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Supported Bifunctional Cobalt Catalysts for CO and H-2 Conversion to Fuel Fractions of Hydrocarbons

机译:用于CO和H-2转化为烃类的CO和H-2转化的双官能钴催化剂

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of Supported bifunctional cobalt catalysts for the direct conversion of synthesis gas to liquid fuelfraction hydrocarbons (HCs) have been studied. The effect of ZSM-5 zeolite in the structure of the support preformed using a boehmite binder on the catalytic and physicochemical properties of the catalysts has been examined. The synthesized catalysts exhibit high mechanical strength; therefore, they can be used in tubular Fischer-Tropsch (FT) synthesis reactors. The efficiency of the supported bifunctional Co/(Dl(2)O(3)-ZSM-5) catalysts is determined by the number of active metal cobalt sites, the degree of dispersion of the cobalt crystallites, and the total surface acidity. An increase in the catalyst acidity leads to an increase in the fuel fraction selectivity owing to long-chain HCs. At the same time, the activity of the catalysts decreases; therefore, a decrease in their efficiency is observed. It is assumed that this finding is attributed to the diffusion limitations between the HC synthesis and hydrotreating sites.
机译:研究了用于将合成气直接转化为液体成本烃(HCS)的双官能钴催化剂。研究了ZSM-5沸石在催化剂的催化和物理化学性质上使用勃姆石粘合剂进行催化剂的支撑件的结构的影响。合成催化剂具有高机械强度;因此,它们可用于管状费 - 托(FT)合成反应器。支持的双官能CO /(DL(2)O(3)-ZSM-5)催化剂的效率由活性金属钴位点,钴微晶的分散度和总表面酸度的数量测定。催化剂酸度的增加导致由于长链HCs的燃料级分选择性的增加。同时,催化剂的活性降低;因此,观察到其效率的降低。假设该发现归因于HC合成和加氢处理位点之间的扩散限制。

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