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dc.contributor.authorCebeci, Yakup
dc.contributor.authorUlusoy, Ugur
dc.date.accessioned2019-07-27T12:10:23Z
dc.date.accessioned2019-07-28T09:58:43Z
dc.date.available2019-07-27T12:10:23Z
dc.date.available2019-07-28T09:58:43Z
dc.date.issued2013
dc.identifier.issn0378-3820
dc.identifier.urihttps://dx.doi.org/10.1016/j.fuproc.2013.04.014
dc.identifier.urihttps://hdl.handle.net/20.500.12418/8544
dc.descriptionWOS: 000324154600014en_US
dc.description.abstractIn this study, a coal washing plant in Zonguldak was optimized using equalization of incremental product quality approach which maximizes plant yield for a given ash constraint based on float-sink data. By maximization of yield using Solver which is an optimization routine available in Excel for the identical elementary ash content and the specified ash level of 9.50%, the optimum cut points were determined for washing of coarser size fraction (100-18 mm) and finer size fraction (18-0.5 mm) by Drewboy Heavy Medium (HM) Bath and HM Cyclone, respectively. The results were compared with the plant operations in terms of product yield and ash content. Calculated yield % and ash % values with experimental yield % and ash % values from float-sink data of the used coal were also compared and they were in good agreement (R-2 > 0.99). By equalization of the incremental ash in order to get composite ash of 9.5%, the composite yield was maximized to 30.71% while the plant's yield was about 24.00%. This approach identified the optimum operating conditions for individual cleaning circuits as 1.693 and 1.682 for Drewboy HM Bath and HM Cyclone, respectively. It is worth pointing out that, this increase (6.71%) in the yield would be remarkable when considering the whole life of the washery and the annual production of the plant (about 700000 tons). In addition, the yield was maximized to 33.41% for the target ash of 11.61% by similar optimization studies. The optimum operating cut points for HM Drewboy Bath and HM Cyclone was determined as 1.900 and 1.888, respectively. Yield optimization was also performed by taking a equals to 80, which can be assumed ideal for HM separators. The results obtained by the two different calculations were very close to each other. (C) 2013 Elsevier B.V. All rights reserved.en_US
dc.language.isoengen_US
dc.publisherELSEVIER SCIENCE BVen_US
dc.relation.isversionof10.1016/j.fuproc.2013.04.014en_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectCoal preparationen_US
dc.subjectWashabilityen_US
dc.subjectHeavy medium separationen_US
dc.subjectOptimizationen_US
dc.subjectSolveren_US
dc.subjectIncremental ashen_US
dc.titleAn optimization study of yield for a coal washing plant from Zonguldak regionen_US
dc.typearticleen_US
dc.relation.journalFUEL PROCESSING TECHNOLOGYen_US
dc.contributor.department[Cebeci, Yakup -- Ulusoy, Ugur] Cumhuriyet Univ, Dept Min Engn, TR-58140 Sivas, Turkeyen_US
dc.contributor.authorIDUlusoy, Ugur -- 0000-0002-2634-7964en_US
dc.identifier.volume115en_US
dc.identifier.endpage114en_US
dc.identifier.startpage110en_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US


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