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    • 4. 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
    • Process for improving the pour point, and a catalyst based on at least one MTT, Ton or Fer zeolite
    • 改善倾点的方法,以及基于至少一种MTT,Ton或Fer沸石的催化剂
    • US06235960B1
    • 2001-05-22
    • US09310181
    • 1999-05-12
    • Eric BenazziSlavik KasztelanNathalie George-Marchal
    • Eric BenazziSlavik KasztelanNathalie George-Marchal
    • C07C513
    • C10G45/64B01J29/67B01J29/7284B01J29/7292B01J29/7484B01J29/7492B01J29/7884B01J29/7892B01J35/1061B01J35/1085B01J2229/26B01J2229/42
    • A process for improving the pour point of a feed comprising paraffins containing more than 10 carbon atoms, in which the feed to be treated is brought into contact with a catalyst comprising at least one zeolite with structure type MTT, TON or FER or any possible combination of these three, at least one hydro-dehydrogenating element selected from elements from group VIB and group VIII of the periodic table, at least one deposited promoter element (boron, silicon, phosphorous), optionally at least one group VIIA element, optionally at least one group VIIB element, at a temperature in the range 170° C. to 500° C., a pressure in the range 1 to 250 bars and at an hourly space velocity in the range 0.05 to 100 h−1, in the presence of hydrogen in an amount of 50 to 2000 l/l of feed. The oils obtained have good pour points and high viscosity indices (VI). The process is also applicable to gas oils, and other feeds requiring a reduction in pour point. The invention also relates to a catalyst containing silicon and to its use for converting hydrocarbon-containing feeds.
    • 一种用于改进含有多于10个碳原子的链烷烃的进料的倾点的方法,其中待处理的进料与包含至少一种结构类型为MTT,TON或FER的沸石或任何可能的组合的催化剂接触 这些三种中的至少一种选自元素周期表第VIB族和第VIII族元素的至少一种加氢脱氢元素,至少一种沉积的促进元素(硼,硅,磷),任选至少一种VIIA族元素,任选至少 一组VIIB元素,在170℃至500℃的温度范围内,压力范围为1至250巴,时间空间速度为0.05至100小时-1,在存在 量为50至2000升/升的进料的氢。 所得油具有良好的倾点和高粘度指数(VI)。 该方法也适用于需要降低倾点的瓦斯油和其它进料。本发明还涉及含硅的催化剂及其用于转化含烃物料的用途。
    • 10. 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。