Preparation of carbon molecular sieve membranes with remarkable CO2/CH4 selectivity for high-pressure natural gas sweetening

被引:52
|
作者
Lei, Linfeng [1 ]
Lindbrathen, Arne [1 ]
Zhang, Xiangping [2 ]
Favvas, Evangelos P. [3 ]
Sandru, Marius [4 ]
Hillestad, Magne [1 ]
He, Xuezhong [1 ,5 ]
机构
[1] Norwegian Univ Sci & Technol, Dept Chem Engn, NO-7491 Trondheim, Norway
[2] Chinese Acad Sci, Beijing Key Lab Ion Liquids Clean Proc, Inst Proc Engn, POB 353, Beijing 100190, Peoples R China
[3] Natl Ctr Sci Res Demokritos, Inst Nanosci & Nanotechnol, Athens 15341, Greece
[4] SINTEF AS, SINTEF Ind, NO-7465 Trondheim, Norway
[5] Guangdong Technion Israel Inst Technol GTIIT, Dept Chem Engn, 241 Daxue Rd, Shantou 515063, Peoples R China
关键词
Carbon hollow fiber membranes; Cellulose; Ionic liquids; Natural gas; CO2; removel; HOLLOW-FIBER MEMBRANES; SITE-CARRIER MEMBRANES; PERMEATION PROPERTIES; CELLULOSE; SEPARATION; PERFORMANCE; CO2; OPTIMIZATION; SOLUBILITY; POLYIMIDE;
D O I
10.1016/j.memsci.2020.118529
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Carbon hollow fiber membranes (CHFMs) were fabricated based on cellulose hollow fiber precursors spun from a cellulose/ionic liquid system. By a thermal treatment on the precursors using a preheating process before carbonization, the micropores of the prepared CHFMs were tightened and thus resulting in highly selective carbon molecular sieve (CMS) membranes. By increasing the drying temperature from RT to 140 degrees C, the cellulose hollow fiber precursors show a substantial shrinkage, which results in a reduction of average pore size of the derived CHFMs from 6 to 4.9 angstrom. Although the narrowed micropore size causes the decrease of gas diffusion coefficient, stronger resistance to the larger gas molecules, such as CH4, eventually results in an ultra-high CO2/CH4 ideal selectivity of 917 tested at 2 bar for CHFM-140C due to the simultaneously enhanced diffusion and sorption selectivity. The CHFM-140C was further tested with a 10 mol%CO2/90 mol%CH4 mixed gas at 60 degrees C and feed pressure ranging from 10 to 50 bar. The obtained remarkable CO2/CH4 separation factor of 131 at 50 bar and good stability make these carbon membranes great potential candidates for CO2 removal from high-pressure natural gas.
引用
收藏
页数:9
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