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

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OP-III-23and parameters <strong>of</strong> syn<strong>the</strong>sis procedure <strong>of</strong> carbon nan<strong>of</strong>ibers <strong>of</strong> desired structure will bereported.The considerable <strong>the</strong>oretical and experimental experience collected for today permits oneto formulate <strong>the</strong> basically challenges to be faced while transferring <strong>the</strong> technology from labscaleto pilot plant level. In any case when searching for <strong>the</strong> principle design <strong>of</strong> reactor for <strong>the</strong>syn<strong>the</strong>sis <strong>of</strong> CNFs, <strong>the</strong> defining peculiarity <strong>of</strong> this process must by taken into account. Thepoint is that <strong>the</strong> initial volume <strong>of</strong> loaded catalyst is supposed to be significantly increasing (inhundreds times fold) during <strong>the</strong> process <strong>of</strong> carbon nan<strong>of</strong>ibers deposition which makesimpossible <strong>the</strong> use <strong>of</strong> conventional reactors with a fixed bed catalyst layer. The carbonnan<strong>of</strong>ibers growing over <strong>the</strong> stationary layer <strong>of</strong> catalyst was found to convert into monolithsoon, which causes <strong>the</strong> suppression <strong>of</strong> fur<strong>the</strong>r process <strong>of</strong> syn<strong>the</strong>sis. That is why <strong>the</strong>fundamentally new design solutions are required while creating <strong>the</strong> reactors for CNFsmanufacturing. It should be also noted that <strong>the</strong> specificity <strong>of</strong> this process imposes a limits onrealization <strong>of</strong> syn<strong>the</strong>sis by uninterrupted technology. As soon as <strong>the</strong> reactor is filled with <strong>the</strong>product it should be stopped, emptied and <strong>the</strong>n refilled with <strong>the</strong> next portion <strong>of</strong> catalyst.We have considered and compared a several different types <strong>of</strong> reactor design:• With <strong>the</strong> fluidized catalyst bed;• With <strong>the</strong> moving catalyst;• With <strong>the</strong> moving catalyst countercurrent to gas flow.Never<strong>the</strong>less, for a variety <strong>of</strong> reasons we have chosen <strong>the</strong> type <strong>of</strong> fully rotating horizontalbarrel with <strong>the</strong> cylinder shape. While <strong>the</strong> reactor is revolving on its axis it makes catalystgranules to be continuously moving and over-pouring inside <strong>the</strong> barrel with favors shakingand stirring <strong>of</strong> carbonated catalyst to intensify <strong>the</strong> mass exchange with gaseous phase. Thenanostructured carbon product depositing on catalyst is to occupy gradually <strong>the</strong> void volume<strong>of</strong> rotor reactor that requires fur<strong>the</strong>r break and overloading.There are three principle structures <strong>of</strong> nanoscale carbon fibers that can be distinguished:coaxial-conic, coaxial-cylinder and platelet. The combination <strong>of</strong> said morphologies allowsone to obtain <strong>the</strong> huge variety <strong>of</strong> o<strong>the</strong>r structures <strong>of</strong> CNFs. The syn<strong>the</strong>sis conditions for CNFsin extended scale using <strong>the</strong> prototype rotor reactor will be discussed in <strong>the</strong> report. Thefollowing types <strong>of</strong> CNFs will be considered:• Coaxial-conic fibers (herringbone);• Platelet fibers;• Fea<strong>the</strong>rlike (disordered) fibers.The morphology <strong>of</strong> developed samples <strong>of</strong> CNFs was analyzed and confirmed by scanning(SEM) and transferring (TEM) high resolution electronic microscopy.136

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