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Combination of continuous diffusion dialysis and electrodialysis for separating NaOH/NaAlO_2 solution

机译:连续扩散渗析与电渗析相结合分离NaOH / NaAlO_2溶液

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Diffusion dialysis (DD), driven by concentration gradient, has inherent defects such as significant water osmosis, low transport rate, and recovery ratio. Meanwhile, electrodialysis (ED) is driven by electric field, which has high transport rate but consumes significant energy. Hence, the DD and ED processes are combined here to separate NaOH/NaAlO2 solution. The continuous DD process is first used to separate the alkaline solution, which is equipped with self-prepared polyvinyl alcohol (PVA)-based cation exchange membrane. The running condition is optimized at feed flow rate of 0.83 L m(-1) h(-1) and water flow rate of 1.0 L m(-1) h(-1), which can obtain recovered NaOH of 0.66 mol L-1 (M), recovery ratio of 44.4%, and rejection ratio of 91.2%. The residual liquor is further separated by ED process. The ED process running at 20 mA cm(-2) for 2 h can recover 0.40 M NaOH. The current efficiency is 79.4% and the energy consumption is 2.2 kWh kg(-1). The combination of DD and ED processes can remove 97.9% NaOH with the AlO2-rejection ratio of 85.4%. The energy is greatly saved due to insignificant energy consumption in DD process. Hence, the combination can elevate separation efficiency and save energy.
机译:由浓度梯度驱动的扩散透析(DD)具有固有的缺陷,例如明显的水渗透,低传输速率和回收率。同时,电渗析(ED)是由电场驱动的,该电场具有较高的传输速率但消耗大量能量。因此,这里将DD和ED工艺结合起来以分离NaOH / NaAlO2溶液。连续DD工艺首先用于分离碱性溶液,该溶液配有自备的基于聚乙烯醇(PVA)的阳离子交换膜。在进料流速为0.83 L m(-1)h(-1)和水流速为1.0 L m(-1)h(-1)的条件下优化了运行条件,可以获得的回收NaOH为0.66 mol L- 1(M),回收率44.4%,废品率91.2%。残留液通过ED工艺进一步分离。 ED过程在20 mA cm(-2)下运行2小时可以回收0.40 M NaOH。当前效率为79.4%,能耗为2.2 kWh kg(-1)。 DD和ED工艺的组合可以去除97.9%的NaOH,AlO2的去除率为85.4%。由于DD过程中的能耗很小,因此大大节省了能量。因此,该组合可以提高分离效率并节省能量。

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