MemBrain s. r. o. (Membrane Innovation Center), Pod Vinicí 87, 471 27 Stráž pod Ralskem, Czech Republic.
Int J Mol Sci. 2019 Apr 18;20(8):1918. doi: 10.3390/ijms20081918.
Electrodialysis (ED) is frequently used in the desalination of whey. However, the fouling onto the membrane surface decreases the electrodialysis efficiency. Pulsed Electrodialysis Reversal (PER), in which short pulses of reverse polarity are applied, is expected to decrease the fouling onto membrane surface during ED. Three (PER) regimes were applied in the desalination of acid whey (pH ≤ 5) to study their effects on the membrane fouling and the ED efficiency. The PER regimes were compared to the conventional ED as the control. For each regime, two consecutive runs were performed without any cleaning step in-between to intensify the fouling. After the second run, the membranes were subjected to the Scanning electron microscope (SEM) imaging and contact angle measurement to investigate the fouling on the membrane surface in different regimes. The ED parameters in the case of conventional ED were almost the same in the first and the second runs. However, the parameters related to the ED efficiency including ED capacity, ash transfer, and ED time, were deteriorated when the PER regimes were applied. The contact angle values indicated that the fouling on the diluate side of anion exchange membranes was more intensified in conventional ED compared to the PER regimes. The SEM images also showed that the fouling on the diluate side of both cation and anion exchange membranes under PER regimes was reduced in respect to the conventional ED. However, the back transfer to the diluate compartment when the reverse pulse was applied is dominant and lowers the ED efficiency slightly when the PER is applied.
电渗析(ED)常用于乳清的脱盐。然而,膜表面的结垢会降低电渗析效率。脉冲电渗析反向(PER),即在电渗析过程中施加短时间的反向极性脉冲,有望减少 ED 过程中膜表面的结垢。在酸性乳清(pH≤5)的脱盐中应用了三种(PER)模式,以研究它们对膜结垢和 ED 效率的影响。PER 模式与传统 ED 作为对照进行比较。对于每种模式,在两次运行之间不进行任何清洗步骤,以强化结垢。第二次运行后,对膜进行扫描电子显微镜(SEM)成像和接触角测量,以研究不同模式下膜表面的结垢情况。在传统 ED 的情况下,ED 参数在第一次和第二次运行中几乎相同。然而,当应用 PER 模式时,与 ED 效率相关的参数,包括 ED 容量、灰分转移和 ED 时间,都恶化了。接触角值表明,与 PER 模式相比,在传统 ED 中,阴离子交换膜稀释侧的结垢更为严重。SEM 图像还表明,与传统 ED 相比,PER 模式下阳离子和阴离子交换膜稀释侧的结垢减少。然而,当施加反向脉冲时,反向转移到稀释室是占主导地位的,并且当 PER 应用时,ED 效率会略有降低。