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    • 1. 发明公开
    • 고활성 미드배럴 수소첨가분해를 위한 촉매 및 그의제조방법
    • 高活性中压水解催化剂及其制备方法
    • KR1020020032410A
    • 2002-05-03
    • KR1020010066392
    • 2001-10-26
    • 차이나 페트로리움 앤드 케미컬 코포레이션후순 리서치 인스티튜트 오브 페트로리움 앤 페트로케미컬즈 씨노펙 코포레이션
    • 왕,펭라이유,젱난구안,밍후아동,리팅
    • B01J29/80B01J29/16B01J29/12
    • C10G47/20B01J29/08B01J29/084B01J29/7007B01J29/80B01J2229/26B01J2229/42
    • PURPOSE: A highly active midbarrel hydrocracking catalyst and the preparation thereof are provided to overcome the drawbacks of the prior catalysts and to develop a hydrocracking catalyst with a high activity and high yield to middle distillates. CONSTITUTION: The midbarrel hydrocracking catalyst with a zeolite, an amorphous silica-alumina and alumina as a support, Group VIII metal(s) and/or Group VIB metal(s) as active components comprises, on the basis of the catalyst weight, 4% to 28% of a modified zeolite-Y and 4% to 28% of a modified zeolite-β, wherein the zeolite-Y has a relative crystallinity of higher than 95%, a silica/alumina molar ratio of 9.0 to 30.6, an infrared acid of 0.30 to 0.90 mmol/g with more than 95% of Bronsted acid, a unit cell size of 24.25x10¬-10 m to 24.45x10¬-10 m, a Na2O weight content of less than 0.16 the modified zeolite-β has a silica/alumina molar ratio of 85 to 153, a Na2O weight content of less than 0.15%, a relative crystallinity of 100 to 110% and an infrared acid of 0.1 to 0.4 mmol/g. The process for preparing the hydrocracking catalyst comprises the steps of (a) mixing the defined amount of the modified zeolite-Y, the modified zeolite-β, optional amorphous silica-alumina and macroporous alumina, microporous alumina, and extrusion aid, forming by extrusion, and drying; (b) calcining the dried material of first step to yield the support; and (c) impregnating the support of the step (a) with an impregnation solution of the active Group VIII and/or Group VIB metal components, and then drying, calcining to yield the catalyst.
    • 目的:提供一种高活性中间条件加氢裂化催化剂及其制备方法,以克服现有催化剂的缺点,开发出具有高活性和高产率的中间馏分的加氢裂化催化剂。 构成:具有沸石,无定形二氧化硅 - 氧化铝和氧化铝作为载体的中间条件加氢裂化催化剂,作为活性组分的第Ⅷ族金属和/或ⅥB族金属包含基于催化剂重量的4 %〜28%的改性沸石-Y和4%〜28%的改性沸石-β,其中沸石Y的相对结晶度高于95%,二氧化硅/氧化铝摩尔比为9.0〜30.6, 红霉酸为0.30〜0.90mmol / g,布朗斯台德酸为95%以上,晶胞尺寸为24.25×10 -10〜24.45×10 -10μm,Na 2 O重量含量小于0.16,改性沸石-β 二氧化硅/氧化铝摩尔比为85〜153,Na2O重量含量小于0.15%,相对结晶度为100〜110%,红外线酸为0.1〜0.4mmol / g。 制备加氢裂化催化剂的方法包括以下步骤:(a)将限定量的改性沸石-Y,改性沸石-β,任选的无定形二氧化硅 - 氧化铝和大孔氧化铝,微孔氧化铝和挤出助剂混合,通过挤出成型 ,干燥; (b)煅烧第一步骤的干燥材料以产生载体; 和(c)用活性VIII族和/或VIB族金属组分的浸渍溶液浸渍步骤(a)的载体,然后干燥,煅烧以产生催化剂。