Preparation of ultra-thin poly(vinyl alcohol) membranes supported on polysulfone hollow fiber and their application for production of pure water from seawater

Abstract Pervaporation membrane process using polymeric membrane is promising for production of high-quality water from seawater. The use of membrane support is necessary for improvements in the membrane performance. In this work, preparation of thin poly(vinyl alcohol) (PVA) membranes over polysulfone hollow fiber support and their application for production of pure water from seawater through pervaporation separation process is reported. The uniformly thin PVA membrane coating over the cylindrical hollow fiber support of about 1.10 mm diameter was obtained by an automatic dip-coating method. The coating solution was a dilute aqueous solution of PVA (61,000 g/mol, molecular weight) and maleic acid having a molar composition in the range of 1 C 2 H 4 O (vinyl alcohol): 0.05–0.20 C 4 H 4 O 4 (maleic acid): 61–815 H 2 O. The conductance of produced water by the membranes from desalination of saline water of 30,000 ppm NaCl concentration was in the conductance range of pure water grade. The thinnest coated membrane exhibited permeate flux of about 7.4 L/m 2 /h from the feed water of 30,000 ppm NaCl at 344 K. The apparent activation energy of the pervaporation desalination based on the volume flux of the membranes was determined as about 23.1–25.8 kJ/mol.

[1]  Zhongyi Jiang,et al.  Analysis of annealing effect on pervaporation properties of PVA-GPTMS hybrid membranes through PALS , 2006 .

[2]  F. Kapteijn,et al.  Production of ultra pure water by desalination of seawater using a hydroxy sodalite membrane , 2010 .

[3]  H. Fujita,et al.  Concentration and temperature dependence of diffusion coefficients for systems polymethyl acrylate and n-alkyl acetates , 1960 .

[4]  N. Peppas,et al.  Crosslinked poly(vinyl alcohol) hydrogels as swollen elastic networks , 1977 .

[5]  Eli Korin,et al.  Water desalination by pervaporation with hollow fiber membranes , 1996 .

[6]  Carlo Vandecasteele,et al.  Concentration polarization and other boundary layer effects in the pervaporation of chlorinated hydrocarbons , 1994 .

[7]  L. Martínez,et al.  Comparison of membrane distillation performance using different feeds , 2004 .

[8]  T. Aminabhavi,et al.  Sodium montmorillonite clay loaded novel mixed matrix membranes of poly(vinyl alcohol) for pervaporation dehydration of aqueous mixtures of isopropanol and 1,4-dioxane , 2006 .

[9]  Y. Aurelle,et al.  Pervaporation: importance of concentration polarization in the extraction of trace organics from water☆ , 1988 .

[10]  S. M. Kuznicki,et al.  Pervaporative desalination of water using natural zeolite membranes , 2012 .

[11]  M. Tsuyumoto,et al.  Separation of water–ethanol by pervaporation through polyion complex composite membrane , 1991 .

[12]  Hongde Zhou,et al.  Water and solute transport in pervaporation hydrophilic membranes to reclaim contaminated water for micro-irrigation , 2005 .

[13]  E. Kruchinina,et al.  Deep desalination of water by evaporation through polymeric membranes , 2007 .

[14]  Matthias Wessling,et al.  Solar driven membrane pervaporation for desalination processes , 2005 .

[15]  Charles H. Gooding,et al.  Spiral wound, hollow fiber membrane modules: A new approach to higher mass transfer efficiency , 1997 .

[16]  H. Ohya,et al.  A study on pore size distribution of modified ultrathin membrances , 1974 .

[17]  Zhen-liang Xu,et al.  Polyvinyl alcohol/polysulfone (PVA/PSF) hollow fiber composite membranes for pervaporation separation of ethanol/water solution , 2005 .

[18]  G. Thomson,et al.  The Antoine equation for vapor-pressure data. , 1946, Chemical reviews.

[19]  J. K. Spelt,et al.  Solid surface tension: the equation of state approach and the theory of surface tension components. Theoretical and conceptual considerations , 1987 .

[20]  I. Karagiannis,et al.  Water desalination cost literature: review and assessment , 2008 .

[21]  C. Yeom,et al.  Pervaporation separation of water-acetic acid mixtures through poly(vinyl alcohol) membranes crosslinked with glutaraldehyde , 1996 .

[22]  M. Hoang,et al.  Effect of heat treatment on pervaporation separation of aqueous salt solution using hybrid PVA/MA/TEOS membrane , 2014 .

[23]  C. A. Smolders,et al.  Removal of trace organics from aqueous solutions. Effect of membrane thickness , 1991 .

[24]  M. Qtaishat,et al.  Heat and mass transfer analysis in direct contact membrane distillation , 2008 .

[25]  W. H. Emerson,et al.  Some physical properties of sea water in various concentrations , 1967 .

[26]  V. Aswal,et al.  Influence of hydrophilic silica nanoparticles to the conformation of hydrophilic polymer chain in dilute solution system. , 2011, Journal of colloid and interface science.

[27]  D. Bhattacharyya,et al.  Changes in morphology and transport characteristics of polysulfone membranes prepared by different demixing conditions , 1995 .

[28]  A. Bhattacharya,et al.  Studies on the Cross-linking of Poly(Vinyl Alcohol) , 2005 .

[29]  Berrin Tansel,et al.  Significance of hydrated radius and hydration shells on ionic permeability during nanofiltration in dead end and cross flow modes , 2006 .

[30]  S. J. Gregg,et al.  Adsorption Surface Area and Porosity , 1967 .

[31]  Xianshe Feng,et al.  Estimation of activation energy for permeation in pervaporation processes , 1996 .

[32]  Robert Y. M. Huang,et al.  Modification of poly(vinyl alcohol) using maleic acid and its application to the separation of acetic acid-water mixtures by the pervaporation technique , 1993 .

[33]  R. Baker Membrane Technology and Applications , 1999 .

[34]  Pankaj Sharma,et al.  Pervaporative seawater desalination using NaA zeolite membrane: Mechanisms of high water flux and hi , 2011 .

[35]  Manh Hoang,et al.  Sol–gel derived poly(vinyl alcohol)/maleic acid/silica hybrid membrane for desalination by pervaporation , 2011 .

[36]  J. Saja,et al.  Structural characterization of an UF membrane by gas adsorption-desorption and AFM measurements , 1996 .

[38]  T. Aminabhavi,et al.  Pervaporation Separation of Water/2-Propanol Mixtures by Use of the Blend Membranes of Sodium Alginate and (Hydroxyethyl)cellulose: Roles of Permeate-Membrane Interactions, Zeolite Filling, and Membrane Swelling , 2005 .

[39]  Manh Hoang,et al.  Separation of aqueous salt solution by pervaporation through hybrid organic–inorganic membrane: Effect of operating conditions , 2011 .