Mixed polymer fragment membranes on large‐area tubes for high‐performance <scp> H <sub>2</sub> </scp> purification

Abstract High‐performance H 2 /CO 2 separation with good scalability is needed in industry. Here, we fabricated mixed polymer fragment membranes on alumina tubes. The synergistic control of monomer diffusion rate promoted the formation of H 2 selective channels, thereby elevating the H 2 /CO 2 separation performance. The membranes, each with an area of 37.7 cm 2 , demonstrated a high H 2 /CO 2 selectivity of 22.5 (with a corresponding H 2 permeance of 209 GPU) at 150°C and 2 bar, high pressure resistance (H 2 permeance and H 2 /CO 2 selectivity were 212 GPU and 11.1 at 200°C and 10 bar, respectively), and good reproducibility. Furthermore, we studied the effects of sweep gas, permeate pressure, reuse of substrates, and H 2 O and H 2 S contaminants on membrane performance, pointing out that the membranes can be well adapted to industrial relevant conditions. In addition, a two‐stage membrane system was designed to produce high concentration H 2 with a good yield.

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Publication Details

Journal
AIChE Journal
Published
2026-01-07
DOI
https://doi.org/10.1002/aic.70220
Primary Topic
Membrane Separation and Gas Transport
Type
article
Field-Weighted Citation Impact
0.00

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Mixed polymer fragment membranes on large‐area tubes for high‐performance H 2 purification

Puxin Shi, Islam Mohammad Mahfuzul, X. P. Liu, Bo Zhang et al.
AIChE Journal
Membrane Separation and Gas Transport
article

Mixed polymer fragment membranes on large‐area tubes for high‐performance H 2 purification

Puxin Shi, Islam Mohammad Mahfuzul, X. P. Liu, Bo Zhang, Zhi Wang, Liping Luan
article en

Abstract

Abstract High‐performance H 2 /CO 2 separation with good scalability is needed in industry. Here, we fabricated mixed polymer fragment membranes on alumina tubes. The synergistic control of monomer diffusion rate promoted the formation of H 2 selective channels, thereby elevating the H 2 /CO 2 separation performance. The membranes, each with an area of 37.7 cm 2 , demonstrated a high H 2 /CO 2 selectivity of 22.5 (with a corresponding H 2 permeance of 209 GPU) at 150°C and 2 bar, high pressure resistance (H 2 permeance and H 2 /CO 2 selectivity were 212 GPU and 11.1 at 200°C and 10 bar, respectively), and good reproducibility. Furthermore, we studied the effects of sweep gas, permeate pressure, reuse of substrates, and H 2 O and H 2 S contaminants on membrane performance, pointing out that the membranes can be well adapted to industrial relevant conditions. In addition, a two‐stage membrane system was designed to produce high concentration H 2 with a good yield.

AIChE JournalVol. 72(4)
Tianjin University (CN), State Key Laboratory of Chemical Engineering (CN)
Ministry of Science and Technology of the People's Republic of China, Ningbo Municipal Bureau of Science and Technology
Industry, innovation and infrastructure
Openalex Percentile: Top 94%
Membrane Separation and Gas Transport
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