DCMD flux curve characteristics of cross-flow hollow fiber membrane

Abstract The membrane flux curve characteristics of cross-flow hollow fiber membrane in direct contact membrane distillation (DCMD) were investigated under various experimental conditions. The results indicate that the increase of feed inlet temperature diminishes the impact of the feed concentration on the flux. Both a low feed inlet temperature and a high feed flow rate lead to a high membrane thermal efficiency. Various operating parameters interact with each other in DCMD process. The feed and distillate inlet temperatures influence the flux mainly by changing temperature difference between two sides of the membrane. The feed flow rate influences the flux mainly by changing the temperature polarization at feed side. The distillate flow rate influences the flux mainly by changing the residence time of the distillate in hollow fiber membrane as well as by impacting the temperature polarization in a certain extent. Consequently, different flux curve characteristics are formed respectively under different operating conditions. This study is helpful to understand the DCMD characteristics.

[1]  K. Smolders,et al.  Terminology for Membrane Distillation , 1989 .

[2]  M. C. García-Payo,et al.  Separation of binary mixtures by thermostatic sweeping gas membrane distillation: II. Experimental results with aqueous formic acid solutions , 2002 .

[3]  Jun-de Li,et al.  Modelling heat and mass transfers in DCMD using compressible membranes , 2012 .

[4]  M. C. García-Payo,et al.  Separation of binary mixtures by thermostatic sweeping gas membrane distillation: I. Theory and simulations , 2002 .

[5]  Anthony G. Fane,et al.  Heat and mass transfer in membrane distillation , 1987 .

[6]  D. R. Lloyd,et al.  Membrane distillation. II. Direct contact MD , 1996 .

[7]  Liming Song,et al.  Pilot plant studies of novel membranes and devices for direct contact membrane distillation-based desalination , 2008 .

[8]  Anthony G. Fane,et al.  A new model for mass transfer in direct contact membrane distillation , 2003 .

[9]  L. Carlsson The New Generation in Sea Water Desalination SU Membrane Distillation System , 1983 .

[10]  R. Reid,et al.  The Properties of Gases and Liquids , 1977 .

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

[12]  Anthony G. Fane,et al.  Heat transport and membrane distillation coefficients in direct contact membrane distillation , 2003 .

[13]  D. R. Lloyd,et al.  Compaction of microporous membranes used in membrane distillation. I. Effect on gas permeability , 1995 .

[14]  Ratana Jiraratananon,et al.  Direct contact membrane distillation: effect of mass transfer on heat transfer , 2001 .

[15]  Junghui Chen,et al.  Modeling and optimization of hollow fiber DCMD module for desalination , 2008 .

[16]  M. Gryta,et al.  Study on the concentration of acids by membrane distillation , 1995 .

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