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Dual-stage forward osmosis/pressure retarded osmosis process for hypersaline solutions and fracking wastewater treatment

机译:高盐溶液和压裂废水的双阶段正向渗透/减压渗透工艺

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摘要

Hypersaline solution with high TDS is not suitable for direct treatment by the conventional membrane and thermal processes. The current study proposes a dual-stage FO/PRO process for hypersaline solution treatment and power generation. The treatment process reduces the concentration of saline wastewater and hence renders it suitable for disposal directly to sea or treatment by the conventional membrane and thermal processes. The draw and feed solutions in the FO process were the hypersaline solutions and wastewater effluent, respectively. Five concentrations were evaluated for the process treatment with different concentrations ranging from 53 g/L to 157 g/L The performance of FO membrane was estimated using pre-developed computer software. The results showed that a higher power can be generated from the PRO-FO system than from the FO-PRO system without compromising the concentration of hypersaline solution after dilution. The study also showed that although increasing the flow rate of draw solution resulted in an increase in the permeate flow rate, it caused a reduction in the dilution of draw solution. On the other hand, the study showed a negligible improvement in the performance of FO membrane upon increasing the feed solution flow rate. Finally, the simulation results showed that the concentration of diluted draw solution was suitable for the conventional membrane and thermal treatments or discharge to seawater after the dual-stage FO membrane treatment.
机译:具有高TDS的高盐溶液不适合通过常规膜和热工艺进行直接处理。当前的研究提出了用于高盐溶液处理和发电的双阶段FO / PRO工艺。该处理过程降低了盐水的浓度,因此使其适合直接排入海中或通过常规的膜和热过程进行处理。 FO过程中的汲取和进料溶液分别是高盐溶液和废水流出物。评估了五个浓度的工艺处理浓度,浓度范围为53 g / L至157 g / L。使用预先开发的计算机软件评估FO膜的性能。结果表明,与FO-PRO系统相比,PRO-FO系统可以产生更高的功率,而不会损害稀释后高盐溶液的浓度。研究还表明,尽管增加汲取溶液的流速会导致渗透液流速的增加,但它会导致汲取溶液的稀释度降低。另一方面,该研究表明,随着进料溶液流速的增加,FO膜性能的改善可忽略不计。最后,模拟结果表明,稀释的汲取溶液的浓度适用于常规的膜和热处理,或者经过两阶段FO膜处理后排入海水。

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