直接接触膜蒸馏低能脱盐:浓度极化研究

Khadije El Kadi, I. Janajreh
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引用次数: 0

摘要

浓度和温度极化引起的膜污染是制约膜蒸馏技术发展的主要因素。然而,由于实验装置的复杂性,浓度极化(CP)现象在该领域的评价中一直没有得到重视。这一工作为直接接触MD中CP的数值观察和评价提供了更深入的见解。建立了非等温稳态多组分流动的计算流体动力学模型,并将其耦合在一起,模拟了CP在料膜界面处的局部效应。此外,还建立了一个集成隔离剂的改进模型,以研究隔离剂在降低膜表面CP效应从而提高膜性能方面的实用性。该模型成功地捕获了海水淡化在典型工况下进料通道内的CP分布,并记录了其浓度极化系数(CPC)为2.5。考虑到这个值,质量通量评估下降了6%。另一方面,间隔进料通道使CPC降至1.83,证明了间隔剂在混合流动中的作用,减缓了浓度极化的发展。
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Low Energy Desalination via Direct Contact Membrane Distillation: Looking Into the Concentration Polarization
Membrane fouling due to concentration and temperature polarization is at the top list of restrictions for membrane distillation (MD) development. Yet, concentration polarization (CP) phenomenon has not been taken seriously in the evaluation of MD mass flux throughout the history of this field due to the complexity in the experimental setup. This work gives more insight into the observation and evaluation of CP in direct contact MD numerically. Computational fluid dynamics models of non-isothermal steady multi-species flow are conducted and coupled together to simulate the localized effect of CP at the feed-membrane interface. Additionally, a modified model with integrated spacers is also developed to investigate the practicality of spacers in reducing the CP effect at membrane surface and hence enhancing the performance. The model successfully captures the CP distribution in the feed channel where a concentration polarization coefficient (CPC) of 2.5 is recorded for seawater desalination running under typical operational conditions. Taking this value into consideration, a drop of 6% in mass flux evaluation is observed. On the other hand, spaced feed channel found to reduce CPC down to 1.83 proving the role of spacer in mixing the flow and mitigate the development of concentration polarization.
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