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Abstract <p>This work presents a comprehensive study on hydrogen recovery from a CO<sub>2</sub>-containing mixture (75/25 mol %) using commercial polymer membranes. The gas transport properties of polyimide (PI), polysulfone (PSF), polyphenylene oxide (PPO), polyetherimide (PEI), and a PEI + PI composite were evaluated. A significant discrepancy was found between single-gas and mixture permeation data, highlighting the necessity of using mixture-based permeance for accurate process design. The PEI membrane demonstrated the optimal combination of H<sub>2</sub>/CO<sub>2</sub> selectivity (5.07) and permeance. An optimized two-stage membrane process with recirculation was developed using Aspen Plus simulation, achieving a hydrogen purity of 95 mol % with 90% recovery. The techno-economic assessment confirmed the process feasibility, demonstrating a lower cost of hydrogen production compared to traditional methods.</p>

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Beyond Pure-Gas Permeation: Designing an Efficient Two-Stage Membrane Process for Hydrogen Recovery from Reformate Mixtures

  • 期刊论文

  • 发表日期：

    2025年12月1日

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  • S. S. Kryuchkov,
  • K. A. Smorodin,
  • A. A. Atlaskin,
  • A. A. Sysoev,
  • M. E. Atlaskina,
  • I. V. Vorotyntsev

摘要

Abstract

This work presents a comprehensive study on hydrogen recovery from a CO2-containing mixture (75/25 mol %) using commercial polymer membranes. The gas transport properties of polyimide (PI), polysulfone (PSF), polyphenylene oxide (PPO), polyetherimide (PEI), and a PEI + PI composite were evaluated. A significant discrepancy was found between single-gas and mixture permeation data, highlighting the necessity of using mixture-based permeance for accurate process design. The PEI membrane demonstrated the optimal combination of H2/CO2 selectivity (5.07) and permeance. An optimized two-stage membrane process with recirculation was developed using Aspen Plus simulation, achieving a hydrogen purity of 95 mol % with 90% recovery. The techno-economic assessment confirmed the process feasibility, demonstrating a lower cost of hydrogen production compared to traditional methods.