Multiple-stage hydroprocessing of hydrocarbon oil
    92.
    发明授权
    Multiple-stage hydroprocessing of hydrocarbon oil 失效
    烃油多级加氢处理

    公开(公告)号:US4431526A

    公开(公告)日:1984-02-14

    申请号:US395832

    申请日:1982-07-06

    Abstract: In the catalytic hydroprocessing of hydrocarbons, a hydrocarbon oil is successively contacted with a first hydroprocessing catalyst in a first reaction zone and a second hydroprocessing catalyst in a second reaction zone. The first catalyst has an average pore diameter at least about 30 angstroms larger than the second catalyst, although both have narrow pore size distributions wherein at least about 90 percent of the total pore volume is in pores of diameter from about 100 angstroms to about 300 angstroms, and with essentially all the pores having diameters greater than 100 angstroms.

    Abstract translation: 在烃的催化加氢处理中,烃油在第一反应区和第二反应区中的第二加氢处理催化剂中依次与第一加氢处理催化剂接触。 第一催化剂具有比第二催化剂大至少约30埃的平均孔径,尽管两者具有窄的孔径分布,其中总孔体积的至少约90%在直径为约100埃至约300埃的孔中 并且基本上所有的孔具有大于100埃的直径。

    Catalyst for hydrotreating residual petroleum oil
    93.
    发明授权
    Catalyst for hydrotreating residual petroleum oil 失效
    用于加氢处理残余石油的催化剂

    公开(公告)号:US4351717A

    公开(公告)日:1982-09-28

    申请号:US208956

    申请日:1980-11-21

    Inventor: Stephen B. Jaffe

    Abstract: A catalyst for hydrotreating residual petroleum oil has a pore size distribution related to the measured size distribution of sulfur, nickel and vanadium containing molecules in the residual oil to be hydrotreated. The size distribution of the sulfur, nickel and vanadium containing molecules in the residual oil is measured by gel permeation chromatography. From this measured size distribution, the catalyst pore size distribution which produces desired demetalization and desulfurization is determined for specified process conditions. A catalyst having the determined pore size distribution is produced by calcining alumina at different temperatures to produce alumina with the determined pore size distribution. The alumina is impregnated with cobalt molybdenum to produce the catalyst which is tailored to produce the desired demetalization and desulfurization of the residual oil to be treated.

    Abstract translation: 用于加氢处理残余石油的催化剂具有与要加氢处理的残油中的硫,含镍和含钒分子的测量尺寸分布相关的孔径分布。 通过凝胶渗透色谱法测定残留油中含硫,镍和钒的分子的大小分布。 根据该测量的尺寸分布,对于特定的工艺条件确定产生期望的脱金属和脱硫的催化剂孔径分布。 具有确定的孔径分布的催化剂通过在不同温度下煅烧氧化铝来制备具有确定的孔径分布的氧化铝。 氧化铝用钴钼浸渍以产生适于产生待处理的残余油的所需脱金属和脱硫的催化剂。

    Method of preparing a controlled pore volume alumina with citric acid
    95.
    发明授权
    Method of preparing a controlled pore volume alumina with citric acid 失效
    用柠檬酸制备受控孔体积氧化铝的方法

    公开(公告)号:US4179411A

    公开(公告)日:1979-12-18

    申请号:US850123

    申请日:1977-11-10

    Abstract: A method for preparing an alumina having controlled pore volume distribution is disclosed. The method requires the presence of 0.1-15% by weight of a water soluble aliphatic polycarboxylic acid having from 2-12 carbon atoms based on the dry weight of Al.sub.2 O.sub.3, during alumina precipitation. The resultant calcined alumina has a pore volume distribution such that:A. Nitrogen desorption measurements indicate that less than 10% of the total pores as determined by said method fall between 100-1200A in diameter;B. Nitrogen adsorption measurements indicate that between 10-50% of the total pore volume as determined fall between 100-1200A in diameter; andC. Mercury penetration porisimetry indicates that less than 10% of the total pores as determined by both nitrogen desorption and mercury methods fall between 100-50,000A in diameter.

    Abstract translation: 公开了一种制备具有受控孔体积分布的氧化铝的方法。 在氧化铝沉淀期间,该方法需要存在0.1-15重量%的基于Al 2 O 3的干重的具有2-12个碳原子的水溶性脂族多元羧酸。 得到的煅烧氧化铝具有孔体积分布,使得:A.氮解吸测量表明通过所述方法测定的小于10%的总孔径直径在100-1200A之间; B.氮吸附测量表明,确定的总孔体积的10-50%直径在100-1200A之间; 汞渗透比值法表明,通过氮解吸和汞法测定的小于10%的总孔径直径在100-50,000A之间。

    Process of hydro-refining hydrocarbon oils
    99.
    发明授权
    Process of hydro-refining hydrocarbon oils 失效
    加氢精炼烃油的工艺

    公开(公告)号:US4008149A

    公开(公告)日:1977-02-15

    申请号:US668609

    申请日:1976-03-19

    Abstract: A hydro-refining catalyst comprising at least one hydrogenation metal component supported on an alumina or alumina-containing carrier containing from about 5 to about 25 wt. % silica, said catalyst having a specific surface area in the range of from about 250 to about 300 m.sup.2 /g and a pore volume distribution characterized in that (1) the volume of pores having a diameter of 60 to 150 A is at least about 80% of the volume of pores having a diameter of 0 to 150 A, (2) the volume of pores having a diameter of 150 to 300 A is less than about 20% of the volume of pores of 0 to 300 A, (3) the volume of pores having a diameter of 150 to 2,000 A is less than about 0.01 ml/g, (4) the volume of pores having a diameter of 0 to 600 A is in the range of from about 0.45 to about 0.60 ml/g. The catalyst is used in the hydro-refining of heavy hydrocarbon oils containing sulfur, nitrogen and metal contaminants.

    Abstract translation: 一种加氢精制催化剂,其包含至少一种负载在含有约5至约25重量%的氧化铝或含氧化铝的载体上的氢化金属组分。 所述催化剂具有约250至约300m 2 / g的比表面积和孔体积分布,其特征在于(1)直径为60至150的孔的体积为至少约 直径为0〜150A的孔的体积的80%,(2)直径为150〜300A的孔的体积小于孔的体积的0〜300A,(3 )直径为150至2,000A的孔的体积小于约0.01ml / g,(4)直径为0至600的孔的体积为约0.45至约0.60ml / G。 催化剂用于含硫,氮和金属污染物的重质烃油的加氢精制。

    Catalyst useful for olefin polymerization process
    100.
    发明授权
    Catalyst useful for olefin polymerization process 失效
    催化剂用于烯烃聚合过程

    公开(公告)号:US3978002A

    公开(公告)日:1976-08-31

    申请号:US486788

    申请日:1974-07-09

    Abstract: An olefin polymerization catalyst comprising a silica xerogel support having a pore volume greater than about 2.0 cc/g, the major portion of which volume is provided by pores having pore diameters ranging from 300 to 600 A and a surface area ranging from 200 to 500 m.sup.2 /g, and having deposited thereon a metal-containing catalytic material, such as chromium oxide, or other metal oxide. Further, a polymerization process utilizing such a catalyst for the preparation of polyolefins having relatively low molecular weights and high melt indexes without loss of catalyst activity, especially a process for the preparation of polymers and copolymers of 1-olefins having a maximum of 8 carbon atoms in the chain and having no branching nearer the double bond than the 4-position, e.g., ethylene polymers.

    Abstract translation: 一种烯烃聚合催化剂,其包含孔体积大于约2.0cc / g的二氧化硅干凝胶载体,其主要部分由孔径范围为300-600A的孔和200-500m2的表面积 / g,并且在其上沉积有含金属的催化材料如氧化铬或其它金属氧化物。 此外,使用这种催化剂用于制备具有相对低的分子量和高熔体指数而不丧失催化剂活性的聚烯烃的聚合方法,特别是制备具有最多8个碳原子的1-烯烃的聚合物和共聚物的方法 在链中没有分支比4位更接近双键,例如乙烯聚合物。

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