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Heat-transfer performance comparison between overlapped and woven spacers for membrane distillation

机译:重叠和机织隔片之间用于膜蒸馏的传热性能比较

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摘要

Sustainable production of fresh water from seawater desalination is a problem of crucial importance nowadays. Recently, some desalination technologies are taking advantage from the coupling with renewable resources. Among emerging technologies, Membrane Distillation (MD) is considered as one of the most promising as it can be easily powered by solar thermal energy or waste-heat.udAs an emerging technology, efforts are required to optimize MD unit geometry and operating conditions in order to reduce fresh water production specific cost. udTemperature polarization phenomenon is a well-known detrimental effect for the MD process. Spacers are traditionally used to enhance mixing and shrink temperature boundary layers yet yielding higher pressure-losses. The present work is devoted to testing the performance of two different two-layer net-spacers: overlapped and woven. Investigations were carried out by both experiments and Computational Fluid Dynamics (CFD) simulations at different Reynolds numbers ranging from creeping to turbulent flow regime. Experiments (intermediate to high Re) were performed via a novel experimental technique making use of thermochromic liquid crystals and digital image analysis. Computational data (low to intermediate Re) were obtained via steady state (low Re) and Direct Numerical Simulations (intermediate Re), adopting the Unit Cell approach. A good agreement between experiments and CFD data was found in the range of superposition.udResults showed that woven spacers guarantee a better mixing than overlapped ones especially in the low-intermediate range of Re thus resulting into a higher Nusselt number. On the other hand, the less disturbed flow field induced by the overlapped wires was found to give raise to lower pumping losses.
机译:如今,海水淡化可持续生产淡水已成为至关重要的问题。最近,一些海水淡化技术正在与可再生资源结合使用。在新兴技术中,膜蒸馏(MD)被认为是最有前途的技术之一,因为它可以很容易地由太阳能或废热提供动力。 ud作为一项新兴技术,需要努力优化MD装置的几何形状和运行条件。为了减少淡水生产的具体成本。温度极化现象是MD过程的众所周知的有害影响。传统上,垫片用于增强混合和收缩温度边界层,但会产生更高的压力损失。本工作致力于测试两种不同的两层网状隔圈的性能:重叠和编织。通过实验和计算流体力学(CFD)模拟,在从蠕变到湍流状态的不同雷诺数下进行了研究。通过使用热致变色液晶和数字图像分析的新型实验技术进行了实验(中级至高Re)。计算数据(低到中等Re)是通过稳态(低Re)和直接数值模拟(中间Re)获得的,采用的是单元格方法。实验结果与CFD数据在重叠范围内发现了很好的一致性。 ud结果表明,织造的隔圈比重叠的隔圈保证更好的混合,尤其是在Re的低中间范围内,从而得到更高的Nusselt数。另一方面,发现由重叠的导线引起的较少扰动的流场引起较低的泵送损失。

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