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    Two-stage hydrocracking-hydrotreating process to make lube oil
    61.
    发明授权
    Two-stage hydrocracking-hydrotreating process to make lube oil 失效
    两级加氢加氢处理制备润滑油

    公开(公告)号：US3642610A

    公开(公告)日：1972-02-15

    申请号：US3642610D

    申请日：1969-09-05

    Applicant: ATLANTIC RICHFIELD CO

    Inventor： DIVIJAK JOSEPH M JR ,  RAUSCH MAURICE K

    IPC: C10G47/12 ,  C10G65/12 ,  C10G23/02 ,  C10G13/06 ,  C10G37/00

    CPC classification number: C10G47/12 ,  C10G2400/10

    Abstract: A high-viscosity-index mineral lubricating oil is produced by treating, for instance, a deasphalted residuum or a raw, heavy lubricating distillate oil in a two-stage process. The feedstock is first catalytically hydrocracked, then catalytically hydrogenated and can be fractionated and dewaxed to produce a finished product. Catalysts such as nickel-tungstate on boriaalumina and nickel-molybdate on alumina are employed in the two stages, respectively. The catalysts are preferably used in sulfided form.

    Abstract translation: 高粘度指数的矿物润滑油是通过在两阶段工艺中处理例如脱沥青残渣或粗，重润滑的馏出油来生产的。 原料首先被催化加氢裂化，然后进行催化氢化，并可以分馏和脱蜡以产生成品。 在两个阶段中分别使用催化剂，例如在氧化铝上的氧化铈 - 氧化铝上的镍 - 钨酸盐和钼酸镍。 催化剂优选以硫化形式使用。

    Two stages of coking to make a high quality coke
    63.
    发明授权
    Two stages of coking to make a high quality coke 失效
    两个阶段的炼焦制作高质量的咖啡

    公开(公告)号：US3617480A

    公开(公告)日：1971-11-02

    申请号：US3617480D

    申请日：1969-05-29

    Applicant: GREAT LAKES CARBON CORP

    Inventor： KEEL HARVEY E

    IPC: C01B31/00 ,  C10B55/00 ,  C10B57/04 ,  C10G37/00

    CPC classification number: C10B55/00 ,  C10B57/045

    Abstract: The coking process disclosed herein provides a method for producing high quality petroleum coke which is particularly suitable for use in manufacturing electrothermic graphite electrodes. A high-boiling gas oil fraction is obtained from the overhead products produced during the coking of a petroleum oil residuum. This high-boiling gas oil fraction is segregated during the manufacture of regular or average quality petroleum coke and is subsequently coked in a separate coking operation under delayed coking conditions of time, temperature and pressure to produce a superior quality petroleum coke.

    Visbreaking process
    69.
    发明授权
    Visbreaking process 失效
    减粘裂化过程

    公开(公告)号：US4169782A

    公开(公告)日：1979-10-02

    申请号：US867548

    申请日：1978-01-06

    Applicant: H. Lytle Thompson

    Inventor： H. Lytle Thompson

    IPC: C10G9/00 ,  C10G37/00

    CPC classification number: C10G9/002 ,  C10G9/007

    Abstract: A process for visbreaking a heavy petroleum fraction wherein the effluent of the visbreaking heater is quenched by admixture with an overhead liquid produced by condensation of the overhead vapors of a secondary flash zone. The visbreaker effluent is then passed into a rectified flash zone, with the bottoms liquid of the rectified flash zone forming the feed stream to the secondary flash zone.

    Abstract translation: 一种用于减粘裂化重质石油馏分的方法，其中减粘裂化加热器的流出物与通过二级闪蒸区的塔顶蒸气的冷凝产生的塔顶液体混合淬火。 然后将脱模剂流出物进入精馏的闪蒸区域，整流的闪蒸区域的底部液体形成进料流至次级闪蒸区域。

    Process for hydrogenized reconditioning of crude oil or residues derived therefrom into saturated light hydrocarbons
    70.
    发明授权
    Process for hydrogenized reconditioning of crude oil or residues derived therefrom into saturated light hydrocarbons 失效
    将原油或由其衍生的残余物氢化再生到饱和轻烃中的方法

    公开(公告)号：US4159936A

    公开(公告)日：1979-07-03

    申请号：US837110

    申请日：1977-09-28

    Applicant: Rainer Dorn ,  Christian Koch ,  Kurt Reiter ,  Konrad Kunstle

    Inventor： Rainer Dorn ,  Christian Koch ,  Kurt Reiter ,  Konrad Kunstle

    IPC: C10G65/10 ,  C10G7/00 ,  C10G67/02 ,  C10G13/00 ,  C10G37/00

    CPC classification number: C10G7/00

    Abstract: Refining of crude petroleum by fractionally distilling the crude into lighter cuts and distillate bottoms constituting more than 50% of the crude. Hydrogenating the distillate bottoms at a temperature above 700.degree. C. in a tubular reactor to produce saturated hydrocarbons, some gas and a solid carbonaceous material. Separating the solid material in a cyclone and returning the hydrogenated oil to the fractionating column. Passing the solid carbonaceous material by an extruder to a second tubular reactor in contact with a mixture at a temperature above 750.degree. C. of steam, 1 and 2 carbon atom gases, and combustion products containing O.sub.2 from a third cyclone. Discharging the reaction products containing unreacted carbonaceous material together with substantially no O.sub.2, production of H.sub.2 and increased amounts of CO and CO.sub.2 into a second cyclone. Separating the gaseous products from the solid, recovering H.sub.2 and passing it to the first reactor tube. Extracting heat from the gaseous reaction products to superheat the steam entering the second tubular reactor and to preheat the distillate bottoms prior to entrance in the first tubular reactor. Passing the remaining solid carbonaceous material by an extruder together with excess O.sub.2 into a third tubular reactor to effect substantially complete combustion. Discharging the unburned solid residue and combustion gases into a third cyclone from which the combustion gases are sent to the second tubular reactor and the residue containing ash is discharged from the system.

    Abstract translation: 通过将原油分馏成较轻馏分和蒸馏塔底馏分构成原油的50％以上来提炼原油。 在管状反应器中在高于700℃的温度下将馏出物塔底物氢化以产生饱和烃，一些气体和固体碳质材料。 将旋转分离器中的固体物质分离并将氢化油返回至分馏塔。 通过挤出机将固体碳质材料通过蒸汽，1和2个碳原子气体以及含有来自第三旋风分离器的O 2的燃烧产物在与750℃以上的温度下接触的第二管式反应器中。 将含有未反应的碳质材料的反应产物与基本上不含O 2的产物一起放出，并将CO和CO 2的量增加到第二旋风分离器中。 将气态产物与固体分离，回收H2并将其送至第一反应器管。 从气态反应产物中提取热量以使进入第二管式反应器的蒸汽过热并在进入第一管式反应器之前预热馏出物塔底物。 通过挤出机将剩余的固体碳质材料与过量的O 2一起传送到第三管式反应器中以实现基本上完全的燃烧。 将未燃烧的固体残余物和燃烧气体排放到第三旋风分离器中，将燃烧气体从该第三旋风分离器送入第二管式反应器，并且将含有灰分的残余物从系统排出。

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