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dc.contributor.authorPütün, Ayşe Eren
dc.contributor.authorApaydın, Elif
dc.contributor.authorPütün, Ersan
dc.date.accessioned2019-10-21T21:12:07Z
dc.date.available2019-10-21T21:12:07Z
dc.date.issued2002
dc.identifier.issn0360-5442
dc.identifier.urihttps://dx.doi.org/10.1016/S0360-5442(02)00015-4
dc.identifier.urihttps://hdl.handle.net/11421/21280
dc.descriptionWOS: 000177448800004en_US
dc.description.abstractThe slow pyrolysis of soybean cake in a fixed-bed reactor was investigated under three different atmospheres: static, for determining the effects of pyrolysis temperature and particle size, nitrogen and steam. The liquid yield of 33.78% was attained at 550 degreesC pyrolysis temperature and 200 cm(3)/min sweeping gas flow rate with the soybean oil cake samples having 0.850<D-p<1.250 mm particle size. And the liquid yield reached a maximum value of 42.79% with a steam velocity of 1.3 cm/s. Column chromatography was used to characterize the liquid product, bio-oil. The aliphatic subfractions of the oils were then analyzed by GC/MS. FTIR and H-1-NMR spectra were used to determine structural analysis of pyrolysis oils and aromatic and polar subfractions. The H/C ratios and the structure analysis of the fractions obtained from the biocrudes show that the fractions are quite similar to currently utilized transport fuelsen_US
dc.language.isoengen_US
dc.publisherPergamon-Elsevier Science LTDen_US
dc.relation.isversionof10.1016/S0360-5442(02)00015-4en_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.titleBio-oil production from pyrolysis and steam pyrolysis of soybean-cake: product yields and compositionen_US
dc.typearticleen_US
dc.relation.journalEnergyen_US
dc.contributor.departmentAnadolu Üniversitesi, Mühendislik Fakültesi, Kimya Mühendisliği Bölümüen_US
dc.identifier.volume27en_US
dc.identifier.issue7en_US
dc.identifier.startpage703en_US
dc.identifier.endpage713en_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US


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