Highly porous and macrovoid-free PVDF hollow fiber membranes for membrane distillation by a solvent-dope solution co-extrusion approach

Abstract Highly porous and macrovoid-free PVDF hollow fiber membranes are of great interest for membrane contactor applications such as sea water desalination by membrane distillation in order to enhance the flux and long term stability of the process. For the first time in this paper, porous PVDF hollow fiber membranes with high outer surface porosity were fabricated by applying a two-phase flow consisting of a solvent and a dope solution in the air-gap region of spinning through a non-solvent induced phase separation process (NIPS). In this approach, the dope solution and the N -methylpyrrolidone (NMP) solvent were co-discharged from the middle and outer channels of a triple orifice spinneret, respectively. Then, the two-phase flow went through an air-gap region and finally entered the coagulation bath. It was observed that the introduction of the two-phase flow greatly increased the outer surface porosity of the PVDF fibers and eliminated the formation of macrovoids in the cross-section of the fibers as well. It was also found that the energy efficiency and the flux of the fibers spun through the solvent-dope solution co-exterusion were two to three times higher than the standard dry jet wet-spun fibers. A water vapor flux as high as 67 kg/(m 2  h) at 80 °C was obtained through the newly spun fibers.

[1]  Takeshi Matsuura,et al.  Preparation and Characterization of Polyvinylidene Fluoride Membranes for Membrane Distillation , 2001 .

[2]  T. Uragami,et al.  Studies on syntheses and permeabilities of special polymer membranes. 27. Concentration of poly(styrene sulphonic acid) in various aqueous solutions using poly(vinylidene fluoride) membranes , 1981 .

[3]  Imona C. Omole Hollow-fiber membrane contactors , 1999 .

[4]  A. Bottino,et al.  High performance ultrafiltration membranes cast from LiCl doped solutions , 1988 .

[5]  J. M. Rodríguez-Maroto,et al.  Membrane thickness reduction effects on direct contact membrane distillation performance , 2008 .

[6]  Rong Wang,et al.  Fabrication of lab-scale hollow fiber membrane modules with high packing density , 2004 .

[7]  K. Kimmerle,et al.  Analysis of the structure-determining process of phase inversion membranes , 1990 .

[8]  Kang Li,et al.  Preparation and characterization of polyvinylidene fluoride (PVDF) hollow fiber membranes , 1999 .

[9]  K. Sirkar,et al.  Novel membrane and device for direct contact membrane distillation-based desalination process , 2004 .

[10]  Mohamed Khayet,et al.  A framework for better understanding membrane distillation separation process , 2006 .

[11]  Kang Li,et al.  Modified silicone–PVDF composite hollow‐fiber membrane preparation and its application in VOC separation , 2006 .

[12]  M. Vahdati,et al.  Direct Contact Membrane Distillation , 2000 .

[13]  D. T. Liang,et al.  Effect of PVDF dope rheology on the structure of hollow fiber membranes used for CO2 capture , 2006 .

[14]  T. He,et al.  Preparation of Porous Hollow Fiber Membranes with a Triple-Orifice Spinneret , 2003 .

[15]  M. Tomaszewska,et al.  Preparation and properties of flat-sheet membranes from poly(vinylidene fluoride) for membrane distillation , 1996 .

[16]  P. Prádanos,et al.  Porosity measurements by a gas penetration method and other techniques applied to membrane characterization , 1999 .

[17]  J. M. Zárate,et al.  Characterization of membrane distillation membranes prepared by phase inversion , 1995 .

[18]  A. Bottino,et al.  The formation of microporous polyvinylidene difluoride membranes by phase separation , 1991 .

[19]  Kai Yu Wang,et al.  Hydrophobic PVDF hollow fiber membranes with narrow pore size distribution and ultra-thin skin for the fresh water production through membrane distillation , 2008 .

[20]  L. Scriven,et al.  Interfacial turbulence: Hydrodynamic instability and the marangoni effect , 1959 .

[21]  Kai Yu Wang,et al.  The observation of elongation dependent macrovoid evolution in single- and dual-layer asymmetric hollow fiber membranes , 2004 .

[22]  M. Khayet,et al.  Heat and mass transfer in vacuum membrane distillation , 2004 .

[23]  Kang Li,et al.  Removal of H2S to ultra-low concentrations using an asymmetric hollow fibre membrane module ☆ , 2002 .

[24]  Mohamed Khayet,et al.  Preparation and characterization of polyvinylidene fluoride hollow fiber membranes for ultrafiltration , 2002 .

[25]  S. M. Aharoni Rigid backbone polymers: 6. Ternary phase relationships of polyisocyanates , 1980 .

[26]  Jack Gilron,et al.  Direct Contact Membrane Distillation-Based Desalination: Novel Membranes, Devices, Larger-Scale Studies, and a Model , 2007 .

[27]  Polydisperse Au nanoclusters on silicon: fractal aggregates via spinodal decomposition? , 2001 .

[28]  Levent Yilmaz,et al.  Analysis of nonsolvent‐solvent‐polymer phase diagrams and their relevance to membrane formation modeling , 1986 .

[29]  T. Uragami,et al.  Studies on syntheses and permeabilities of special polymer membranes: 24. Permeation characteristics of poly(vinylidene fluoride) membranes , 1980 .

[30]  May May Teoh,et al.  Investigation of different hollow fiber module designs for flux enhancement in the membrane distillation process , 2008 .