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    FRACTIONATION SYSTEM AND METHOD INCLUDING DEPROPANIZER COLUMN AND BOTTOMS STRIPPING COLUMN
    84.
    发明申请
    FRACTIONATION SYSTEM AND METHOD INCLUDING DEPROPANIZER COLUMN AND BOTTOMS STRIPPING COLUMN 审中-公开
    分离系统和方法，包括分离器柱和底部剥离柱

    公开(公告)号：US20150052940A1

    公开(公告)日：2015-02-26

    申请号：US14041565

    申请日：2013-09-30

    Applicant: UOP LLC

    Inventor： Stephen T. King ,  Steven Lankton ,  Xin X. Zhu

    IPC: F25J3/02

    CPC classification number: B01D3/143 ,  B01D1/2856

    Abstract: Fractionation systems utilizing a rectifying column with a stripping column are described. The liquid from the rectifying column bottoms is sent to the first tray of the stripping column, while the overhead stream from the stripping column is sent to the bottom of the rectifying column. Processes for separating feed streams are also described.

    Abstract translation: 描述了利用具有汽提塔的精馏塔的分馏系统。 来自精馏塔底部的液体被送到汽提塔的第一塔板，而来自汽提塔的塔顶料流被送到精馏塔的底部。 还描述了用于分离进料流的方法。

    METHODS AND APPARATUSES FOR HEATING HYDROCARBON STREAMS FOR PROCESSING
    85.
    发明申请
    METHODS AND APPARATUSES FOR HEATING HYDROCARBON STREAMS FOR PROCESSING 有权
    加氢处理加氢处理方法与装置

    公开(公告)号：US20140291205A1

    公开(公告)日：2014-10-02

    申请号：US13853802

    申请日：2013-03-29

    Applicant: UOP LLC

    Inventor： William M. Hartman ,  Xin X. Zhu ,  William Yanez ,  Lisa M. Lane

    IPC: C10G35/04

    CPC classification number: C10G9/20

    Abstract: Methods and apparatuses for processing hydrocarbon streams are provided. In an embodiment, a method for processing a hydrocarbon stream includes heating a feed stream in a convective bank. In the method, the feed stream is reacted in a first reaction zone to form a first effluent. The first effluent is heated in a first radiant cell that combusts fuel gas to heat the first effluent and forms a first exhaust gas. The method includes contacting the first exhaust gas with the convective bank to heat the feed stream.

    Abstract translation: 提供了处理烃流的方法和装置。 在一个实施方案中，用于处理烃流的方法包括加热对流库中的进料流。 在该方法中，进料流在第一反应区中反应形成第一流出物。 第一流出物在燃烧燃料气体的第一辐射电池中加热以加热第一流出物并形成第一废气。 该方法包括使第一废气与对流库接触以加热进料流。

    INTEGRATION OF NAPHTHA TO ETHANE AND PROPANE FRACTIONATION SECTION WITH ETHANE STEAM CRACKER
    88.
    发明公开
    INTEGRATION OF NAPHTHA TO ETHANE AND PROPANE FRACTIONATION SECTION WITH ETHANE STEAM CRACKER 审中-公开

    公开(公告)号：US20240190792A1

    公开(公告)日：2024-06-13

    申请号：US18508453

    申请日：2023-11-14

    Applicant: UOP LLC

    Inventor： Sudipta K. Ghosh ,  Xin X. Zhu ,  Kyle Cuellar

    IPC: C07C4/04

    CPC classification number: C07C4/04

    Abstract: A process of producing ethylene and propylene from naphtha, the process comprising: producing light paraffins—ethane, hydrogen/methane/residual ethane and propane rich streams—in a dividing wall fractionation column from a stream of hydrogen, methane, propane, and residual C4+ produced in the reactor section of a naphtha-to-ethane-and-propane processing unit by reacting naphtha with hydrogen, a naphtha reactor effluent stream produced by a naphtha reactor of the naphtha-to-ethane-and-propane processing unit is cooled to produce a feed stream. The feed stream is passed to a dividing wall fractionation column. An ethane stream from the dividing wall fractionation column is passed to an ethane steam cracker to produce a cracking heater effluent stream. The cracking heater effluent stream is passed to a coldbox of the ethane steam cracker after multiple steps such as quenching, compression, cooling, caustic scrubbing, drying. One or more fluids for cooling the naphtha (NEP) reactor effluent stream and for cooling the coldbox of the ethane steam cracker are provided by a common refrigeration system.

    PROCESSES FOR RECOVERING LPG FROM A REFORMING-ZONE EFFLUENT
    89.
    发明申请
    PROCESSES FOR RECOVERING LPG FROM A REFORMING-ZONE EFFLUENT 审中-公开

    公开(公告)号：US20200263922A1

    公开(公告)日：2020-08-20

    申请号：US16278017

    申请日：2019-02-15

    Applicant: UOP LLC

    Inventor： Thuy T. Vu ,  Robert E. Tsai ,  Xin X. Zhu ,  Amit Goyal ,  William Yanez ,  Sudipta K. Ghosh

    IPC: F25J3/02 ,  C01B3/34 ,  C01B3/52 ,  C07C7/00

    Abstract: Embodiments of apparatuses and methods for reforming of hydrocarbons including recovery of products are provided. In one example, a method comprises separating a reforming-zone effluent into a net gas phase stream and a liquid phase hydrocarbon stream. The net gas phase stream is separated for forming an H2-rich stream and a first liquid phase hydrocarbon stream. The H2-rich stream may be contacted with an adsorbent to form an H2-ultra rich stream and a gas stream. C3/C4 hydrocarbons are absorbed from the gas stream with the liquid phase hydrocarbon stream. The gas stream may be contacted with an H2/hydrocarbon separation membrane to separate the PSA tail gas stream and form an H2-rich permeate stream and an H2 depleted non-permeate residue stream.

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