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Rasheed SH, Ibrahim SS, Alsalhy QF, Majdi HS. Polydimethylsiloxane (PDMS) Membrane for Separation of Soluble Toluene by Pervaporation Process. MEMBRANES 2023; 13:289. [PMID: 36984676 PMCID: PMC10057562 DOI: 10.3390/membranes13030289] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Figures] [Subscribe] [Scholar Register] [Received: 01/23/2023] [Revised: 02/19/2023] [Accepted: 02/23/2023] [Indexed: 06/18/2023]
Abstract
A commercial polydimethylsiloxane (PDMS) membrane was employed to separate the soluble toluene compounds (C7H8) from an aqueous solution via the pervaporation (PV) process. The performance and the efficacy of the PDMS PV membrane were evaluated through the estimation of the permeation flux and separation factor under various operating parameters. The response surface method (RSM) built in the Minitab-18 software was used for the design of the experiment in this study, and the responses of the permeation flux and the separation factor were analyzed and optimized based on the operating conditions. A nonlinear regression analysis was applied to the experimental output and input, and as a result, a quadratic equation model with parameters interactions was obtained as mathematical expressions to predict the permeation flux and separation factor. At the optimal conditions of temperature 30 °C, initial toluene concentration 500 ppm, and feed flowrate 3.5 L/min, the toluene permeation flux and separation factor were 125.855 g/m2·h and 1080, respectively. The feed concentration was the most impactful and significant in the improvement of the permeation flux and separation factor of the PDMS membrane.
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Affiliation(s)
- Salam H. Rasheed
- Membrane Technology Research Unit, Department of Chemical Engineering, University of Technology-Iraq, Alsinaa Street 52, Baghdad 10066, Iraq
| | - Salah S. Ibrahim
- Membrane Technology Research Unit, Department of Chemical Engineering, University of Technology-Iraq, Alsinaa Street 52, Baghdad 10066, Iraq
| | - Qusay F. Alsalhy
- Membrane Technology Research Unit, Department of Chemical Engineering, University of Technology-Iraq, Alsinaa Street 52, Baghdad 10066, Iraq
| | - Hasan Sh. Majdi
- Department of Chemical Engineering and Petroleum Industries, Al-Mustaqbal University College, Babylon 51001, Iraq
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Qiu B, Wang Y, Fan S, Liu J, Jian S, Qin Y, Xiao Z, Tang X, Wang W. Ethanol mass transfer during pervaporation with PDMS membrane based on solution-diffusion model considering concentration polarization. Sep Purif Technol 2019. [DOI: 10.1016/j.seppur.2019.03.021] [Citation(s) in RCA: 16] [Impact Index Per Article: 3.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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Influence of feed flow rate, temperature and feed concentration on concentration polarization effects during separation of water-methyl acetate solutions with high permeable hydrophobic pervaporation PDMS membrane. J Memb Sci 2018. [DOI: 10.1016/j.memsci.2018.07.001] [Citation(s) in RCA: 29] [Impact Index Per Article: 4.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/18/2022]
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Dytrych P, Vajglová Z, Morávková L, Jandová V, Izák P, Petrusová Z. Minimization of the Theoretical Error of Input Parameters for a Vapor Permeation Apparatus. Chem Eng Technol 2018. [DOI: 10.1002/ceat.201800163] [Citation(s) in RCA: 5] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Pavel Dytrych
- Institute of Chemical Process Fundamentals of the Czech Academy of Sciences; Rozvojová 135/2 16502 Prague Czech Republic
| | - Zuzana Vajglová
- Institute of Chemical Process Fundamentals of the Czech Academy of Sciences; Rozvojová 135/2 16502 Prague Czech Republic
| | - Lenka Morávková
- Institute of Chemical Process Fundamentals of the Czech Academy of Sciences; Rozvojová 135/2 16502 Prague Czech Republic
| | - Věra Jandová
- Institute of Chemical Process Fundamentals of the Czech Academy of Sciences; Rozvojová 135/2 16502 Prague Czech Republic
| | - Pavel Izák
- Institute of Chemical Process Fundamentals of the Czech Academy of Sciences; Rozvojová 135/2 16502 Prague Czech Republic
| | - Zuzana Petrusová
- Institute of Chemical Process Fundamentals of the Czech Academy of Sciences; Rozvojová 135/2 16502 Prague Czech Republic
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A novel catalytically active membrane with highly porous catalytic layer for the conversion enhancement of esterification: Focusing on the reduction of mass transfer resistance of the catalytic layer. J Memb Sci 2017. [DOI: 10.1016/j.memsci.2017.05.065] [Citation(s) in RCA: 14] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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Naik PV, Bernstein R, Vankelecom IFJ. Influence of support layer and PDMS coating conditions on composite membrane performance for ethanol/water separation by pervaporation. J Appl Polym Sci 2016. [DOI: 10.1002/app.43670] [Citation(s) in RCA: 29] [Impact Index Per Article: 3.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
Affiliation(s)
- Parimal V Naik
- Centre for Surface Chemistry and Catalysis, Faculty of Bioengineering Sciences; KU Leuven, Kasteelpark Arenberg 23, PO Box 2461 Leuven 3001 Belgium
| | - Roy Bernstein
- Centre for Surface Chemistry and Catalysis, Faculty of Bioengineering Sciences; KU Leuven, Kasteelpark Arenberg 23, PO Box 2461 Leuven 3001 Belgium
| | - Ivo F. J Vankelecom
- Centre for Surface Chemistry and Catalysis, Faculty of Bioengineering Sciences; KU Leuven, Kasteelpark Arenberg 23, PO Box 2461 Leuven 3001 Belgium
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Influence of downstream pressure on pervaporation properties of PDMS and POMS based membranes. Sep Purif Technol 2016. [DOI: 10.1016/j.seppur.2015.12.057] [Citation(s) in RCA: 58] [Impact Index Per Article: 7.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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Kansara AM, Jadav GL, Chaudhri SG, Singh PS. Preparation of Poly(dimethylsiloxane)-Polysulfone Composite Membrane by Sequential Absorption-Reaction-Evaporation Process and its Application in Treatment of Aqueous Solution Containing Volatile Organics. SEP SCI TECHNOL 2014. [DOI: 10.1080/01496395.2014.944619] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Submit a Manuscript] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
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11
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Hyder M, Huang R, Chen P. Composite poly(vinyl alcohol)–poly(sulfone) membranes crosslinked by trimesoyl chloride: Characterization and dehydration of ethylene glycol–water mixtures. J Memb Sci 2009. [DOI: 10.1016/j.memsci.2008.10.017] [Citation(s) in RCA: 36] [Impact Index Per Article: 2.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/21/2022]
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12
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Fouad EA, Feng X. Use of pervaporation to separate butanol from dilute aqueous solutions: Effects of operating conditions and concentration polarization. J Memb Sci 2008. [DOI: 10.1016/j.memsci.2008.06.054] [Citation(s) in RCA: 114] [Impact Index Per Article: 7.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/13/2022]
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Hyder M, Huang R, Chen P. Effect of selective layer thickness on pervaporation of composite poly(vinyl alcohol)–poly(sulfone) membranes. J Memb Sci 2008. [DOI: 10.1016/j.memsci.2008.03.002] [Citation(s) in RCA: 30] [Impact Index Per Article: 1.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/22/2022]
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Sodium montmorillonite clay loaded novel mixed matrix membranes of poly(vinyl alcohol) for pervaporation dehydration of aqueous mixtures of isopropanol and 1,4-dioxane. J Memb Sci 2006. [DOI: 10.1016/j.memsci.2006.08.022] [Citation(s) in RCA: 119] [Impact Index Per Article: 6.6] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
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Removal of chlorinated volatile organic contaminants from water by pervaporation using a novel polyurethane urea–poly (methyl methacrylate) interpenetrating network membrane. Chem Eng Sci 2006. [DOI: 10.1016/j.ces.2006.06.014] [Citation(s) in RCA: 24] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/18/2022]
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Fialová K, Petrychkovych R, Sharma M, Uchytil P. Steady state sorption measurement and the transport mechanism in polymeric membrane during vapor permeation. J Memb Sci 2006. [DOI: 10.1016/j.memsci.2005.09.015] [Citation(s) in RCA: 19] [Impact Index Per Article: 1.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/27/2022]
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Liang L, Dickson JM, Jiang J, Brook MA. Mass transfer of dilute 1,2-dimethoxyethane aqueous solutions during pervaporation process. J Appl Polym Sci 2006. [DOI: 10.1002/app.23056] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
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Villaluenga J, Khayet M, Godino P, Seoane B, Mengual J. Analysis of the membrane thickness effect on the pervaporation separation of methanol/methyl tertiary butyl ether mixtures. Sep Purif Technol 2005. [DOI: 10.1016/j.seppur.2005.06.006] [Citation(s) in RCA: 29] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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Sun L, Baker GL, Bruening ML. Polymer Brush Membranes for Pervaporation of Organic Solvents from Water. Macromolecules 2005. [DOI: 10.1021/ma047510o] [Citation(s) in RCA: 57] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Lei Sun
- Department of Chemistry, Michigan State University, East Lansing, Michigan 48824
| | - Gregory L. Baker
- Department of Chemistry, Michigan State University, East Lansing, Michigan 48824
| | - Merlin L. Bruening
- Department of Chemistry, Michigan State University, East Lansing, Michigan 48824
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Liang L, Dickson JM, Zhu Z, Jiang J, Brook MA. Removal of 1,2-dichloroethane from aqueous solutions with novel composite polydimethylsiloxane pervaporation membranes. J Appl Polym Sci 2005. [DOI: 10.1002/app.21752] [Citation(s) in RCA: 7] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
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Liang L, Dickson JM, Jiang J, Brook MA. Effect of low flow rate on pervaporation of 1,2-dichloroethane with novel polydimethylsiloxane composite membranes. J Memb Sci 2004. [DOI: 10.1016/j.memsci.2003.10.038] [Citation(s) in RCA: 20] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/26/2022]
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Peng M, Vane LM, Liu SX. Recent advances in VOCs removal from water by pervaporation. JOURNAL OF HAZARDOUS MATERIALS 2003; 98:69-90. [PMID: 12628778 DOI: 10.1016/s0304-3894(02)00360-6] [Citation(s) in RCA: 84] [Impact Index Per Article: 4.0] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/24/2023]
Abstract
Pervaporation (PV) is a separation process in which minor components of a liquid mixture are preferentially transported by partial vaporization through a non-porous permselective (selectively permeable) membrane. PV is an emerging technology in environment cleanup operations, especially in the removal of volatile organic compounds (VOCs) from industrial wastewaters or contaminated groundwaters. Current state of PV membrane development in VOC removal and improvement in process engineering, and better understanding of the interactions between VOCs and membrane materials are reviewed. Among PV process parameters documented here are process temperature, permeate pressure, feed concentration, and feed flow rate. The effects of these parameters on PV selectivity and permeation flux have been studied extensively and these studies have borne fruit in a better understanding of many aspects of PV processes. The challenge in implementing PV in practical operations lies in the further enhancement of membrane quality for specific VOCs as well as improved management and control of possible adverse hurdles coming from real systems.
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Affiliation(s)
- Ming Peng
- Department of Food Science, Cook College, Rutgers University, 65 Dudley Road, New Brunswick, NJ 08901, USA
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Kim HJ, Nah SS, Min BR. A new technique for preparation of PDMS pervaporation membrane for VOC removal. ACTA ACUST UNITED AC 2002. [DOI: 10.1016/s1093-0191(01)00056-9] [Citation(s) in RCA: 54] [Impact Index Per Article: 2.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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Han S, Puech L, Law RV, Steinke JH, Livingston A. Selection of elastomeric membranes for the separation of organic compounds in acidic media. J Memb Sci 2002. [DOI: 10.1016/s0376-7388(01)00639-1] [Citation(s) in RCA: 16] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/01/2022]
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Huang RYM, Moon GY, Pal R. Ethylene Propylene Diene Monomer (EPDM) Membranes for the Pervaporation Separation of Aroma Compound from Water. Ind Eng Chem Res 2002. [DOI: 10.1021/ie010246s] [Citation(s) in RCA: 15] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
- R. Y. M. Huang
- Department of Chemical Engineering, University of Waterloo, Waterloo, Ontario, Canada N2L 3G1
| | - G. Y. Moon
- Department of Chemical Engineering, University of Waterloo, Waterloo, Ontario, Canada N2L 3G1
| | - R. Pal
- Department of Chemical Engineering, University of Waterloo, Waterloo, Ontario, Canada N2L 3G1
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29
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Incorporation effect of fluorinated side groups into polyimide membranes on their pervaporation properties. J Memb Sci 2000. [DOI: 10.1016/s0376-7388(99)00346-4] [Citation(s) in RCA: 45] [Impact Index Per Article: 1.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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Affiliation(s)
- C. K. Yeom
- Chemical Process and Engineering Center, Applied and Engineering Chemistry Division, Korea Research Institute of Chemical Technology, P.O. Box 107, Yusong, Taejon 305‐606, South Korea
| | - H. K. Kim
- Energy and Environment Research Team, Research and Development Center, Korea Heavy Industries and Construction Co., Changwon P.O. Box 77, Kyongnam 641‐792, South Korea
| | - J. W. Rhim
- Department of Chemical Engineering, Hannam University 133 Ojung‐Dong, Daedeog‐Ku, Taejon 300‐791
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Mass transfer analysis of the pervaporative separation of chloroform from aqueous solutions in hollow fiber devices. J Memb Sci 1999. [DOI: 10.1016/s0376-7388(98)00350-0] [Citation(s) in RCA: 29] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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35
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Pervaporative extraction of volatile organic compounds from aqueous systems with use of a tubular transverse flow module. J Memb Sci 1998. [DOI: 10.1016/s0376-7388(98)00002-7] [Citation(s) in RCA: 20] [Impact Index Per Article: 0.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
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36
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Crowder ML, Gooding CH. Spiral wound, hollow fiber membrane modules: A new approach to higher mass transfer efficiency. J Memb Sci 1997. [DOI: 10.1016/s0376-7388(97)00174-9] [Citation(s) in RCA: 26] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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38
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Pervaporation of methanol from a triglyme solution using a Nafion membrane: 2. Concentration polarization. J Memb Sci 1997. [DOI: 10.1016/s0376-7388(97)00066-5] [Citation(s) in RCA: 13] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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Affiliation(s)
- Xianshe Feng
- Department of Chemical Engineering, University of Waterloo, Waterloo, Ontario, Canada N2L 3G1
| | - Robert Y. M. Huang
- Department of Chemical Engineering, University of Waterloo, Waterloo, Ontario, Canada N2L 3G1
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Charbit G, Charbit F , Molina C. Study of Mass Transfer Limitations in the Deterpenation of Waste Waters by Pervaporation. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 1997. [DOI: 10.1252/jcej.30.382] [Citation(s) in RCA: 10] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Gérard Charbit
- Laboratoire d’Etudes et d’Applications de Procédés Séparatifs, Université d’Aix-Marseille
| | - Françoise Charbit
- Laboratoire d’Etudes et d’Applications de Procédés Séparatifs, Université d’Aix-Marseille
| | - Carole Molina
- Laboratoire de Chimie des Produits Naturels-Université d’Aix-Marseille
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Optimization of multicomponent pervaporation for removal of volatile organic compounds from water. J Memb Sci 1994. [DOI: 10.1016/0376-7388(94)00153-p] [Citation(s) in RCA: 38] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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44
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Ji W, Sikdar SK, Hwang ST. Modeling of multicomponent pervaporation for removal of volatile organic compounds from water. J Memb Sci 1994. [DOI: 10.1016/0376-7388(94)85011-9] [Citation(s) in RCA: 87] [Impact Index Per Article: 2.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/18/2022]
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