A Method to Obtain Gas-PDMS Membrane Interaction Parameters for UNIQUAC Model

The recovery or capture of one or more components from gas mixture by membrane separation has become a research focus in recent years.This study investigates the gas-membrane solution equilibrium,for which Henry’s law is not applicable if the gas phase is a mixture.This problem can be solved by usin...

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Published inChinese journal of chemical engineering Vol. 21; no. 5; pp. 485 - 493
Main Author 林东杰 丁忠伟 刘丽英 马润宇
Format Journal Article
LanguageEnglish
Published Elsevier B.V 01.05.2013
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ISSN1004-9541
2210-321X
DOI10.1016/S1004-9541(13)60513-3

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Summary:The recovery or capture of one or more components from gas mixture by membrane separation has become a research focus in recent years.This study investigates the gas-membrane solution equilibrium,for which Henry’s law is not applicable if the gas phase is a mixture.This problem can be solved by using UNIQUAC model to calculate the activity coefficient of gas dissolved in the membrane.A method was proposed in this study to obtain the gas-membrane interaction parameter for UNIQUAC model.By the experiments of gas permeation through polydimethylsiloxane PDMS membrane,the solubility coefficients of some gases(N2,CO2,CH4) were measured.Through non-linear fitting UNIQUAC model to the experimental results from this study and in literature(H2,O2,C3H8),the gas-membrane interaction parameters for these gases were obtained.Based on these parameters,the activity coefficients of the dissolved gas were calculated by UNIQUAC model,and their values agree well with the experimental data.These results confirm the feasibility and effectiveness of the proposed method,which makes it possible to better predict gas-membrane solution equilibrium.
Bibliography:diffusion coefficient;solubility coefficient;polydimethylsiloxane(PDMS) membrane;UNIQUAC model
LIN Dongjie 1,2,DING Zhongwei1,2,*,LIU Liying1,2 and MA Runyu 1,2 1 College of Chemical Engineering,Beijing University of Chemical Technology,Beijing 100029,China 2 Beijing Key Laboratory of Membrane Science and Technology,Beijing University of Chemical Technology,Beijing 100029,China
The recovery or capture of one or more components from gas mixture by membrane separation has become a research focus in recent years.This study investigates the gas-membrane solution equilibrium,for which Henry’s law is not applicable if the gas phase is a mixture.This problem can be solved by using UNIQUAC model to calculate the activity coefficient of gas dissolved in the membrane.A method was proposed in this study to obtain the gas-membrane interaction parameter for UNIQUAC model.By the experiments of gas permeation through polydimethylsiloxane PDMS membrane,the solubility coefficients of some gases(N2,CO2,CH4) were measured.Through non-linear fitting UNIQUAC model to the experimental results from this study and in literature(H2,O2,C3H8),the gas-membrane interaction parameters for these gases were obtained.Based on these parameters,the activity coefficients of the dissolved gas were calculated by UNIQUAC model,and their values agree well with the experimental data.These results confirm the feasibility and effectiveness of the proposed method,which makes it possible to better predict gas-membrane solution equilibrium.
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ISSN:1004-9541
2210-321X
DOI:10.1016/S1004-9541(13)60513-3