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Performance evaluation of reverse osmosis (RO) pre-treatment technologies for in-land brackish water treatment

机译:内陆微咸水处理的反渗透(RO)预处理技术性能评估

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摘要

Integration of renewable energy with desalination technologies has emerged as an attractive solution to augment fresh water supply sustainably. Fouling and scaling are still considered as limiting factors in membrane desalination processes. For brackish water treatment, pre-treatment of reverse osmosis (RO) feed water is a key step in designing RO plants avoiding membrane fouling. This study aims to compare at pilot scale the rejection efficiency of RO membranes with multiple pre-treatment options at different water recoveries (30, 35, 40, 45 and 50%) and TDS concentrations (3500, 4000, and 4500mg/L). Synthetic brackish water was prepared and performance evaluation were carried out using brackish water reverse osmosis (BWRO) membranes (Filmtec LC-LE-4040 and Hydranautics CPA5-LD-4040) preceded by 5 and 1μm cartridge filters, 0.02μm ultra-filtration (UF) membrane, and forward osmosis (FO) membrane using 0.25M NaCl and MgCl2 as draw solutions (DS). It was revealed that FO membrane with 0.25M MgCl2 used as a draw solution (DS) and Ultra-filtration (UF) membrane followed by Filmtec membrane gave overall 98% rejection but UF facing high fouling potential due to high applied pressure. Use of 5 and 1μm cartridge filter prior to Filmtec membrane also showed effective results with 95% salt rejection.
机译:可再生能源与海水淡化技术的集成已成为一种吸引人的解决方案,可以可持续地增加淡水供应。结垢和结垢仍被认为是膜脱盐过程中的限制因素。对于微咸水处理,反渗透(RO)进水的预处理是设计避免膜污染的反渗透设备的关键步骤。这项研究的目的是在不同的水回收率(30%,35%,40%,45%和50%)和TDS浓度(3500、4000和4500mg / L)下,以中试规模比较具有多种预处理选项的RO膜的截留效率。制备了微咸水,并使用微咸水反渗透(BWRO)膜(Filmtec LC-LE-4040和Hydranautics CPA5-LD-4040)进行了性能评估,随后使用了5和1μm的筒式过滤器,0.02μm的超滤(UF)膜和使用0.25M NaCl和MgCl2作为汲取溶液(DS)的正渗透(FO)膜。结果表明,使用0.25M MgCl2作为吸收溶液(DS)的FO膜和随后采用Filmtec膜的超滤(UF)膜的总截留率达98%,但由于高施加压力,UF面临着高结垢的可能性。在Filmtec膜之前使用5和1μm的筒式过滤器也显示出95%的脱盐效果。

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