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    Hydrocracking process utilizing high surface area catalysts
    11.
    发明授权
    Hydrocracking process utilizing high surface area catalysts 失效
    使用高表面积催化剂的加氢裂化工艺

    公开(公告)号：US4313818A

    公开(公告)日：1982-02-02

    申请号：US105249

    申请日：1979-12-19

    Applicant: Clyde L. Aldridge ,  Roby Bearden, Jr.

    Inventor： Clyde L. Aldridge ,  Roby Bearden, Jr.

    IPC: B01J37/08 ,  C10G11/02 ,  C10G35/06 ,  C10G49/02 ,  C10G47/06

    CPC classification number: B01J37/08 ,  B01J37/086 ,  C10G11/02 ,  C10G35/06 ,  C10G49/02

    Abstract: A hydrocracking process is provided utilizing high surface area metal-containing catalysts prepared by dispersing a thermally decomposable metal compound in a hydrocarbon oil having a Conradson carbon content of up to about 50 weight percent, the thermally decomposable metal compound being added in an amount sufficient to obtain a specified ratio of atoms of Conradson carbon of the oil chargestock to atoms of metal constituent of the thermally decomposable compound, heating the compound in the presence of a gas comprising either hydrogen or hydrogen sulfide or hydrogen and hydrogen sulfide to form a solid high surface area catalyst. The metal constituent of the thermally decomposable metal compound may be a metal of Groups II, III, IV, V, VIB, VIIB, VIII or mixtures thereof.

    Abstract translation: 使用通过将可热分解的金属化合物分散在具有高达约50重量％的康拉逊碳含量的烃油中而制备的高表面积含金属催化剂的加氢裂化方法，所述可热分解的金属化合物的加入量足以 获得指定比例的含油原料的康拉德森碳与可热分解化合物的金属成分原子，在包含氢或硫化氢或氢气和硫化氢的气体存在下加热该化合物，形成固体高表面 区域催化剂。 可热分解的金属化合物的金属组分可以是II，III，IV，V，VIB，VIIB，VIII族的金属或其混合物。

    Catalyst for the hydroconversion of heavy hydrocarbons
    12.
    发明授权
    Catalyst for the hydroconversion of heavy hydrocarbons 失效
    用于加氢转化重质烃的催化剂

    公开(公告)号：US4226742A

    公开(公告)日：1980-10-07

    申请号：US924818

    申请日：1978-07-14

    Applicant: Roby Bearden, Jr. ,  Clyde L. Aldridge

    Inventor： Roby Bearden, Jr. ,  Clyde L. Aldridge

    IPC: B01J23/28 ,  C10G45/16 ,  B01J31/12 ,  B01J27/04

    CPC classification number: B01J23/28 ,  C10G2300/107

    Abstract: A catalytic hydroconversion process for a hydrocarbonaceous oil is effected by dissolving an oil-soluble metal compound in the oil, converting the compound to a solid, non-colloidal catalyst within the oil and reacting the oil containing the catalyst with hydrogen. Preferred compounds are molybdenum compounds.

    Abstract translation: 烃油的催化加氢转化方法是通过将油溶性金属化合物溶解在油中，将化合物转化成油中的固体非胶态催化剂并使含有催化剂的油与氢反应。 优选的化合物是钼化合物。

    Coal liquefaction process
    16.
    发明授权
    Coal liquefaction process 失效
    煤液化过程

    公开(公告)号：US4793916A

    公开(公告)日：1988-12-27

    申请号：US33682

    申请日：1987-04-03

    Applicant: Clyde L. Aldridge ,  Roby Bearden, Jr.

    Inventor： Clyde L. Aldridge ,  Roby Bearden, Jr.

    IPC: C10G1/08

    CPC classification number: C10G1/086

    Abstract: An improved process is provided for hydroconverting of coal in which a hydrocarbon-dispersible chromium compound is mixed with a hydrocarbonaceous material, in the absence of coal, to form a high metals-containing catalyst precursor concentrate which is heated in the presence of a hydrogen sulfide-containing gas to form a solid chromium-containing catalyst. A portion of the concentrate containing the catalyst is introduced into a diluent to which coal is added or in which coal is present. The resulting mixture is subjected to hydroconversion conditions to convert the coal to a hydrocarbonaceous oil product.

    Abstract translation: 提供了一种改进的方法，用于在不存在煤的情况下将烃分散的铬化合物与烃类材料混合的煤的加氢转化，以形成在硫化氢存在下加热的含高金属的催化剂前体浓缩物 的气体形成固体含铬催化剂。 将含有催化剂的一部分浓缩物引入添加了煤或其中存在煤的稀释剂中。 将所得混合物进行加氢转化条件以将煤转化为含烃油产物。

    Hydroconversion process with combined temperature and feed staging
    17.
    发明授权
    Hydroconversion process with combined temperature and feed staging 失效
    加氢转化过程与组合温度和饲料分期

    公开(公告)号：US4762607A

    公开(公告)日：1988-08-09

    申请号：US037511

    申请日：1987-04-13

    Applicant: Clyde L. Aldridge ,  William E. Lewis ,  Roby Bearden, Jr. ,  Francis X. Mayer

    Inventor： Clyde L. Aldridge ,  William E. Lewis ,  Roby Bearden, Jr. ,  Francis X. Mayer

    IPC: C10G49/12 ,  C10G65/10

    CPC classification number: C10G49/12 ,  C10G65/10

    Abstract: A slurry catalytic hydroconversion process comprising at least two hydroconversion zones is provided in which the heavy hydrocarbonaceous fresh oil feed is added to more than one hydroconversion zone. Additional portions of catalysts or catalyst precursors are also added to the first hydroconversion zone and to additional hydroconversion zones wherein said additional hydroconversion zones are maintained at a temperature of at least 10.degree. F. higher than an immediate preceding hydroconversion zone.

    Abstract translation: 提供了包含至少两个加氢转化区的淤浆催化加氢转化方法，其中将重质烃类新鲜油进料加入多于一个加氢转化区。 催化剂或催化剂前体的另外部分也加入到第一加氢转化区和另外的加氢转化区中，其中所述另外的加氢转化区保持在比紧邻的前一个加氢转化区高至少10°F的温度。

    Hydroconversion of an oil-coal mixture
    19.
    发明授权
    Hydroconversion of an oil-coal mixture 失效
    油 - 煤混合物的加氢转化

    公开(公告)号：US4298454A

    公开(公告)日：1981-11-03

    申请号：US83671

    申请日：1979-10-11

    Applicant: Clyde L. Aldridge ,  Roby Bearden, Jr.

    Inventor： Clyde L. Aldridge ,  Roby Bearden, Jr.

    IPC: C10G1/00 ,  C10G1/08 ,  C10G45/16 ,  C10G1/06

    CPC classification number: C10G1/086 ,  C10G1/006 ,  C10G1/083 ,  C10G2300/107 ,  Y10S208/951

    Abstract: A process for catalytically hydroconverting a mixture of coal and a hydrocarbonaceous oil is effected by forming a mixture of a thermally decomposable metal compound, oil and coal, converting the compound to a catalyst within the mixture and reacting the mixture with hydrogen. Preferred compounds are molybdenum compounds.

    Abstract translation: 通过形成可热分解的金属化合物，油和煤的混合物，将该化合物转化成混合物内的催化剂并使该混合物与氢气反应，来实现催化加氢转化煤和烃油的混合物的方法。 优选的化合物是钼化合物。

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