An Investigation of Catalyt Preparation Conditions and Promoter Loading (sn) Effects on Activity and Selectivity of Pt Catalyists in Citiral Hydrogenation

dc.contributor.advisor Yilmaz, Selahattin
dc.contributor.author Depboylu, Can Okan
dc.date.accessioned 2014-07-22T13:50:47Z
dc.date.available 2014-07-22T13:50:47Z
dc.date.issued 2010
dc.description Thesis (Master)--Izmir Institute of Technology, Materials Science and Engineering, Izmir, 2010 en_US
dc.description Includes bibliographical references (leaves: 52-54) en_US
dc.description Text in English; Abstract: Turkish and English en_US
dc.description x, 59 leaves en_US
dc.description.abstract In this study, citral hydrogenation reaction in liquid phase over silica gel supported Pt and PtSn catalysts were studied. It was desired to hydrogenate carbonyl group (C.O) selectively to produce valuable unsaturated alcohols, namely nerol, geraniol and citronellol. Pt/SiO2 catalysts were prepared by impregnation method while PtSn/SiO2 catalysts were prepared by catalytic reduction (CR), co-impregnation (CI) and successive impregnation (SI) methods. Pt loading over silica gel support was 1 % (w/w). For bimetallic catalysts, the (Sn/Pt) loading ratios were varied as 0.3, 0.5 and 0.7. The effects of parameters investigated in the present study included catalyst activation temperature (350 °C, 450 °C), calcination temperature (400 °C, 500 °C), solvent type (ethanol, 2-pentanol), catalyst activation without calcination, washing of catalyst with 0.1 M NaOH solution, Pt precursor type (hexachloroplatinic acid, platinum II acetylacetonate (PAA)) and Sn loading ratio. For Pt/SiO2 catalysts, maximum citral conversion (89 %) was achieved at lower activation (350 °C) and calcination (500 °C) temperatures when PAA was used. Increasing the activation temperature to 450 °C decreased the citral conversion to 52 % but increased the selectivity to unsaturated alcohols (nerol and geraniol) (SNE+GE) from 8 % to 60 %. It was observed that the lower activation temperature provided higher citral conversion but lower selectivity to unsaturated alcohols. Washing of catalyst and using of 2-pentanol prevented the acetal formation. Catalyst activated without calcination step gave lower conversion (20 %) and SNE+GE of 30 %. For bimetallic catalyst (PtSn/SiO2), maximum citral conversion was observed as 91.1 % when catalyst was prepared by CR method and calcined at 500 °C. Higher citral conversion and selectivity to unsaturated alcohols were achieved at the higher calcination temperature and higher reduction temperature. CR method was the most appropriate preparation method for bimetallic catalysts compared to CI and SI. An optimum of activity (91.1 %) and selectivity (89.7 %) was found at a Sn/Pt ratio 0.5. en_US
dc.identifier.uri https://hdl.handle.net/11147/3047
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 Catalysts en
dc.subject.lcsh Catalysts--Testing en
dc.subject.lcsh Hydrogenation en
dc.title An Investigation of Catalyt Preparation Conditions and Promoter Loading (sn) Effects on Activity and Selectivity of Pt Catalyists in Citiral Hydrogenation en_US
dc.type Master Thesis en_US
dspace.entity.type Publication
gdc.author.institutional Depboylu, Can Okan
gdc.coar.access open access
gdc.coar.type text::thesis::master thesis
gdc.description.department Thesis (Master)--İzmir Institute of Technology, Materials Science and Engineering en_US
gdc.description.publicationcategory Tez en_US
gdc.description.scopusquality N/A
gdc.description.wosquality N/A
relation.isAuthorOfPublication.latestForDiscovery 383d88ac-56b2-4451-a813-f8456d2fa034
relation.isOrgUnitOfPublication.latestForDiscovery 9af2b05f-28ac-4021-8abe-a4dfe192da5e

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