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

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PP-I-11KINETICS STUDIES AND MECHANISM OF β-PICOLINE OXIDATIONTO NICOTINIC ACID OVER V 2 O 5 –TiO 2 CATALYSTE.V. Ovchinnikova, G.Ya. Popova, T.V. Andrushkevich, V.A. Chumachenko<strong>Boreskov</strong> <strong>Institute</strong> <strong>of</strong> <strong>Catalysis</strong> SB RAS, pr. Akademika Lavrentieva, 5, Novosibirsk, 630090,Russia; e-mail: evo@catalysis.ru , phone: +7 383 3269412IntroductionThe gas-phase catalytic oxidation <strong>of</strong> β-picoline over oxide vanadia-titania catalysts allows<strong>the</strong> nicotinic acid (NA) production with <strong>the</strong> yield above 80% [1-3]. A previous study <strong>of</strong> thisreaction with β-picoline conversion 20-85% revealed a parallel-consecutive scheme <strong>of</strong> NAformation, via <strong>the</strong> intermediate pyridine-3-carbaldehyde (PA) and directly from β-picoline(βP) [4]. The prospect <strong>of</strong> industrial implementation <strong>of</strong> this method makes it necessary to studykinetics and to develop a kinetic model applicable to real-shaped pellets <strong>of</strong> <strong>the</strong> catalyst.Experimental procedureThe catalyst 20%V 2 O 5 –80%TiO 2 (wt.%) was prepared by spray drying <strong>of</strong> an aqueoussuspension <strong>of</strong> vanadyl oxalate and TiO 2 (anatase) followed by its shaping into rings 2 mm ID,4 mm OD and 5 mm length and calcining in air at 450 °C [1]. The BET specific area <strong>of</strong> <strong>the</strong>catalyst was 25 m 2 /g.The kinetic studies were performed in a differential reactor in a flow-circulating setupwith chromatographic analysis <strong>of</strong> <strong>the</strong> reaction mixture components.Kinetic experiments were performed at ambient pressure and range temperature 250-300 °C over a wide range <strong>of</strong> reagent initial concentrations, %vol.: 0.5-2.5% <strong>of</strong> βP, 10-22% <strong>of</strong>O 2 , 5-40% steam, and nitrogen – balance.In situ FTIR spectroscopy was used to study <strong>the</strong> mechanism <strong>of</strong> oxidation <strong>of</strong> βP and PAinto NA on a V 2 O 5 –TiO 2 catalyst.Results and discussionIn fig., <strong>the</strong> rate <strong>of</strong> βP consumption and <strong>the</strong> rates <strong>of</strong> product accumulation (a) andselectivities (b) are shown as a function <strong>of</strong> βP conversion in <strong>the</strong> temperature range 270-300 °C. The main product <strong>of</strong> <strong>the</strong> reaction in <strong>the</strong> whole investigated range <strong>of</strong> conversion is NA.Selectivity to it is 85-90 %, o<strong>the</strong>r products is 3-pyridine nitrile (PN) and carbon oxides (COx).The complementary support <strong>of</strong> a parallel-consecutive network for <strong>the</strong> NA formation is aFTIR in situ study <strong>of</strong> βP and PA oxidation. NA is formed through <strong>the</strong> same surface speciesfrom βP as well as from PA [5, 6].231

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