PROCESS TO PRODUCE PROPYLENE FROM REFINERY DRY GAS

    公开(公告)号:US20240109821A1

    公开(公告)日:2024-04-04

    申请号:US18474040

    申请日:2023-09-25

    Applicant: UOP LLC

    CPC classification number: C07C4/06

    Abstract: The process converts ethylene in a dilute ethylene (dry gas) stream that may be derived from an FCC product to propylene. The process includes an oligomerization step to convert ethylene in the dilute ethylene stream to heavier olefins, and a second reaction step to convert the heavier olefins to propylene. The oligomerization catalyst may be an amorphous silica-alumina base with a Group VIII and/or VIB metal. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, hydrogen and ammonia. At least 50 wt-% of the ethylene in the dilute ethylene stream can be converted to C4+ olefins and recycled to the FCC for cracking to propylene.

    PROCESS FOR CRACKING TO LIGHT OLEFINS
    5.
    发明公开

    公开(公告)号:US20240026234A1

    公开(公告)日:2024-01-25

    申请号:US18225061

    申请日:2023-07-21

    Applicant: UOP LLC

    Abstract: A process for catalytic production of olefins comprises contacting a first hydrocarbon stream and a first stream of fluid catalyst in a first riser to produce a first cracked product stream and a spent catalyst stream. The first cracked product stream is separated in a main column. An overhead stream from the main column is separated into a second hydrocarbon stream. The second hydrocarbon stream is contacted with a second stream of fluid catalyst in a second riser to produce a second cracked product stream and a first stream of cool catalyst. A third hydrocarbon stream is obtained from the overhead stream and/or from the second cracked product stream. The third hydrocarbon stream is contacted with a third stream of fluid catalyst in a third riser to produce a third cracked product stream and a second stream of cool catalyst.

    PROCESSES FOR ACTIVATING DEHYDROGENATION CATALYST

    公开(公告)号:US20240173699A1

    公开(公告)日:2024-05-30

    申请号:US18457059

    申请日:2023-08-28

    Applicant: UOP LLC

    CPC classification number: B01J23/62 B01J37/08 B01J38/02

    Abstract: Processes and apparatuses for activating a dehydrogenation catalyst that include gallium on a support. An additive particle comprising platinum is mixed with the catalyst particles, which may be fresh or deactivated catalyst. The mixture is exposed, in an oxygen containing environment, to a temperature between 650° C. and 1,000° C. The additive particles may be fluidized with the catalyst particles and may active the catalyst in a regenerator.

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