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

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OP-V-15DEVELOPMENT OF TWO-STAGE PROCESS OF PREPARATION OFMICRO- AND MESOPOROUS CARBONS WITH DEVELOPEDTEXTURE FROM HIGH-ASH BIOMASSP.M. Yeletsky 1 , V.A. Yakovlev 1 , E.A. Ustinov 2 , M.S. Mel’gunov 1 , V.N. Parmon 11 <strong>Boreskov</strong> <strong>Institute</strong> <strong>of</strong> <strong>Catalysis</strong> SB RAS, pr. Akademika Lavrentieva, 5, 630090 Novosibirsk,Russia2 Provita Ltd., 3-7, Line 24, Vasilievsky ostrov, 199106 Saint-Petersburg, RussiaE-mail: yeletsky@catalysis.ruThere are many ways to syn<strong>the</strong>sis <strong>of</strong> amorphous carbon materials with high specificsurface area from a lot <strong>of</strong> precursors – from chemicals and polymers to petrochemical wastesand biomass [1]. Vegetable biomass is <strong>of</strong>ten used for preparation <strong>of</strong> carbon materials byphysical or chemical activation. There is <strong>the</strong> type <strong>of</strong> biomass, possessing anomaly high ashcontent, <strong>the</strong> main component <strong>of</strong> <strong>the</strong> ash is amorphous SiO 2 (more than 95 w. %). O<strong>the</strong>r ashcomponents are <strong>the</strong> oxides and some <strong>of</strong> o<strong>the</strong>r compounds <strong>of</strong> alkaline and alkaline-earthmetals, iron, copper etc. Rice husk (RH) is a «leader» on content <strong>of</strong> <strong>the</strong> ash among <strong>the</strong>biomass and contains up to 23 w. % <strong>of</strong> silica [2-4]. So <strong>the</strong> main feature <strong>of</strong> RH as a carbonprecursor is that <strong>the</strong> silica can affect on texture properties <strong>of</strong> <strong>the</strong> preparing carbon materials.The work is devoted to a development <strong>of</strong> a two-stage method <strong>of</strong> micro- and mesoporouscarbons preparation from high-ash biomass by <strong>the</strong> example <strong>of</strong> rice husk (RH). The process <strong>of</strong>carbonaceous materials preparation, in <strong>the</strong> whole, consists <strong>of</strong> two main stages: a preliminarycarbonization <strong>of</strong> <strong>the</strong> high-ash biomass in fluidized catalyst bed reactor and a treatment <strong>of</strong> <strong>the</strong>prepared carbon-silica composite with sodium and/or potassium compounds in a staticreactor. At <strong>the</strong> same time, <strong>the</strong> both stages have <strong>the</strong> following principle differences:− in order to prepare <strong>the</strong> microporous carbons, one impregnates <strong>the</strong> product <strong>of</strong> <strong>the</strong> RHcarbonization by solution <strong>of</strong> KOH with following drying and activation at 700–900 °С;− in order to prepare <strong>the</strong> mesoporous carbons, one mixes equimolar mixture <strong>of</strong> Na 2 CO 3and K 2 CO 3 with <strong>the</strong> product <strong>of</strong> RH carbonization mechanically with following hightemperatureleaching at 750–1000 °С.Fig. 1. The principle scheme <strong>of</strong> <strong>the</strong> process <strong>of</strong> micro- and mesoporous carbons producing from rice husk196

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