds：
- DOI：10.1016/j.cjche.2018.11.022
  中图分类号：
- 纸质出版：2019
- Accepted：
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Huiru Li, Zuwei Liao, Jingyuan Sun, 等. Modelling and simulation of two-bed PSA process for separating H₂ from methane steam reforming[J]. 中国化学工程学报（英文版）, 2019,27(8):1870-1878. DOI: 10.1016/j.cjche.2018.11.022.

from methane steam reforming[J]. 中国化学工程学报, 2019, 27(8): 1870-1878.
Huiru Li, Zuwei Liao, Jingyuan Sun, 等. Modelling and simulation of two-bed PSA process for separating H₂ from methane steam reforming[J]. 中国化学工程学报（英文版）, 2019,27(8):1870-1878. DOI: 10.1016/j.cjche.2018.11.022. DOI：

from methane steam reforming[J]. 中国化学工程学报, 2019, 27(8): 1870-1878. DOI： 10.1016/j.cjche.2018.11.022.

摘要

Abstract

Methane steam reforming is the main hydrogen production method in the industry. The product of methane steam reforming contains H

CO and CO

and is then purified by pressure swing adsorption (PSA) technology. In this study

a layered two-bed PSA process was designed theoretically to purify H

from methane steam reforming off gas. The effects of adsorption pressure

adsorption time and purgeto-feed ratio (P/F ratio) on process performance were investigated to design a PSA process with more than 99.95% purity and 80% recovery. Since the feed composition of the PSA process changes with the upstream process

the effect of the feed composition on the process performance was discussed as well. The result showed that the increase of CH

concentration

which was the weakest adsorbate

would have a negative impact on product purity.

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Modelling and simulation of two-bed PSA process for separating H2 from methane steam reforming

Modelling and simulation of two-bed PSA process for separating H2 from methane steam reforming

DOI：10.1016/j.cjche.2018.11.022

摘要

Abstract

关键词

Keywords

references

Modelling and simulation of two-bed PSA process for separating H₂ from methane steam reforming

Modelling and simulation of two-bed PSA process for separating H₂ from methane steam reforming