首页> 美国卫生研究院文献>Membranes >Fouling Mitigation by Optimizing Flow Rate and Pulsed Electric Field during Bipolar Membrane Electroacidification of Caseinate Solution
【2h】

Fouling Mitigation by Optimizing Flow Rate and Pulsed Electric Field during Bipolar Membrane Electroacidification of Caseinate Solution

机译:通过优化酪乳酸酯溶液的双极膜电气涂覆过程中流速和脉冲电场进行污垢缓解

代理获取
本网站仅为用户提供外文OA文献查询和代理获取服务,本网站没有原文。下单后我们将采用程序或人工为您竭诚获取高质量的原文,但由于OA文献来源多样且变更频繁,仍可能出现获取不到、文献不完整或与标题不符等情况,如果获取不到我们将提供退款服务。请知悉。

摘要

The efficiency of separation processes using ion exchange membranes (IEMs), especially in the food industry, is significantly limited by the fouling phenomenon, which is the process of the attachment and growth of certain species on the surface and inside the membrane. Pulsed electric field (PEF) mode, which consists in the application of constant current density pulses during a fixed time (Ton) alternated with pause lapses (Toff), has a positive antifouling impact. The aim of this study was to investigate the combined effect of three different relatively high flow rates of feed solution (corresponding to Reynolds numbers of 187, 374 and 560) and various pulse–pause ratios of PEF current regime on protein fouling kinetics during electrodialysis with bipolar membranes (EDBM) of a model caseinate solution. Four different pulse/pause regimes (with Ton/Toff ratios equal to 10 s/10 s, 10 s/20 s, 10 s/33 s and 10 s/50 s) during electrodialysis (ED) treatment were evaluated at a current density of 5 mA/cm2. It was found that increasing the pause duration and caseinate solution flow rate had a positive impact on the minimization of protein fouling occurring on the cationic surface of the bipolar membrane (BPM) during the EDBM. Both a long pause and high flow rate contribute to a more effective decrease in the concentration of protons and caseinate anions at the BPM surface: a very good membrane performance was achieved with 50 s of pause duration of PEF and a flow rate corresponding to Re = 374. A further increase in PEF pause duration (above 50 s) or flow rate (above Re = 374) did not lead to a significant decrease in the amount of fouling.
机译:使用离子交换膜(IEM),特别是在食品工业中的分离过程的效率受到污垢现象的显着限制,这是表面和膜内的某些物种的附着和生长的过程。脉冲电场(PEF)模式包括在固定时间(吨)在与暂停停滞(Toff)交替的固定时间(TOFF)中施加恒流密度脉冲的应用具有积极的防污影响。本研究的目的是研究三种不同饲料溶液的综合效应(对应于187,374和560的Reynolds数)和PEF在电渗析中蛋白质污染动力学的PEF电流制度的各种脉冲暂停比率模型酪蛋白酸酯溶液的双极膜(EDBM)。在电渗析(ED)处理期间,在电渗析(ED)处理期间,四个不同的脉冲/暂停方案(具有等于10 s / 10 s,10 s,10 s / 33s和10 s / / 33s和10 s / 50s)的脉冲/暂停状态5 mA / cm2。发现增加暂停持续时间和酪乳酸酯溶液流速对EDBM期间双极膜(BPM)的阳离子表面上发生的蛋白质污染最小化的积极影响。长暂停和高流量均有助于在BPM表面的质子浓度和酪蛋白酸盐阴离子的更有效降低:通过PEF的暂停持续时间和对应于RE =的流速来实现非常好的膜性能。 374. PEF暂停持续时间的进一步增加(高于50秒)或流速(上述RE = 374)不会导致污垢量的显着降低。

著录项

  • 期刊名称 Membranes
  • 作者单位
  • 年(卷),期 2021(11),7
  • 年度 2021
  • 页码 534
  • 总页数 18
  • 原文格式 PDF
  • 正文语种
  • 中图分类 外科学;
  • 关键词

    机译:电化学酸化;电渗析;酪蛋白;浓度极化;离子交换膜;污垢;雷诺数;当前模式;暂停持续时间;

相似文献

  • 外文文献
  • 专利
代理获取

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号