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    HYDROTREATMENT CATALYST WITH A HIGH DENSITY OF MOLYBDENUM, AND PROCESS FOR ITS PREPARATION
    6.
    发明申请
    HYDROTREATMENT CATALYST WITH A HIGH DENSITY OF MOLYBDENUM, AND PROCESS FOR ITS PREPARATION 审中-公开
    具有高密度多晶硅的水力催化剂及其制备方法

    公开(公告)号：US20160001272A1

    公开(公告)日：2016-01-07

    申请号：US14790678

    申请日：2015-07-02

    Applicant: IFP Energies Nouvelles

    Inventor： Antoine DAUDIN

    IPC: B01J27/19 ,  B01J37/02 ,  B01J35/10 ,  C10G45/08

    CPC classification number: B01J27/19 ,  B01J21/04 ,  B01J23/882 ,  B01J23/883 ,  B01J35/1014 ,  B01J35/1019 ,  B01J37/0201 ,  B01J37/0205 ,  B01J37/0236 ,  B01J37/024 ,  C10G45/08 ,  C10G69/04

    Abstract: The present invention concerns a hydrotreatment catalyst comprising an alumina-based support, at least one metal from group VIB, at least one metal from group VIII and phosphorus, in which: the specific surface area of the catalyst is in the range 20 to 150 m2/g; the density of the metal from group VIB, expressed as the number of atoms of metal from group VIB per unit surface area of catalyst, is in the range 7 to 30 atoms of metal from group VIB per nm2 of catalyst; the catalyst being prepared by impregnation of the metals from group VIB, group VIII and phosphorus onto the support in order to obtain an impregnated catalyst precursor, then drying said impregnated catalyst precursor at a temperature of less than 200° C. and without subsequent calcining.

    Abstract translation: 本发明涉及一种加氢处理催化剂，其包含氧化铝基载体，至少一种来自VIB族的金属，至少一种来自VIII族的金属和磷，其中：催化剂的比表面积为20-150m2 /G; 来自VIB族金属的金属的密度，以每单位表面积催化剂的VIB族金属原子数表示，在每个催化剂的VIB / VIB中为7〜30原子的金属; 通过将VIB族，VIII族和磷族金属浸渍到载体上以获得浸渍的催化剂前体，然后在低于200℃的温度下干燥所述浸渍的催化剂前体并且不进行随后的煅烧来制备催化剂。

    CATALYTIC ADSORBENT FOR THE CAPTURE OF ARSENIC AND THE SELECTIVE HYDRODESULFURIZATION OF GASOLINES
    7.
    发明申请
    CATALYTIC ADSORBENT FOR THE CAPTURE OF ARSENIC AND THE SELECTIVE HYDRODESULFURIZATION OF GASOLINES 审中-公开
    吸收吸附剂和吸附剂选择性氢化的催化吸附剂

    公开(公告)号：US20140323778A1

    公开(公告)日：2014-10-30

    申请号：US14259577

    申请日：2014-04-23

    Applicant: IFP ENERGIES NOUVELLES

    Inventor： Philibert LEFLAIVE ,  Marie Claire MARION ,  Antoine DAUDIN

    IPC: B01J27/19 ,  B01J23/882 ,  C07C7/12

    CPC classification number: B01J27/19 ,  B01J23/882 ,  C07C7/12 ,  C10G25/003 ,  C10G45/02 ,  C10G45/32 ,  C10G2300/205

    Abstract: A catalytic adsorbent, comprising at least cobalt and molybdenum deposited on a porous substrate in which the content of cobalt, expressed in terms of CoO oxide, is between 11 and 30% by weight relative to the total weight of said adsorbent and the content of molybdenum, expressed in terms of MoO3 oxide, is between 3 and 30% by weight relative to the total weight of said adsorbent, is described. This invention also relates to a process for hydrotreatment using said catalytic adsorbent.

    Abstract translation: 一种催化吸附剂，其至少包含沉积在多孔基材上的钴和钼，其中以CoO氧化物表示的钴的含量相对于所述吸附剂的总重量为11至30重量％，并且钼的含量 以相对于所述吸附剂的总重计为3〜30重量％，以氧化钼为基准表示。 本发明还涉及使用所述催化吸附剂的加氢处理方法。

    METHOD FOR HYDROCRACKING HYDROCARBON FEEDSTOCKS USING A CATALYST COMPRISING A ZEOLITE AND AN AMORPHOUS MESOPOROUS ALUMINA
    10.
    发明申请
    METHOD FOR HYDROCRACKING HYDROCARBON FEEDSTOCKS USING A CATALYST COMPRISING A ZEOLITE AND AN AMORPHOUS MESOPOROUS ALUMINA 审中-公开

    公开(公告)号：US20180362861A1

    公开(公告)日：2018-12-20

    申请号：US16060069

    申请日：2016-11-16

    Applicant: IFP ENERGIES NOUVELLES

    Inventor： Malika BOUALLEG ,  Antoine DAUDIN ,  Emmanuelle GUILLON

    IPC: C10G47/20 ,  B01J21/04 ,  B01J29/08 ,  B01J29/16 ,  B01J37/00 ,  B01J37/03 ,  B01J37/08

    Abstract: The present invention describes a process for hydrocracking at least one hydrocarbon feed in which at least 50% by weight of the compounds have an initial boiling point of more than 300° C. and a final boiling point of less than 540° C. using at least one catalyst comprising at least one metal from group VIB and/or at least one metal from group VIII of the periodic classification of the elements and a support comprising at least one zeolite containing at least one series of channels the opening of which is defined by a ring containing 12 oxygen atoms (12MR), and at least one binder, said support being prepared from a highly dispersible alumina gel, said hydrocracking process being operated at a temperature in the range 200° C. to 480° C., at a total pressure in the range 1 MPa to 25 MPa, with a ratio of the volume of hydrogen to the volume of hydrocarbon feed in the range 80 to 5000 litres per litre and with an hourly space velocity (HSV), defined as the ratio of the volume flow rate of liquid hydrocarbon feed to the volume of catalyst charged into the reactor, in the range 0.1 to 50 h−1.

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