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Effect of Process Parameters on Supercritical Liquefaction of Xanthium Strumarium for Bio-Oil Production

dc.authorscopusid 9333192500
dc.authorscopusid 8854237200
dc.authorscopusid 54879310600
dc.authorscopusid 57189003304
dc.authorwosid Durak, Halil/I-8841-2019
dc.contributor.author Genel, Yasar
dc.contributor.author Durak, Halil
dc.contributor.author Aysu, Tevfik
dc.contributor.author Genel, Ilyas
dc.date.accessioned 2025-05-10T17:40:59Z
dc.date.available 2025-05-10T17:40:59Z
dc.date.issued 2016
dc.department T.C. Van Yüzüncü Yıl Üniversitesi en_US
dc.department-temp [Genel, Yasar; Genel, Ilyas] Yuzuncu Yil Univ, Fac Educ, Dept Chem, TR-65080 Van, Turkey; [Durak, Halil] Yuzuncu Yil Univ, Vocat Sch Hlth Serv, TR-65080 Van, Turkey; [Aysu, Tevfik] Yuzuncu Yil Univ, Fac Sci, Dept Chem, TR-65080 Van, Turkey en_US
dc.description.abstract Supercritical liquefaction process is used for producing energy from biomass. The common reaction conditions for supercritical liquefaction process are the 240-380 degrees C temperature range and 5-20 MPa pressure values range. Xanthium strumarium liquefaction experiments were performed in a cylindrical reactor (75 mL) in organic solvents (acetone, ethanol, methanol) under supercritical conditions with (zinc oxide, calcium hydroxide) and without catalyst at the temperatures of 250, 275 and 300 degrees C. The produced liquids at 300 degrees C in liquefaction were analyzed and characterized by Elemental, GC-MS and FT-IR. 36, 37 and 50 different types of compounds were identified by GC-MS obtained in acetone, ethanol and methanol respectively. The liquid product efficiency has been obtained at 300 degrees C in acetone with zinc oxide catalyst (74.80%). The highest HHV value has been calculated as 32.16 MJ/kg with calcium hydroxide catalyst in acetone. (C) 2016 Elsevier B.V. All rights reserved. en_US
dc.description.sponsorship Yuzuncu Yil University [2015-HIZ-EF165] en_US
dc.description.sponsorship The authors gratefully acknowledge the Yuzuncu Yil University Research Fund for financial support (No: 2015-HIZ-EF165). en_US
dc.description.woscitationindex Science Citation Index Expanded
dc.identifier.doi 10.1016/j.supflu.2016.04.009
dc.identifier.endpage 53 en_US
dc.identifier.issn 0896-8446
dc.identifier.issn 1872-8162
dc.identifier.scopus 2-s2.0-84964570449
dc.identifier.scopusquality Q1
dc.identifier.startpage 42 en_US
dc.identifier.uri https://doi.org/10.1016/j.supflu.2016.04.009
dc.identifier.uri https://hdl.handle.net/20.500.14720/15379
dc.identifier.volume 115 en_US
dc.identifier.wos WOS:000377731800006
dc.identifier.wosquality Q2
dc.language.iso en en_US
dc.publisher Elsevier en_US
dc.relation.publicationcategory Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı en_US
dc.rights info:eu-repo/semantics/closedAccess en_US
dc.subject Energy en_US
dc.subject Biomass en_US
dc.subject Bio-Oil en_US
dc.subject Supercritical Fluid en_US
dc.title Effect of Process Parameters on Supercritical Liquefaction of Xanthium Strumarium for Bio-Oil Production en_US
dc.type Article en_US

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