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    • 1. 发明授权
    • Catalyst containing phosphorous and a process hydrotreatment of petroleum feeds using the catalyst
    • 含有磷的催化剂和使用催化剂的石油进料的工艺加氢处理
    • US06332976B1
    • 2001-12-25
    • US09310105
    • 1999-05-12
    • Samuel MignardNathalie George-MarchalVirginie HarleSlavik Kasztelan
    • Samuel MignardNathalie George-MarchalVirginie HarleSlavik Kasztelan
    • C10G4508
    • B01J27/188B01J35/002B01J35/1019B01J35/1061B01J35/108C10G45/08C10G49/04
    • The invention concerns an alumina based catalyst containing, expressed as the oxide content by weight, 2-10% by weight of cobalt oxide CoO, 10-30% by weight of molybdenum oxide MoO3 and 4-10% of phosphorous oxide P2O5, with a BET surface area in the range 100-300 m2/g, a crushing strength CSH of more than 1.4 MPa, and an average pore diameter in the range 8-11 nm, the pore volume of pores with diameter of more than 14 nm being less than 0.08 ml/g, or less than 22% of total pore volume, the volume of pores with a diameter of less than 8 nm being at most 0.05 ml/g, or less than 10% of total pore volume, the volume of pores with diameter less than 10 nm being in the range of 20%-70%, the volume of pores with diameter between 10 nm and 13 nm being in the range of 20%-60%, and the volume of pores with a diameter which is in the range 8 to 14 nm being in the range 0.20 ml/g to 0.8 ml/g. The invention also concerns a hydrotreatment process using the catalyst, in particular hydrodesulphuration.
    • 本发明涉及一种氧化铝基催化剂,其含有氧化物含量为2-10重量%的氧化钴CoO,10-30重量%的氧化钼MoO 3和4-10重量%的氧化磷P2O5,其中a BET表面积在100-300m2 / g范围内,抗碎强度CSH大于1.4MPa,平均孔径在8-11nm范围内,孔径大于14nm的孔体积较小 直径小于8nm的孔的体积至少为0.05ml / g,或小于总孔体积的10%,孔的体积小于0.08ml / g,或小于总细孔容积的22% 直径小于10nm的范围在20%-70%的范围内,直径在10nm和13nm之间的孔的体积在20%-60%的范围内,直径的孔的体积是 在8至14nm的范围内在0.20ml / g至0.8ml / g的范围内。本发明还涉及使用该催化剂,特别是加氢脱硫的加氢处理方法。
    • 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
    • US06420296B2
    • 2002-07-16
    • US09305296
    • 1999-05-05
    • Samuel MignardNathalie George-MarchalSlavik Kasztelan
    • Samuel MignardNathalie George-MarchalSlavik Kasztelan
    • B01J2910
    • C10G47/20B01J29/166
    • A catalyst comprising 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); 0.1-20% by weight of at least one group VIIB element, useful for hydrocracking processes, especially at low pressures of 7.5 to 11 MPa.
    • 包含0.1-99.7重量%的至少一种氧化铝基质的催化剂; 0.1-80重量%的至少一种全球非脱铝Y沸石,其晶格参数大于2.438nm,全球SiO 2 / Al 2 O 3摩尔比小于8,框架SiO 2 / Al 2 O 3摩尔比小于21, 超过全球SiO2 / Al2O3摩尔比; 0.1-30重量%的至少一种VIII族金属和/或1-40重量%的至少一种VIB族金属(%氧化物); 至少一种选自硼和硅(%氧化物)形成的基团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%); 0.1-20重量%的至少一种VIIB族元素,可用于加氢裂化过程,特别是在7.5至11MPa的低压下。
    • 8. 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。