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    Upgrading Hydrocarbon Pyrolysis Products
    3.
    发明申请
    Upgrading Hydrocarbon Pyrolysis Products 审中-公开

    公开(公告)号：US20180334622A1

    公开(公告)日：2018-11-22

    申请号：US15971590

    申请日：2018-05-04

    Applicant: ExxonMobil Chemical Patents Inc.

    Inventor： Gaurav Agrawal ,  Stephen T. Cohn ,  Kapil Kandel ,  Subramanya V. Nayak ,  Teng Xu

    IPC: C10G47/04

    CPC classification number: C10G47/04 ,  C10G9/36 ,  C10G45/38 ,  C10G47/00 ,  C10G65/04 ,  C10G65/12 ,  C10G2300/301 ,  C10G2400/04

    Abstract: A hydrocarbon conversion process comprises providing a hydrocarbon feedstock comprising an effluent fraction from a pyrolysis process, wherein the effluent fraction has an initial boiling point at atmospheric pressure of at least 177° C. and a final boiling point at atmospheric pressure of no more than 343° C. and comprises at least 0.5 wt. % of olefinic hydrogen atoms based on the total weight of hydrogen atoms in the effluent fraction. The hydrocarbon feedstock is hydroprocessed in at least one hydroprocessing zone in the presence of treatment gas comprising molecular hydrogen under catalytic hydroprocessing conditions to produce a hydroprocessed product comprising less than 0.5 wt. % of olefinic hydrogen atoms based on the total weight of hydrogen atoms in the hydroprocessed product. The hydroprocessing conditions comprise a temperature from 150 to 350° C. and a pressure from 500 to 1500 psig (3550 to 10445 kPa-a).

    METHOD FOR CONVERTING HEAVY HYDROCARBON FEEDSTOCKS
    6.
    发明申请
    METHOD FOR CONVERTING HEAVY HYDROCARBON FEEDSTOCKS 审中-公开

    公开(公告)号：US20180195013A1

    公开(公告)日：2018-07-12

    申请号：US15558846

    申请日：2016-02-16

    Applicant: IFP ENERGIES NOUVELLES

    Inventor： Matthieu DREILLARD ,  Frederic FEUGNET ,  Joao MARQUES ,  Frederic MOREL

    IPC: C10G65/12 ,  C10G47/04 ,  C10G47/12 ,  B01J23/28 ,  B01J23/755 ,  B01J21/04

    CPC classification number: C10G65/12 ,  B01J21/04 ,  B01J23/28 ,  B01J23/755 ,  C10G47/04 ,  C10G47/12 ,  C10G65/00 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/4018

    Abstract: The invention concerns a process for the conversion of a heavy hydrocarbon feed, said process comprising the following steps: a) a step for hydroconversion of the heavy hydrocarbon feed in the presence of hydrogen in at least one or more three-phase reactors disposed in series or in parallel, containing at least one hydroconversion catalyst, so as to obtain a liquid effluent with a reduced Conradson carbon, metals, sulphur and nitrogen content, b) one or more optional steps for separating the effluent obtained from step a) in order to obtain at least one light liquid fraction boiling at a temperature of less than 350° C. and a heavy liquid fraction boiling at a temperature of more than 350° C., c) a step for hydroconversion of the liquid effluent obtained from the hydroconversion step a) in the case in which the separation step b) is not carried out, or of the heavy liquid fraction obtained from the separation step b) when said step b) is carried out, in the presence of hydrogen in at least one or more three-phase reactors disposed in series or in parallel and containing at least one hydroconversion catalyst, in which process the overall hourly space velocity employed is in the range 0.05 to 0.18 h−1.

    Process for Partial Upgrading of Heavy Oil
    9.
    发明申请
    Process for Partial Upgrading of Heavy Oil 审中-公开

    公开(公告)号：US20170306252A1

    公开(公告)日：2017-10-26

    申请号：US15496921

    申请日：2017-04-25

    Applicant: Sherritt International Corporation

    Inventor： Mohammad Reza MALEK ABBASLOU ,  Ali ABBASPOUR GHARAMALEK ,  Iftikhar HUQ ,  John Henry MARSH

    IPC: C10G65/10 ,  C10G45/58 ,  C10G47/00

    CPC classification number: C10G65/10 ,  C10G45/00 ,  C10G45/58 ,  C10G47/00 ,  C10G47/04 ,  C10G47/06 ,  C10G47/26 ,  C10G49/12 ,  C10G65/00

    Abstract: A process is provided to partially upgrade heavy oil using two or more reaction zones connected in series, each reaction zone being a continuous stirred tank maintained at hydrocracking conditions. The heavy oil feedstock and a solid particulate catalyst are stirred to form pumpable slurry which is heated to a target hydrocracking temperature and then continuously fed to the first reaction zone. Hydrogen is continuously introduced to the reaction zone to achieve hydrocracking and to produce a volatile vapour stream carried upwardly by the hydrogen to produce an overhead vapour stream. The hydrocracked heavy oil slurry from one reaction zone is fed to a next reaction zone also maintained under hydrocracking conditions with a continuous hydrogen feed to produce a volatile vapour stream. The overhead vapour stream from each reactor zone is continuously removed, and the hydrocracked heavy oil slurry from the last of the reaction zones is removed.

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