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Calcium carbonate scaling in seawater desalination by ammonia-carbon dioxide forward osmosis: Mechanism and implications

机译:氨-二氧化碳正向渗透海水淡化中碳酸钙结垢的机理与意义

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摘要

Forward osmosis (FO) is an osmotically driven membrane process, where the membrane separates a draw solution (DS) with high salinity from a feed solution (FS) with low salinity. There can be a counter direction flow of salt (i.e., salt leakage) that may interact with the water flux through the FO membrane. For the first time reported, this study describes a new calcium carbonate scaling phenomenon in the seawater FO desalination process using ammonium bicarbonate as the DS. The scaling on the membrane surface at the feed side is caused by the interaction between an anion reversely diffused from the DS and a cation present in the FS, causing a significant decline of the water flux. The composition of the scaling layer is dominated by the solubility (represented as solubility product constant, Ksp) of salt formed by the paired anion and cation. Membrane surface morphology plays a crucial role in the reversibility of the scaling. If the scaling occurs on the active layer of the FO membrane, hydraulic cleaning (increasing crossflow velocity) efficiency to restore the water flux is up to 82%. When scaling occurs on the support layer of the FO membrane, the hydraulic cleaning efficiency is strongly reduced, with only 36% of the water flux recovered. The present study reveals the risk of scaling induced by the interaction of feed solute and draw solute, which is different from the scaling caused by the supersaturation in reverse osmosis and other FO studies reported. The scaling investigated in this study can occur with a very low solute concentration at an early stage of the FO process. This finding provides an important implication for selection of draw solution and development of new membranes in the FO process.
机译:正渗透(FO)是渗透驱动的膜工艺,其中膜将高盐度的汲取溶液(DS)与低盐度的进料溶液(FS)分开。盐可能存在逆向流动(即盐泄漏),这可能与通过FO膜的水通量相互作用。首次报道,该研究描述了使用碳酸氢铵作为DS的海水FO脱盐过程中的一种新的碳酸钙结垢现象。进料侧膜表面的结垢是由从DS反向扩散的阴离子与FS中存在的阳离子之间的相互作用引起的,从而导致水通量显着下降。结垢层的组成主要是由成对的阴离子和阳离子形成的盐的溶解度(表示为溶解度常数,Ksp)。膜表面形态在结垢的可逆性中起关键作用。如果在FO膜的活性层上发生结垢,则用于恢复水通量的液压清洁(增加错流速度)效率最高可达82%。当在FO膜的支撑层上发生结垢时,水力清洁效率会大大降低,只有36%的水通量得以回收。本研究揭示了进料溶质和吸引溶质相互作用引起的结垢风险,这与反渗透和其他FO研究中过饱和引起的结垢不同。在本研究中研究的结垢可能在FO过程的早期以非常低的溶质浓度发生。这一发现为在FO工艺中选择溶液和开发新膜提供了重要的启示。

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