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Ion-exchange-ultrafiltration system for surfactants removal from water solutions

机译:离子交换超滤系统,用于从水溶液中去除表面活性剂

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Studies were performed to determine the effectiveness of hybrid system combining ion exchange and ultrafiltration for surfactant separation from water solutions. During the experiments the influence of membrane cut-off, type of ion-exchange resin, resin dose and contact time was evaluated. The results obtained for the hybrid system were also compared with the effectiveness of the single processes, i.e. ultrafiltration and ion exchange. It was found that the combination of ion exchange and ultrafiltration was more effective in surfactant removal than ultrafiltration process alone. In the hybrid system because of the resin presence, the systematic increase in surfactant separation along with the filtration time was noticed. From among the ion-exchange resins tested the most effective was MIEX~R one. For the smallest resin dose equal to 5 cm~3/dm~3 the reduction of anionic surfactants from model solution with concentration of 0.25 CMC reached almost 100% for the hybrid process with 30 kDa polyethersulfone membrane. The retention coefficient of anionic surfactant achieved by the ion-exchange-ultrafiltration system with A100 and A200 resins was lower and amounted to 47% and 94% after 60 min of the process, respectively.
机译:进行了研究以确定结合离子交换和超滤的混合体系对于从水溶液中分离表面活性剂的有效性。在实验过程中,评估了膜截留率,离子交换树脂类型,树脂用量和接触时间的影响。还将从混合系统获得的结果与单个过程即超滤和离子交换的有效性进行了比较。发现离子交换和超滤的组合比单独的超滤过程更有效地去除表面活性剂。在混合体系中,由于存在树脂,注意到表面活性剂分离随着过滤时间的系统增加。在测试的离子交换树脂中,最有效的是MIEX〜R。对于等于5 cm〜3 / dm〜3的最小树脂剂量,在30 kDa聚醚砜膜的混合工艺中,阴离子表面活性剂从0.25 CMC浓度的模型溶液中的还原几乎达到100%。通过离子交换-超滤系统使用A100和A200树脂获得的阴离子表面活性剂的保留系数较低,在处理60分钟后分别达到47%和94%。

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