1. Separation of light gas mixtures using zeolite SSZ-13 membranes.
- Author
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Wang, Bin, Zheng, Yihong, Zhang, Jinfeng, Zhang, Wenjuan, Zhang, Feng, Xing, Weihong, and Zhou, Rongfei
- Subjects
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ZEOLITE analysis , *MULLITE synthesis , *DYNAMICS , *CALCINATION (Heat treatment) , *POLYMERS - Abstract
Abstract High-quality SSZ-13 membranes with enhanced permeances were synthesized on the symmetric mullite supports by modifying the synthesis recipes, and shown to be useful for light gas separations. The best SSZ-13 membrane displayed doubled CO 2 permeance and comparative CO 2 /CH 4 selectivities compared to our previous mullite supported SSZ-13 membranes. Single-gas permeance of CO 2 , H 2 , N 2 , CH 4 , C 2 H 6 and C 3 H 8 decreased at 298 K with increasing kinetic diameter, except for CO 2. The CO 2 /CH 4 , CO 2 /N 2 , H 2 /CH 4 and N 2 /CH 4 ideal selectivities were 360, 20, 62 and 16, respectively, at room temperature. The mixture selectivities for the same equimolar gas pairs at 298 K were 406, 32, 43 and 16, and the faster-gas permeances of 4.4, 3.2, 1.8 and 0.22 mol/(m2 s Pa), respectively. Calcination times, long-time operation and long-term storage had few effects on membrane performance. Graphical abstract Image 1 Highlights • High-quality SSZ-13 membranes were synthesized on symmetric supports. • The SSZ-13 membrane exceeded the upper bounds of polymer membranes for CO 2 and H 2 separations. • The SSZ-13 membrane showed the highest N 2 /CH 4 separation selectivity. • SSZ-13 membranes displayed excellent stabilities in multi-calcinations, long-time operation and long-term storage. [ABSTRACT FROM AUTHOR]
- Published
- 2019
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