Comparative behaviour of hydrophilic membranes in the pervaporative dehydration of cyclohexane

被引:9
作者
Gomez, P.
Daviou, M. C.
Ibánez, R.
Eliceche, A. M.
Ortiz, I.
机构
[1] Univ Cantabria, ETSIIT, Dept Ingn Quim, E-39005 Santander, Spain
[2] Univ Nacl Sur, PLAPIQUI, Dept Ingn Quim, RA-8000 Bahia Blanca, Argentina
关键词
pervaporation; dehydration; cyclohexane; commercial membranes; SPEEK; SPEEK/PES; CATION-EXCHANGE MEMBRANES; POLY(ETHER ETHER KETONE); CONCENTRATION-POLARIZATION; POLYMER BLENDS; FUEL-CELLS; RESISTANCE; SCALE; TRANSPORT;
D O I
10.1016/j.memsci.2005.12.061
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work focuses on the performance analysis of several commercial membranes, provided by Celfa (VP-31, VP-43 and CF-23) and Sulzer (Pervap2201 and Pervap2201D) companies, as well as some tailor made sulfonated poly(ether ether ketone) (SPEEK) membranes. in the pervaporative dehydration of cyclohexane which is commonly employed as solvent in the synthetic rubber manufacture. Water permeate fluxes in the range of 13-250 mg/m(2) min and satisfactory selectivity values were observed at very low water contents in the feed (below 90 mg/kg). A mathematical model based on the solution-diffusion theory is also presented, taking into account the mass transfer resistance offered by the fluid layer and the membrane itself, supported with experimental data obtained in a bench-scale radial flow pervaporation cell. Permeability values of the studied membranes resulted in the range of 3.2 x 10(-11) to 2.3 x 10(-9) m(2)/s. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:635 / 644
页数:10
相关论文
共 24 条
[1]   Preparation and characterisation of monovalent ion selective cation exchange membranes based on sulphonated poly(ether ether ketone) [J].
Balster, J ;
Krupenko, O ;
Pünt, I ;
Stamatialis, DF ;
Wessling, M .
JOURNAL OF MEMBRANE SCIENCE, 2005, 263 (1-2) :137-145
[2]  
Bruschke H.E.A., 2001, Membrane Technology in the Chemical Industry
[3]   Pervaporative recovery of acetic acid from an acetylation industrial effluent using commercial membranes [J].
Gorri, D ;
Urtiaga, A ;
Ortiz, I .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (04) :977-985
[4]  
Huang R.Y.M., 1991, PERVAPORATION MEMBRA, p.111
[5]   Pervaporation separation of water/isopropanol mixture using sulfonated poly(ether ether ketone) (SPEEK) membranes: transport mechanism and separation performance [J].
Huang, RYM ;
Shao, P ;
Feng, X ;
Burns, CM .
JOURNAL OF MEMBRANE SCIENCE, 2001, 192 (1-2) :115-127
[6]   Sulfonation of poly(ether ether ketone)(PEEK): Kinetic study and characterization [J].
Huang, RYM ;
Shao, PH ;
Burns, CM ;
Feng, X .
JOURNAL OF APPLIED POLYMER SCIENCE, 2001, 82 (11) :2651-2660
[7]   Role of membrane surface in concentration polarization at cation exchange membranes [J].
Ibanez, R ;
Stamatialis, DF ;
Wessling, M .
JOURNAL OF MEMBRANE SCIENCE, 2004, 239 (01) :119-128
[8]   Pervaporation dehydration of ethanol-water mixtures with chitosan/hydroxyethylcellulose (CS/HEC) composite membranes II. Analysis of mass transport [J].
Jiraratananon, R ;
Chanachai, A ;
Huang, RYM .
JOURNAL OF MEMBRANE SCIENCE, 2002, 199 (1-2) :211-222
[9]   Industrial state-of-the-art of pervaporation and vapour permeation in the western countries [J].
Jonquières, A ;
Clément, R ;
Lochon, P ;
Néel, J ;
Dresch, M ;
Chrétien, B .
JOURNAL OF MEMBRANE SCIENCE, 2002, 206 (1-2) :87-117
[10]  
KIRKOTHMER, 1984, ENCY CHEM TECHNOLOGY