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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Evaluation of ethanol as draw solute for forward osmosis (FO) process of highly saline (waste)water
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Evaluation of ethanol as draw solute for forward osmosis (FO) process of highly saline (waste)water

机译:评价乙醇作为高渗(废物)水的前渗透(Fo)过程的溶质

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摘要

In the study, ethanol was evaluated for its potential as a draw solution in forward osmosis (FO) in terms of performance for treating highly saline (waste)waters and energy requirements for regeneration. When compared to NH4HCO3 (a thermolytic draw solution) ethanol exhibited significantly higher osmotic pressure and significantly easier regeneration. In FO experiments using commercial TFC FO membranes, the ethanol draw solution exhibited a water flux comparable to that of NH4HCO3 at equivalent osmotic pressure albeit a relatively high reverse solute flux (RSF) due to its volatility. The modeling prediction based on membrane transport properties obtained from the FO experiments revealed the critical role of the ethanol permeability of the membrane in the overall FO performance, thereby suggesting the necessity of a higher water-ethanol selective membranes for the extensive application of the ethanol draw solution for the treatment of highly saline wastewater. Easy-regeneration of the ethanol draw solution was also demonstrated based on experimental results obtained using laboratory scale vacuum distillation at room temperature and exergy analysis of the integrated system. The results indicated that the regeneration process required an estimated 8.8 kWh/m(3), thereby supporting the feasibility of ethanol as a potent draw solution for FO application of highly saline waters.
机译:在该研究中,在治疗高盐水(废物)水和再生能量要求的性能方面,评价其作为前渗透(FO)中的渗透溶液的潜力。与NH4HCO3(热解溶液)相比(热溶解溶液)相比,乙醇表现出显着更高的渗透压和显着更容易再生。在使用商业TFC FO膜的FO实验中,乙醇脱脂溶液表现出与当量渗透压时NH 4 HCO 3的水助熔剂,尽管具有相对高的逆转溶质通量(RSF)由于其挥发性而相当。基于FO实验中获得的膜传输性质的建模预测揭示了膜在总体性能中乙醇渗透性的关键作用,从而表明需要更高水 - 乙醇选择性膜的必要性,用于广泛应用乙醇绘制溶液处理高盐水废水。还基于在室温下使用实验室规模真空蒸馏和集成系统的漏洞分析获得的实验结果,证明了乙醇汲取溶液的易再生。结果表明,再生过程需要估计的8.8千瓦时/ m(3),从而支持乙醇作为施用高盐水施用的有效脱脂溶液的可行性。

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