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The effect of net-type spacer on the performance of direct contact membrane distillation system for seawater desalination: Heat and mass transfer analysis

机译:净间隔器对海水淡化直接接触膜蒸馏系统性能的影响:传热和传质分析

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This work aims to study the effects of the net-type spacer on the performance of direct contact membrane distillation (DCMD) modules. Laminar and k - ω SST turbulence models are used to conduct simulations in three-dimensional modules with and without spacers. The spacers are placed in the middle of the feed and permeate channel. The net type spacers of diameter 0.25h and 0.5h were considered, where h is the height of each channel. The inlet temperature of the feed and the permeate channel set to 353 K and 293 K. The feed Reynolds number is varied (500, 1500) while the permeate Reynolds number is fixed at 330. We revealed that the presence of spacer in the flow channels mitigates both the temperature and the concentration polarization and yields higher vapor permeation. We also showed that the module containing larger size spacers yields better flux performance and lower level of temperature and concentration polarization. Moreover, the modules containing spacers become more efficient as the feed flow rate is increased.
机译:这项工作旨在研究网型间隔物对直接接触膜蒸馏(DCMD)模块性能的影响。层流和k-ωSST湍流模型用于在带有和不带有间隔物的三维模块中进行仿真。间隔物放置在进料和渗透通道的中间。考虑了直径为0.25h和0.5h的网型隔片,其中h是每个通道的高度。进料和渗透通道的入口温度设置为353 K和293K。进料雷诺数变化(500,1500),而渗透雷诺数固定为330。我们发现流道中存在间隔物减轻了温度和浓差极化,并产生了更高的蒸汽渗透性。我们还表明,包含较大间隔物的模块可产生更好的通量性能,并具有较低的温度和浓度极化水平。此外,随着进料流速的增加,包含间隔物的模块变得更加有效。

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