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

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CATACON CATACON CATACON CATACON CATACONGROUP OF CATALYSTS TESTINGThe group <strong>of</strong> catalysts and supports testingperforms: comparison and lifetime tests, studies<strong>of</strong> catalytic process kinetics and catalysts activityin <strong>the</strong> catalysts deactivation processes, tests <strong>of</strong>laboratory samples, experimental batch catalystsamples and commercial samples (fresh andunloaded from commercial setups).An approach to control <strong>of</strong> catalytic properties isprimarily determined by <strong>the</strong> fact that catalysis isa kinetic phenomenon which is associated withan increase <strong>of</strong> chemical reaction rates undercatalysts action. For this reason, it is reasonableto use specific rate <strong>of</strong> a chemical reactioncalculated per unit catalyst volume (weight,volume, surface) as a criterion <strong>of</strong> catalyticactivity.The flow-circulating method involving differentmodifications and improvements <strong>of</strong> schematicdiagrams <strong>of</strong> a technological setup, associatedwith process peculiar features, is <strong>the</strong> mostpromising method <strong>of</strong> determining catalystsCatalytic processes performed on <strong>the</strong> setup <strong>of</strong> <strong>the</strong> departmentAmination <strong>of</strong> aromaticsNOx reduction by ammonia and syngasSÎ2 reduction by methaneGas-phase nitration <strong>of</strong> aromaticsHydrocrackingHydrolysis <strong>of</strong> COS and HCN during cleaning <strong>of</strong> syngasOxidation <strong>of</strong> binary liquid hydrocarbonsOxidative dimerization <strong>of</strong> methaneOxidation <strong>of</strong> hydrocarbons, ammonia, sulfur dioxide, hydrogen sulfideOxidative ammonolysis <strong>of</strong> propane (propylene) into acroleinPurification <strong>of</strong> ethylene (propylene) from acetylene fractionsSteam and air reforming <strong>of</strong> methaneDehydrogenation <strong>of</strong> hydrocarbonsFischer-Tropsch processSteam conversion and oxidation <strong>of</strong> ÑÎSteam reforming <strong>of</strong> methanol (ethanol)Syn<strong>the</strong>sis <strong>of</strong> ammonia, methanol, vinyl acetateSyn<strong>the</strong>sis <strong>of</strong> unleaded gasoline from gas condensate and by-products <strong>of</strong> oil refiningTests are performed in <strong>the</strong> setups supplied with reactors, 1 to 100 ml in volume, at atmospheric pressure andunder conditions <strong>of</strong> increased pressure (to 100 bar) and maximal temperatures as high as 850 CThe reactor designs allow investigations <strong>of</strong> granules <strong>of</strong> commercial catalysts as well as honeycombcatalysts reinforced with a stainless steel net or <strong>the</strong>ir fragmentsTo obtain reliable data on catalyst activity, we use differential reactors with an externalsteam-gas mixture circulation

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