Studies of the kinetic and sorption characteristics of OFAM-K and OPMN-P membranes in the process of electron-nanofiltration separation of an aqueous solution of potassium sulfate

D. N. Konovalov, S. I. Lazarev, Pepe Lua, K. K. Polyansky
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Abstract

The paper presents an analysis of existing methods of membrane separation of solutions on semipermeable and ion-exchange membranes, where their advantages and disadvantages are noted. The objects of study were OFAM-K and OPMN-P nanofiltration membranes and aqueous solutions of potassium sulfate used in the production of mineral fertilizers. The change in the retention coefficient on the near-anode OFAM-K membrane for sulfate ions and on the near-cathode membrane OPMN-P for potassium ions was studied at current densities of 12,82 and 15,38 A/m2 with varying transmembrane pressure. An analysis of the retention coefficient of the OPMN-P cathode membrane for potassium ions with increasing pressure shows its increase by 20–30%, which is probably caused by an increase in the water permeability rate, which causes permeate dilution. In the case of analysis of the retention coefficient for sulfate ions on the anode OFAM-K membrane in the region of low current densities, the retention capacity first decreases with an increase in the transmembrane pressure, and then reaches a constant value with a slight increase at a pressure of 1,5 MPa. At higher current densities, the retention coefficient for sulfate ions on the anode OFAM-K membrane with an increase in transmembrane pressure, as well as on the OPMN-P cathode membrane, for potassium ions increases. The time dependences of the specific output flux are given at transmembrane pressures of 0,75, 1, and 1,5 MPa and current densities of 12,82 and 15,38 A/m2. It is noted that the specific output flux increases on the near-anode OFAM-K membrane, while on the near-cathode membrane OPMN-P it decreases with time, which is due to the transformation of the physical properties of the membranes and boundary layers formed on their working surface. On the near-anode OFAM-K membrane, water permeability increases with time, and on the near-cathode membrane OPMN-P it decreases. The presented data on the desorption of potassium ions and sulfate ions on the near-anode membrane OFAM-K and near-cathode membrane OPMN-P indicate that the desorption of ions decreases with time, and the desorption index of potassium ions on the near-anode OFAM-K membrane is higher, although in the process Electronanofiltration ions are transferred in equivalent ratios.
OFAM-K和OPMN-P膜在硫酸钾水溶液电子纳滤分离过程中的动力学和吸附特性研究
本文分析了半透膜和离子交换膜上现有的溶液分离方法,指出了它们的优缺点。研究对象为用于矿质肥料生产的OFAM-K和OPMN-P纳滤膜及硫酸钾水溶液。研究了在电流密度为12、82和15.38 A/m2时,近阳极OFAM-K膜上硫酸盐离子和近阴极OPMN-P膜上钾离子保留系数的变化。分析了OPMN-P阴极膜对钾离子的保留系数随压力的增加而增加了20-30%,这可能是由于水渗透速率的增加导致渗透稀释所致。在低电流密度区域分析阳极OFAM-K膜上硫酸盐离子的保留系数时,保留容量先随着跨膜压力的增加而降低,在压力为1.5 MPa时达到一个恒定值,并略有增加。在较高的电流密度下,阳极OFAM-K膜上硫酸盐离子的保留系数随着跨膜压力的增加而增加,阴极OPMN-P膜上钾离子的保留系数也增加。在跨膜压力分别为0、75、1和1.5 MPa,电流密度分别为12、82和15.38 A/m2时,给出了比输出通量的时间依赖性。在近阳极OFAM-K膜上,比输出通量随时间增加,而在近阴极OPMN-P膜上,比输出通量随时间减少,这是由于膜的物理性质发生了变化,并在其工作表面形成了边界层。近阳极OFAM-K膜的透水性随时间增加而增加,近阴极OPMN-P膜的透水性随时间减少。近阳极膜OFAM-K和近阴极膜OPMN-P对钾离子和硫酸盐离子的解吸数据表明,离子的解吸随时间的延长而减少,近阳极膜OFAM-K对钾离子的解吸指数更高,尽管在电子滤过过程中离子以等比转移。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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