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    • 2. 发明授权
    • Hydrocracking process using a catalyst comprising an IM-5 zeolite and a catalyst comprising an IM-5 zeolite and a promoter element
    • 使用包含IM-5沸石的催化剂和包含IM-5沸石和促进剂元素的催化剂的加氢裂化方法
    • US06344135B1
    • 2002-02-05
    • US09511490
    • 2000-02-23
    • Eric BenazziSlavik Kasztelan
    • Eric BenazziSlavik Kasztelan
    • C10G4716
    • C10G47/20B01J29/78C10G47/16
    • The invention concerns a hydrocracking process using a catalyst comprising at least one matrix, an IM-5 zeolite, at least one metal selected from the group formed by metals from group VIB and group VIII of the periodic table, optionally at least one element selected from the group formed by phosphorous, boron and silicon, and optionally at least one group VIIA and/or at least one group VIIB and/or at least one group VB element (in particular niobium). The invention also concerns a catalyst containing at least one matrix, an IM-5 zeolite, at least one metal from groups VIII and/or VIB and at least one promoter element which is boron and/or silicon. The catalyst can also contain at least one group VIIA element and/or at least one group VIIB element and/or at least one group VB element.
    • 本发明涉及使用包含至少一种基质,IM-5沸石,至少一种选自元素周期表第VIB族和第VIII族金属形成的金属的金属的催化剂的加氢裂化方法,任选地至少一种选自 由磷,硼和硅以及任选的至少一种VIIA族和/或至少一种VIIB族组合和/或至少一种VB族元素(特别是铌)形成的基团。 本发明还涉及含有至少一种基质,IM-5沸石,至少一种来自VIII族和/或VIB族的金属和至少一种作为硼和/或硅的助催化剂元素的催化剂。 催化剂还可含有至少一种VIIA族元素和/或至少一种VIIB族元素和/或至少一种VB族元素。
    • 5. 发明授权
    • Catalyst comprising a zeolite Y globally non-dealuminated and containing boron and/or silicon
    • 催化剂包含全部非脱铝并含有硼和/或硅的沸石Y
    • US06719895B2
    • 2004-04-13
    • US09965804
    • 2001-10-01
    • Samuel MignardNathalie George-MarchalSlavik Kasztelan
    • Samuel MignardNathalie George-MarchalSlavik Kasztelan
    • C10G4716
    • C10G47/20B01J29/166
    • The present invention relates to a hydrocracking process including contacting a hydrocarbon feed with a catalyst which is carried out at a pressure of at least 2 MPa, a temperature of at least 230° C., using a quantity of hydrogen of at least 100 Nl hydrogen/l of feed and with an hourly space velocity of 0.1-10 h−1. The catalyst includes 0.1-99.7% by weight of at least one alumina matrix; 0.1-80% by weight of at least one globally non dealuminated Y zeolite with a lattice parameter of more than 2.438 nm, a global SiO2/Al2O3 mole ratio of less than 8, and a framework SiO2/Al2O3 mole ratio of less than 21 and more than the global SiO2/Al2O3 mole ratio; 0.1-30% by weight of at least one group VIII metal and/or 1-40% by weight of at least one group VIB metal (% oxide); 0.1-20% by weight of at least one promoter element selected from the group formed by boron and silicon (% oxide); 0-20% by weight of at least one group VIIA element; 0-20% by weight of phosphorous (% oxide); and 0.1-20% by weight of at least one group VIIB element.
    • 本发明涉及一种加氢裂化方法,包括使烃进料与催化剂接触,所述催化剂在至少2MPa的压力,至少230℃的温度下使用至少100N氢气的氢气进行 / l的饲料,每小时空速为0.1-10小时-1。 催化剂包含0.1-99.7重量%的至少一个氧化铝基质; 0.1-80重量%的至少一种全部非脱铝Y沸石,其晶格参数大于2.438nm,全体SiO 2 / Al 2 O 3摩尔比 小于8,并且SiO 2 / Al 2 O 3的骨架比小于21且大于全局SiO 2 / Al 2 O 3摩尔比; 0.1-30重量%的至少一种VIII族金属和/或1-40重量% 至少一种VIB族金属(%氧化物); 0.1-20%重量的选自硼和硅(氧化物%)的至少一种助催化剂元素; 0-20%重量的至少一种VIIA族元素 ; 0-20重量%的磷(%氧化物); 和0.1-20重量%的至少一种VIIB族元素。