A three-stage chemical cleaning of ion-exchange membranes used in the treatment by electrodialysis of wastewaters generated in brass electroplating industries
[EN] 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 treat...
| Autores: | , , , |
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| Tipo de recurso: | artículo |
| Fecha de publicación: | 2020 |
| País: | España |
| Institución: | Universitat Politècnica de València (UPV) |
| Repositorio: | RiuNet. Repositorio Institucional de la Universitat Politécnica de Valéncia |
| Idioma: | inglés |
| OAI Identifier: | oai:riunet.upv.es:10251/166271 |
| Acceso en línea: | https://riunet.upv.es/handle/10251/166271 |
| Access Level: | acceso abierto |
| Palabra clave: | Alkaline cleaning Chronopotentiometry Ion-exchange membranes Membrane cleaning Membrane fouling INGENIERIA QUIMICA |
| Sumario: | [EN] 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. |
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