电渗析法合成高效聚合氯化铝的研究

采用了一种新的电渗析法制备聚合氯化铝.该法的特点是以2张阴离子交换膜构成反应室,确定了影响有效铝聚合形态的电化学和溶液化学因素,成功地制备出有效絮凝成分Alb含量60％以上的优质聚合氯化铝液体产品.水处理絮凝实验结果证明,电渗析法制备的聚合氯化铝的絮凝效果明显优于硫酸铝,与普通聚合氯化铝相当.     

逆电渗析反应器阴、阳极联合降解酸性橙Ⅱ实验研究

通过对由溶液浓差能驱动的逆电渗析(RED)反应器阴、阳极联合降解酸性橙Ⅱ模拟废水串、并联两种流程的实验研究,结果发现:在膜电势作用下,有机废水流经RED反应器阴、阳极时会生成两种强氧化剂—次氯酸(HClO)和过氧化氢(H_2O_2),在强氧化剂的作用下废水中有机物会发生氧化降解.在通过正交实验方法获得的最佳操作条件下,对1 L浓度为150 mg·L~(-1)酸性橙Ⅱ模拟废水进行20 min的降解实验.3次实验结果表明,串、并联流程的酸性橙Ⅱ平均降解率分别为59.26%和87.93%,平均脱色率分别为57.08%和86.87%,均低于RED阴、阳极独立降解时的降解率和脱色率.原因在于:在联合降解条件下反应器阴、阳极之间的产物会相互干扰,使得废水中有机物降解率降低.但降解过程中循环废水的pH值可以保持稳定.     

高含硅量高盐地下水处理工艺

本文通过对高含硅量，高盐地下水这一特殊水质进行纯化处理研究，经实际运行及分析，得出一套行之有效的工艺流程。     

双极膜电渗析法处理谷氨酸水溶液的过程性能研究

对利用双极膜水解离技术处理谷氨酸水溶液的各种工艺参数进行了探索。讨论了电流效率、转化率及能耗等因素对双极膜水解离技术应用的影响。根据实验研究结果 ,提出了双极膜法处理谷氨酸水溶液的最佳工艺流程     

脱硫废液电渗析法再生用膜的研究

通过对脱硫废液电渗析再生用膜的探讨,说明了离子交换膜的理论、制法和性能.对电渗析所采用之膜的性能特点和制备工艺作了分析.     

Tracing the impact of stack configuration on interface resistances in reverse electrodialysis by in situ electrochemical impedance spectroscopy

• RED performance and stack resistance were studied by EIS and LSV. • Interface resistance were discriminated from Ohmic resistance by EIS. • Impacts of spacer shadow effect and concentration polarization were analyzed. • Ionic short current reduced the power density for more cell pairs. • The results enabled to predict RED performance with different configurations. Reverse electrodialysis (RED) is an emerging membrane-based technology for the production of renewable energy from mixing waters with different salinities. Herein, the impact of the stack configuration on the Ohmic and non-Ohmic resistances as well as the performance of RED were systematically studied by using in situ electrochemical impedance spectroscopy (EIS). Three different parameters (membrane type, number of cell pairs and spacer design) were controlled. The Ohmic and non-Ohmic resistances were evaluated for RED stacks equipped with two types of commercial membranes (Type I and Type II) supplied by Fujifilm Manufacturing Europe B.V: Type I Fuji membranes displayed higher Ohmic and non-Ohmic resistances than Type II membranes, which was mainly attributed to the difference in fixed charge density. The output power of the stack was observed to decrease with the increasing number of cell pairs mainly due to the increase in ionic shortcut currents. With the reduction in spacer thickness from 750 to 200 µm, the permselectivity of membranes in the stack decreased from 0.86 to 0.79 whereas the energy efficiency losses increased from 31% to 49%. Overall, the output of the present study provides a basis for understanding the impact of stack design on internal losses during the scaling-up of RED.