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    Process for transforming a gas oil cut to produce a dearomatised and desulphurised fuel with a high cetane number
    41.
    发明授权
    Process for transforming a gas oil cut to produce a dearomatised and desulphurised fuel with a high cetane number 失效
    用于转换瓦斯油切割以产生具有高十六烷值的脱芳香和脱硫燃料的方法

    公开(公告)号：US6042716A

    公开(公告)日：2000-03-28

    申请号：US992486

    申请日：1997-12-18

    Applicant: Frederic Morel ,  Henri Delhomme ,  Nathalie George-Marchal

    Inventor： Frederic Morel ,  Henri Delhomme ,  Nathalie George-Marchal

    IPC: B01J23/42 ,  B01J27/19 ,  C10G45/08 ,  C10G45/52 ,  C10G65/08 ,  C10G69/02

    CPC classification number: C10G65/08 ,  C10G2400/04

    Abstract: A process for transforming a gas oil cut into a dearomatized fuel with a high cetane number comprises at least one first, deep desulphurization and deep denitrogenation step in which the gas oil cut and hydrogen are passed over a catalyst comprising a mineral support, at least one group VIB metal or metal compound, at least one group VIII metal or metal compound, and phosphorous or at least one phosphorous compound, and at least one subsequent second step, dearomatization, in which the desulphurized and denitrogenated product from the first step is passed with hydrogen over a catalyst comprising a mineral support and at least one group VIII noble metal or noble metal compound.

    Abstract translation: 将切割成含有高十六烷值的脱气燃料的瓦斯油转化为至少一个第一，深度脱硫和深度脱氮步骤，其中将所述瓦斯油馏分和氢气通过含有矿物载体的催化剂，至少一种 VIB族金属或金属化合物，至少一种VIII族金属或金属化合物，以及磷或至少一种磷化合物，以及至少一个随后的第二步，脱芳化，其中来自第一步骤的脱硫和脱氮产物通过， 氢气在包含矿物载体和至少一种VIII族贵金属或贵金属化合物的催化剂上。

    Single stage, stacked bed hydrotreating process utilizing a noble metal catalyst in the upstream bed
    42.
    发明授权
    Single stage, stacked bed hydrotreating process utilizing a noble metal catalyst in the upstream bed 失效
    在上游床中使用贵金属催化剂的单级堆叠床加氢处理方法

    公开(公告)号：US5868921A

    公开(公告)日：1999-02-09

    申请号：US903680

    申请日：1997-07-31

    Applicant: Guy Barre ,  Johannes Petrus Van Den Berg ,  Pierre Grandvallet

    Inventor： Guy Barre ,  Johannes Petrus Van Den Berg ,  Pierre Grandvallet

    IPC: B01J27/051 ,  B01J27/224 ,  B01J29/14 ,  B01J29/16 ,  C10G65/08 ,  C10G45/04 ,  C10G45/44

    CPC classification number: C10G65/08

    Abstract: A hydrocarbon distillate fraction is hydrotreated in a single stage by passing the distillate fraction downwardly over a stacked bed of two hydrotreating catalysts. The catalyst in the upper bed contains 0.1 to 15% by weight of platinum and/or palladium and also contains 2 to 40% by weight of at least one of tungsten, chromium, a Group VIIB metal, and an actinium series metal supported on an acidic refractory oxide carrier. The catalyst in the lower bed contains 1 to 15% by weight of a non-noble Group VIII metal and 1 to 25% by weight of a Group VIB metal on an amorphous, refractory oxide carrier. The liquid hydrocarbon product recovered has a reduced content of aromatics and a reduced heteroatom content.

    Abstract translation: 通过将馏出物馏分向下通过两个加氢处理催化剂的堆叠床，在单个阶段中加氢处理烃馏分。 上床中的催化剂含有0.1至15重量％的铂和/或钯，并且还含有2至40重量％的钨，铬，ⅦB族金属和支撑在其上的锕系金属中的至少一种 酸性耐火氧化物载体。 下床层中的催化剂含有1至15重量％的非贵金属Ⅷ族金属和1至25重量％的无定形耐火氧化物载体上的VIB族金属。 回收的液体烃产物的芳族化合物含量降低，杂原子含量降低。

    Selective upgrading of naphtha
    43.
    发明授权
    Selective upgrading of naphtha 失效
    石脑油选择性升级

    公开(公告)号：US5401385A

    公开(公告)日：1995-03-28

    申请号：US104835

    申请日：1993-08-10

    Applicant: Robert J. Schmidt ,  Paula L. Bogdan ,  R. Joe Lawson ,  J. W. Adriaan Sachtler

    Inventor： Robert J. Schmidt ,  Paula L. Bogdan ,  R. Joe Lawson ,  J. W. Adriaan Sachtler

    IPC: C10G59/02 ,  C10G59/06 ,  C10G65/08 ,  C10G69/08 ,  C10L1/02 ,  C10G45/00

    CPC classification number: C10L1/023 ,  C10G59/02 ,  C10G59/06 ,  C10G65/08 ,  C10G69/08 ,  C10G2400/02

    Abstract: A process combination is disclosed to selectively upgrade catalytically cracked gasoline to obtain products suitable for further upgrading to reformulated fuels. A naphtha feedstock, preferably heavy naphtha, is hydrogenated to saturate aromatics, followed by selective isoparaffin synthesis to yield light and heavy synthesis naphtha and isobutane. The heavy synthesis naphtha may be processed by reforming, light naphtha may be isomerized, and isobutane may be upgraded by dehydrogenation, etherification and/or alkylation to yield gasoline components from the process combination suitable for production of reformulated gasoline.

    Abstract translation: 公开了一种方法组合以选择性地升级催化裂化汽油以获得适于进一步升级至重整燃料的产品。 氢化石脑油原料，优选重石脑油，使芳烃饱和，然后进行选择性异链烷烃合成，得到轻质和重质合成石脑油和异丁烷。 重质合成石脑油可以通过重整进行加工，轻质石脑油可以被异构化，并且异丁烷可以通过脱氢，醚化和/或烷基化来提高，从适用于生产重整汽油的方法组合产生汽油组分。

    Multizone hydrocracking process for hvi lubricating oils
    44.
    发明授权
    Multizone hydrocracking process for hvi lubricating oils 失效
    用于HVI润滑油的MULTIZONE HYDROCRACKING PROCESS

    公开(公告)号：US3682813A

    公开(公告)日：1972-08-08

    申请号：US3682813D

    申请日：1970-05-20

    Applicant: SHELL OIL CO

    Inventor： DUN PETER W ,  WEEREN PIETER A VAN

    IPC: C10G65/08 ,  C10G13/04 ,  C10G31/14

    CPC classification number: C10G65/08 ,  C10G2400/10

    Abstract: HIGH VISCOSITY INDEX LUBRICATING BASE OILS ARE PRODUCED FROM A DEASPHALTED OIL IN A MULTIZONE HYDROCRACKING PROCESS IN WHICH A SULFIDED NONACIDIC CATALYST COMPRISING ONE OR MORE METALS OF THE GROUP VI-B, VVII-B OR VIII METALS IS USED IN EACH REACTION ZONE. PREFERABLY, HYDROGEN SULFIDE AND/OR AMMONIA ARE REMOVED FROM THE FIRSTZONE EFFLUENT BEFORE INTRODUCING IT INTO THE SECOND ZONE. THE FIRST REACTION ZONE TEMPERATURE IS AT LEAST 750*F. WHILE THE SECOND REACTION ZONE TEMPERATURE IS AT LEAST 700*F.

    PROCESS FOR THE PRODUCTION OF FLUIDS
    47.
    发明公开
    PROCESS FOR THE PRODUCTION OF FLUIDS 审中-公开

    公开(公告)号：US20230279302A1

    公开(公告)日：2023-09-07

    申请号：US18006658

    申请日：2021-08-05

    Applicant: TOTALENERGIES ONETECH

    Inventor： Cristina FERREIRA ,  Fabien CAUDRELIER ,  Amine BENGHALEM

    IPC: C10G65/08

    CPC classification number: C10G65/08 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2300/1096 ,  C10G2300/1059

    Abstract: The invention is a process for dearomatization and isomerization of a feedstock having less than or equal to 10 ppm by weight of sulphur, the process comprising:



    Hydrodearomatizing the feedstock at a temperature ranging from 150 to 220° C. and at a pressure ranging from 20 to 150 bars, in order to provide a dearomatized product;
    Hydroisomerizing the dearomatized product at a temperature ranging from 250 to 320° C. and at a pressure ranging from 40 to 60 bars in the presence of a catalyst based on platinum or palladium, in order to provide an isomerized product;
    Hydrodearomatizing the isomerized product at a temperature ranging from 150 to 220° C. and at a pressure ranging from 20 to 150 bars, in order to provide an isomerized and dearomatized product.

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