摘要
Hydrogen separation is a significant process in hydrogen production from syngas. Membrane separation is well-known as an energy-saving and environmental-friendly technique to remove CO2 from syngas. ZSM-58 zeolite membrane, owning good affinity to CO2 molecules and narrowed aperture size (0.36 nm × 0.44 nm), has been attractive in CO2 gas separations. In this work, all-silica ZSM-58 zeolite membranes were synthesized on ceramic hollow fibers to lower the membrane cost and firstly employed in CO2/H2 gas separation. A high-quality ZSM-58 zeolite membrane was hydrothermally synthesized for 48 h by using ball-milled zeolite seeds. The membrane exhibited a high CO2/H2 separation selectivity of 81.6 as well as a CO2 gas permeance of 1.08 × 10−7 mol m−2 s−1 Pa−1 at 233 K. Effects of temperature, feed pressure and feed CO2 concentration on separation performance of the membrane were investigated extensively. High separation selectivity was favored at low temperature, low feed pressure and high feed CO2 concentration. The maximum CO2 permeance was obtained at 253 K. The membrane also maintained very good stability in the separation at low temperature, indicating the availability of ZSM-58 zeolite membrane in CO2 removal from syngas.
源语言 | 英语 |
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页(从-至) | 524-533 |
页数 | 10 |
期刊 | International Journal of Hydrogen Energy |
卷 | 78 |
DOI | |
出版状态 | 已出版 - 12 8月 2024 |