A three-stage chemical cleaning of ion-exchange membranes used in the treatment by electrodialysis of wastewaters generated in brass electroplating industries

被引:32
作者
Barros, Kayo Santana [1 ,2 ]
Cesar Marti-Calatayud, Manuel [2 ]
Perez-Herranz, Valentin [2 ]
Espinosa, Denise Crocce Romano [1 ]
机构
[1] Univ Sao Paulo, Dept Chem Engn, Conjunto Quim, Av Prof Lineu Prestes 580,Bloco 18, BR-05434070 Sao Paulo, SP, Brazil
[2] Univ Politecn Valencia, ISIRYM, IEC Grp, Cami Vera S-N,46022,POB 22012, E-46071 Valencia, Spain
关键词
Membrane fouling; Membrane cleaning; Ion-exchange membranes; Alkaline cleaning; Chronopotentiometry; TRANSPORT-PROPERTIES; WASTE-WATER; FTIR; COMPLEXES; EDTA; CHRONOPOTENTIOMETRY; TRANSITION; COPOLYMER; RECOVERY; REMOVAL;
D O I
10.1016/j.desal.2020.114628
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
After long-term electrodialysis, cleaning the membranes is crucial to extend their lifetime. In this work, we evaluate the effects of a three-stage chemical cleaning on electrochemical and structural properties of anion- and cation-exchange membranes. Membranes used in the electrodialytic treatment of a synthetic effluent from the cyanide-free brass electrodeposition were cleaned using 0.1, 0.5 and 1.0 mol.L-1 NaOH solutions. The electrochemical behavior of the membranes was evaluated after each cleaning step by chronopotentiometry. Additionally, changes in the membrane structure and composition were analyzed by FTIR-ATR and SEM/EDS. While the membranes undergo a decline in some electrochemical features after the electrodialysis process, the cleaning with 0.1 mol.L-1 NaOH showed to be the most effective in recovering the properties characteristic of the virgin membranes: the limiting current density increased by 84% after the cleaning, whereas the ohmic and overlimiting resistances decreased by 47% and 55%, respectively. In contrast, the 0.5 and 1.0 mol.L-1 NaOH solutions degraded the membranes and reduced their fraction of conducive area, especially for the anion-exchange one. This favored fouling/scaling occurrence, as noticed by a prominent increase in the potential drop of the anion-exchange membrane. FTIR-ATR and SEM/EDS analyses confirmed fouling/scaling, as well as degradation of the ion-exchange membranes.
引用
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页数:11
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