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A novel ammonia-carbon dioxide forward(direct)osmosis desalination process

机译:一种新型的氨-二氧化碳正(直接)渗透淡化工艺

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摘要

A novel forward(direct)osmosis(FO)desalination process is presented.The process uses an ammonium bicarbonate draw solution to extract water from a saline feed water across a semi-permeable polymeric membrane.Very large osmotic pressures generated by the highly soluble ammonium bicarbonate draw solution yield high water fluxes and can result in very high feed water recoveries.Upon moderate heating,ammonium bicarbonate decomposes into ammonia and carbon dioxide gases that can be separated and recycled as draw solutes,leaving the fresh product water.Experiments with a laboratory-scale FO unit utilizing a flat sheet cellulose tri-acetate membrane demonstrated high product water flux and relatively high salt rejection.The results further revealed that reverse osmosis(RO)membranes are not suitable for the FO process because of relatively low product water fluxes attributed to severe internal concentration polarization in the porous support and fabric layers of the RO membrane.
机译:提出了一种新颖的正向(FO)海水淡化工艺,该工艺使用碳酸氢铵抽提液通过半渗透性聚合物膜从盐水进水中提取水。高度溶解的碳酸氢铵产生很大的渗透压汲取溶液产生高的水通量,并且可以导致非常高的给水回收率。在适度加热下,碳酸氢铵分解为氨气和二氧化碳气体,可以将其分离并作为汲取溶质再循环,从而保留了新鲜的生产用水。使用平板状三醋酸纤维素膜的大规模FO装置显示出较高的产品水通量和较高的脱盐率。结果进一步表明,反渗透(RO)膜不适合用于FO工艺,因为归因于较低的产品水通量RO膜的多孔支撑层和织物层中出现严重的内部浓度极化。

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