Pervaporation Separation of Butanol-Water Mixtures Using Polydimethylsiloxane/Ceramic Composite Membrane
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Pervaporation Separation of Butanol-Water Mixtures Using Polydimethylsiloxane/Ceramic Composite Membrane
Pervaporation Separation of Butanol-Water Mixtures Using Polydimethylsiloxane/Ceramic Composite Membrane
中国化学工程学报(英文版)2011年19卷第1期 页码:40-44
Affiliations:
State Key Laboratory of Materials-Oriented Chemical Engineering, College of Chemistry and Chemical Engineering, Nanjing University of Technology,Nanjing,China,210009
Author bio:
Funds:
Supported by the National Basic Research Program of China(2009CB623406);the National Natural Science Foundation of China(20990222);the Natural Science Foundation of Jiangsu Province(SBK200930313);the“Six Kinds of Important Talents”Program of Jiangsu Province(2007007)
刘公平, 侯丹, 卫旺, 等. Pervaporation Separation of Butanol-Water Mixtures Using Polydimethylsiloxane/Ceramic Composite Membrane[J]. 中国化学工程学报(英文版), 2011,19(1):40-44.
LIU Gongping, HOU Dan, WEI Wang, XIANGLI Fenjuan, JIN Wanqin. Pervaporation Separation of Butanol-Water Mixtures Using Polydimethylsiloxane/Ceramic Composite Membrane[J]. , 2011, 19(1): 40-44.
刘公平, 侯丹, 卫旺, 等. Pervaporation Separation of Butanol-Water Mixtures Using Polydimethylsiloxane/Ceramic Composite Membrane[J]. 中国化学工程学报(英文版), 2011,19(1):40-44.DOI: 10.1016/S1004-9541(09)60174-9.
LIU Gongping, HOU Dan, WEI Wang, XIANGLI Fenjuan, JIN Wanqin. Pervaporation Separation of Butanol-Water Mixtures Using Polydimethylsiloxane/Ceramic Composite Membrane[J]. , 2011, 19(1): 40-44.DOI: 10.1016/S1004-9541(09)60174-9.
Pervaporation Separation of Butanol-Water Mixtures Using Polydimethylsiloxane/Ceramic Composite Membrane
Pervaporation has attracted considerable interest owing to its potential application in recovering biobutanol from biomass acetone-butanol-ethanol(ABE)fermentation broth.In this study
butanol was recovered from its aqueous solution using a polydimethylsiloxane(PDMS)/ceramic composite pervaporation membrane.The effects of operating temperature
feed concentration
feed flow rate and operating time on the membrane pervaporation performance were investigated.It was found that with the increase of temperature or butanol concentration in the feed
the total flux through the membrane increased while the separation factor decreased slightly.As the feed flow rate increased
the total flux increased gradually while the separation factor changed little.At 40℃ and 1%(by mass) butanol in the feed
the total flux and separation factor of the membrane reached 457.4 g·m
2
·h
-1
and 26.1
respectively.The membrane with high flux is suitable for recovering butanol from ABE fermentation broth.
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references
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Fabrication of graphene oxide composite membranes and their application for pervaporation dehydration of butanol
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Advances in inorganic membranes for xylene isomers separation: Fabrication strategies and mechanistic insights
Study on the recovery of NMP waste liquid in lithium battery production by coupled pervaporation–adsorption process and evaluation of technical and economic performances
相关作者
Xianfu Chen
Gongping Liu
Hanyu Zhang
Yiqun Fan
吴洪
芦霞
李宪实
李奕帆
相关机构
Laboratory of Materials-Oriented Chemical Engineering, College of Chemistry and Chemical Engineering, Nanjing Tech University
3 Tianjin Key Laboratory of Membrane Science & Desalination Technology
2 Synergetic Innovation Center of Chemical Science and Engineering (Tianjin)
State Key Laboratory of Chemical Engineering, Department of Chemical Engineering, Tsinghua University
Center of Excellence for Renewable Energy and Storage Technologies, Division of Physical Science and Engineering, King Abdullah University of Science and Technology, Thuwal 23955-6900, Saudi Arabia