A comparative study between synthetic solution and electroplating effluent regarding kinetic and equilibrium Zn ions removal behavior by Amberlite IR 120 resin
Author:
Funder
Fundação Araucária
Coordination for the Improvement of Higher Education
National Council for Scientific and Technological Development
Publisher
Springer Science and Business Media LLC
Subject
General Chemical Engineering
Link
https://link.springer.com/content/pdf/10.1007/s43153-023-00367-2.pdf
Reference39 articles.
1. Alguacil FJ, Alonso M, Lozano LJ (2004) Chromium (III) recovery from waste acid solution by ion exchange processing using Amberlite IR-120 resin: batch and continuous ion exchange modelling. Chemosphere 57(8):789–793. https://doi.org/10.1016/j.chemosphere.2004.08.085
2. Amrane C, Bouhidel K (2018) Hydrometallurgy integrated diffusion dialysis precipitation—cementation for selective recovery of leaching chemicals and metal values from electroplating sludge. Hydrometallurgy 177(February):34–40. https://doi.org/10.1016/j.hydromet.2018.02.011
3. APHA (2005) Standard methods for the examination of water and wastewater. In: Standard methods, 21st edn. American Public Health Association
4. Bodamer GW, Kunin R (1953) Behavior of ion exchange resins in solvents other than water. Rohm & Haas Co., Philadelphia, PA.. https://doi.org/10.1021/ie50527a057
5. Borba CE, Silva EA, Spohr S, Santos GHF, Guirardello R (2010) Ion exchange equilibrium prediction for the system Cu2+−Zn2+−Na+. J Chem Eng Data 55(3):1333–1341. https://doi.org/10.1021/je900649e
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