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    ESTERIFICATION UNIT FOR PRODUCING CRUDE METHYL METHACRYLATE, ESTERIFICATION PROCESS USING SAID UNIT AND PLANT COMPRISING SAID UNIT
    32.
    发明申请
    ESTERIFICATION UNIT FOR PRODUCING CRUDE METHYL METHACRYLATE, ESTERIFICATION PROCESS USING SAID UNIT AND PLANT COMPRISING SAID UNIT 审中-公开
    用于生产甲基丙烯酸甲酯的制备单元，使用上述单元和包含所述单元的设备的确定过程

    公开(公告)号：US20160257639A1

    公开(公告)日：2016-09-08

    申请号：US15028745

    申请日：2014-10-17

    Applicant: ARKEMA FRANCE

    Inventor： Yves BERNARDIN ,  Romain BILLON ,  Xavier MARCARIAN ,  Florent VALLET

    IPC: C07C67/20 ,  B01J10/00

    CPC classification number: C07C67/20 ,  B01J4/002 ,  B01J10/00 ,  B01J19/1862 ,  B01J19/2445 ,  B01J19/245 ,  B01J19/2465 ,  B01J2219/0004 ,  C07C69/54

    Abstract: The invention relates to an esterification unit (150) and esterification process for producing crude methyl methacrylate (MMA) from methacrylamide (MAM), which enable particularly to improve the yield, meaning that the organics spent acids are low; and at the same time, providing crude MMA with rather good quality, meaning that MMA concentration in crude MMA is rather high and preferably from 50 wt % to 80 wt %. According to the invention, the esterification unit comprises esterification reactors (1, . . . , 5 (or 6) set up in a serial way so that there is a counter current flow between gaseous phase and liquid phase, the liquid phase flowing from first reactor (1) of the series to last reactor (5 (or 6)), and the gaseous phase flowing from reactor to first reactor (1).

    Abstract translation: 本发明涉及由甲基丙烯酰胺（MAM）制备粗甲基丙烯酸甲酯（MMA）的酯化单元（150）和酯化方法，其特别能够提高产率，意味着有机废酸为低; 同时提供质量较好的粗MMA，这意味着粗MMA中的MMA浓度相当高，优选为50wt％至80wt％。 根据本发明，酯化单元包括以串联方式设置的酯化反应器（1，...，5（或6）），使得在气相和液相之间存在逆流，液相从第一 （5（或6））和从反应器流向第一反应器（1）的气相的反应器（1）。

    PYROLYTIC REACTOR
    36.
    发明申请
    PYROLYTIC REACTOR 审中-公开
    热解反应器

    公开(公告)号：US20160228847A1

    公开(公告)日：2016-08-11

    申请号：US15131316

    申请日：2016-04-18

    Applicant: UOP LLC

    Inventor： Carl J. Stevens ,  Antoine Negiz ,  Vinayender Kuchana

    IPC: B01J19/26 ,  B01J19/24 ,  C07C2/78

    CPC classification number: B01J19/26 ,  B01J3/008 ,  B01J4/002 ,  B01J6/008 ,  B01J19/02 ,  B01J19/2415 ,  B01J2219/0004 ,  B01J2219/00051 ,  B01J2219/00094 ,  B01J2219/00123 ,  B01J2219/00157 ,  B01J2219/0204 ,  B01J2219/0263 ,  B01J2219/0281 ,  B01J2219/0286 ,  B01J2219/029 ,  C07C2/78 ,  C07C11/24

    Abstract: A pyrolytic reactor comprising a fuel injection zone, a combustion zone adjacent to the fuel injections zone, an expansion zone adjacent to the combustion zone, a feedstock injection zone comprising a plurality of injection nozzles and disposed adjacent to the expansion zone, a mixing zone configured to mix a carrier stream and feed material and disposed adjacent to the feedstock injection zone, and a reaction zone adjacent to the mixing zone. The plurality of injection nozzles are radially distributed in a first assembly defining a first plane transverse to the feedstock injection zone and in a second assembly transverse to the feedstock injection zone.

    Abstract translation: 一种热解反应器，包括燃料喷射区域，与燃料喷射区域邻近的燃烧区域，与燃烧区域相邻的膨胀区域，包括多个喷嘴并且邻近膨胀区域设置的原料喷射区域，配置为 混合载体料流和进料，并与原料注入区相邻设置，以及与混合区相邻的反应区。 多个注射喷嘴径向分布在限定垂直于原料注射区的第一平面的第一组件中，并且横向于原料注入区的第二组件中。

    APPARATUS AND PROCESS FOR PREPARING ACETYLENE AND SYNTHESIS GAS
    37.
    发明申请
    APPARATUS AND PROCESS FOR PREPARING ACETYLENE AND SYNTHESIS GAS 审中-公开
    制备乙烯和合成气体的装置和方法

    公开(公告)号：US20160207767A1

    公开(公告)日：2016-07-21

    申请号：US14912809

    申请日：2014-08-28

    Applicant: BASF SE

    Inventor： Matthias KERN ,  Michael RUSS ,  Peter RENZE ,  Maximilian VICARI

    IPC: C01B3/36 ,  C07C2/78 ,  B01J19/24

    CPC classification number: C01B3/36 ,  B01J4/002 ,  B01J19/24 ,  B01J2219/24 ,  C01B2203/0255 ,  C01B2203/062 ,  C01B2203/1235 ,  C07C2/78 ,  C07C11/24

    Abstract: An apparatus (10) for preparing acetylene and synthesis gas by partial oxidation of hydrocarbons with oxygen is proposed, comprising a mixing unit (12), a mixing section and a mixing diffuser (16). The mixing unit (12) has a feed orifice (18) for supply of a hydrocarbonaceous stream, a feed orifice (20) for supply of an oxygenous stream, a swirl register and a distributor plate (24). The distributor plate (24) is disposed between the mixing section (14) and the feed orifice (18) for supply of a hydrocarbonaceous stream. The distributor plate (24) has orifices (28). The swirl register (22) is disposed between the feed orifice (20) for supply of an oxygenous stream and the mixing section (14). The mixing diffuser (16) is connected to the mixing section (14).There is a further proposal of a process for preparing acetylene and synthesis gas by partial oxidation of hydrocarbons with oxygen.

    Abstract translation: 提出了一种用于通过用氧气分解氧化烃来制备乙炔和合成气的装置（10），包括混合单元（12），混合段和混合扩散器（16）。 混合单元（12）具有用于供应烃流的进料孔（18），用于供应氧气流的进料孔（20），涡流定位器和分配板（24）。 分配板（24）设置在混合部分（14）和进料孔（18）之间，用于供应烃流。 分配板（24）具有孔（28）。 旋流寄存器（22）设置在供给孔（20）之间，用于供应氧气流和混合部分（14）。 混合扩散器（16）连接到混合部分（14）。 还有一个进一步的建议是通过用氧气对烃进行部分氧化制备乙炔和合成气的方法。

    METHOD AND DEVICE FOR INTRODUCING REACTIVE GASSES INTO A REACTION CHAMBER
    39.
    发明申请
    METHOD AND DEVICE FOR INTRODUCING REACTIVE GASSES INTO A REACTION CHAMBER 审中-公开
    将反应性入口引入反应室的方法和装置

    公开(公告)号：US20160145099A1

    公开(公告)日：2016-05-26

    申请号：US14938315

    申请日：2015-11-11

    Applicant: Hanno Tautz

    Inventor： Hanno Tautz

    IPC: C01B3/36 ,  B01J19/24

    CPC classification number: C01B3/36 ,  B01F5/0256 ,  B01F13/1013 ,  B01F2215/0422 ,  B01F2215/0427 ,  B01J4/002 ,  B01J19/2415 ,  B01J2219/0015 ,  B01J2219/00157 ,  F23D14/22

    Abstract: A method and a device for the separate introduction of a fuel gas and also of an oxidizing agent into the reaction chamber of a tubular reactor, in order there to be mixed and reacted with the release of heat. Not only the fuel gas but also the oxidizing agent are introduced into the reaction chamber in each case in more than three gas jets, wherein the margin between a fuel gas jet and an oxidizing agent jet as adjacent as possible thereto, on entry into the reaction chamber, is between 2 and 500 mm, preferably between 5 and 50 mm.

    Abstract translation: 一种用于将燃料气体和氧化剂单独引入管式反应器的反应室的方法和装置，以便与热释放混合并反应。 在三种以上的气体喷射中，不仅燃料气体而且氧化剂都被引入反应室，其中燃料气体射流和氧化剂射流之间的边界在进入反应过程中尽可能相邻 在2至500mm之间，优选在5至50mm之间。

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