Investigation of the permeability and selectivity of gases and volatile organic compounds for polydimethylsiloxane membranes

被引:43
作者
De Bo, I
Van Langenhove, H
Pruuost, P
De Neve, J
Pieters, J
Vankelecom, IFJ
Dick, E
机构
[1] State Univ Ghent, Dept Organ Chem, Res Grp Environm Organ Chem & Technol, Fac Agr & Appl Biol Sci, B-9000 Ghent, Belgium
[2] State Univ Ghent, Res Grp Biosyst Engn, Dept Agr Engn, Fac Agr & Appl Biol Sci, B-9000 Ghent, Belgium
[3] Catholic Univ Louvain, Dept Interphase Chem, Ctr Surface Chem & Catalysis, Fac Agr & Appl Biol Sci, B-3001 Heverlee, Belgium
[4] State Univ Ghent, Fluid Mech Lab, Dept Flow Heat & Combust Mech, Fac Sci Appl, B-9000 Ghent, Belgium
关键词
permeability; diffusivity; selectivity; volatile organic compounds; polydimethylsiloxane;
D O I
10.1016/S0376-7388(03)00024-3
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Selectivity of oxygen, carbon dioxide, ethylene, dimethyl sulphide, trichloroethylene and toluene from air and their permeability (P) and diffusivity (D-m) are reported for a polydimethylsiloxane (PDMS) membrane at 30degreesC. All are constants within the studied feed concentration interval (0.04-233 g m(-3)). The presence of oxygen in the vapour/air mixtures has no significant influence on the vapour permeation. All resistances for mass transfer are determined in the PDMS membrane while gas phase resistances are negligible. Increasing feed concentration or decreasing membrane thickness results in a linear increase of the compound's permeation. Computer simulations of the permeation tests indicate that the concentration in the permeate stream along the membrane sheet can be approximated by a logarithmic concentration profile. The highest permeability and lowest diffusivity are found for toluene, followed by trichloroethylene, dimethyl sulphide, ethylene, carbon dioxide and oxygen. Ratios between lowest and highest value for P and D-m were 300 and 11, respectively. The relative high selectivity of vapours compared to oxygen can hinder an optimal bioreactor operation for breaking down gaseous pollutants when a PDMS membrane is used as gas/liquid contactor. In some cases, it is expected that unsufficient amounts of oxygen permeate for complete metabolisation of the pollutants. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:303 / 319
页数:17
相关论文
共 39 条
[1]   Biodegradation of BTEX vapors in a silicone membrane bioreactor system [J].
Attaway, H ;
Gooding, CH ;
Schmidt, MG .
JOURNAL OF INDUSTRIAL MICROBIOLOGY & BIOTECHNOLOGY, 2001, 26 (05) :316-325
[2]  
BAKER RW, 1986, CHEMTECH, V16, P232
[3]  
BAUERLE U, 1986, LUFT, V5, P233
[4]   VAPOR SORPTION AND PERMEATION PROPERTIES OF POLY(DIMETHYLSILOXANE) FILMS [J].
BLUME, I ;
SCHWERING, PJF ;
MULDER, MHV ;
SMOLDERS, CA .
JOURNAL OF MEMBRANE SCIENCE, 1991, 61 :85-97
[5]  
Chandak MV, 1998, J APPL POLYM SCI, V67, P165, DOI 10.1002/(SICI)1097-4628(19980103)67:1<165::AID-APP19>3.0.CO
[6]  
2-0
[7]  
De Bo I, 2001, Meded Rijksuniv Gent Fak Landbouwkd Toegep Biol Wet, V66, P167
[8]   Application of vapour phase calibration method for determination of sorption of gases and VOC in polydimethylsiloxane membranes [J].
De Bo, I ;
Van Langenhove, H ;
De Keijser, J .
JOURNAL OF MEMBRANE SCIENCE, 2002, 209 (01) :39-52
[9]  
DEBO I, 2000, P 4 ISEB S NOODW NET
[10]   Mixed gas transport study through polymeric membranes [J].
Dhingra, SS ;
Marand, E .
JOURNAL OF MEMBRANE SCIENCE, 1998, 141 (01) :45-63