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Optimising thermal efficiency of direct contact membrane distillation by brine recycling for small-scale seawater desalination

机译:通过盐水循环用于小规模海水淡化来优化直接接触膜蒸馏的热效率

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摘要

A technique to optimise thermal efficiency using brine recycling during direct contact membrane distillation (DCMD) of seawater was investigated. By returning the hot brine to the feed tank, the system water recovery could be increased and the sensible heat of the hot brine was recovered to improve thermal efficiency. The results show that in the optimal water recovery range of 20 to 60% facilitated by brine recycling, the specific thermal energy consumption of the process could be reduced by more than half. It is also noteworthy that within this optimal water recovery range, the risk of membrane scaling is negligible - DCMD of seawater at a constant water recovery of 70% was achieved for over 24. h without any scale formation on the membrane surface. In contrast, severe membrane scaling was observed when water recovery reached 80%. In addition to water recovery, other operating conditions such as feed temperature and water circulation rates could influence the process thermal efficiency. Increasing the feed temperature and reducing the circulation flow rates increased thermal efficiency. Increasing the feed temperature could also mitigate the negative effect of elevated feed concentration on the distillate flux, particularly at a high water recovery.
机译:研究了在海水的直接接触膜蒸馏(DCMD)过程中利用盐水循环利用来优化热效率的技术。通过将热盐水返回给料罐,可以增加系统的水回收率,并回收热盐水的显热以提高热效率。结果表明,在盐水再循环的促进下,在20%至60%的最佳水回收率范围内,该过程的比热能消耗可减少一半以上。还值得注意的是,在此最佳水回收率范围内,膜结垢的风险可忽略不计-在超过24. h的时间内,以70%的恒定水回收率实现了海水的DCMD,而膜表面未形成任何水垢。相反,当水回收率达到80%时,观察到严重的膜结垢。除了回收水以外,其他操作条件(例如进料温度和水循环速率)也可能影响过程的热效率。升高进料温度并降低循环流速可提高热效率。进料温度的升高还可以减轻进料浓度升高对馏分通量的负面影响,特别是在高水回收率下。

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