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A Combined Forward Osmosis and Membrane Distillation System for Sidestream Treatment

机译:联合正渗透和膜蒸馏系统用于侧流处理

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Separate treatment of high-nutrient sidestream is an efficient and cost effective way to decrease the loading on the main plant, resulting in lower effluent nutrient concentration. This study investigated the use of a combined forward osmosis-membrane distillation (FO-MD) system for the removal of nitrogen present in high concentration in sidestream from anaerobic digestion process. The combined system was able to achieve almost 100% rejection of solids and acetic acid, and more than 98% rejection of NH_3-N from the sidestream. The high rejection of NH_3-N was mainly achieved by the FO process. The solids in the feed solution contributed to fouling problem in both FO and MD, resulting in significant decline in flux. However, 76% or higher flux recovery was achieved for FO membrane by cleaning with tap water. We observed that flux recovery was due to removal of solids from the membrane surface by the cleaning process. FO membrane also demonstrated excellent performance for continuous operation when cleaned for 15 min in every 24 h interval. Overall, the combined FO-MD system was found to be an effective solution for treatment of nutrient rich sidestream.
机译:高养分侧流的分离处理是减少主要植物负荷,降低污水中养分浓度的一种有效且具有成本效益的方法。这项研究调查了使用组合式正渗透膜蒸馏(FO-MD)系统从厌氧消化过程中去除侧流中高浓度氮的情况。合并的系统能够实现几乎100%的固体和乙酸截留率,以及98%以上的侧流NH_3-N截留率。 NH_3-N的高排阻主要是通过FO工艺实现的。进料溶液中的固体导致FO和MD结垢问题,导致通量显着下降。但是,通过用自来水清洗,FO膜的通量回收率达到了76%或更高。我们观察到通量恢复是由于通过清洁过程从膜表面去除了固体。 FO膜在每24小时间隔清洁15分钟后,还表现出出色的连续操作性能。总体而言,组合式FO-MD系统被认为是处理富含营养物的侧流的有效解决方案。

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