A Mathematical Model for the Evaluation ofSeparation Performances of Hollow FiberMembrane N_2-H_2 Permeators

Zhu Baolin and Jiang Kuoliang(Dalian Institute of Chemical Physics; Academia Sinica)

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A Mathematical Model for the Evaluation ofSeparation Performances of Hollow FiberMembrane N_2-H_2 Permeators

更新时间：2025-12-16

- A Mathematical Model for the Evaluation ofSeparation Performances of Hollow FiberMembrane N_2-H_2 Permeators
- CIESC Journal Issue 3, (1987)
- 作者机构：
  
  中国科学院大连化学物理研究所,中国科学院大连化学物理研究所
- 作者简介：
- 基金信息：
- DOI：
  CLC：
- Online First：25 September 1987，
  
  Published：25 September 1987
- 稿件说明：
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Zhu Baolin and Jiang Kuoliang(Dalian Institute of Chemical Physics, Academia Sinica). A Mathematical Model for the Evaluation ofSeparation Performances of Hollow FiberMembrane N_2-H_2 Permeators[J]. CIESC Journal, 1987, (3).
DOI：

Zhu Baolin and Jiang Kuoliang(Dalian Institute of Chemical Physics, Academia Sinica). A Mathematical Model for the Evaluation ofSeparation Performances of Hollow FiberMembrane N_2-H_2 Permeators[J]. CIESC Journal, 1987, (3). DOI：

摘要

本文提出了计算中空纤维膜N_2-H_2分离器及器组分离性能的数学模型;在计算机上考察了各操作参数和膜性能参数对渗透气中H_2浓度及H_2的回收率的影响;井以三根φ100 ×3000mm分离器现场试验结果进行了验证.

Abstract

A mathematical model for evaluating the separation performances of hollow fiber membrane N2-H2 permeators has been established. The effects of operating parameters and membrane characteristics on the concentration of hydrogen in the permannte gas and the percentage recovery of hydrogen have been studied with the help of a digital computer using this mathematical model. Results computed are compared with data obtained from field tests of three φ100 × 3000mm full-scale permeators

confirming the adaptability of the mathematical model.

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