Biodiesel Production From Safflower Using Heterogeneous Cao Based Catalysts

dc.contributor.advisor Şeker, Erol
dc.contributor.author Yalman, Emir
dc.contributor.author Şeker, Erol
dc.date.accessioned 2014-07-22T13:51:38Z
dc.date.available 2014-07-22T13:51:38Z
dc.date.issued 2012
dc.description Thesis (Master)--Izmir Institute of Technology, Energy Engineering, Izmir, 2012 en_US
dc.description Includes bibliographical references (leaves: 35-39) en_US
dc.description Text in English; Abstract: Turkish and English en_US
dc.description viii, 39 leaves en_US
dc.description.abstract In this study, the activities of heterogeneous mixed oxide catalyst; calcium oxide on alumina was investigated in the transesterification of canola and safflower vegetable oils to produce biodiesel, i.e. methyl esters. The primary goal of this study is to understand the effect of calcination temperature and calcium oxide (CaO) loading on the conversion activity of calcium oxide on alumina in the transesterification of canola and safflower vegetable oils. The mixed oxide catalyst was prepared by a modified single step sol-gel method. Calcium oxide was chosen because of its well known basic property. This study shows that calcium oxide on alumina catalysts having high CaO dispersion, calcined at high temperature, gave high biodiesel yields even under the reaction conditions, such as low reaction temperature, 50 °C, 9 of methanol/Oil molar ratio, 6 wt. % of catalyst/oil, and also short biodiesel reaction time, such as 4 – 10 minutes in the transesterification of safflower and canola oils. Also, it was observed that 70% CaO/Al2O3 catalyst when calcined at 700 °C was the most active catalyst among all the catalysts prepared in this study. Moreover, the reusability of CaO/Al2O3 demonstrated that ~20 – 250 ppm of Ca was lost during the reaction and the amount of Ca cation leaching depended on the reaction time, CaO loading and the calcination temperature. Also, it was found that Ca cation loss occurred during the reaction did not hinder the activity of the catalysts, which was found by the reusing the catalysts for couple times. Besides, when the biodiesel yield was higher than 70%, the system was influenced by external mass transfer limitation. en_US
dc.identifier.uri https://hdl.handle.net/11147/3483
dc.language.iso en en_US
dc.publisher Izmir Institute of Technology en_US
dc.rights info:eu-repo/semantics/openAccess en_US
dc.subject.lcsh Biodiesel fuels en
dc.subject.lcsh Vegetable oils as fuel en
dc.subject.lcsh Safflower en
dc.subject.lcsh Canola oil en
dc.subject.lcsh Catalysts en
dc.subject.lcsh Lime en
dc.subject.lcsh Heterogeneous catalysis en
dc.title Biodiesel Production From Safflower Using Heterogeneous Cao Based Catalysts en_US
dc.type Master Thesis en_US
dspace.entity.type Publication
gdc.author.institutional Yalman, Emir
gdc.coar.access open access
gdc.coar.type text::thesis::master thesis
gdc.description.department Thesis (Master)--İzmir Institute of Technology, Energy Systems Engineering en_US
gdc.description.publicationcategory Tez en_US
relation.isAuthorOfPublication.latestForDiscovery 9cd609c1-0abd-471c-bc86-0a3b835c3120
relation.isOrgUnitOfPublication.latestForDiscovery 9af2b05f-28ac-4021-8abe-a4dfe192da5e

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