Selective separation of mono- and di-valent cations in electrodialysis during brackish water desalination: Bench and pilot-scale studies

电渗析 海水淡化 选择性 微咸水 化学 离子交换 色谱法 化学工程 离子 催化作用 盐度 工程类 有机化学 地质学 生物化学 海洋学
作者
Xuesong Xu,Qun He,Guanyu Ma,Huiyao Wang,Nagamany Nirmalakhandan,Pei Xu
出处
期刊:Desalination [Elsevier BV]
卷期号:428: 146-160 被引量:92
标识
DOI:10.1016/j.desal.2017.11.015
摘要

Selective separation of mono- and multi-valent ions has important applications in water reuse, desalination, and salt production. Innovative monovalent permselective cation-exchange membrane CR671 was developed by modifying the normal grade membrane CR67 with polyethyleneimine coating. Bench- and pilot-scale electrodialysis experiments were conducted at a brackish groundwater desalination facility to investigate desalination performance and ion selectivity using the CR671 and CR67 under different operating conditions. Both normal grade (CR67 and AR204) and selective (CR671 and AR112B) membranes achieved same desalting efficiency. Na-selectivity in terms of relative transport number using sodium as the standard ion was affected significantly by current density and linear velocity for the normal grade membranes while the selective membranes exhibited stable good Na-selectivity. The Na-selectivity of the CR671 was demonstrated up to 9 and 5 times better than the CR67 during pilot- and bench-scale electrodialysis, respectively. Hydraulic retention time and electrodialysis stack staging had minor impact on Na-selectivity at high current density. With the same hydraulic conditions, overall desalination behavior and ion selectivity were highly comparable between bench- and pilot-scale electrodialysis. It infers that bench-scale testing results can be used to simulate and project desalination performance and ion selectivity of pilot- and potentially full-scale electrodialysis applications.

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