A new hybrid ion exchange-nanofiltration (HIX-NF) separation process for energy-efficient desalination: Process concept and laboratory evaluation

Abstract The study presents the results of a new energy-efficient hybrid ion exchange-nanofiltration (HIX-NF) process to desalinate brackish and sea water. From a scientific viewpoint, the HIX-NF process is unique in its approach for it partially alters the feed water chemistry prior to the membrane treatment. Specifically it converts monovalent chloride, the predominant anion in salt water, into divalent sulfate through a reversible anion-exchange process without requiring any external regenerant. As a result, reverse osmosis (RO) membrane can be replaced altogether by nanofiltration (NF) membrane resulting in a marked reduction in energy requirement. Also, conversion of chloride to sulfate reduces the osmotic pressure of the feed water by nearly thirty percent and consequently decreases the theoretical energy requirement. The reject stream from nanofiltration, rich in sulfate, is used to regenerate the anion exchanger. Laboratory results validate that sodium sulfate can be desalinated with NF membranes at much lower transmembrane pressure than with RO membranes, all other conditions remaining identical. The reversible sulfate–chloride anion exchange and, in particular, sulfate/chloride selectivity plays a central role for the success of the proposed process. The most significant finding is that a single anion-exchange resin cannot sustain the HIX-NF process for different feed water concentrations. The investigation, however, shows that by changing the size of the amine functional group (e.g., quaternary-, tertiary-, secondary- and mixed amine), the sulfate/chloride selectivity of the anion-exchange resin can be tailored for a specific feed water salinity allowing optimum reversibility of the anion-exchange process. Laboratory studies have validated the basic premise of the hybrid process including greater than two times lesser energy requirement than RO process for the same feed water. Future proto-type experimental studies are strongly recommended to confirm the overall viability of the HIX-NF process.

[1]  Ping Li,et al.  Sorption of hydrophobic ionizable organic compounds (HIOCs) onto polymeric ion exchangers , 2004 .

[2]  C. Vandecasteele,et al.  Influence of ion size and charge in nanofiltration , 1998 .

[3]  A. SenGupta,et al.  Evidence of Tunable On−Off Sorption Behaviors of Metal Oxide Nanoparticles: Role of Ion Exchanger Support , 2006 .

[4]  D. Butterfield,et al.  Permeability and Separation Characteristics of Polypeptide-Functionalized Polycarbonate Track-Etched Membranes , 2004 .

[5]  William J. Koros,et al.  Polymeric membrane materials for solution-diffusion based permeation separations , 1988 .

[6]  Y. El-Sayed,et al.  The energetics of desalination processes , 2001 .

[7]  R. Kunin Elements of ion exchange , 1960 .

[9]  Hisham Ettouney,et al.  Evaluating the economics of desalination , 2002 .

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

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

[12]  Nidal Hilal,et al.  Prediction of permeate fluxes and rejections of highly concentrated salts in nanofiltration membranes , 2007 .

[13]  Eric M.V. Hoek,et al.  Impacts of reaction and curing conditions on polyamide composite reverse osmosis membrane properties , 2008 .

[14]  D. Clifford,et al.  More on Mechanism and Some Important Properties of Chromate Ion Exchange , 1988 .

[15]  J. Greenleaf,et al.  Polymer supported inorganic nanoparticles: characterization and environmental applications , 2003 .

[16]  A. Mohammad,et al.  Performance of Nanofiltration Membranes in the Treatment of Synthetic and Real Seawater , 2007 .

[17]  Kamalesh K. Sirkar,et al.  Novel membrane and device for vacuum membrane distillation-based desalination process , 2005 .

[18]  A. SenGupta Ion exchange technology advances in pollution control , 1995 .

[19]  O. J. Morin,et al.  Design and operating comparison of MSF and MED systems , 1993 .

[20]  Tzahi Y. Cath,et al.  Membrane contactor processes for wastewater reclamation in space: II. Combined direct osmosis, osmotic distillation, and membrane distillation for treatment of metabolic wastewater , 2005 .

[21]  A. SenGupta,et al.  Ion Exchange Selectivity as a Surrogate Indicator of Relative Permeability of Ions in Reverse Osmosis Processes , 2003 .

[22]  Eric M.V. Hoek,et al.  Interfacial polymerization of thin film nanocomposites: A new concept for reverse osmosis membranes , 2007 .

[23]  N. Vlachakis,et al.  Energy consumption and membrane replacement cost for seawater RO desalination plants , 2003 .

[24]  Wolfgang Meier,et al.  Highly permeable polymeric membranes based on the incorporation of the functional water channel protein Aquaporin Z , 2007, Proceedings of the National Academy of Sciences.

[25]  F. Helfferich,et al.  Chloride/sulfate ion exchange kinetics at high solution concentration , 1987 .

[26]  W. Weber,et al.  The determinants of divalent/monovalent selectivity in anion exchangers , 1983 .

[27]  J. Greenleaf,et al.  Arsenic removal using a polymeric/inorganic hybrid sorbent. , 2003, Water research.

[28]  John R. Stillian,et al.  Factors controlling ion-exchange selectivity in suppressed ion chromatography , 1997 .

[29]  D. Clifford,et al.  Important process variables in chromate ion exchange. , 1986, Environmental science & technology.

[30]  A. SenGupta,et al.  Modified anion-exchange resins for improved chromate selectivity and increased efficiency of regeneration , 1988 .

[31]  Amy E. Childress,et al.  Forward osmosis: Principles, applications, and recent developments , 2006 .

[32]  Mark R. Wiesner,et al.  The promise of membrane technology , 1999 .

[33]  Menachem Elimelech,et al.  Energy requirements of ammonia-carbon dioxide forward osmosis desalination , 2007 .

[34]  Robert L McGinnis,et al.  Desalination by ammonia–carbon dioxide forward osmosis: Influence of draw and feed solution concentrations on process performance , 2006 .

[35]  Raphael Semiat,et al.  Desalination : Present and future , 2000 .