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    Two-stage hydroconversion process (hydrocracking and reforming) using a stabilized aluminosilicate hydrocracking catalyst
    16.
    发明授权
    Two-stage hydroconversion process (hydrocracking and reforming) using a stabilized aluminosilicate hydrocracking catalyst 失效
    使用稳定化的硅铝酸盐加氢裂化催化剂的两阶段加氢转化方法（加氢裂化和重整）

    公开(公告)号：US4137146A

    公开(公告)日：1979-01-30

    申请号：US769625

    申请日：1977-02-16

    Applicant: Jarold A. Meyer

    Inventor： Jarold A. Meyer

    IPC: B01J21/12 ,  B01J23/44 ,  B01J37/03 ,  C10G47/14 ,  C10G69/10 ,  C10G37/00

    CPC classification number: C10G47/14 ,  B01J21/12 ,  B01J37/036 ,  C10G69/10 ,  B01J23/44 ,  Y10S502/50 ,  Y10S502/508 ,  Y10S502/509

    Abstract: A process is described for producing gasoline from a paraffinic hydrocarbon feed wherein the feed is catalytically cracked and then reformed. In the process a novel porous hydrocracking catalyst composite is employed. This catalyst comprises a silica-alumina cracking base component and a noble metal hydrogenation component. It is stabilized as a result of a unique method used for introducing the noble metal in the form of a highly dispersed gravimetric precipitate into a gelatinous silica-alumina cogel precursor of the cracking base component. An organic gravimetric reagent is used for the precipitation. The resulting crackate is reformed by ordinary methods.

    Abstract translation: 描述了从石蜡烃进料生产汽油的方法，其中进料被催化裂化，然后重整。 在此过程中，采用新型多孔加氢裂化催化剂复合材料。 该催化剂包括二氧化硅 - 氧化铝裂解基础组分和贵金属氢化组分。 作为通过将高分散重量沉淀物形式的贵金属引入裂化基础组分的凝胶状二氧化硅 - 氧化铝共凝胶前体的独特方法，其稳定化。 使用有机重量试剂进行沉淀。 所形成的裂解物是通过普通的方法进行改造的。

    Process for producing low density low-sulfur crude oil
    17.
    发明授权
    Process for producing low density low-sulfur crude oil 失效
    生产低密度低硫原油的方法

    公开(公告)号：US4092238A

    公开(公告)日：1978-05-30

    申请号：US743443

    申请日：1976-11-19

    Applicant: Mario Iona

    Inventor： Mario Iona

    IPC: C10G47/00 ,  C10G37/00

    CPC classification number: C10G47/00

    Abstract: Process for producing low density low-sulfur crude oil as feedstock to refinery processes in which a high density, starting crude oil is divided into a base stream and a dilution stream. The dilution stream is separated into a straight run light fraction, at least a medium fraction and an asphaltic residue. At least the medium fraction is subjected to hydrocracking. The hydrocracked fraction and the light fraction are mixed with the base stream and a crude oil of low density and low sulfur content is recovered.

    Abstract translation: 用于生产低密度低硫原油作为炼油方法的原料的方法，其中将高密度起始原油分成基料流和稀释流。 将稀释流分离成直馏轻馏分，至少中等馏分和沥青残余物。 至少中等馏分进行加氢裂化。 将加氢裂化馏分和轻馏分与基料流混合，回收低密度和低硫含量的原油。

    Hydrocracking extraction process for lubes
    18.
    发明授权
    Hydrocracking extraction process for lubes 失效
    润滑油加氢裂化提取工艺

    公开(公告)号：US3929617A

    公开(公告)日：1975-12-30

    申请号：US47060874

    申请日：1974-05-16

    Applicant: EXXON RESEARCH ENGINEERING CO

    Inventor： HENRY H CLARKE ,  GILBERT JOHN B

    IPC: C10G47/12 ,  C10G67/04 ,  C10G37/00

    CPC classification number: C10G47/12 ,  C10G2400/10

    Abstract: High quality UV stable lubricating oil stocks are prepared by hydrocracking a hydrocarbon feedstock under mild hydrocracking conditions to increase the viscosity index of the feedstock. The hydrocrackate product is subsequently solvent-extracted with a solvent having preferential solubility for aromatics, thereby forming extract and raffinate phases. The extract phase is stripped of solvent, and at least a portion of the substantially solvent-free extract phase is recycled to the hydrocracking step.

    Abstract translation: 通过在轻度加氢裂化条件下加氢裂化烃原料来制备高品质的UV稳定润滑油原料，以增加原料的粘度指数。 随后用对芳族化合物具有优先溶解度的溶剂对加氢裂化产物进行溶剂萃取，从而形成萃取液和萃余相。 萃取相被除去溶剂，并且将至少一部分基本上无溶剂的萃取相再循环至加氢裂化步骤。

    Integrated process combining catalytic cracking with hydrotreating
    19.
    发明授权
    Integrated process combining catalytic cracking with hydrotreating 失效
    综合工艺组合催化裂化与加氢处理

    公开(公告)号：US3801495A

    公开(公告)日：1974-04-02

    申请号：US3801495D

    申请日：1972-05-19

    Applicant: CHEVRON RES

    Inventor： GOULD G

    IPC: C01B3/38 ,  C10G69/00 ,  C10G37/00

    CPC classification number: C10G49/007 ,  C01B3/38 ,  C10G69/00 ,  Y02P20/125

    Abstract: AN INTEGRATED PROCESS IS DISCLOSED, COMPRISING CATALYTICALLY CRACKING A HYDROCARBON FEEDSTOCK IN A CATALYTIC CRACKING ZONE; PASSING THE GAS OIL PORTION OF THE EFFLUENT FROM THE CATALYTIC CRACKING ZONE TO A HYDROTREATING ZONE; REGENERATING THE CATALYTIC CRACKING CATALYST USED IN THE CATALYTIC CRACKING ZONE BY BURNING CARBONACEOUS DEPOSITS THEREFROM, THEREBY PRODUCING HEAT; HEATING WATER TO PRODUCE STEAM USING THIS HEAT; PRODUCING HYDROGEN FROM THIS STEAM; PASSING AT LEAST A PORTION OF THE HYDROGEN FORMED TO THE HYDROTREATING ZONE; AND CATALYTICALLY HYDROTREATING THE GAS OIL PORTION IN THE HYDROTREATING ZONE. ALTERNATIVELY, THE HYDROGEN CAN BE PRODUCED BY REACTING THE CARBONACEOUS DEPOSITS ON THE CATALYTIC CRACKING CATALYST WITH STEAM.

    Process for the production of gaseous olefins from petroleum distillate feedstocks
    20.
    发明授权
    Process for the production of gaseous olefins from petroleum distillate feedstocks 失效
    从石油天然产物生产气态烯烃的方法

    公开(公告)号：US3781195A

    公开(公告)日：1973-12-25

    申请号：US3781195D

    申请日：1971-12-30

    Applicant: BP CHEM INT LTD

    Inventor： TREVOR DAVIS P ,  GLOVER T ,  JONES J

    IPC: C10G69/06 ,  C10G37/00

    CPC classification number: C10G69/06 ,  C10G2400/20

    Abstract: Olefins, e.g., ethylene and propylene, are produced by hydrogenating a petroleum distillate feedstock, e.g., a petroleum vacuum distillate feedstock (b. pt. 300* - 650*C), over a catalyst containing combinations of Ni, Mo, Co and Won SiO2/Al2O3 bases, preferably Ni/W/SiO2/Al2O3, under reaction conditions such that a substantial quantity of aromatics in the feedstock are hydrogenated. The whole product of hydrogenation is then thermally cracked in the presence of steam, producing an increased yield of gaseous olefin products.

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