Removal of aqueous cyanide with strongly basic ion-exchange resin

dc.contributor.authorSimsek, Halis
dc.contributor.authorKobya, Mehmet
dc.contributor.authorKhan, Eakalak
dc.contributor.authorBezbaruah, Achintya N.
dc.date.accessioned2025-10-29T11:17:05Z
dc.date.issued2015
dc.departmentFakülteler, Mühendislik Fakültesi, Çevre Mühendisliği Bölümü
dc.description.abstractThe removal of cyanide (CN-) from aqueous solutions using a strongly basic ion-exchange resin, Purolite A-250, was investigated. The effects of contact time, initial CN- concentration, pH, temperature, resin dosage, agitation speed, and particle size distribution on the removal of CN- were examined. The adsorption equilibrium data fitted the Langmuir isotherm very well. The maximum CN- adsorption capacity of Purolite A-250 was found to be 44 mg CN- g(-1) resin. More than 90% CN- adsorption was achieved for most CN- solutions (50, 100, and 200 mg CN- L-1) with a resin dose of 2 g L-1. The equilibrium time was similar to 20 min, optimum pH was 10.0-10.5, and optimum agitation speed was 150 rpm. An increase in adsorption of CN- with increasing resin dosage was observed. Adsorption of CN- by the resin was marginally affected (maximum 4% variation) within an environmentally relevant temperature range of 20-50 degrees C. Fixed-bed column (20.5 mm internal diameters) experiments were performed to investigate the effects of resin bed depth and influent flow rate on breakthrough behaviour. Breakthrough occurred in 5 min for 0.60 cm bed depth while it was 340 min for 5.40 cm bed depth. Adsorption capacity was 25.5 mg CN- g(-1) for 5 mL min(-1) flow rate and 3.9 mg CN- g(-1) for 20 mL min(-1) flow rate. The research has established that the resin can be effectively used for CN- removal from aqueous solutions.
dc.identifier.doi10.1080/09593330.2014.999829
dc.identifier.endpage1622
dc.identifier.issn0959-3330
dc.identifier.issn1479-487X
dc.identifier.issue13
dc.identifier.orcid0000-0001-5052-7220
dc.identifier.orcid0000-0001-9031-5142
dc.identifier.pmid25558868
dc.identifier.scopus2-s2.0-84926522660
dc.identifier.scopusqualityQ1
dc.identifier.startpage1612
dc.identifier.urihttps://doi.org/10.1080/09593330.2014.999829
dc.identifier.urihttps://hdl.handle.net/20.500.14854/7905
dc.identifier.volume36
dc.identifier.wosWOS:000351845000002
dc.identifier.wosqualityQ3
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.indekslendigikaynakPubMed
dc.language.isoen
dc.publisherTaylor & Francis Ltd
dc.relation.ispartofEnvironmental Technology
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.snmzKA_WOS_20251020
dc.subjectindustrial pollution control
dc.subjection-exchange resin
dc.subjectcyanide
dc.subjectadsorption
dc.subjectisotherms
dc.titleRemoval of aqueous cyanide with strongly basic ion-exchange resin
dc.typeArticle

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