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

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PP-III-18DEVELOPMENT OF INDUSTRIAL CATALYST SELECTIVITY INTHE HYDROGENATION PROCESS OF DIENES С 9 –С 14Egor M. Yuriev, Elena N. Ivashkina, E.D. Ivanchina, A. KolupaevTomsk Polytechnic University, 634050, Lenin Street, 30, Tomsk, Russia;fax: +7(3822)563-435; e-mail: emyu@anchem.chtd.tpu.ru, emyu@sibmail.comTraditionally increase <strong>of</strong> catalyst efficiency for <strong>the</strong> oil refining processes requireslaboratory and pilot research. The ways <strong>of</strong> Ni-catalyst development which we propose arebased on a calculation with use <strong>of</strong> a ma<strong>the</strong>matical model for higher diolefines hydrogenationprocess.For <strong>the</strong> most part diolefines are hydrogenated to olefins, which, in <strong>the</strong>ir turn, can behydrogenated to paraffins and thus <strong>the</strong> process selectivity and <strong>the</strong> yield <strong>of</strong> desired product arereduced.The main peculiarity <strong>of</strong> this process is a selective catalyst poisoning with a sulfur-bearingsubstance in order to raise catalyst selectivity.The ma<strong>the</strong>matical model <strong>of</strong> hydrogenation process is based on a scheme <strong>of</strong> chemicaltransformations. Sulfur-bearing substance (DMDS) takes part in <strong>the</strong> following reactions:CH −S −S − CH + 1.5H + 1.5Ni → 1.5NiS + 2CH + 0.5H S3 3 2 4 2Ni+ H2S → NiS+H2(2)Reaction (2) leads to desorption <strong>of</strong> Ni from catalyst surface. In <strong>the</strong> presence <strong>of</strong> water <strong>the</strong>deactivation <strong>of</strong> catalyst is very probable:NiS + H2O → NiO + H2S(3)Thermodynamic analysis shows that reaction (1) is irreversible, and so quantity <strong>of</strong>poisoning substance on <strong>the</strong> catalyst surface depends on <strong>the</strong> reaction (2) equilibrium. Catalystactivity reduces as a result <strong>of</strong> this reaction. Quantity <strong>of</strong> sulphide, in its turn, increases with <strong>the</strong>rise <strong>of</strong> sulfur-bearing substance consumption, with rise <strong>of</strong> equilibrium constant (2) anddecrease <strong>of</strong> hydrogen quantity in <strong>the</strong> system.As <strong>the</strong> dependences <strong>of</strong> hydrogenation reaction rate on <strong>the</strong> catalyst activity are different forolefins and diolefines, <strong>the</strong> determination <strong>of</strong> optimal catalytic activity is ra<strong>the</strong>r complexproblem.The following dependence <strong>of</strong> <strong>the</strong> DMDS residual quantity on <strong>the</strong> temperature in reactorwas discovered while analyzing experimental data (Fig. 1).(1)337

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