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    PROCESS FOR INCREASING BENZENE AND TOLUENE PRODUCTION
    3.
    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：WO2012148813A2

    公开(公告)日：2012-11-01

    申请号：PCT/US2012/034463

    申请日：2012-04-20

    Applicant: UOP LLC ,  SERBAN, Manuela ,  NEGIZ, Antoine ,  VANDEN BUSSCHE, Kurt, M.

    Inventor： SERBAN, Manuela ,  NEGIZ, Antoine ,  VANDEN BUSSCHE, Kurt, M.

    IPC: C10G61/02 ,  C10G59/02 ,  C10G35/04

    CPC classification number: C07C2/76 ,  C10G59/02 ,  C10G69/08 ,  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。

    FIRED HEATER FOR A HYDROCARBON CONVERSION PROCESS
    4.
    发明申请
    FIRED HEATER FOR A HYDROCARBON CONVERSION PROCESS 审中-公开
    用于油气转化过程的燃烧加热器

    公开(公告)号：WO2010117614A2

    公开(公告)日：2010-10-14

    申请号：PCT/US2010/028270

    申请日：2010-03-23

    Applicant: UOP LLC ,  PETERS, Kenneth D.

    Inventor： PETERS, Kenneth D.

    IPC: C10G47/00 ,  C10G11/18 ,  C07C4/02 ,  C10G9/20 ,  F22B37/00

    CPC classification number: C10G29/205 ,  C10G9/00 ,  C10G35/02 ,  C10G45/02 ,  C10G45/58 ,  C10G45/68 ,  C10G47/00 ,  C10G49/002 ,  C10G59/02 ,  C10G69/08

    Abstract: One exemplary embodiment of the present invention can be a fired heater for a hydrocarbon conversion process. The fired heater includes inlet and outlet headers or manifolds, a set of heater tubes with each heater tube having an inlet and an outlet, at least one restriction orifice adjacent the inlet of at least one heater tube. The restriction orifice may be within the inlet manifold and adjacent the inlet of a heater tube, or between the inlet manifold and the inlet to the heater tube. A process may include passing a hydrocarbon stream through the fired heater described herein during the course of operating a hydrocarbon conversion process.

    Abstract translation: 本发明的一个示例性实施方案可以是用于烃转化方法的燃烧加热器。 燃烧的加热器包括入口和出口集管或歧管，一组加热器管，每个加热器管具有入口和出口，与至少一个加热器管的入口相邻的至少一个限制孔。 限制孔口可以在进气歧管内并且邻近加热器管的入口，或者在入口歧管和加热器管的入口之间。 在操作烃转化过程的过程中，方法可以包括使烃流通过本文所述的燃烧加热器。

    A PROCESS FOR HEATING A HYDROCARBON STREAM ENTERING A REACTION ZONE WITH A HEATER CONVECTION SECTION
    5.
    发明申请
    A PROCESS FOR HEATING A HYDROCARBON STREAM ENTERING A REACTION ZONE WITH A HEATER CONVECTION SECTION 审中-公开
    用加热器对流段加热进入反应区的烃流的方法

    公开(公告)号：WO2008060848A3

    公开(公告)日：2008-07-31

    申请号：PCT/US2007082939

    申请日：2007-10-30

    Applicant: UOP LLC ,  YUAN LEON ,  FECTEAU DAVID J ,  HARTMAN WILLIAM M ,  SCHLUETER WILLIAM D

    Inventor： YUAN LEON ,  FECTEAU DAVID J ,  HARTMAN WILLIAM M ,  SCHLUETER WILLIAM D

    IPC: C10G35/02 ,  B01J10/00 ,  C10G59/02

    CPC classification number: C10G35/02 ,  C10G59/02

    Abstract: An exemplary process can include passing a hydrocarbon stream through a reforming unit (100). The reforming unit (100) may include a heater (210), which in turn generally includes a convection section (230) and a radiant section (250), and a plurality of reforming reaction zones. Generally, the hydrocarbon stream is heated in the convection section (230) for reacting in one of the reforming reaction zones (412) to which the hydrocarbon stream is sent and the hydrocarbon stream is heated in the radiant section (250) of the heater for reacting in the other reforming reaction zone (418) to which the hydrocarbon stream is sent.

    Abstract translation: 示例性工艺可以包括使烃流通过重整单元（100）。 重整单元（100）可以包括加热器（210），该加热器又通常包括对流区段（230）和辐射区段（250）以及多个重整反应区。 通常，烃流在对流段（230）中被加热，以便在其中输送烃流的重整反应区（412）之一中反应，并且在加热器的辐射段（250）中加热烃流 在烃流被送入的另一个重整反应区（418）中反应。

    COUNTERCURRENT ALKYLATION PROCESS
    7.
    发明申请
    COUNTERCURRENT ALKYLATION PROCESS 审中-公开
    逆流烷化过程

    公开(公告)号：WO9903804A9

    公开(公告)日：1999-09-02

    申请号：PCT/US9712710

    申请日：1997-07-16

    Applicant: CATALYTIC DISTILLATION TECH ,  CHEN JAMIN

    Inventor： CHEN JAMIN

    IPC: C07C2/66 ,  C10G50/00 ,  C10G59/02 ,  C07B37/02

    CPC classification number: C10G59/02 ,  C07C2/66 ,  C07C2529/06 ,  C10G50/00 ,  C07C15/02

    Abstract: A countercurrent process for the alkylation of organic aromatic materials with olefins which takes place in a multi-phase system. The aromatic material is in the liquid phase; the olefin is in the gaseous phase; and the catalyst is in the solid phase. The olefinic material is fed below the catalyst bed in the gaseous phase and the aromatic material is fed as a liquid phase above the catalyst bed under conditions of temperature and pressure to maintain the aromatic and alkyl aromatic product in the liquid phase and the olefins in the vapor phase.

    Abstract translation: 一种逆流过程，用于在多相体系中进行有机芳香族物质与烯烃的烷基化反应。 芳香材料处于液相; 烯烃处于气相; 并且催化剂处于固相。 将烯烃材料在气相下供给到催化剂床的下方，并且在温度和压力条件下将芳族材料作为液相在催化剂床的上方供给，以将芳族和烷基芳族产物保持在液相中，并将烯烃保持在 蒸气相。

    INTEGRATED PROCESS FOR INCREASING C6 TO C8 AROMATICS CONTENT IN REFORMATE PREPARED FROM C9+ AROMATICS-CONTAINING FEED
    8.
    发明申请
    INTEGRATED PROCESS FOR INCREASING C6 TO C8 AROMATICS CONTENT IN REFORMATE PREPARED FROM C9+ AROMATICS-CONTAINING FEED 审中-公开
    用于增加C6〜C8芳香族化合物的整合方法由含有进料的C9 +芳族化合物制备的改性剂

    公开(公告)号：WO1996017040A1

    公开(公告)日：1996-06-06

    申请号：PCT/US1995014757

    申请日：1995-11-14

    Applicant: MOBIL OIL CORPORATION

    Inventor： MOBIL OIL CORPORATION ,  SHIH, Stuart, Shansen

    IPC: C10G69/02

    CPC classification number: C10G59/02 ,  C10G69/08

    Abstract: An integrated process for increasing C6 to C8 aromatics content in reformate prepared from C9 aromatics-containing feed comprises: 1) pretreating a raw naphtha feedstream containing C9 aromatics and sulfur by contacting with a) a hydrodesulfurization catalyst under hydrodesulfurization conditions to produce a hydrodesulfurized feedstream and thereafter b) cascading said hydrodesulfurized feedstream over a noble metal- and/or Group VIA metal-containing porous crystalline inorganic oxide catalyst comprising pores having openings of 12-member rings under conditions sufficient to effect conversion of C9 aromatics, thereby providing a pretreated effluent stream of enhanced C8 aromatics content relative to that obtained in the absence of said cascading; and 2) reforming at least a portion of said pretreated effluent stream to provide a reformate stream.

    Abstract translation: 从含有C9 +芳族化合物的原料制备的重整油中C6至C8芳族化合物含量增加的综合方法包括：1）在加氢脱硫条件下，通过与a）加氢脱硫催化剂接触，预处理含有C 9+芳族化合物和硫的原始石脑油原料流 以产生加氢脱硫的原料流，然后b）在足以实现C 9+的转化条件下，在包含具有12个成员环开口的孔的贵金属和/或VIA族VIA金属多孔结晶无机氧化物催化剂上层叠所述加氢脱硫原料流 >芳烃，从而提供相对于在不存在所述级联的情况下获得的预处理的具有增强的C8-芳烃含量的流出物流; 和2）重整至少一部分所述预处理的流出物流以提供重整产物流。

    NAPHTHA UPGRADING
    9.
    发明申请
    NAPHTHA UPGRADING 审中-公开
    NAPHTHA升级

    公开(公告)号：WO1994020438A1

    公开(公告)日：1994-09-15

    申请号：PCT/US1994002108

    申请日：1994-02-14

    Applicant: MOBIL OIL CORPORATION

    Inventor： MOBIL OIL CORPORATION ,  CHIN, Arthur, Achhing ,  COLLINS, Nick, Allen ,  HARANDI, Mohsen, Nadimi ,  THOMSON, Robert, Thomas ,  WARE, Robert, Adams

    IPC: C07C02/66

    CPC classification number: C10G59/02

    Abstract: A process for upgrading low octane naphtha (10) to produce gasoline products (16) having low levels of benzene and aromatics. A paraffinic naphtha feed is dehaxanized (11) to provide a fraction which has seven or more carbon content wherein such fraction is fed to a reformer (13). The reformer effluent is subsequently upgraded (21) to produce high content gasoline.

    Abstract translation: 一种用于升级低辛烷值石脑油（10）以生产具有低水平苯和芳族化合物的汽油产品（16）的方法。 将石蜡石脑油进料脱气（11）以提供具有七个或更多碳含量的馏分，其中将该馏分进料至重整器（13）。 改性剂废水随后升级（21），生产高含量汽油。

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