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    Process and Apparatus for the Production of Para-xylene
    2.
    发明申请
    Process and Apparatus for the Production of Para-xylene 有权
    对二甲苯生产工艺和设备

    公开(公告)号：US20160272558A1

    公开(公告)日：2016-09-22

    申请号：US14969298

    申请日：2015-12-15

    Applicant: ExxonMobil Chemical Patents Inc.

    Inventor： Timothy P. Bender ,  John R. Porter ,  Dana L. Pilliod

    IPC: C07C5/27 ,  B01J19/24

    CPC classification number: C07C5/2729 ,  B01D15/185 ,  B01J19/2445 ,  B01J2219/24 ,  C07C5/2737 ,  C07C5/2767 ,  C07C5/2775 ,  C07C15/08

    Abstract: A process for producing para-xylene (PX) comprises supplying a hydrocarbon feed comprising xylenes and ethylbenzene (EB) to a PX recovery unit, where a PX-rich stream and at least one PX-depleted stream are recovered from the feed. The PX-depleted stream is then separated into an EB-rich stream and an EB-depleted stream in a divided wall column. The EB-depleted stream is then isomerized under at least partial liquid phase conditions to produce a first isomerized stream having a higher PX concentration than the PX-depleted stream, and the EB-rich stream is isomerized under at least partial vapor phase conditions to produce a second isomerized stream having a higher PX concentration than the PX-depleted stream. The first and second isomerized streams are then recycled to the PX recovery unit to recover additional PX and the process is repeated to define a so-called xylene isomerization loop.

    Abstract translation: 制备对二甲苯（PX）的方法包括将包含二甲苯和乙苯（EB）的烃进料供应到PX回收单元，其中富含PX的料流和至少一种不含PX的料流从进料中回收。 然后将PX-贫化的物流分离成富EB的流和分离壁塔中的EB-贫化的流。 然后将EB-贫化的物流在至少部分液相条件下异构化，以产生具有比PX贫化物流更高的PX浓度的第一异构化物流，并且在至少部分气相条件下使富含EB的物流异构化以产生 具有比PX贫化物流更高的PX浓度的第二异构化物流。 然后将第一和第二异构化物流再循环到PX回收单元以回收另外的PX，并重复该过程以定义所谓的二甲苯异构化回路。

    METHOD FOR PRODUCING HYDROCARBON PRODUCTS
    3.
    发明申请
    METHOD FOR PRODUCING HYDROCARBON PRODUCTS 审中-公开
    生产碳氢化合物产品的方法

    公开(公告)号：US20160194258A1

    公开(公告)日：2016-07-07

    申请号：US14916157

    申请日：2014-09-04

    Applicant: LINDE AKTIENGESELLSCHAFT

    Inventor： Stefanie Walter ,  Helmut Fritz

    IPC: C07C4/04 ,  C07C41/09 ,  C07C5/03 ,  C07C41/34 ,  C07C5/27 ,  C07C5/25

    CPC classification number: C07C4/04 ,  C07C5/03 ,  C07C5/13 ,  C07C5/25 ,  C07C5/2767 ,  C07C41/09 ,  C07C41/34 ,  C10G9/36 ,  C10G45/58 ,  C10G65/04 ,  C10G69/06 ,  C10G70/041 ,  C10G2300/104 ,  C10G2300/20 ,  C10G2300/4081 ,  C07C11/08

    Abstract: A method for producing hydrocarbon products is proposed which comprises providing a C4 hydrocarbon stream (C4) that predominantly comprises branched and unbranched hydrocarbons each having four carbon atoms, and an n-C4 partial stream (n-C4), which predominantly comprises unbranched hydrocarbons with four carbon atoms and an iso-C4 partial stream (i-C4) which predominantly comprises branched hydrocarbons with four carbon atoms, from the C4 hydrocarbon stream (C4) or a stream derived therefrom. It is envisaged that at least part of the n-C4 partial stream (n-C4) or a stream derived therefrom should be cracked at a cracking severity at which not more than 92% of n-butane contained in the n-C4 partial stream (n-C4) or in the derived stream is converted.

    Abstract translation: 提出了一种生产烃产物的方法，其包括提供主要包含具有四个碳原子的支链和非支链烃的C 4烃流（C 4）和主要包含未分支烃的n-C4部分流（n-C4） 四个碳原子和主要包含具有四个碳原子的支链烃，来自C4烃流（C4）或由其衍生的物流的异C4部分流（i-C4）。 设想至少部分n-C4部分流（n-C4）或由其衍生的流应在破坏严重性下破裂，其中在n-C4部分流中包含不超过92％的正丁烷 （n-C4）或在衍生流中转化。

    Process and apparatus for the production of para-xylene
    7.
    发明授权
    Process and apparatus for the production of para-xylene 有权

    公开(公告)号：US10059643B2

    公开(公告)日：2018-08-28

    申请号：US15345990

    申请日：2016-11-08

    Applicant: ExxonMobil Chemical Patents Inc.

    Inventor： Timothy P. Bender ,  John R. Porter ,  Dana L. Pilliod

    IPC: B01J19/00 ,  B01J19/24 ,  B01D15/18 ,  C07C5/27

    CPC classification number: C07C5/2729 ,  B01D15/185 ,  B01J19/2445 ,  B01J2219/24 ,  C07C5/2737 ,  C07C5/2767 ,  C07C5/2775 ,  C07C15/08

    Abstract: A process for producing para-xylene (PX) comprises supplying a hydrocarbon feed comprising xylenes and ethylbenzene (EB) to a PX recovery unit, where a PX-rich stream and at least one PX-depleted stream are recovered from the feed. The PX-depleted stream is then separated into an EB-rich stream and an EB-depleted stream in a divided wall column. The EB-depleted stream is then isomerized under at least partial liquid phase conditions to produce a first isomerized stream having a higher PX concentration than the PX-depleted stream, and the EB-rich stream is isomerized under at least partial vapor phase conditions to produce a second isomerized stream having a higher PX concentration than the PX-depleted stream. The first and second isomerized streams are then recycled to the PX recovery unit to recover additional PX and the process is repeated to define a so-called xylene isomerization loop.

    Process and apparatus for the production of para-xylene
    8.
    发明授权
    Process and apparatus for the production of para-xylene 有权
    用于生产对二甲苯的方法和设备

    公开(公告)号：US09517979B2

    公开(公告)日：2016-12-13

    申请号：US14969298

    申请日：2015-12-15

    Applicant: ExxonMobil Chemical Patents Inc.

    Inventor： Timothy P. Bender ,  John R. Porter ,  Dana L. Pilliod

    IPC: C07C5/27 ,  B01J19/24

    CPC classification number: C07C5/2729 ,  B01D15/185 ,  B01J19/2445 ,  B01J2219/24 ,  C07C5/2737 ,  C07C5/2767 ,  C07C5/2775 ,  C07C15/08

    Abstract: A process for producing para-xylene (PX) comprises supplying a hydrocarbon feed comprising xylenes and ethylbenzene (EB) to a PX recovery unit, where a PX-rich stream and at least one PX-depleted stream are recovered from the feed. The PX-depleted stream is then separated into an EB-rich stream and an EB-depleted stream in a divided wall column. The EB-depleted stream is then isomerized under at least partial liquid phase conditions to produce a first isomerized stream having a higher PX concentration than the PX-depleted stream, and the EB-rich stream is isomerized under at least partial vapor phase conditions to produce a second isomerized stream having a higher PX concentration than the PX-depleted stream. The first and second isomerized streams are then recycled to the PX recovery unit to recover additional PX and the process is repeated to define a so-called xylene isomerization loop.

    Abstract translation: 制备对二甲苯（PX）的方法包括将包含二甲苯和乙苯（EB）的烃进料供应到PX回收单元，其中富含PX的料流和至少一种不含PX的料流从进料中回收。 然后将PX-贫化的物流分离成富EB的流和分离壁塔中的EB-贫化的流。 然后将EB-贫化的物流在至少部分液相条件下异构化，以产生具有比PX贫化物流更高的PX浓度的第一异构化物流，并且在至少部分气相条件下使富含EB的物流异构化以产生 具有比PX贫化物流更高的PX浓度的第二异构化物流。 然后将第一和第二异构化物流再循环到PX回收单元以回收另外的PX，并重复该过程以定义所谓的二甲苯异构化回路。

    PROCESS FOR PRODUCING BRANCHED OLEFINS FROM LINEAR OLEFIN/ PARAFFIN FEED
    10.
    发明申请
    PROCESS FOR PRODUCING BRANCHED OLEFINS FROM LINEAR OLEFIN/ PARAFFIN FEED 失效
    从线性烯烃/帕拉芬饲料生产分支油脂的方法

    公开(公告)号：US20080242748A1

    公开(公告)日：2008-10-02

    申请号：US12134811

    申请日：2008-06-06

    Applicant: Peter Arnoldy

    Inventor： Peter Arnoldy

    IPC: C07C27/06

    CPC classification number: C07C303/06 ,  C07C5/2767 ,  C07C7/148 ,  C07C11/02 ,  C07C15/107 ,  C07C309/31

    Abstract: A process for producing branched olefins from a mixed linear olefin/paraffin isomerisation feed comprising linear olefins having at least 7 carbon atoms in 5-50% w comprising in a first stage skeletally isomerising linear olefins in the isomerisation feed and in a second stage separating branched and linear molecules wherein branched molecules are substantially olefinic and linear molecules are olefinic and/or paraffinic; novel stages and combinations thereof; apparatus therefor; use of catalysts and the like therein; and use of branched olefins obtained thereby.

    Abstract translation: 一种从混合的线性烯烃/链烷烃异构化原料生产支链烯烃的方法，包括在5-50％w中具有至少7个碳原子的直链烯烃，其包括在第一阶段中在异构化原料中骨架异构化线型烯烃和在分离的 和线性分子，其中支链分子基本上是烯属的并且线性分子是烯属和/或链烷烃; 新颖的阶段及其组合; 装置; 在其中使用催化剂等; 和使用由此获得的支链烯烃。

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