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Enhancement of brackish water desalination using hybrid membrane distillation and reverse osmosis systems

机译:使用混合膜蒸馏和反渗透系统增强微咸水脱盐

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摘要

Desalination of geothermal brackish water by membrane distillation (MD) provides a low recovery rate, but integrating MD with reverse osmosis (RO) can maximize the production rate. In this study, different design configurations of a hybrid system involving brine recycling and cascading are studied via simulations, and the performance improvement due to the process integration is substantiated via the increased recovery rate and reduced specific energy consumption. Brine recycling is also found to improve the recovery rate considerably to 40% at an energy cost of 0.9 $/m3. However, this achievement is only valid when the final brine is recycled to the RO feed: when the final brine is recycled to the MD feed, the overall performance degrades because the recycled brine cools the feed and causes a serious reduction in the driving force and the consequent production rate. Configuring the hybrid system in multiple stages connected in series increases the recovery rate to 90% and reduces the specific energy consumption to 0.9 MJ/kg. Although the specific energy cost increases dramatically because external inter-stage heating is implemented, using a free energy source (such as a geothermal or waste-energy source) for inter-stage heating could provide the optimum configuration.
机译:通过膜蒸馏(MD)对地热微咸水进行脱盐处理的回收率较低,但是将MD与反渗透(RO)集成可以使生产率最大化。在这项研究中,通过模拟研究了涉及盐水再循环和级联的混合系统的不同设计配置,并且由于提高了回收率并降低了比能耗,从而证明了由于过程集成而导致的性能提高。还发现盐水的回收可以以0.9 $ / m 3 的能源成本将回收率显着提高到40%。但是,此成就仅在将最终盐水再循环到RO进料中时才有效:当将最终盐水再循环到MD进料时,整体性能会降低,因为再循环的盐水会冷却进料并导致驱动力和动力的显着降低。结果生产率。在串联连接的多个阶段中配置混合动力系统可将回收率提高到90%,并将单位能耗降低到0.9 MJ / kg。尽管由于实施了外部级间加热而使特定能源成本急剧增加,但是使用自由能源(例如地热或废物能源)进行级间加热可以提供最佳配置。

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