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dc.contributor.authorBombach, H.
dc.contributor.authorORHAN, GÖKHAN
dc.contributor.authorStelter, M.
dc.contributor.authorArslan, Cüneyt
dc.date.accessioned2021-03-03T10:11:22Z
dc.date.available2021-03-03T10:11:22Z
dc.date.issued2002
dc.identifier.citationORHAN G., Arslan C., Bombach H., Stelter M., "Nickel recovery from the rinse waters of plating baths", HYDROMETALLURGY, cilt.65, sa.1, ss.1-8, 2002
dc.identifier.issn0304-386X
dc.identifier.otherav_21391c58-a4f4-4349-9a8c-69010118ae0d
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/27377
dc.identifier.urihttps://doi.org/10.1016/s0304-386x(02)00038-5
dc.description.abstractAn electrolytic process is applied to the de-metalization of rinse waters emerging from nickel-plating baths. Optimum conditions of nickel recovery from this type of solution have been investigated through a series of experiments carried out in a rotating packed cell (Rollsehichtzelle(R)). The effects of temperature and pH of electrolyte, current density, cell rotation speed, and diameter of the cathode granules were examined. Ninety percent of the nickel was recovered from a solution of 450 mL volume, with a pH of 5.5 +/- 0.05, 2 g/L initial nickel concentration, and by using cathode granules of 5 mm in diameter. At 50 degreesC electrolyte temperature and 325 A/m(2) current density, 74% current efficiency was attained with 4.2 kWh/kg Ni energy consumption. (C) 2002 Published by Elsevier Science B.V.
dc.language.isoeng
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectMühendislik ve Teknoloji
dc.subjectMETALURJİ VE METALURJİ MÜHENDİSLİĞİ
dc.subjectMalzeme Bilimi
dc.subjectMetalurji ve Malzeme Mühendisliği
dc.titleNickel recovery from the rinse waters of plating baths
dc.typeMakale
dc.relation.journalHYDROMETALLURGY
dc.contributor.departmentİstanbul Üniversitesi , ,
dc.identifier.volume65
dc.identifier.issue1
dc.identifier.startpage1
dc.identifier.endpage8
dc.contributor.firstauthorID631296


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