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Ion exchange treatment of rinse water generated in the galvanizing process

dc.contributor.authorMarañón Maison, María Elena 
dc.contributor.authorFernández Nava, Yolanda 
dc.contributor.authorCastrillón Peláez, Leonor 
dc.date.accessioned2015-01-07T11:58:54Z
dc.date.available2015-01-07T11:58:54Z
dc.date.issued2005
dc.identifier.citationWater Environment Research, 77 (7), p. 3054-3058 (2005); doi:10.2175/106143005X73947
dc.identifier.issn1061-4303
dc.identifier.urihttp://hdl.handle.net/10651/29132
dc.description.abstractA study was conducted of the viability of using the cationic exchange resins Amberlite IR-120 and Lewatit SP-112 to treat rinse water generated in the galvanizing process as well as acidic wastewater containing zinc (Zn) and iron (Fe). Solutions containing either 100 mg/L of Zn at pH 5.6 (rinse water) or Fe and Zn at concentrations of 320 and 200 mg/L at pH 1.5 (acidic water), respectively, were percolated through packed beds until the resins were exhausted. Breakthrough capacities obtained ranged between 1.1 and 1.5 meq metal/mL resin. The elution of metal and the regeneration of resins were performed with hydrochloric acid. The influence of the flowrate used during the loading stage was also studied, with 0.5 bed volumes/min (3.2 cm/min) found to be the optimum flowratespa
dc.description.sponsorshipFoundation for the Support of Resarch in Applied Science and Technology (FICYT) and AGALSA (Ref.PA-MAS92-03)
dc.format.extentp. 3054-3058spa
dc.language.isoengspa
dc.publisherWater Environment Federation
dc.relation.ispartofWater Environment Research, 77 (7)en
dc.subjectRinse wateren
dc.subjectAcidic wateren
dc.subjectZincen
dc.subjectIronen
dc.subjectCationic resinen
dc.subjectIon exchangeen
dc.subjectRemovalen
dc.titleIon exchange treatment of rinse water generated in the galvanizing processen
dc.typejournal article
dc.identifier.doi10.2175/106143005X73947
dc.relation.publisherversionhttp://dx.doi.org/10.2175/106143005X73947


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