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    • 1. 发明授权
    • Noble metal hydrocracking catalysts
    • 贵金属加氢裂化催化剂
    • US06174430B1
    • 2001-01-16
    • US09536770
    • 2000-03-28
    • Bruce Herman Charles WinquistDavid Allen Cooper
    • Bruce Herman Charles WinquistDavid Allen Cooper
    • C10G4704
    • C10G47/18B01J21/04B01J29/126B01J35/0026B01J35/0073B01J35/1023B01J35/1038B01J35/1042B01J35/108B01J37/0009
    • A noble metal hydrocracking catalyst which has high selectivity for naphtha range products is provided. The hydrocracking catalyst comprises: a) from about 70 to about 90 weight percent of a Y zeolite, based on the catalyst having a silica to alumina mole ratio of from about 4.8 to less than 6.0, a unit cell constant within the range of about 24.50 to about 24.57, a Na2O level of less than or equal to about 0.2 weight percent; b) from about 10 to about 30 weight percent, based on the catalyst of an alumina having a mercury intrusion pore volume within the range from about 0.55 to about 0.85 cc/g; and c) from about 0.5 to 1 weight percent, based on the catalyst of a noble metal wherein said hydrocracking catalyst have a dispersivity of the noble metal of equal or greater than about 50% by hydrogen chemisorption measurement, a surface area of greater than or equal to 700 m2/g by BET surface area measurement, a compacted bulk density within the range of from about 0.40 to 0.58 g/cc, and a mercury pore volume within the range of from about 0.4 to about 0.7 ml/g.
    • 提供了对石脑油范围产品具有高选择性的贵金属加氢裂化催化剂。 加氢裂化催化剂包括:a)约70至约90重量%的Y沸石,基于氧化硅与氧化铝摩尔比为约4.8至小于6.0的催化剂,单位晶胞常数在约24.50 至约24.57,小于或等于约0.2重量%的Na 2 O水平; b)约10至约30重量%,基于催化剂,其具有在约0.55至约500的范围内的水银侵入孔体积 0.85cc / g; andc)为约0.5至1重量%,基于贵金属的催化剂,其中所述加氢裂化催化剂通过氢化学吸附测量具有等于或大于约50%的贵金属的分散性,表面积大于或等于 通过BET表面积测量至700m 2 / g,压实堆积密度在约0.40至0.58g / cc的范围内,并且水银孔体积在约0.4至约0.7ml / g的范围内。
    • 3. 发明授权
    • Hydrocracking catalyst having a unique silica-alumina substrate
    • 具有独特二氧化硅 - 氧化铝底物的加氢裂化催化剂
    • US06733657B2
    • 2004-05-11
    • US10045678
    • 2002-01-15
    • Eric BenazziTivadar CseriMagalie Roy-AubergerPatrick Euzen
    • Eric BenazziTivadar CseriMagalie Roy-AubergerPatrick Euzen
    • C10G4704
    • C10G47/12B01J21/12B01J35/1019B01J35/1042B01J35/1047B01J35/1061B01J35/108B01J37/0009B01J37/20
    • A hydrocarbon conversion catalyst contains at least one silica-alumina having the following characteristics: A content by weight of silica SiO2 of between 10 and 60% by weight; an Na content less than 300 ppm by weight; a total pore volume of between 0.5 and 1.2 m/g measured by mercury porosimetry; a porosity of said silica-alumina wherein: the volume of mesopores whose diameter is between 40 Å and 150 Å, and whose mean diameter varies between 80 and 120 Å represents between 30 and 80% of the total pore volume, and (ii) the volume of macropores, whose diameter is greater than 500 Å and preferably between 1000 Å and 10,000 Å represents between 20 and 80% of the total pore volume; a specific surface area greater than 200 m2/g, and at least one hydro-dehydrogenating element selected metals of group VIB and group VIII, and optionally phosphorus, boron, silicon, or elements of group VIIA, VIIB or VB.
    • 烃转化催化剂含有至少一种具有以下特征的二氧化硅 - 氧化铝:二氧化硅SiO 2的重量含量为10至60重量%; Na含量小于300重量ppm; 通过水银孔率法测量的总孔体积为0.5-1.2m 2 / g; 所述二氧化硅 - 氧化铝的孔隙率,其中直径为介于40和150之间,其平均直径在80和120之间变化的介孔的体积占总孔体积的30至80%,和(ii) 其直径大于500埃,优选在1000埃至10,000埃之间的大孔体积占总孔体积的20至80%; 比表面积大于200m 2 / g,以及至少一种加氢脱氢元素选择VIB族和VIII族的金属,以及任选的磷,硼,硅或VIIA,VIIB或VB族的元素。