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Catalytic converter null for hydrogen treating of coal liquefaction wraparound

机译:煤液化包裹氢处理的催化转化器无效

摘要

PURPOSE:To form a catalyst for petroleum refining by depositing an oxide of the group VI metal in the periodic table and an oxide of the group VIII metal on the carrier consisting of gamma-alumina and the pentasil type zeolite containing SiO2 and Al2O3. CONSTITUTION:Alumina hydrate gel, together with pentasil type zeolite added thereto, is heated and mixed in a kneader to prepare a paste which, after formation, is baked at a temperature of 400-600 deg.C to make a catalyst carrier consisting of 80-20wt.% of gamma-alumina and 20-80wt.% of pentasil type zeolite wherein the molar ratio of SiO2 to Al2O3 is 25-100 and the acid concentration is 0.35-1.25mmol/g. 10-20wt.% of an oxide of the group VI metal in the periodic table and 3-10wt.% of an oxide of the group metal VIII are deposited on this carrier, thereby producing a catalyst having an average pore diameter of 120-220Angstrom for hydrogenation of a circulation solvent for coal liquefaction.
机译:用途:通过在周期表中沉积VI族金属的氧化物和VIII族金属的氧化物在由γ-氧化铝和含有SiO2和Al2O3的pentasil型沸石组成的载体上沉积来形成石油精制催化剂。组成:将水合氧化铝凝胶与加入其中的pentasil型沸石一起在捏合机中加热并混合,制得糊状物,形成后将其在400-600℃的温度下烘烤,制成由80%组成的催化剂载体-20wt。%的γ-氧化铝和20-80wt。%的pentasil型沸石,其中SiO 2与Al 2 O 3的摩尔比为25-100,酸浓度为0.35-1.25mmol / g。在该载体上沉积10-20重量%的元素周期表中VI族金属的氧化物和3-10重量%的VIII族金属中的氧化物,从而产生平均孔径为120-220埃的催化剂用于循环液加氢以煤液化。

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