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

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PP-III-1for <strong>the</strong> traditional scheme <strong>of</strong> <strong>the</strong> industrial process organization: two adiabatic stages andintermediate heat removal.Novel schemes <strong>of</strong> <strong>the</strong> heat-transfer with use <strong>of</strong> <strong>the</strong> heat-conducting compositecatalytically active materials [iii,iv] may allow approaching <strong>the</strong> optimal temperature field infixed catalyst bed and improving <strong>the</strong> process performance. The application <strong>of</strong> such schemesrequests new high-performance catalysts, which can stably operate in a wide temperaturerange, e.g. those described in recent patents [v,vi].The topic <strong>of</strong> <strong>the</strong> present study is considering <strong>the</strong> variants <strong>of</strong> <strong>the</strong> catalyst layer organizationwith controlled temperature pr<strong>of</strong>ile close to optimal for <strong>the</strong> WGSR process. The results permitconcluding that <strong>the</strong> use <strong>of</strong> high-performance catalysts in apparatuses with controlledtemperature pr<strong>of</strong>ile can greatly increase efficiency <strong>of</strong> <strong>the</strong> WGSR stage <strong>of</strong> <strong>the</strong> natural gasutilization in <strong>the</strong> schemes <strong>of</strong> ammonia syn<strong>the</strong>ses and hydrogen production as well as inschemes <strong>of</strong> electric power production using <strong>the</strong> fuel cells.Referencesi Pismen М.К. Hydrogen production in petroleum refining industry (in rus). М.: Chimija, 1976.ii Production <strong>of</strong> process gas for ammonia syn<strong>the</strong>sis and methanol from hydrocarbon gas (in rus) /А.G. Leybusch. М.: Chimija, 1971. P. 286.iii N.A. Baronskaya, T.P. Minyukova, A.G. Sipatrov, M.P. Demeshkina, A.A. Khassin, S.V. Dimov, S.P. Kozlov,V.V. Kuznetsov, V.Ya. Terentiev, A.P. Khristolyubov, O.F. Brizitskiy, T.M. Yurieva. / Compact reactor for watergas shift reaction over <strong>the</strong>rmal-conducting catalysts. Chem. Eng. J. 134 (2007) 195-199.iv Pat. 2295385 (RU). Heat-conducting composit catalyst and method carbon monoxide water steam conversionprocess / N.A. Baronskaya, O.F. Brizitskiy, N.А. Buchenko, M.P. Demeshkina, S.V. Dimov, V.V. Kuznetsov,T.P. Minyukova, V.Ya. Terentiev, A.A. Khassin, A.P. Khristolyubov, T.M. Yurieva. 2007, to <strong>Boreskov</strong> <strong>Institute</strong><strong>of</strong> <strong>Catalysis</strong>.v Pat. 2314870 (RU). Catalyst <strong>of</strong> carbon monoxide water steam conversion process, method <strong>of</strong> preparing andmethod <strong>of</strong> using / T.M. Yurieva, M.P. Demeshkina, A.A. Khassin, T.P. Minyukova, L.M. Pljasova,N.A. Baronskaya, М.V. Lebedeva, I.D. Reznichenko, L.G. Volchatov, А.P. Bocharov, М.I. Tseljutina,О.М. Posohova, Т.I. Andreeva. 2008, to <strong>Boreskov</strong> <strong>Institute</strong> <strong>of</strong> <strong>Catalysis</strong> and Angarsk Plant <strong>of</strong> Catalysts andOrganic syn<strong>the</strong>sis.vi Pat. 2281805 (RU). Catalyst and method carbon monoxide water steam conversion process /N.A. Baronskaya, N.А. Buchenko, M.P. Demeshkina, I.SH. Itenberg, Е.V. Korzh, T.P. Minyukova,A.A. Khassin, T.M. Yurieva. 2006, to <strong>Boreskov</strong> <strong>Institute</strong> <strong>of</strong> <strong>Catalysis</strong>.304

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