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Morphological architecture of dual-layer hollow fiber for membrane distillation with higher desalination performance

机译:具有更高脱盐性能的膜蒸馏用双层中空纤维的形态结构

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摘要

A new strategy to enhance the desalination performance of polyvinylidene fluoride (PVDF) hollow fiber membrane for membrane distillation (MD) via architecture of morphological characteristics is explored in this study. It is proposed that a dual-layer hollow fiber consisting of a fully finger-like macrovoid inner-layer and a sponge-like outer-layer may effectively enhance the permeation flux while maintaining the wetting resistance. Dual-layer fibers with the proposed morphology have been fabricated by the dry-jet wet spinning process via careful choice of dopes composition and coagulation conditions. In addition to high energy efficiency (EE) of 94%, a superior flux of 98.6 L m~(-2) h~(-1) is obtained during the direct contact membrane distillation (DCMD) desalination experiments. Moreover, the liquid entry pressure (LEP) and long-term DCMD performance test show high wetting resistance and long-term stability. Mathematical modeling has been conducted to investigate the membrane mass transfer properties in terms of temperature profile and apparent diffusivity of the membranes. It is concluded that the enhancement in permeation flux arises from the coupling effect of two mechanisms; namely, a higher driving force and a lower mass transfer resistance, while the later is the major contribution. This work provides an insight on MD fundamentals and strategy to tailor making ideal membranes for DCMD application in desalination industry.
机译:本研究探索了一种通过形态特征结构提高聚偏二氟乙烯(PVDF)中空纤维膜用于膜蒸馏(MD)的脱盐性能的新策略。提出了由完全指状的大孔隙内层和海绵状的外层组成的双层中空纤维可以有效地提高渗透通量,同时保持抗湿性。通过仔细地选择浓液组成和凝结条件,通过干喷湿法纺丝工艺制备了具有建议形态的双层纤维。除了94%的高能效(EE)外,在直接接触膜蒸馏(DCMD)脱盐实验中还获得了98.6 L m〜(-2)h〜(-1)的优异通量。此外,液体进入压力(LEP)和长期DCMD性能测试显示出较高的抗湿性和长期稳定性。已经进行了数学建模以研究温度分布和膜的表观扩散率方面的膜传质特性。结论是渗透通量的增加是由于两种机理的耦合作用引起的。即,较高的驱动力和较低的传质阻力,而后者是主要的贡献。这项工作提供了有关MD基本原理和策略的见解,以量身定制适合DCMD在海水淡化行业中应用的理想膜。

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