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Process Modeling of Hybrid Forward Osmosis-Distillation Desalination Systems

机译:杂交前期渗透蒸馏水脱盐系统的过程建模

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Forward osmosis (FO), also known as engineered osmosis, is two step process for desalinating seawater and other complex aqueous feed streams. The first step, the passive diffusion of water across a polyamide thin-film composite membrane (similar to that used in reverse osmosis) is driven by an osmotic gradient between the feed stream and a high osmotic pressure draw solution. When using a thermolytic salt, the second step of draw solute recovery uses low-temperature heat to recycle the draw solution and produce a permeate stream of fresh water. Compared to alternative techniques for water desalination this process does not require electricity to power high-pressure pumps (as in reverse osmosis) or high grade thermal energy to evaporate the water (as in multistage flash distillation). One promising draw solute/recovery pair are the thermolytic salts created by ammonia and carbon dioxide (NH4HCO3, (NH4)2CO3, and NH2CO2NH4) which can be driven out of water at relatively low temperatures (<70°C) in distillation columns.
机译:转发渗透(Fo),也称为工程化渗透,是脱盐海水和其他复合物水性进料流的两步方法。第一步,通过进料流和高渗透压抽取溶液之间的渗透梯度驱动,在聚酰胺薄膜复合膜上(类似于反渗透的类似渗透渗透)驱动的第一步。当使用热解盐时,溶质回收的第二步使用低温热来回收液化溶液并产生渗透物流的淡水流。与水脱盐的替代技术相比,该过程不需要电力电力高压泵(如反渗透)或高级热能以蒸发水(如在多级闪蒸蒸馏中)。一个有希望的绘制溶质/恢复对是由氨和二氧化碳产生的热解盐(NH 4 HCO 3,(NH 4)2CO3和NH 2 CO 2 NH 4),其可以在蒸馏塔中的相对低温(<70℃)的水中被驱动。

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