Co-liquefaction of Yataan lignite and waste tire under catalytic conditions. Part 1. Effect of fresh tetraline and recycled tetraline on the conversion

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dc.authoridKaraca, Huseyin/0000-0002-0543-8947
dc.authorwosidKaraca, Huseyin/ABG-8103-2020
dc.contributor.authorKoyunoglu, Cemil
dc.contributor.authorEksioglu, Oktay
dc.contributor.authorYildirim, Onur
dc.contributor.authorKaraca, Huseyin
dc.date.accessioned2024-08-04T20:44:28Z
dc.date.available2024-08-04T20:44:28Z
dc.date.issued2018
dc.departmentİnönü Üniversitesien_US
dc.description.abstractIn this study, the effect of solvent type and the solvent/solid ratio on the liquefaction of Mula-Yatagan lignite (YL) combined with waste tire (WT) under catalytic conditions investigated. Liquefaction experiments carried out the following conditions, a reaction temperature of 400 degrees C, a catalyst concentration of 3%, solvent/solid ratio from 1/1 to 9/1, reaction time of 90 min, lignite/waste ratio of 1/1. In addition, mixing speed was 400 rpm, and the nitrogen gas pressure fixed at 30 bar. After the each of liquefaction experiments finished, the soluble products (SP) classified as preasphaltene (PAS), asphaltene (AS) and oil+gas (OG), by solvent extraction. Due to the optimum total conversion determined, fresh tetraline obtained as the most favorable solvent with 71.71%, for the liquefaction of YL with WT. However, the total conversion for recycling tetraline is 68.6%. According to the results, co-liquefaction of YL combined with WT using recycle solvent is the one way to offer, alternatively of using crude oil, producing SP for not crude oil, producing SP for not only fuel-oil production but also prefer chemical raw materials. With respect to the optimum oil+gas yield results, the most convenient solvent type and the solvent/solid ratio are the recycled solvent and its 3/1 ratio.en_US
dc.identifier.doi10.1080/15567036.2018.1469689
dc.identifier.endpage1075en_US
dc.identifier.issn1556-7036
dc.identifier.issn1556-7230
dc.identifier.issue9en_US
dc.identifier.scopus2-s2.0-85046457068en_US
dc.identifier.scopusqualityQ2en_US
dc.identifier.startpage1068en_US
dc.identifier.urihttps://doi.org/10.1080/15567036.2018.1469689
dc.identifier.urihttps://hdl.handle.net/11616/98270
dc.identifier.volume40en_US
dc.identifier.wosWOS:000432631300007en_US
dc.identifier.wosqualityQ4en_US
dc.indekslendigikaynakWeb of Scienceen_US
dc.indekslendigikaynakScopusen_US
dc.language.isoenen_US
dc.publisherTaylor & Francis Incen_US
dc.relation.ispartofEnergy Sources Part A-Recovery Utilization and Environmental Effectsen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectCo-liquefactionen_US
dc.subjectconversionen_US
dc.subjectfresh tetralineen_US
dc.subjectligniteen_US
dc.subjectrecycled tetralineen_US
dc.subjectsolvent typeen_US
dc.subjectwaste tireen_US
dc.titleCo-liquefaction of Yataan lignite and waste tire under catalytic conditions. Part 1. Effect of fresh tetraline and recycled tetraline on the conversionen_US
dc.typeArticleen_US

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