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时变压力分布下的间歇式反渗透海水淡化建模

Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile.

作者信息

Chougradi Abdeljalil, Zaviska François, Abed Ahmed, Harmand Jerome, Jellal Jamal-Eddine, Heran Marc

机构信息

Civil Engineering Department, Mohammadia School of Engineering, Mohammed V University, Rabat 10090, Morocco.

Institut Européen des Membranes, UMR 5635, CNRS, ENSCM, University of Montpellier, 34095 Montpellier, France .

出版信息

Membranes (Basel). 2021 Feb 28;11(3):173. doi: 10.3390/membranes11030173.

Abstract

As world demand for clean water increases, reverse osmosis (RO) desalination has emerged as an attractive solution. Continuous RO is the most used desalination technology today. However, a new generation of configurations, working in unsteady-state feed concentration and pressure, have gained more attention recently, including the batch RO process. Our work presents a mathematical modeling for batch RO that offers the possibility of monitoring all variables of the process, including specific energy consumption, as a function of time and the recovery ratio. Validation is achieved by comparison with data from the experimental set-up and an existing model in the literature. Energetic comparison with continuous RO processes confirms that batch RO can be more energy efficient than can continuous RO, especially at a higher recovery ratio. It used, at recovery, 31% less energy for seawater and 19% less energy for brackish water. Modeling also proves that the batch RO process does not have to function under constant flux to deliver good energetic performance. In fact, under a linear pressure profile, batch RO can still deliver better energetic performance than can a continuous configuration. The parameters analysis shows that salinity, pump and energy recovery devices efficiencies are directly linked to the energy demand. While increasing feed volume has a limited effect after a certain volume due to dilution, it also shows, interestingly, a recovery ratio interval in which feed volume does not affect specific energy consumption.

摘要

随着全球对清洁水的需求增加,反渗透(RO)海水淡化已成为一种有吸引力的解决方案。连续反渗透是当今最常用的海水淡化技术。然而,新一代在非稳态进料浓度和压力下运行的配置最近受到了更多关注,包括间歇式反渗透工艺。我们的工作提出了一种间歇式反渗透的数学模型,该模型能够监测该过程的所有变量,包括特定能耗随时间和回收率的变化。通过与实验装置的数据以及文献中现有模型的数据进行比较来实现验证。与连续反渗透工艺的能量比较证实,间歇式反渗透比连续反渗透更节能,尤其是在较高回收率时。在回收率方面,处理海水时能耗降低31%,处理微咸水时能耗降低19%。建模还证明,间歇式反渗透工艺不必在恒定通量下运行就能实现良好的能量性能。事实上,在线性压力分布下,间歇式反渗透仍能比连续配置提供更好的能量性能。参数分析表明,盐度、泵和能量回收装置的效率与能量需求直接相关。虽然进料量在达到一定量后因稀释而对能耗的影响有限,但有趣的是,它也显示出一个进料量不影响特定能耗的回收率区间。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/ba83/7997241/a57c37e764e8/membranes-11-00173-g001.jpg

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