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

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OP-III-10REACTOR FOR CARBON NANOFIBERS SYNTHESYSPeshnev B.V., Nikolaev A.I., Asilova N.Y.M.V. Lomonosov Moscow State Academy <strong>of</strong> Fine Chemical Technology, Moscow, RussiaThe constructions <strong>of</strong> <strong>the</strong> reactors, proposed for <strong>the</strong> syn<strong>the</strong>sis <strong>of</strong> carbon nan<strong>of</strong>ibers by<strong>the</strong>rmocatalytic decomposition <strong>of</strong> hydrocarbons or disproportionation <strong>of</strong> CO are discussed.The most typical deficiencies in <strong>the</strong>ir constructions are <strong>the</strong> narrow range <strong>of</strong> a change in <strong>the</strong>characteristics <strong>of</strong> <strong>the</strong> obtained product, <strong>the</strong> low degree <strong>of</strong> <strong>the</strong> conversion <strong>of</strong> raw material, <strong>the</strong>difficulty for separation <strong>of</strong> product from catalyst and separation <strong>of</strong> solid and vapor phases, <strong>the</strong>increased requirements for <strong>the</strong> utilized equipment. The original construction <strong>of</strong> reactor for thispurpose is proposed. This reactor makes possible to carry out <strong>the</strong> syn<strong>the</strong>sis <strong>of</strong> carbonnan<strong>of</strong>ibers, to divide solid and vapor phases, to separate <strong>the</strong> formed product from <strong>the</strong> catalystin one apparatus. The possibility <strong>of</strong> obtaining <strong>the</strong> product with different characteristics is <strong>the</strong>merit <strong>of</strong> <strong>the</strong> proposed reactor. The catalyst block, located along <strong>the</strong> axis <strong>of</strong> apparatus is <strong>the</strong>basic element <strong>of</strong> reactor. The form <strong>of</strong> it is <strong>the</strong> inverted, truncated cone. The maximum contact<strong>of</strong> reagent is reached as a result <strong>of</strong> <strong>the</strong> filtration <strong>of</strong> <strong>the</strong> gas through <strong>the</strong> situated in <strong>the</strong> blockcatalyst. The process <strong>of</strong> <strong>the</strong> carbon nan<strong>of</strong>ibers formes on <strong>the</strong> upper catalyst layers is mosteffective. The product is derived through radial clearance between <strong>the</strong> reactor vessel andcatalyst block. Separation <strong>of</strong> solid and vapor phases and separation <strong>of</strong> product from catalyst asa result occurs. It is possible to change <strong>the</strong> time <strong>of</strong> an increase in carbon nan<strong>of</strong>ibers varyingdistance from <strong>the</strong> catalyst surface area to <strong>the</strong> upper edge <strong>of</strong> catalyst block. The result <strong>of</strong> thischanging is <strong>the</strong> possibility <strong>of</strong> obtaining <strong>the</strong> product with different concentration <strong>of</strong> mineralpart in nan<strong>of</strong>ibers and specific adsorptive surface. The diameter <strong>of</strong> <strong>the</strong> fibers and <strong>the</strong>irgraphitization degree are determined by <strong>the</strong> temperature <strong>of</strong> process, by composition and flow<strong>of</strong> reaction gas, by nature <strong>of</strong> catalyst. The results <strong>of</strong> studies carried out at <strong>the</strong> department <strong>of</strong>petrochemical syn<strong>the</strong>sis and syn<strong>the</strong>tic liquid fuel <strong>of</strong> M.V. Lomonosov Moscow state academy<strong>of</strong> fine chemical technology are represented. They confirm <strong>the</strong> possibility <strong>of</strong> syn<strong>the</strong>sis in <strong>the</strong>reactor <strong>of</strong> <strong>the</strong> proposed construction <strong>the</strong> product with different characteristics.109

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