Co-processing behavior of Golbasi lignite and poplar sawdust by factorial experimental design method

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dc.authoridKaraca, Huseyin/0000-0002-0543-8947
dc.authorwosidKaraca, Huseyin/ABG-8103-2020
dc.contributor.authorKaraca, Huseyin
dc.contributor.authorKoyunoglu, Cemil
dc.contributor.authorOzdemir, Ali
dc.contributor.authorErgun, Kenan
dc.date.accessioned2024-08-04T20:46:02Z
dc.date.available2024-08-04T20:46:02Z
dc.date.issued2019
dc.departmentİnönü Üniversitesien_US
dc.description.abstractIn this work, the liquefaction of coal and biomass with direct liquefaction strategy was explored. The point of liquefaction is both to utilize a greater amount of the current coal and biomass assets all the more productively and to create an alternative liquid fuel to oil. Along these lines, the procedure parameters must be resolved to expand the liquefaction efficiency. In addition, it is proposed to do the liquefaction efficiency, particularly in the reactant conditions, to expand the measure of oil. Process parameters were controlled by utilizing Factorial Experimental Design technique in the liquefaction procedures. The solid/liquid ratio was changed as 1/2-1/4, the catalyst concentration was 2-6%, the temperature was 375-400 degrees C and the duration was 30-90 min. Starting nitrogen pressure was set at 30 bar, stirring speed was 400 rpm, coal/biomass proportion was settled at 1/1. Tetralin as a solvent and MoO3 as catalyst were utilized. Toward the finish of the liquefaction procedure, the total conversions were computed in view of the acquired non-reactive solid (char). As indicated by the outcomes obtained, the most total conversion (81.9%) was acquired at a solid/liquid proportion of 1/2, a catalyst concentration of 2%, a reaction time of 90 min and a reaction temperature of 400 degrees C. In light of total conversions and elective liquid fuel (oil) in the given conditions, the solid/liquid ratio should be taken as 1/2, the catalyst concentration is 2%, the reaction time is 30-90 min and the reaction temperature is 400 degrees C. The lowest reaction time found, in this study, is the innovative solution for reducing co-liquefaction cost preferred. (C) 2019 Elsevier Ltd. All rights reserved.en_US
dc.identifier.doi10.1016/j.energy.2019.06.157
dc.identifier.endpage1048en_US
dc.identifier.issn0360-5442
dc.identifier.issn1873-6785
dc.identifier.scopus2-s2.0-85068498161en_US
dc.identifier.scopusqualityQ1en_US
dc.identifier.startpage1040en_US
dc.identifier.urihttps://doi.org/10.1016/j.energy.2019.06.157
dc.identifier.urihttps://hdl.handle.net/11616/98857
dc.identifier.volume183en_US
dc.identifier.wosWOS:000483005400088en_US
dc.identifier.wosqualityQ1en_US
dc.indekslendigikaynakWeb of Scienceen_US
dc.indekslendigikaynakScopusen_US
dc.language.isoenen_US
dc.publisherPergamon-Elsevier Science Ltden_US
dc.relation.ispartofEnergyen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectLigniteen_US
dc.subjectPoplar sawdusten_US
dc.subjectCo-liquefactionen_US
dc.subjectProcess parametersen_US
dc.subjectConversionen_US
dc.subjectOilen_US
dc.titleCo-processing behavior of Golbasi lignite and poplar sawdust by factorial experimental design methoden_US
dc.typeArticleen_US

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