DISTILLATION TRAY HAVING THROUGH HOLES WITH DIFFERENT DIAMETERS

    公开(公告)号:US20220249973A1

    公开(公告)日:2022-08-11

    申请号:US17608224

    申请日:2020-05-05

    Abstract: This disclosure describes one or more trays for use in distillation columns. The trays include a plate having a plurality of through holes that extend between a first surface of the plate and a second surface of the plate. The plurality of through holes include a first set of through holes each having substantially a first diameter and a second set of through holes each having substantially a second diameter that is different from the first diameter. The trays also include a weir coupled to the plate and extending from the first surface. The weir is positioned between the first set of through holes and the second set of through holes.

    DISTILLATION TRAY HAVING THROUGH HOLES WITH DIFFERENT DIAMETERS

    公开(公告)号:US20220219248A1

    公开(公告)日:2022-07-14

    申请号:US17608314

    申请日:2020-05-05

    Abstract: One or more trays for use in distillation columns and methods of manufacture of such trays. The trays include a plate having a plurality of through holes that extend between a first surface of the plate and a second surface of the plate. The plurality of through holes include a first set of through holes each having substantially a first diameter and a second set of through holes each having substantially a second diameter that is different from the first diameter. The trays also include a weir coupled to the plate and extending from the first surface. The weir is positioned between the first set of through holes and the second set of through holes.

    SYSTEM AND METHOD FOR PRODUCTION OF MTBE
    5.
    发明公开

    公开(公告)号:US20230271907A1

    公开(公告)日:2023-08-31

    申请号:US18005593

    申请日:2021-07-16

    CPC classification number: C07C41/06

    Abstract: Systems and methods for producing MTBE without using a catalytic distillation column or a super fractionator have been disclosed. An optimum volume of methanol stream required to maximize MTBE production and reduce slippage of isobutylene to minimum acceptable values together with a crude C4 stream are flowed into a primary reaction unit that comprises a first reactor and a second reactor in parallel configured to produce maximum values of final MTBE volumes under higher or equal established purity commercial quality specifications levels. The combined effluent from the first reactor and the second reactor is split to form a first portion, a second portion and a third portion. The first portion is flowed to a third reactor configured to produce additional MTBE. The second portion is combined with an effluent from the third reactor for further separation. The third portion is recycled to the first reactor and/or second reactor.

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