Forward osmosis :a new approach to water purification and desalination.

Fresh, potable water is an essential human need and thus looming water shortages threaten the world's peace and prosperity. Waste water, brackish water, and seawater have great potential to fill the coming requirements. Unfortunately, the ability to exploit these resources is currently limited in many parts of the world by both the cost of the energy and the investment in equipment required for purification/desalination. Forward (or direct) osmosis is an emerging process for dewatering aqueous streams that might one day help resolve this problem. In FO, water from one solution selectively passes through a membrane to a second solution based solely on the difference in the chemical potential (concentration) of the two solutions. The process is spontaneous, and can be accomplished with very little energy expenditure. Thus, FO can be used, in effect, to exchange one solute for a different solute, specifically chosen for its chemical or physical properties. For desalination applications, the salts in the feed stream could be exchanged for an osmotic agent specifically chosen for its ease of removal, e.g. by precipitation. This report summarizes work performed at Sandia National Laboratories in the area of FO and reviews the status of the technology for desalination applications. Atmore » its current state of development, FO will not replace reverse osmosis (RO) as the most favored desalination technology, particularly for routine waters. However, a future role for FO is not out of the question. The ability to treat waters with high solids content or fouling potential is particularly attractive. Although our analysis indicates that FO is not cost effective as a pretreatment for conventional BWRO, water scarcity will likely drive societies to recover potable water from increasingly marginal resources, for example gray water and then sewage. In this context, FO may be an attractive pretreatment alternative. To move the technology forward, continued improvement and optimization of membranes is recommended. The identification of optimal osmotic agents for different applications is also suggested as it is clear that the space of potential agents and recovery processes has not been fully explored.« less

[1]  Julius Glater,et al.  A desalination primer: by K.S. Spiegler and Y.M. El-Sayed ISBN 0-86689-034-3, 1994, hard cover 215 pp, price $49.00 Balaban Desalination Publications , 1995 .

[2]  Lindsey R. Evans,et al.  Sweeping Gas Membrane Desalination Using Commercial Hydrophobic Hollow Fiber Membranes , 2002 .

[3]  Richard H. Schlosberg,et al.  Organic chemistry of calcium. II: Alkylation of hydroxycalcium phenoxides , 1989 .

[4]  M S Bader,et al.  Separation of critical radioactive and non-radioactive species from aqueous waste streams. , 2001, Journal of hazardous materials.

[5]  W H Streng The Gibbs constant and pH solubility profiles. , 1999, International journal of pharmaceutics.

[6]  Ronald A. Siegel,et al.  Studies of precipitating and soluble hydrophobic polyelectrolytes , 1992 .

[7]  Z T Chowhan,et al.  pH-solubility profiles or organic carboxylic acids and their salts. , 1978, Journal of pharmaceutical sciences.

[8]  R Thiering,et al.  Isoelectric precipitation of soybean protein using carbon dioxide as a volatile acid. , 2000, Journal of chromatography. B, Biomedical sciences and applications.

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

[10]  W H Streng,et al.  General treatment of pH-solubility profiles of weak acids and bases and the effects of different acids on the solubility of a weak base. , 1984, Journal of pharmaceutical sciences.

[11]  Geert-Jan Witkamp,et al.  Isoelectric Precipitation of Casein Using High-Pressure CO2 , 1999 .

[12]  James E. Miller,et al.  Review of Water Resources and Desalination Technologies , 2003 .

[13]  Manish Sharma,et al.  Separation of close-boiling substituted phenols by anhydrous calcium hydroxide and recovery of phenols from calcium phenoxides by carbonation , 1992 .

[14]  S. Loeb,et al.  Countercurrent flow osmotic processes for the production of solutions having a high osmotic pressure , 1973 .

[15]  Silvia Bolado,et al.  Liquid−Liquid Equilibria for Aqueous Solutions of Lithium Sulfate or Lithium Formate and Triethylamine or Diisopropylamine , 2000 .

[16]  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 .

[17]  Chunmei Shi,et al.  Remediation of Metal-Bearing Aqueous Waste Streams via Direct Carbonation , 2001 .

[18]  David Bradbury,et al.  The Development of Magnetic Molecules for the Selective Removal of Contaminants , 2006 .

[19]  Menachem Elimelech,et al.  A novel ammonia-carbon dioxide forward (direct) osmosis desalination process , 2005 .

[20]  James C. Craig,et al.  A continuous process for casein production using high-pressure carbon dioxide☆ , 1997 .

[21]  W. M. Haynes CRC Handbook of Chemistry and Physics , 1990 .

[22]  Michael Flynn,et al.  Membrane contactor processes for wastewater reclamation in space Part I. Direct osmotic concentration as pretreatment for reverse osmosis , 2005 .

[23]  R Engelman,et al.  People in the balance. Population and natural resources at the turn of the millennium. , 2000 .

[24]  H. Ng,et al.  Performance of forward (direct) osmosis process: membrane structure and transport phenomenon. , 2006, Environmental science & technology.

[25]  Alex Avdeef,et al.  pH‐metric Solubility. 1. Solubility‐pH Profiles from Bjerrum Plots. Gibbs Buffer and pKa in the Solid State , 1998 .

[26]  Lindsey R. Evans,et al.  Batch Microreactor Studies of Lignin Depolymerization by Bases. 2. Aqueous Solvents , 2002 .

[27]  A. Avdeef,et al.  pH-metric solubility. 3. Dissolution titration template method for solubility determination. , 2001, European journal of pharmaceutical sciences : official journal of the European Federation for Pharmaceutical Sciences.

[28]  Geert-Jan Witkamp,et al.  Antisolvent Crystallization as an Alternative to Evaporative Crystallization for the Production of Sodium Chloride , 2000 .

[29]  Charles G. Scouten,et al.  Organic chemistry of calcium. 3. Steam stripping of metal phenoxides liberates phenol and regenerates the metal hydroxide , 1990 .