CO2/CH4 separation by high performance co-casted ZIF-8/Pebax 1657/PES mixed matrix membrane

被引:112
作者
Jomekian, Abolfazi [1 ,2 ]
Behbahani, Reza Mosayebi [1 ]
Mohammadi, Toraj [2 ]
Kargari, Ali [3 ]
机构
[1] Petr Univ Technol, Ahvaz Fac Petr Engn, Gas Engn Dept, POB 63431, Ahvaz, Iran
[2] Iran Univ Sci & Technol, Fac Chem Engn, Tehran, Iran
[3] Amirkabir Univ Technol, Dept Petrochem Engn, Mahshahr, Iran
关键词
CO2/CH4; separation; ZIF-8; Pebax; 1657; Mixed matrix membrane; Co-casting method; GAS SEPARATION; FRAMEWORK MEMBRANES; BLEND MEMBRANES; PARTICLE-SIZE; DUAL-LAYER; ZIF-8; PERMEABILITY; TEMPERATURE; CAPTURE;
D O I
10.1016/j.jngse.2016.03.067
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
ZIF-8 particles were synthesized at different temperatures. The resulted ZIF-8 particles were characterized by particle size analyzer, SEM, XRD, N-2 adsorption and BET tests. ZIF-8/Pebax 1657 mixed matrix membranes (MMMs) were prepared by co-casting. A thin (1.6-7.1 mu m thickness) and defect free selective top layer of ZIF-8/Pebax 1657 was formed on top of polyethersulfone (PES) sub layer. The resulted MMMs with thin selective layer showed significant improvement in CO2 permeability and CO2/CH4 selectivity in both pure and mixed gas permeation tests compared with pure Pebax 1657 membrane. Remarkable permeability of 758 Barrer with CO2/CH4 selectivity of 16.1 was observed for the MMM synthesized by smallest ZIF-8 particles (fabricated in 60 degrees C) with about 2 mu m thickness of selective layer. The synthesized MMMs in this study showed competitive CO2/CH4 separation performance compared with reported state of the art Pebax based membranes in pure gas permeation tests. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:562 / 574
页数:13
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