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Optimization of microstructured hollow fiber design for membrane distillation applications using CFD modeling

机译:用CFD模型优化膜蒸馏应用的微结构中空纤维设计

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摘要

This study explores the potential of microstructured hollow fiber designs to enhance process performance in a direct contact membrane distillation (DCMD) system. Hollow fibers with 10 different geometries (wavy- and gear-shaped cross sections) were evaluated. A series of three-dimensional computational fluid dynamic (CFD) simulations were carried out to investigate their capability in terms of depolarizing the buildup of liquid boundary layers, thus improving water productivity.\ud\udAnalyses of heat and mass transfer as well as the flow-field distribution in respective MD modules were obtained. It was found that the enhancement of the heat-transfer coefficients, hf, was up to 4.5-fold for a module with a wavy fiber design 07 and an approximate 5.5-fold hp increase for a gear-shaped fiber design. The average temperature polarization coefficient and mass flux Nm of the gear-shaped fiber module showed an improvement of 57% and 66%, respectively, over the original straight fiber design, followed by the wavy designs 07 and 08. The enhanced module performance was attributed to the improved hydrodynamics through the flow channels of various fiber geometries, which was confirmed by the visualization of flow-field and temperature profiles in CFD. Investigations of the fiber-length effect showed that the gear-shaped fiber modules exhibited the highest flux enhancement of 57–65% with the same length, compared to the modules with original straight and wavy fibers.\ud\udIn addition, the gear-shaped fiber module is very sensitive to feed velocity changes. Therefore, employing a smart microstructured design on the membrane surface would bring in a significant improvement under adverse flow conditions. Moreover, the computed water production and hydraulic energy consumption (HEC) among the modules with various fiber geometries were compared. With 1.9-fold surface area increase per unit volume, the gear-shaped fiber configuration had the highest water production but the lowest HEC, followed by wavy designs 07 and 08.
机译:这项研究探索了微结构化中空纤维设计在直接接触膜蒸馏(DCMD)系统中增强工艺性能的潜力。对具有10种不同几何形状(波浪形和齿轮形横截面)的中空纤维进行了评估。进行了一系列三维计算流体动力学(CFD)模拟,以研究它们在消弱液体边界层堆积方面的能力,从而提高了水的生产率。\ ud \ ud分析了传热和传质以及流动获得了各个MD模块中的磁场分布。已经发现,对于具有波浪形纤维设计07的模块,传热系数hf的提高高达4.5倍,对于齿轮形纤维设计的传热系数提高了约5.5倍。齿轮形光纤模块的平均温度极化系数和质量通量Nm分别比原始的直纤维设计和波形设计07和08分别提高了57%和66%。通过各种纤维几何形状的流道改善了流体动力学,这一点已通过CFD中流场和温度分布的可视化得到证实。对纤维长度效应的研究表明,与原始长度的直线形和波浪形纤维相比,在相同的长度下,齿轮形纤维组件显示出57-65%的最高通量增强。\ ud \ ud异形纤维模块对进料速度变化非常敏感。因此,在不利的流动条件下,在膜表面采用智能微结构设计将带来显着改善。此外,比较了具有各种纤维几何形状的模块之间的计算出的产水量和水力消耗(HEC)。随着单位体积表面积增加1.9倍,齿轮状纤维结构的出水量最高,但HEC最低,其后是波浪形设计07和08。

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