Development of a hardware configuration and a calculating program for a membrane plant equipped with polarization layer separation units

B. Lobasenko, A. Shafray, M. Prosin, A. Semenov, A. Kakimov, A. Akimov
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Abstract

Various types of membrane units, including standard units for permeate separating, which are currently used for various liquids processing, are considered. Their advantages and disadvantages, working conditions and operating features are assessed. The principle of operation of membrane units with the bleed of the polarization layer is analyzed. A distinctive feature of such devices is the separation of the feed stream into three parts: adjacent to the membrane, including a polarization layer, with an increased concentration of high molecular substances (HMS) – concentrate, a spent stream core to be re-processed – retentate, and permeate, that practically contains no HMS. The unit scheme and the principle of operation of the plant completed with this equipment are given. A feature of this plant is the parallel arrangement of the membrane devices. In this configuration of the plant, there are two flow circulation loops and two tanks, in one of which there will be a depleted solution, in the other the retentate. During operation, the circulation of the depleted flow is provided. In this case, the resulting polarization layer (concentrate) will be discharged into the second tank. The working process continues until the complete depletion of the solution in the first tank. In the event that the solution in this tank is exhausted, and the required concentration of the product has not been reached, the second tank with the concentrate activates and the process continues. The principle of operation in this case is similar. The rotation of tanks continues until the required degree of concentration of the product is obtained. A calculation algorithm, a block diagram and a program for calculating the operating time of a membrane installation are proposed, for which a certificate of state registration of a computer program has been obtained. The calculation algorithm and program interface are presented. This program makes it possible to predict the operation of such installations and provides for the possibility of optimizing their operation.т.п.)
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研制了配备极化层分离装置的膜装置的硬件配置和计算程序
考虑了目前用于各种液体处理的各种类型的膜单元,包括渗透分离的标准单元。评估了它们的优缺点、工作条件和操作特点。分析了带极化层渗漏的膜装置的工作原理。这种装置的一个显著特点是将进料流分成三部分:靠近膜的部分,包括一个极化层,其中含有高浓度的高分子物质(HMS) -浓缩物,待再处理的废流核心-保留物和渗透物,实际上不含HMS。给出了用该装置完成的装置方案和运行原理。该装置的一个特点是膜装置的平行布置。在工厂的这种配置中,有两个流动循环回路和两个储罐,其中一个储罐中将有耗尽的溶液,另一个储罐中将有保留液。在运行期间,提供了耗尽流体的循环。在这种情况下,产生的极化层(浓缩物)将被排放到第二个罐中。工作过程一直持续到第一个槽内的溶液完全耗尽。如果这个罐中的溶液被用尽,而产品的所需浓度没有达到,则装有浓缩物的第二个罐中被激活,该过程继续进行。这种情况下的操作原理是相似的。继续旋转储罐,直到获得所需的产品浓度。提出了膜装置运行时间的计算算法、框图和程序,并获得了计算机程序的国家注册证书。给出了计算算法和程序接口。该程序可以预测此类装置的运行,并提供优化其operation.т.п的可能性。)
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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