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    PRESSURE SWING ADSORPTION PROCESSES AND SYSTEMS FOR RECOVERY OF HYDROGEN AND C2+ HYDROCARBONS
    11.
    发明申请
    PRESSURE SWING ADSORPTION PROCESSES AND SYSTEMS FOR RECOVERY OF HYDROGEN AND C2+ HYDROCARBONS 有权
    氢气和C2 +烃回收压力吸收过程和系统

    公开(公告)号：US20150375159A1

    公开(公告)日：2015-12-31

    申请号：US14739315

    申请日：2015-06-15

    Applicant: UOP LLC

    Inventor： Robert E. Tsai ,  Xin X. Zhu ,  Joel J. Kaye ,  Eleftherios Adamopoulos

    IPC: B01D53/047

    CPC classification number: B01D53/047 ,  B01D2256/16 ,  B01D2257/7022 ,  B01D2257/7025 ,  C01B3/56 ,  Y02C20/20

    Abstract: The invention involves a process for treating a gas stream from a hydroprocessor that contains hydrogen, methane and C2+ hydrocarbons. In embodiments of the invention, the gas stream is sent through at least two pressure swing adsorption units to produce a high quality hydrogen stream, a fuel gas stream containing most of the methane and a tail gas stream that is sent to a steam cracker. Lean gas from a gas plant and other refinery off gases may also be processed together with the gas stream from the hydroprocessor.

    Abstract translation: 本发明涉及一种处理含有氢气，甲烷和C 2 +烃的加氢处理器的气流的方法。 在本发明的实施方案中，气流通过至少两个变压吸附单元送出，以产生高质量的氢气流，含有大部分甲烷的燃料气流和送到蒸汽裂解器的尾气流。 来自天然气厂和其他炼油厂废气的精煤也可以与来自加氢处理器的气流一起加工。

    Methods and apparatuses for heating hydrocarbon streams for processing
    12.
    发明授权
    Methods and apparatuses for heating hydrocarbon streams for processing 有权
    用于加热烃流加工的方法和装置

    公开(公告)号：US09206358B2

    公开(公告)日：2015-12-08

    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: C10G35/085 ,  C10G9/20 ,  C10G35/00 ,  C10G35/04 ,  C10G35/06

    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，一种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。

    PROCESS FOR REDUCING THE AMOUNT OF NORMAL PENTANE FROM A FEEDSTOCK
    13.
    发明申请
    PROCESS FOR REDUCING THE AMOUNT OF NORMAL PENTANE FROM A FEEDSTOCK 审中-公开
    从饲料中减少正常香精量的方法

    公开(公告)号：US20150251972A1

    公开(公告)日：2015-09-10

    申请号：US14247477

    申请日：2014-04-08

    Applicant: UOP LLC

    Inventor： David James Shecterle ,  Stephen Thomas King ,  Xin X. Zhu

    IPC: C07C5/27 ,  C07C7/04

    CPC classification number: C10G35/00 ,  C10G9/36 ,  C10G45/58 ,  C10G2400/30

    Abstract: A process for separation and treatment of a naphtha feedstock to increase overall octane in a gasoline blending pool by reducing or removing the normal pentane in the feedstock. The feedstock is passed into a divided wall column having an undivided top portion, an undivided bottom portion and a wall dividing a middle portion into two sections. The intermediate faction can include either all normal pentane, which can be utilized on other processes, or it can include a mixture of normal pentane and C6 hydrocarbons, which can be isomerized in an isomerization zone to increase the octane and then passed to a gasoline blending pool.

    Abstract translation: 通过还原或除去原料中的正戊烷，分离和处理石脑油原料以提高汽油共混池中的总辛烷值的方法。 原料进入具有不分割顶部，未分割底部和将中间部分分成两部分的壁的分隔壁柱。 中间相可以包括可以用于其它方法的所有正戊烷，或者可以包括正戊烷和C 6烃的混合物，其可以在异构化区中异构化以增加辛烷值，然后传递到汽油混合物 游泳池

    PROCESS FOR RECOVERING HEAT FROM A HYDROCARBON SEPARATION
    14.
    发明申请
    PROCESS FOR RECOVERING HEAT FROM A HYDROCARBON SEPARATION 审中-公开
    从油气分离中回收热量的方法

    公开(公告)号：US20150101921A1

    公开(公告)日：2015-04-16

    申请号：US14445512

    申请日：2014-07-29

    Applicant: UOP LLC

    Inventor： Stephen T. King ,  Adam J. Kanyuh ,  Xin X. Zhu

    IPC: C10G53/02 ,  C10G7/00 ,  B01D3/14

    CPC classification number: C10G53/02 ,  B01D1/28 ,  B01D1/2856 ,  B01D3/14 ,  B01D3/143 ,  B01D3/148 ,  B01D5/0039 ,  C07C7/00 ,  C07C7/04 ,  C10G7/00 ,  Y02P70/34

    Abstract: A process for recovering heat from the separation of hydrocarbons. The overhead vapor stream from a fractionation column is passed to a two stage heat pump compressor. The first stage of compression is used to reboil the fractionation column. The second stage is compressed and cooled passed to a separation zone. The liquid in the separation zone may be passed back to the fractionation column as secondary reflux, and/or recovered as liquid product. Heat may also be removed from the second stage. A suction drum on the first stage may be used to protect the heat pump compressor from any droplets in the overhead stream.

    Abstract translation: 从烃分离中回收热量的方法。 来自分馏塔的塔顶蒸气流被传送到两级热泵压缩机。 压缩的第一阶段用于重新沸腾分馏塔。 第二阶段被压缩并冷却通过分离区。 分离区中的液体可以作为二次回流返回到分馏塔，和/或作为液体产物回收。 也可以从第二阶段除去热量。 可以使用第一级上的吸入鼓来保护热泵压缩机免于塔顶流中的任何液滴。

    ETHANE SEPARATION WITH CRYOGENIC HEAT EXCHANGER
    18.
    发明申请
    ETHANE SEPARATION WITH CRYOGENIC HEAT EXCHANGER 有权

    公开(公告)号：US20220316798A1

    公开(公告)日：2022-10-06

    申请号：US17671365

    申请日：2022-02-14

    Applicant: UOP LLC

    Inventor： Kyle Cuellar ,  Stephen T. King ,  Glen John Pomorski ,  Xin X. Zhu

    IPC: F25J3/02

    Abstract: A process and apparatus integrate a deethanizer column with a cryogenic heat exchanger by reboiling the deethanizer column with a refrigerant stream and/or cooling a deethanizer overhead line in the cryogenic heat exchanger. A single stage separator and a single deethanizer column may be used to obtain high purity hydrogen in the net gas stream and an ethane rich off-gas stream, whereas conventionally a dual stage separator and two deethanizer columns were necessary for equivalent purity, respectively.

    Processes for recovering LPG from a reforming-zone effluent
    19.
    发明授权
    Processes for recovering LPG from a reforming-zone effluent 有权

    公开(公告)号：US11441838B2

    公开(公告)日：2022-09-13

    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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