Moving Bed Lipid Conversion With Fluid Bed Catalyst Regeneration

    公开(公告)号:US20240157320A1

    公开(公告)日:2024-05-16

    申请号:US18054293

    申请日:2022-11-10

    CPC classification number: B01J8/26 B01J8/0055 B01J29/90

    Abstract: A reactor system includes a moving bed reactor that treats a lipid feedstock using a metal oxide catalyst to produce a treated stream comprising a bio-oil. The reactor system further includes a fluidized bed regenerator that regenerates spent metal oxide catalyst from the treating process in the moving bed reactor. Once the spent metal oxide catalyst is regenerated into metal oxide catalyst, it is returned to the moving bed reactor. The metal oxide catalyst returned to the moving bed reactor can contribute heat to the lipid feedstock to raise the lipid feedstock to a reaction temperature.

    GAS-LIQUID SEPARATION DEVICE FOR AN EBULLATED BED REACTOR

    公开(公告)号:US20240157274A1

    公开(公告)日:2024-05-16

    申请号:US18511835

    申请日:2023-11-16

    CPC classification number: B01D19/0057 B01L5/02 B01L2300/0681 B01L2400/0463

    Abstract: A gas-liquid separator, adapted for separating liquid and gas in an ebullated bed reactor under operating conditions, is disclosed. The device may be used in the petroleum and chemical processing industries in catalytic reactions of hydrocarbonaceous feedstocks in the presence of hydrogen, at an elevated temperature and pressure, to separate gas and liquid from gas and liquid mixtures within the reactor. The device is generally vertically oriented and may be installed in the flow through pan of an ebullated bed reactor. The device comprises a transfer conduit for transferring a gas-liquid mixture stream from a lower section of an ebullated bed reactor to an upper section of the reactor, a vortex separation section having gas-rich and liquid-rich stream outlets, and a gas-rich stream outlet conduit located on top of and adjacent to the vortex separation section. The transfer conduit includes internal means to produce a spiral flow in the gas-liquid mixture, such as a helical or spiral insert. The vortex separation section is located at the top of the transfer conduit and includes separation means to separate the gas-liquid mixture stream into a liquid-rich stream and a gas-rich stream. A separator conduit extending from the top of the vortex separation section to the transfer conduit upper opening, aligned with and having substantially the same cross-sectional dimensions as the gas-rich stream outlet, may be used as the separation means. Among the benefits provided are improved efficiency of gas and liquid separation and reduced gas holdup within the reactor.

    High speed rotor dynamics centralizer

    公开(公告)号:US11976521B2

    公开(公告)日:2024-05-07

    申请号:US17631816

    申请日:2020-07-30

    CPC classification number: E21B17/1021 E21B17/1028 E21B17/1057

    Abstract: A centralizer for use in high speed rotor dynamics applications includes a housing having a first end portion and a second end portion. The centralizer further includes a rotatable shaft positioned within a cavity of the housing. The centralizer also includes flexure springs that are each attached to and extend between the first end portion and the second end portion. The flexure springs are compressible toward a middle portion of the housing that is between the first end portion and the second end portion. The centralizer further includes roller wheels attached to the flexure springs.

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