Removal of aqueous cyanide with strongly basic ion-exchange resin
| dc.contributor.author | Simsek, Halis | |
| dc.contributor.author | Kobya, Mehmet | |
| dc.contributor.author | Khan, Eakalak | |
| dc.contributor.author | Bezbaruah, Achintya N. | |
| dc.date.accessioned | 2025-10-29T11:17:05Z | |
| dc.date.issued | 2015 | |
| dc.department | Fakülteler, Mühendislik Fakültesi, Çevre Mühendisliği Bölümü | |
| dc.description.abstract | The 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.doi | 10.1080/09593330.2014.999829 | |
| dc.identifier.endpage | 1622 | |
| dc.identifier.issn | 0959-3330 | |
| dc.identifier.issn | 1479-487X | |
| dc.identifier.issue | 13 | |
| dc.identifier.orcid | 0000-0001-5052-7220 | |
| dc.identifier.orcid | 0000-0001-9031-5142 | |
| dc.identifier.pmid | 25558868 | |
| dc.identifier.scopus | 2-s2.0-84926522660 | |
| dc.identifier.scopusquality | Q1 | |
| dc.identifier.startpage | 1612 | |
| dc.identifier.uri | https://doi.org/10.1080/09593330.2014.999829 | |
| dc.identifier.uri | https://hdl.handle.net/20.500.14854/7905 | |
| dc.identifier.volume | 36 | |
| dc.identifier.wos | WOS:000351845000002 | |
| dc.identifier.wosquality | Q3 | |
| dc.indekslendigikaynak | Web of Science | |
| dc.indekslendigikaynak | Scopus | |
| dc.indekslendigikaynak | PubMed | |
| dc.language.iso | en | |
| dc.publisher | Taylor & Francis Ltd | |
| dc.relation.ispartof | Environmental Technology | |
| dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | |
| dc.rights | info:eu-repo/semantics/closedAccess | |
| dc.snmz | KA_WOS_20251020 | |
| dc.subject | industrial pollution control | |
| dc.subject | ion-exchange resin | |
| dc.subject | cyanide | |
| dc.subject | adsorption | |
| dc.subject | isotherms | |
| dc.title | Removal of aqueous cyanide with strongly basic ion-exchange resin | |
| dc.type | Article |









