Preparation of supported carbon molecular sieve membrane from novolac phenol-formaldehyde resin

被引:73
作者
Wei, Wei
Qin, Guotong
Hu, Haoquan
You, Longbo
Chen, Guohua
机构
[1] Beijing Union Univ, Coll Arts & Sci, Dept Environm Sci, Beijing 100083, Peoples R China
[2] Beihang Univ, Dept Environm Engn, Beijing 100083, Peoples R China
[3] Dalian Univ Technol, Inst Coal Chem Engn, State Key Lab Fine Chem, Dalian 116012, Peoples R China
[4] Hong Kong Univ Sci & Technol, Dept Chem Engn, Kowloon, Hong Kong, Peoples R China
基金
中国国家自然科学基金;
关键词
phenol-formaldehyde resin; carbon membrane; gas separation; molecular sieve;
D O I
10.1016/j.memsci.2007.06.055
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An asymmetric carbon membrane was prepared by coating alcohol solution of novolac phenol-formaldehyde resin containing a little hexamine on a porous resin support from the same material. After drying in air for two days at room temperature, the coated support was heated at 150 degrees C for I h in air (heating rate: 0.5 degrees C/min) and then carbonized at 800 degrees C (heating rate: 0.5 degrees C/min) in Ar atmosphere. The support and the membrane layer were carbonized simultaneously. The coating-pyrolysis cycle only needed one time. SEM photographs showed the carbon membrane had an asymmetric structure formed by a dense skin layer with a thickness of around 35 mu m and a porous substrate. Pure gases of different molecular size (H-2, CO2, O-2, N-2 and CH4) were used to test the carbon membrane permeance property. The membrane has a good selectivity for H-2/N-2 and H-2/CH4 with H-2 permeance of 4.05 x 10(-6) cm(3) cm(-2) s(-1) cmHg(-1). The permeance is independent of pressure. The results indicate that the gases transport through the membrane according to molecular sieve mechanism. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:80 / 85
页数:6
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