USE OF COLEMANITE IN FERRONICKEL SMELTING

dc.authoridTOPKAYA, YAVUZ/0009-0009-3671-3655
dc.authoridEray, Said/0000-0001-7310-9726
dc.authoridKeskinkilic, Ender/0000-0002-4186-0694
dc.authorscopusid6504342315
dc.authorscopusid43762122800
dc.authorscopusid6506436603
dc.authorscopusid6602494621
dc.contributor.authorKeskinkılıç, Ender
dc.contributor.authorPournaderi, S.
dc.contributor.authorGeveci, A.
dc.contributor.authorTopkaya, Y. A.
dc.contributor.otherMetallurgical and Materials Engineering
dc.date.accessioned2024-07-05T15:28:40Z
dc.date.available2024-07-05T15:28:40Z
dc.date.issued2019
dc.departmentAtılım Universityen_US
dc.department-temp[Keskinkilic, E.] Atilim Univ, Met & Mat Engn Dept, Ankara, Turkey; [Pournaderi, S.] Ibrahim Cecen Univ Agri, Agri, Turkey; [Geveci, A.; Topkaya, Y. A.] METU, Met & Mat Engn Dept, Ankara, Turkeyen_US
dc.descriptionTOPKAYA, YAVUZ/0009-0009-3671-3655; Eray, Said/0000-0001-7310-9726; Keskinkilic, Ender/0000-0002-4186-0694en_US
dc.description.abstractUse of colemanite in metal-slag systems aims primarily to decrease the viscosity of slag and, therefore, achieve better metal-slag separation. Enhanced metal-slag separation is helpful to decrease the number of suspended metal/alloy droplets in slag, i.e. the physical losses. In the literature, successful use of colemanite was reported both in steelmaking and copper matte smelting processes. Ferronickel smelting slags contain nickel in the range of 0.1-0.2% and correspondingly, metal-slag distribution ratio values of nickel are reported even above 200. On the contrary, nickel recoveries are hard to exceed 95%. This can be mostly attributed to the physical losses of nickel due to very high slag volume in ferronickel smelters; for 1 ton of ferronickel, 10-15 tonnes of slag are generated regardless of the type of the laterite, which contains significant quantity of ,gangue components. The authors thought that use of colemanite could be a solution to decrease physical losses. Therefore, the use of colemanite in ferronickel smelting was investigated in the present work. Laboratory-scale smelting experiments were conducted using calcined and prereduced laterites in a vertical tube furnace under different gas atmospheres. The amount of colemanite added was in the range of 0 - 2.5% of the total charge. The experiments were also performed using ferronickel and slag samples obtained from a ferronickel smelter.en_US
dc.description.sponsorshipScientific Research Projects (BAP) Department of the Middle East Technical University [BAP03-08-2012-002]en_US
dc.description.sponsorshipThe authors would like to thank the Scientific Research Projects (BAP) Department of the Middle East Technical University for the financial support under project no. BAP03-08-2012-002. The authors also wish to express their thanks to the META Nickel Cobalt Co. and Eti Mine Works General Management of Turkey for supplying the lateritic ore and the ground colemanite, respectively. The LARCO smelter in Greece is acknowledged for supplying the ferronickel and slag samples.en_US
dc.identifier.citation2
dc.identifier.doi10.2298/JMMB181009007K
dc.identifier.endpage8en_US
dc.identifier.issn1450-5339
dc.identifier.issue1en_US
dc.identifier.scopus2-s2.0-85064158499
dc.identifier.scopusqualityQ3
dc.identifier.startpage1en_US
dc.identifier.urihttps://doi.org/10.2298/JMMB181009007K
dc.identifier.urihttps://hdl.handle.net/20.500.14411/2831
dc.identifier.volume55en_US
dc.identifier.wosWOS:000465008300001
dc.identifier.wosqualityQ4
dc.language.isoenen_US
dc.publisherTechnical Faculty, Bor-serbiaen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/openAccessen_US
dc.subjectColemaniteen_US
dc.subjectFerronickelen_US
dc.subjectSmeltingen_US
dc.titleUSE OF COLEMANITE IN FERRONICKEL SMELTINGen_US
dc.typeArticleen_US
dspace.entity.typePublication
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