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    Catalyst supports—composition and process of manufacture
    3.
    发明授权
    Catalyst supports—composition and process of manufacture 有权

    公开(公告)号：US11547985B2

    公开(公告)日：2023-01-10

    申请号：US17405245

    申请日：2021-08-18

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

    Inventor： Madan Mohan Bhasin

    IPC: C07C15/46 ,  B01J27/224 ,  B01J35/02 ,  C07C5/333 ,  B01J23/50 ,  B01J35/10 ,  C10G45/04 ,  B01J37/08 ,  B01J37/02 ,  C10G47/02 ,  C07D301/06 ,  C10G11/02

    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).

    Catalyst and process of upgrading heavy oil in the presence of steam
    4.
    发明授权
    Catalyst and process of upgrading heavy oil in the presence of steam 有权

    公开(公告)号：US11542445B2

    公开(公告)日：2023-01-03

    申请号：US17397234

    申请日：2021-08-09

    Applicant: Saudi Arabian Oil Company

    Inventor： Mazin M. Fathi ,  Ki-Hyouk Choi ,  Mohammed R. Aldossary

    IPC: C10G47/02 ,  C10G47/32 ,  C10G47/36

    Abstract: Embodiments of the disclosure provide an aqueous reforming system and a method for upgrading heavy hydrocarbons. A hydrocarbon feed and a surfactant stream are combined to produce a first precursor stream. The first precursor stream and an alkali feed are combined to produce a second precursor stream. The second precursor stream and a transition metal feed are combined to produce a catalytic emulsion stream. The catalytic emulsion stream is heated to produce a catalytic suspension and a decomposition gas, where the decomposition gas is separated by a first separator. The catalytic suspension is combined with a preheated water stream to produce an aqueous reformer feed. The aqueous reformer feed is introduced to an aqueous reformer such that the heavy hydrocarbons undergo conversion reactions to produce an effluent stream. The effluent stream is introduced to a second separator to produce a heavy stream and a light stream. The light stream is introduced to a third separator to produce a gas stream, a distillate stream, and a spent water stream. Optionally, a portion of the distillate stream and the hydrocarbon feed can be combined to produce the first precursor stream such that the first precursor stream is in the absence of a surfactant.

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