Production of olefins
    1.
    发明授权
    Production of olefins 失效
    生产烯烃

    公开(公告)号:US06388161B1

    公开(公告)日:2002-05-14

    申请号:US09594282

    申请日:2000-06-15

    IPC分类号: C10G4702

    摘要: A process for cracking an olefin-rich hydrocarbon feedstock which is selective towards propylene in the effluent, the process comprising contacting a hydrocarbon feedstock containing one or more olefinic components of C4 or greater with a crystalline silicate catalyst to produce an effluent having a second composition of one or more olefinic components of C3 or greater, the feedstock and the effluent having substantially the same olefin content by weight therein characterized in that ethylene is added to the feedstock before the feedstock contacts the catalyst.

    摘要翻译: 一种用于裂解在流出物中对丙烯有选择性的富烯烃的原料的方法,该方法包括将含有一种或多种C4或更多烯烃组分的烃原料与结晶硅酸盐催化剂接触以产生具有第二组成的流出物 C3或更高的一种或多种烯烃组分,所述原料和流出物具有基本上相同的烯烃含量,其特征在于在原料接触催化剂之前将乙烯加入到原料中。

    Process for improving the pour point of feeds containing paraffins using a catalyst based on a bridged dioctahedral 2:1 phyllosilicate
    2.
    发明授权
    Process for improving the pour point of feeds containing paraffins using a catalyst based on a bridged dioctahedral 2:1 phyllosilicate 有权
    使用基于桥联二八面体2:1页硅酸盐的催化剂改善含有链烷烃的进料的倾点的方法

    公开(公告)号:US06736959B2

    公开(公告)日:2004-05-18

    申请号:US09909805

    申请日:2001-07-23

    IPC分类号: C10G4702

    CPC分类号: C10G45/60

    摘要: The invention concerns 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. The catalyst comprises at least one dioctahedral 2:1 phyllosilicate, preferably synthesised in a fluoride medium in the presence of the acid HF and/or a further source of fluoride anions, and preferably having an interplanar spacing of at least 20×10−10 m (2 nm) and comprising pillars based on at least one oxide of elements from groups IVB, VB, VIB, VIII, IB, IIB, IIA or IVA or any combination of these oxides, and preferably selected from the group SiO2, Al2O3, TiO2, ZrO2 and V2O5, or any combination of these latter. The catalyst further comprises at least one hydrodehydrogenating element in the metallic form. The process is carried out at a temperature in the range 170° C. to 500° C., a pressure in the range 1 to 250 bar 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 1/1 of feed. The oils obtained have good pour points and high viscosity indices (VI). The process is also applicable to gas oils and to other feeds requiring a reduction in their pour point.

    摘要翻译: 本发明涉及改进含有多于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催化剂接触。 催化剂包含至少一种二八面体2:1页硅酸盐,优选在氟化物介质中在酸性HF和/或另外的氟化物阴离子的存在下合成,并且优选具有至少20×10 -10 m的晶面间距 (2nm),并且包含基于IVB,VB,VIB,VIII,IB,IIB,IIA或IVA族元素的至少一种氧化物的柱或这些氧化物的任何组合,优选选自SiO 2,Al 2 O 3,TiO 2 ,ZrO 2和V 2 O 5,或这些后者的任何组合。 催化剂还包含至少一种金属形式的氢化氢化元素。 该方法在170℃至500℃的温度,1至250巴的压力和0.05至100小时-1的小时空间速度下进行,在 存在氢的量为50至2000 1/1的进料。 所得油具有良好的倾点和高粘度指数(VI)。 该方法也适用于瓦斯油和需要降低其倾点的其它进料。

    Hydrocracking catalyst, producing method thereof, and hydrocracking method
    4.
    发明授权
    Hydrocracking catalyst, producing method thereof, and hydrocracking method 有权
    加氢裂化催化剂及其制备方法和加氢裂化法

    公开(公告)号:US06551500B1

    公开(公告)日:2003-04-22

    申请号:US09530445

    申请日:2000-07-27

    IPC分类号: C10G4702

    摘要: A hydrocracking catalyst has a carrier that has particles of a compound oxide and a binder present between these particles, and at least one metal component selected from Group 6, Group 9 or Group 10 of the Periodic Table supported on the carrier. The catalyst has a median pore diameter of 40 to 100 Å and the volume of pores whose pore diameter falls within a range of 40 to 100 Å is at least 0.1 mL/g. Moreover, the volume of pores of the catalyst whose pore diameter falls within a range of 0.05 to 5 &mgr;m is 0.05 to 0.5 mL/g, and the volume of pores whose pore diameter is 0.5 to 10 &mgr;m is less than 0.05 mL/g. This catalyst is mechanically strong enough for practical use and has a high conversion rate and middle distillate selectivity in hydrocracking of hydrocarbon oils, particularly vacuum gas oil.

    摘要翻译: 加氢裂化催化剂具有载体,该载体具有复合氧化物和存在于这些颗粒之间的粘合剂的颗粒,以及至​​少一种选自载体上负载的元素周期表第6族,第9族或第10族的金属组分。 催化剂的中值孔径为40〜100,孔径在40〜100范围内的孔体积为0.1mL / g以上。 此外,孔径在0.05〜5μm的范围内的催化剂的孔的体积为0.05〜0.5mL / g,孔径为0.5〜10μm的孔的体积小于0.05mL / g。 该催化剂机械强度足以用于实际应用,并且在烃油,特别是减压瓦斯油的加氢裂化中具有高转化率和中等馏出物选择性。

    Catalyst that comprises a clay and an element of group VB, and its use in hydrocraking of petroleum feedstocks that contain hydrocarbon
    7.
    发明授权
    Catalyst that comprises a clay and an element of group VB, and its use in hydrocraking of petroleum feedstocks that contain hydrocarbon 失效
    包含粘土和VB族元素的催化剂,以及其用于加氢裂化含有烃的石油原料

    公开(公告)号:US06251261B1

    公开(公告)日:2001-06-26

    申请号:US09344348

    申请日:1999-06-25

    IPC分类号: C10G4702

    CPC分类号: C10G47/12 B01J21/16 B01J23/20

    摘要: The invention relates to a hydrocracking catalyst that comprises at least one oxide-type amorphous or poorly crystallized matrix, at least one element of group VB, preferably niobium, and at least one clay that is selected from the group that is formed by the 2:1 dioctahedral phyllosilicates and the 2:1 trioctahedral phyllosilicates, optionally at least one element that is selected from among the elements of group VIB and group VIII, optionally at least one element that is selected from the group that is formed by P, B, Si, and optionally at least one element of group VIIA. The invention also relates to the use of this catalyst in hydrocracking of feedstocks that contain hydrocarbon.

    摘要翻译: 本发明涉及一种加氢裂化催化剂,其包括至少一种氧化物型无定形或结晶不良的基体,VB族的至少一种元素,优选铌,以及至少一种选自由2: 1个二八面体页硅酸盐和2:1三八面体页硅酸盐,任选地至少一种选自VIB族和VIII族元素的元素,任选地至少一种选自由P,B,Si ,和任选的VIIA族的至少一种元素。 本发明还涉及该催化剂在含有烃的原料的加氢裂化中的用途。

    Cogel containing oxidic compounds of tetravalent, trivalent, and divalent metallic elements
    10.
    发明授权
    Cogel containing oxidic compounds of tetravalent, trivalent, and divalent metallic elements 有权
    Cogel含有四价,三价和二价金属元素的氧化物

    公开(公告)号:US06537442B1

    公开(公告)日:2003-03-25

    申请号:US09720852

    申请日:2001-02-20

    IPC分类号: C10G4702

    CPC分类号: B01J37/036

    摘要: The invention pertains to a cogel comprising oxidic compounds of one or more trivalent metallic elements selected from the group of aluminum, borium, gallium, chromium, iron, cobalt, manganese, vanadium, molybdenum, tungsten, indium, rhodium, scandium, or mixtures thereof, oxidic compounds of one or more tetravalent metallic elements selected from the group of silicon, titanium, germanium, or mixtures thereof and oxidic compounds of one or more divalent metallic elements with at least one divalent metallic element not selected from Group VIII non-noble metallic elements, wherein a) the cogel is essentially X-ray amorphous apart from saponite, if present; b) the saponite content CA of the cogel is less than 60%; c) the cogel has a surface area of at least 400 m2/g; d) the cogel has a cation-exchange capacity of at least 0.5 wt %; and e) the total of sodium and potassium contained in the cogel amounts to less than 0.5 wt %, based on the total weight of the cogel. The invention further relates to a process for preparing said cogel as well as to catalysts comprising these cogels as cracking component, a process for preparing said catalysts, and the use of these catalysts for hydroprocessing applications.

    摘要翻译: 本发明涉及包含选自铝,硼,镓,铬,铁,钴,锰,钒,钼,钨,铟,铑,钪或其混合物中的一种或多种三价金属元素的氧化物的共凝胶 选自硅,钛,锗或其混合物的一种或多种四价金属元素的氧化化合物和一种或多种二价金属元素的氧化化合物与至少一种未选自VIII族非贵金属的二价金属元素 元素,其中a)如果存在,共聚胶基本上是除皂石外的X射线无定形的; b)共聚胶的皂石含量CA小于60%; c)共凝胶的表面积至少为400m 2 / g; d)共聚物具有至少0.5重量%的阳离子交换容量; 基于共聚胶的总重量,共聚胶中所含的钠和钾的总量小于0.5重量%。 本发明还涉及一种制备所述共聚物的方法以及包含这些凝结剂作为裂化组分的催化剂,制备所述催化剂的方法以及这些催化剂用于加氢处理应用的方法。