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Challenges in Forward Osmosis of Seawater Using Ammonium Bicarbonate as Osmotic Agent

机译:碳酸氢铵作为渗透剂对海水进行正向渗透的挑战

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This study aimed at exploring whether product quality, membrane fouling and salt reverse flow would be challenges in forward osmosis (FO) of seawater using NH43 as an osmotic agent. Experiments were conducted with a lab scale FO system containing effective membrane area of 95 cm2. Synthetic seawater (SSW) with 3.5-7.0 mg/L boron and a real seawater (RSW) were used as feeds and 1.5-2.5 M NH43 as draw solutions. The experimental operation could be stablized within 0.5 h. For the SSW, boron rejection ranged of 47-85% and increased with increasing water flux while boron in the permeate was greater than 0.8mg/L. Water flux with RSW was 3 times lower than that with SSW, indicating that there might be serious membrane fouling with RSW. It was surprisingly observed that non volatile organic in the FO permeate was 8-10 mg/L, which was from the draw solution although NH43 used was analytical grade. Additional water cost would be $0.4/m3 because of NH43 loss. It was concluded that product quality in terms of high TOC contaminant in NH43 and low boron removal, serious fouling with RSW and salt reverse flow could be challenges for the FO process using NH43 as osmotic agent for seawater desalination.
机译:这项研究旨在探讨使用NH43作为渗透剂对海水进行正向渗透(FO)时,产品质量,膜污染和盐分回流是否会成为挑战。实验使用实验室规模的FO系统进行,该系统的有效膜面积为95 cm2。含3.5-7.0 mg / L硼的合成海水(SSW)和真实海水(RSW)用作进料,而1.5-2.5 M NH43作为汲取溶液。实验操作可以在0.5小时内稳定下来。对于SSW,硼截留率范围为47-85%,并且随着水通量的增​​加而增加,而渗透液中的硼大于0.8mg / L。 RSW的水通量比SSW的水通量低3倍,这表明RSW可能会严重污染膜。令人惊讶地观察到,FO渗透液中的非挥发性有机物为8-10 mg / L,尽管使用的NH43是分析纯,但来自抽提液。由于NH43的损失,额外的水成本为0.4美元/立方米。得出的结论是,就NH43中高TOC污染物和低硼去除,RSW严重结垢和盐回流等方面而言,产品质量可能对使用NH43作为海水淡化渗透剂的FO工艺提出挑战。

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