Improved Synthesis of Hollow Fiber SSZ-13 Zeolite Membranes for High-Pressure CO2/CH4 Separation

Journal Article (2024)
Author(s)

Xingyu Peng (Nanjing Tech University)

Lingjie Chen (Nanjing Tech University, Quzhou Membrane Material Innovation Institute)

Lekai You (Nanjing Tech University)

Yang Jin (Nanjing Tech University)

Chun Zhang (Nanjing Tech University)

Shengyuan Ren (Nanjing Tech University)

Freek Kapteijn (TU Delft - ChemE/Catalysis Engineering)

Xuerui Wang (Nanjing Tech University, Quzhou Membrane Material Innovation Institute)

Xuehong Gu (Nanjing Tech University, Quzhou Membrane Material Innovation Institute)

Research Group
ChemE/Catalysis Engineering
DOI related publication
https://doi.org/10.1002/anie.202405969 Final published version
More Info
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Publication Year
2024
Language
English
Research Group
ChemE/Catalysis Engineering
Bibliographical Note
Green Open Access added to TU Delft Institutional Repository 'You share, we take care!' - Taverne project https://www.openaccess.nl/en/you-share-we-take-care Otherwise as indicated in the copyright section: the publisher is the copyright holder of this work and the author uses the Dutch legislation to make this work public.
Journal title
Angewandte Chemie - International Edition
Issue number
31
Volume number
63
Article number
e202405969
Downloads counter
365
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Abstract

High-silica CHA zeolite membranes are highly desired for natural gas upgrading because of their separation performance in combination with superior mechanical and chemical stability. However, the narrow synthesis condition range significantly constrains scale-up preparation. Herein, we propose a facile interzeolite conversion approach using the FAU zeolite to prepare SSZ-13 zeolite seeds, featuring a shorter induction and a longer crystallization period of the membrane synthesis on hollow fiber substrates. The membrane thickness was constant at ~3 μm over a wide span of synthesis time (24-96 h), while the selectivity (separation efficiency) was easily improved by extending the synthesis time without compromising permeance (throughput). At 0.2 MPa feed pressure and 303 K, the membranes showed an average CO2 permeance of (5.2±0.5)×10−7 mol m−2 s−1 Pa−1 (1530 GPU), with an average CO2/CH4 mixture selectivity of 143±7. Minimal defects ensure a high selectivity of 126 with a CO2 permeation flux of 0.4 mol m−2 s−1 at 6.1 MPa feed pressure, far surpassing requirements for industrial applications. The feasibility for successful scale-up of our approach was further demonstrated by the batch synthesis of 40 cm-long hollow fiber SSZ-13 zeolite membranes exhibiting CO2/CH4 mixture selectivity up to 400 (0.2 MPa feed pressure and 303 K) without using sweep gas.

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