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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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PP-V-23ONE-STAGE PRODUCTION OF HIGH QUALITY DIESEL FROMSUNFLOWER OIL OVER Pd/SAPO-31A.E. Rubanov, O.V. Kikhtyanin, A.V. Toktarev and G.V. Echevsky<strong>Boreskov</strong> <strong>Institute</strong> <strong>of</strong> <strong>Catalysis</strong> SB RAS, Lavrentiev Ave., 5, Novosibirsk 630090, RussiaTel.: +7 383 3309827, e-mail: rubanov@catalysis.ruIntroductionIn last decade production <strong>of</strong> bi<strong>of</strong>uels from renewable sources has become more and moreimportant and this tendency is expected to continue. There are many benefits <strong>of</strong> bi<strong>of</strong>uelsincluding domestic production <strong>of</strong> fuels, decreased greenhouse gas emissions, decreaseddependence on fossil fuels, improvement <strong>of</strong> rural economies and increased national security.Nowadays <strong>the</strong> mixture <strong>of</strong> vegetable oil fatty acid methyl esters produced bytransesterification <strong>of</strong> various vegetable oils was found to be suitable to operate diesel engines.However this technology has numerous disadvantages [1]. These drawbacks can be eliminatedif <strong>the</strong> vegetable oils are converted to a paraffin-rich mixture <strong>of</strong> hydrocarbons overconventional NiMo/Al 2 O 3 and CoMo/Al 2 O 3 catalyst. However this mixture consists <strong>of</strong> n-paraffins (90-95%), it is solid and possesses unfavorable cold flow properties, so it requires tobe isomerized over suitable catalysts.This work presents results on one-stage production <strong>of</strong> a diesel hydrocarbons withimproved temperature characteristics from sunflower oil using Pd-SAPO-31 catalyst.ExperimentalSAPO-31 material was syn<strong>the</strong>sized according to [2]. The calcinedsilicoaluminophosphate was Pd loaded by wet impregnation method followed by drying at120 °C for 4 h and calcining at 600 °C for 3 h in air. Hydroconversion <strong>of</strong> sunflower oil wascarried out using a fixed-bed, downflow, tubular SS reactor at P = 1.2-3.0 MPa, T = 320 –360 °C, WHSV=0.9-1.7 h –1 and H 2 /feed volume ratio = 1000-2000.Results and discussionObviously, diesel production over Pd/SAPO-31 catalyst from vegetable oil is ra<strong>the</strong>rcomplicated process, <strong>the</strong> following reactions take place: hydrogenation <strong>of</strong> double bonds andC-O bonds in <strong>the</strong> molecules on <strong>the</strong> metallic sites, decarboxylation, dehydration andisomerization on <strong>the</strong> acid sites. Hydrogenation and decarboxylation <strong>of</strong> sunflower oil results ina formation <strong>of</strong> n-C17 paraffin predominantly, which is isomerized on acid sites <strong>of</strong> <strong>the</strong> catalystas described in [3]. The yields <strong>of</strong> both diesel hydrocarbons and C 17 fraction as well as i-C 17 /n-C 17 ratio in dependence on reaction conditions are shown in Table 1. The diesel fraction499

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