Co-Liquefaction of Elbistan Lignite with Manure Biomass; Part 3-Effect of Reaction Time and Temperature

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dc.authoridKaraca, Huseyin/0000-0002-0543-8947
dc.authorwosidKaraca, Huseyin/ABG-8103-2020
dc.contributor.authorKoyunoglu, Cemil
dc.contributor.authorKaraca, Huseyin
dc.date.accessioned2024-08-04T20:44:15Z
dc.date.available2024-08-04T20:44:15Z
dc.date.issued2017
dc.departmentİnönü Üniversitesien_US
dc.description3rd World Multidisciplinary Earth Sciences Symposium (WMESS) -- SEP 11-15, 2017 -- Prague, CZECH REPUBLICen_US
dc.description.abstractMost of the liquefaction process were carried out in a batch reactor, in which the residence time of the liquefaction products is long enough to favour the retrogressive reactions. To minimize retrogressive reactions, the liquefaction of coal was carried out in a flowing solvent reactor in which a fixed bed of coal is continuously permeated by hot solvent. Solvent flowing through the coal bed carries the liquefaction products out of the reactor. Unlike experiments carried out under similar conditions in a batch reactor no increase in solid residue is observed during long time high temperature runs in the flowing solvent reactor. There is a greater appreciation of the importance of retrograde, or polymerization, reactions. If the free radicals formed when coal breaks down are not quickly capped with hydrogen, they react with each other to form large molecules that are much harder to break down than the original coal. Reaction time impacts both the co-liquefaction cost and the product yield. So as to study this idea, the experiments of Elbistan Lignite (EL) with manure co-liquefaction carried out by changing the reaction time from 30 to 120 minutes. As a result, the greatest oil products yields obtained at 60 minutes. Therefore, by thinking about the oil products yield values acquired, the optimal reaction time was obtained to be 60 minutes for Elbistan lignite (EL) with manure liquefied with the temperature of 350 degrees C and 400 degrees C. Above 425 degrees C did not examine because solvent (tetraline) loses its function after 425 degrees C. The obtained optimum temperature found 400 degrees C due to higher total conversion of liquefaction products and also oil+gas yields.en_US
dc.description.sponsorshipLAMA Energy Grp,LAMA Gas & Oilen_US
dc.description.sponsorshipInonu University Scientific Research Projects Coordination Unit [I.U.B.A.P.B. 2008/03]en_US
dc.description.sponsorshipIt is a pleasure to acknowledge the support of this work (Project No: I.U.B.A.P.B. 2008/03) by Inonu University Scientific Research Projects Coordination Unit.en_US
dc.identifier.doi10.1088/1755-1315/95/4/042075
dc.identifier.issn1755-1307
dc.identifier.scopus2-s2.0-85040596137en_US
dc.identifier.scopusqualityN/Aen_US
dc.identifier.urihttps://doi.org/10.1088/1755-1315/95/4/042075
dc.identifier.urihttps://hdl.handle.net/11616/98115
dc.identifier.volume95en_US
dc.identifier.wosWOS:000426768500170en_US
dc.identifier.wosqualityN/Aen_US
dc.indekslendigikaynakWeb of Scienceen_US
dc.indekslendigikaynakScopusen_US
dc.language.isoenen_US
dc.publisherIop Publishing Ltden_US
dc.relation.ispartofWorld Multidisciplinary Earth Sciences Symposium (Wmess 2017)en_US
dc.relation.publicationcategoryKonferans Öğesi - Uluslararası - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/openAccessen_US
dc.subjectExtractionen_US
dc.subjectWasteen_US
dc.titleCo-Liquefaction of Elbistan Lignite with Manure Biomass; Part 3-Effect of Reaction Time and Temperatureen_US
dc.typeConference Objecten_US

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