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    PROCESS FOR PRE-HEATING REACTOR FEED STREAM
    5.
    发明申请
    PROCESS FOR PRE-HEATING REACTOR FEED STREAM 有权

    公开(公告)号：US20220204869A1

    公开(公告)日：2022-06-30

    申请号：US17610824

    申请日：2020-06-19

    Applicant: HALDOR TOPSØE A/S

    Inventor： Lars JØRGENSEN

    IPC: C10G45/04 ,  C10G69/06 ,  C10G31/08

    Abstract: A process plant and process for conversion of a hydrocarbonaceous feed, having a feed temperature, to a hydrocarbonaceous effluent, having an effluent temperature, by hydrotreatment, in the presence of a material catalytically active in hydrotreatment and an amount of hydrogen, wherein the conversion is exothermal and wherein an amount of the effluent will solidify at a solidification temperature above the feed temperature and below the effluent temperature, and wherein the feed is preheated by heat exchange, utilizing thermal energy from said effluent, wherein the heat exchange is mediated by a fluid heat exchange medium being physically separated from the feed and the effluent and having a temperature above the solidification temperature, with the associated benefit of such a process being highly energy effective, while avoiding solidification in the process lines, especially when hydrotreating feedstocks including halides.

    Catalyst supports—composition and process of manufacture
    8.
    发明授权
    Catalyst supports—composition and process of manufacture 有权

    公开(公告)号：US11213806B1

    公开(公告)日：2022-01-04

    申请号：US16448632

    申请日：2019-06-21

    Applicant: Mid-Atlantic Technology, Research & Innovation Center, Inc.

    Inventor： Madan Bhasin

    IPC: B01J27/224 ,  B01J35/10 ,  B01J37/08 ,  B01J35/02 ,  B01J23/50 ,  B01J37/02 ,  C07D301/06 ,  C10G45/04 ,  C10G11/02 ,  C07C5/333 ,  C10G47/02

    Abstract: A catalyst support comprising at least 95% silicon carbide, having surface areas of ≤10 m2/g and pore volumes of ≤1 cc/g. A method of producing a catalyst support, the method including mixing SiC particles of 0.1-20 microns, SiO2 and carbonaceous materials to form an extrusion, under inert atmospheres, heating the extrusion at temperatures of greater than 1400° C., and removing residual carbon from the heated support under temperatures below 1000° C. A catalyst on a carrier, comprising a carrier support having at least about 95% SiC, with a silver solution impregnated thereon comprising silver oxide, ethylenediamine, oxalic acid, monoethanolamine and cesium hydroxide. A process for oxidation reactions (e.g., for the production of ethylene oxide, or oxidation reactions using propane or methane), or for endothermic reactions (e.g., dehydrogenation of paraffins, of ethyl benzene, or cracking and hydrocracking hydrocarbons).

    Hydroprocessing of hydrocarbon feeds with a catalyst comprising an aluminium material comprising carbon
    10.
    发明授权
    Hydroprocessing of hydrocarbon feeds with a catalyst comprising an aluminium material comprising carbon 有权

    公开(公告)号：US11091702B2

    公开(公告)日：2021-08-17

    申请号：US16769736

    申请日：2018-11-26

    Applicant: IFP Energies Nouvelles

    Inventor： Amandine Cabiac ,  Alexandra Chaumonnot ,  Etienne Girel ,  Audrey Bonduelle-Skrzypczak

    IPC: C10G45/04 ,  B01J37/02 ,  C10G45/50 ,  C10G45/54 ,  B01J27/188 ,  B01J37/20 ,  B01J37/08 ,  B01J23/883

    Abstract: The invention relates to a method for hydroprocessing a hydrocarbon feed, operated at a temperature of between 180° C. and 450° C., in the presence of a catalyst comprising i) a composite material comprising a compound based on at least one crystalline aluminium solid and carbon, the deposited carbon content being between 1 and 25 wt. % of the total mass of the composite material, and ii) at least one element of group VIB and at least one element of group VIII, in the sulfide form thereof, said catalyst being produced by a method comprising at least: a) a step of bringing a carbon precursor into contact with a compound based on at least one crystalline aluminium solid, b) a step of thermally treating the solid produced by step a), c) repeating steps a) and b) until the desired deposited carbon content is reached, d) depositing at least one element of group VIB and at least one element of group VIII on the surface of the solid produced by step c), and e) a step of sulfidisation of the solid produced in step d).

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