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Exploration of an innovative draw solution for a forward osmosis-membrane distillation desalination process

机译:渗透渗透膜蒸馏水脱盐过程的创新绘制解决方案的探讨

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摘要

Forward osmosis (FO) has emerged as a viable technology to alleviate the global water crisis. The greatest challenge facing the application of FO technology is the lack of an ideal draw solution with high water flux and low reverse salt flux. Hence, the objective of this study was to enhance FO by lowering reverse salt flux and maintaining high water flux; the method involved adding small concentrations of Al2(SO4)3 to a MgCl2 draw solution. Results showed that 0.5 M MgCl2 mixed with 0.05 M of Al2(SO4)3 at pH 6.5 achieved a lower reverse salt flux (0.53 gMH) than that of pure MgCl2 (1.55 gMH) using an FO cellulose triacetate nonwoven (CTA-NW) membrane. This was due possibly to the flocculation of aluminum hydroxide in the mixed draw solution that constricted membrane pores, resulting in reduced salt diffusion. Moreover, average water fluxes of 4.09 and 1.74 L/m2-h (LMH) were achieved over 180 min, respectively, when brackish water (5 g/L) and sea water (35 g/L) were used as feed solutions. Furthermore, three types of membrane distillation (MD) membranes were selected for draw solution recovery; of these, a polytetrafluoroethylene membrane with a pore size of 0.45 μm proved to be the most effective in achieving a high salt rejection (99.90%) and high water flux (5.41 LMH) in a diluted draw solution.
机译:正向渗透(FO)已成为一个可行的技术,以缓解全球水资源危机。面对FO技术的应用的最大挑战是缺乏具有高水通量和低反向盐熔剂的理想汲取溶液。因此,本研究的目的是通过降低反向盐通量和保持高的水通量,以增强FO;该方法涉及加入小浓度下Al2(SO4)3的一个的MgCl 2驱动溶液。结果表明,0.5M的MgCl 2的用0.05M下Al2(SO4)3的混合在pH 6.5使用FO三乙酸纤维素非织造材料(CTA-NW)膜比纯的MgCl 2(1.55 GMH)的实现了更低的反向盐通量(0.53 GMH) 。这是可能由于氢氧化铝在该收缩膜孔,从而降低盐扩散混合汲取溶液絮凝。此外,4.09和1.74升/米2·H平均水通量(LMH)在180分钟分别实现,分别,当微咸水(5克/升)和海水(35克/升)作为进料溶液。另外,被选择用于汲取溶液恢复三种类型的膜蒸馏(MD)的膜;其中,具有0.45μm孔径的聚四氟乙烯膜被证明是最有效的实现在稀汲取溶液高的盐截留(99.90%)和高的水通量(5.41 LMH)。

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