Novel PTMSP-based membranes containing elastomeric fillers: Enhanced 1-butanol/water pervaporation selectivity and permeability

被引:62
作者
Borisov, Ilya L. [1 ]
Malakhov, Alexander O. [1 ]
Khotimsky, Valery S. [1 ]
Litvinova, Elena G. [1 ]
Finkelshtein, Eugene Sh. [1 ]
Ushakov, Nikolay V. [1 ]
Volkov, Vladimir V. [1 ]
机构
[1] Russian Acad Sci, AV Topchiev Petrochem Synth Inst, Moscow, Russia
基金
俄罗斯基础研究基金会;
关键词
Pervaporation; PTMSP; Elastomeric filler; Butanol; Membrane selectivity; MIXED MATRIX MEMBRANES; GAS-SEPARATION; FREE-VOLUME; COMPOSITE MEMBRANES; AQUEOUS-SOLUTIONS; BUTANOL; ETHANOL; MIXTURES; POLY(1-TRIMETHYLSILYL-1-PROPYNE); POLYMERS;
D O I
10.1016/j.memsci.2014.04.037
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
To improve organic solvent preferential permeation of poly[1-(trimethylsilyl)-1-propyne] (PTMSP) and to provide efficient separation of dilute 1-butanol/water mixtures, the membranes were modified by the addition of minor amounts of a soft elastomeric filler, poly(dimethylsilmethylene) (PDMSM), to the host polymeric matrix. As compared with virgin PTMSP membranes, the modified membranes demonstrate better 1-butanol/water pervaporation selectivity and permeability. This unique coupled phenomenon is observed at low concentrations of the elastomeric filler (similar to 1-3 wt%) in the host matrix and for the feed aqueous mixtures containing 0.6-3.6 wt% of butanol. For vacuum pervaporation of butanol solutions, introduction of only 1.2 wt% of PDMSM into the PTMSP matrix makes it possible to increase the permeate flux up to 75% and the separation factor up to 67%. When studying pervaporation of the feed solution containing 2 wt% of butanol, the dependences of the permeate flux and separation factor on the elastomeric filler content in the host matrix show the well-pronounced maxima at 1.2-3 wt% (MW of the elastomer is 83-1000 kg/mol). In this case, the attained permeate flux is 1.5-1.8 times higher than that of the virgin PTMSP, and the separation factor increases by a factor of 1.4-1.7. The corresponding values of thickness-corrected flux and separation factor for the PTMSP/PDMSM membranes are 3.5-4.0 kg m/(m(2) h) and 112-136, respectively. More specifically, the 30 urn thick PTMSP/PDMSM (98/2) membrane exhibited permeate flux 0.12 kg/(m(2) h) and separation factor 128 upon pervaporation of 2 wt% aqueous butanol solution at 25 C. The experiments on the equilibrium sorption of butanol solutions on the PTMSP membranes modified by the elastomeric filler revealed similar dependences with their well-pronounced maxima in the same region of the PDMSM content. The highest value of membrane selectivity alpha(mem) for PTMSP/PDMSM is 8.9 as compared with 5.3 for the virgin PTMSP membranes. Qualitative explanation of the enhanced pervaporation selectivity coupled with the improved permeate flux for the PTMSP/PDMSM membranes was advanced. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:322 / 330
页数:9
相关论文
共 38 条
[1]
Permeability, permeance and selectivity: A preferred way of reporting pervaporation performance data [J].
Baker, Richard W. ;
Wijmans, J. G. ;
Huang, Yu .
JOURNAL OF MEMBRANE SCIENCE, 2010, 348 (1-2) :346-352
[2]
Polymeric mixed matrix membranes containing zeolites as a filler for gas separation applications: A review [J].
Bastani, Dariush ;
Esmaeili, Nazila ;
Asadollahi, Mahdieh .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2013, 19 (02) :375-393
[3]
SELECTION OF POLYMERS FOR PERVAPORATION MEMBRANES [J].
BELL, CM ;
GERNER, FJ ;
STRATHMANN, H .
JOURNAL OF MEMBRANE SCIENCE, 1988, 36 :315-329
[4]
Simulation of the Temperature-Driven Pervaporation of Dilute 1-Butanol Aqueous Mixtures through a PTMSP Membrane in a Cross-Flow Module [J].
Borisov, I. L. ;
Volkov, V. V. ;
Kirsh, V. A. ;
Roldugin, V. I. .
PETROLEUM CHEMISTRY, 2011, 51 (07) :542-554
[5]
Mixed matrix membranes (MMMs) comprising organic polymers with dispersed inorganic fillers for gas separation [J].
Chung, Tai-Shung ;
Jiang, Lan Ying ;
Li, Yi ;
Kulprathipanja, Santi .
PROGRESS IN POLYMER SCIENCE, 2007, 32 (04) :483-507
[6]
High flux composite PTMSP-silica nanohybrid membranes for the pervaporation of ethanol/water mixtures [J].
Claes, S. ;
Vandezande, P. ;
Mullens, S. ;
Leysen, R. ;
De Sitter, K. ;
Andersson, A. ;
Maurer, F. H. J. ;
Van den Rul, H. ;
Peeters, R. ;
Van Bael, M. K. .
JOURNAL OF MEMBRANE SCIENCE, 2010, 351 (1-2) :160-167
[7]
Fouling of poly[-1-(trimethylsilyl)-1-propyne] membranes in pervaporative recovery of butanol from aqueous solutions and ABE fermentation broth [J].
Fadeev, AG ;
Meagher, MM ;
Kelley, SS ;
Volkov, VV .
JOURNAL OF MEMBRANE SCIENCE, 2000, 173 (01) :133-144
[8]
Effect of yeast fermentation by-products on poly[1-(trimethylsilyl)-1-propyne] pervaporative performance [J].
Fadeev, AG ;
Kelley, SS ;
McMillan, JD ;
Selinskaya, YA ;
Khotimsky, VS ;
Volkov, VV .
JOURNAL OF MEMBRANE SCIENCE, 2003, 214 (02) :229-238
[9]
Extraction of butanol from aqueous solutions by pervaporation through poly(1-trimethylsilyl-1-propyne) [J].
Fadeev, AG ;
Selinskaya, YA ;
Kelley, SS ;
Meagher, MM ;
Litvinova, EG ;
Khotimsky, VS ;
Volkov, VV .
JOURNAL OF MEMBRANE SCIENCE, 2001, 186 (02) :205-217
[10]
Thermo pervap: The next step in energy efficient pervaporation [J].
Fernandez, Eva Sanchez ;
Geerdink, Peter ;
Goetheer, Earl L. V. .
DESALINATION, 2010, 250 (03) :1053-1055