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    REFORMING PROCESS
    1.
    发明公开
    REFORMING PROCESS 审中-公开

    公开(公告)号：US20240263084A1

    公开(公告)日：2024-08-08

    申请号：US18617309

    申请日：2024-03-26

    Applicant: Chevron U.S.A. Inc.

    Inventor： Cong-Yan CHEN ,  Emmanuel BEHRAZ

    IPC: C10G59/06 ,  B01D3/00 ,  B01J29/40

    CPC classification number: C10G59/06 ,  B01D3/00 ,  B01J29/40 ,  C10G2300/1044 ,  C10G2300/308 ,  C10G2300/4018 ,  C10G2400/02

    Abstract: An improved reforming process for producing aromatic hydrocarbons is disclosed. The process includes two reformers arranged in parallel flow configuration, with the first reformer being a conventional reformer comprising a catalyst selective for reforming C8+ hydrocarbons to a reformate and the second reformer comprising a catalyst selective for reforming C7− hydrocarbons to a reformate. In certain embodiments, the first reformer catalyst comprises a conventional alumina catalyst and the second reformer catalyst comprises a ZSM-5 catalyst.

    PROCESS FOR INCREASING BENZENE AND TOLUENE PRODUCTION
    4.
    发明申请
    PROCESS FOR INCREASING BENZENE AND TOLUENE PRODUCTION 审中-公开
    增加苯并芘生产的方法

    公开(公告)号：US20140187831A1

    公开(公告)日：2014-07-03

    申请号：US14199145

    申请日：2014-03-06

    Applicant: UOP LLC

    Inventor： Antoine Negiz ,  Manuela Serban ,  Kurt M. VandenBussche ,  Mark D. Moser

    IPC: C07C2/76

    CPC classification number: C07C2/76 ,  C10G35/04 ,  C10G35/06 ,  C10G35/065 ,  C10G35/085 ,  C10G59/06 ,  C10G2300/1044 ,  C10G2400/30

    Abstract: A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.

    Abstract translation: 提出了一种重整烃流的方法。 该方法包括将石脑油进料流分成至少两个进料流并将每个进料流通过分离重整器。 改性剂在不同条件下运行，以利用不同烃组分的反应性质的差异。 该方法利用普通的催化剂和用于回收生成的所需芳族化合物的常见的下游方法。

    Process Development By Parallel Operation Of Paraffin Isomerization Unit With Reformer
    5.
    发明申请
    Process Development By Parallel Operation Of Paraffin Isomerization Unit With Reformer 有权
    石油异构化单元与重整器并联运行的过程开发

    公开(公告)号：US20130026066A1

    公开(公告)日：2013-01-31

    申请号：US13192062

    申请日：2011-07-27

    Applicant: Cemal Ercan ,  Yuguo Wang ,  Mohammad R. Al-Dossary ,  Rashid M. Al-Othman

    Inventor： Cemal Ercan ,  Yuguo Wang ,  Mohammad R. Al-Dossary ,  Rashid M. Al-Othman

    IPC: C10G35/02

    CPC classification number: C10G59/06 ,  C10G61/08 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/305 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/02

    Abstract: A process for refining naphtha that results in an improved octane value in a subsequent gasoline blend. Certain embodiments include separating a naphtha feed into light naphtha and heavy naphtha; separating the heavy naphtha into a paraffin stream and non-paraffin stream; introducing the light naphtha to a first isomerization unit, introducing the paraffin stream to a second isomerization unit; introducing the non-paraffin stream to a reforming unit and combining the resulting effluents to form a gasoline blend. The resulting gasoline blend has improved characteristics over gasoline blends that are made without introducing the paraffin stream to a second isomerization unit.

    Abstract translation: 精炼石脑油的方法，其导致随后的汽油混合物中改善的辛烷值。 某些实施方案包括将石脑油进料分离成轻质石脑油和重质石脑油; 将重质石脑油分离成石蜡流和非石蜡流; 将轻石脑油引入第一异构化单元，将石蜡流引入第二异构化单元; 将非石蜡流引入重整单元并将所得的流出物组合以形成汽油混合物。 所得到的汽油共混物具有比在不将石蜡流引入第二异构化单元的情况下制备的汽油共混物更好的特性。

    Hydrocarbon reforming process
    8.
    发明授权
    Hydrocarbon reforming process 失效
    烃重整过程

    公开(公告)号：US4002555A

    公开(公告)日：1977-01-11

    申请号：US647035

    申请日：1976-01-07

    Applicant: Robert A. Farnham

    Inventor： Robert A. Farnham

    IPC: C10G35/09 ,  C10G59/06 ,  C10G35/08 ,  C10G39/00

    CPC classification number: C10G35/09 ,  C10G59/06

    Abstract: A process is disclosed for reforming two hydrocarbon feedstocks by contacting one feedstock and hydrogen with a reforming catalyst in a first reforming zone at reforming conditions including a relatively high reforming pressure; separating a hydrogen-rich gas and first hydrocarbon product from the effluent from the first zone at a pressure below the first reforming pressure; recycling a first portion of the hydrogen-rich gas to provide hydrogen for the first reforming zone; contacting the other feedstock and a second portion of the hydrogen-rich gas with a second reforming catalyst in a second reforming zone at reforming conditions including a pressure lower than the first reforming pressure, with all of the hydrogen gas introduced into the second reforming zone being obtained solely from the first reforming zone effluent; and recovering a second hydrocarbon product from the effluent from the second reforming zone. The process eliminates a hydrogen recycle compressor for the second reforming zone and operates without compressing hydrogen passed from the first reforming zone to the second reforming zone.

    Abstract translation: 公开了一种通过在包括相对高的重整压力的重整条件下使一种原料和氢气与第一重整区中的重整催化剂接触来重整两种烃原料的方法; 在低于第一重整压力的压力下，从第一区域的流出物中分离富氢气体和第一烃产物; 回收第一部分富氢气体以为第一重整区提供氢气; 在包括低于第一重整压力的压力的重整条件下，在第二重整区中将另一种原料和第二部分富氢气体与第二重整催化剂接触，导入第二重整区的所有氢气为 仅从第一重整区流出物获得; 以及从所述第二重整区的流出物回收第二烃产物。 该方法消除了用于第二重整区的氢再循环压缩机，并且在不压缩从第一重整区传递到第二重整区的氢的情况下操作。

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