FLUID SEPARATION ASSEMBLY TO REMOVE CONDENSABLE CONTAMINANTS AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR
    74.
    发明申请
    FLUID SEPARATION ASSEMBLY TO REMOVE CONDENSABLE CONTAMINANTS AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR 审中-公开
    流体分离装置使用超声波流体反应器去除可燃性污染物和甲烷转化过程

    公开(公告)号:WO2014031431A1

    公开(公告)日:2014-02-27

    申请号:PCT/US2013/055087

    申请日:2013-08-15

    Applicant: UOP LLC

    Abstract: Methods and systems are provided for converting methane in a feed stream to acetylene. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. The method according to certain aspects includes controlling the level of water, carbon dioxide and other condensable contaminants in the hydrocarbon stream by use of a fluid separation assembly such as a supersonic inertia separator. In addition, one or more adsorbent beds may be used to remove remaining trace amounts of condensable contaminants. The fluid separation assembly has a cyclonic fluid separator with a tubular throat portion arranged between a converging fluid inlet section and a diverging fluid outlet section and a swirl creating device.

    Abstract translation: 提供了将进料流中的甲烷转化为乙炔的方法和系统。 将烃流引入超音速反应器中并热解以将至少一部分甲烷转化为乙炔。 反应器流出物流可以被处理以将乙炔转化成另一个烃过程。 根据某些方面的方法包括通过使用诸如超音速惯性分离器的流体分离组件来控制烃流中的水,二氧化碳和其它可冷凝污染物的水平。 此外,可以使用一个或多个吸附剂床来除去剩余痕量的可冷凝污染物。 流体分离组件具有气旋流体分离器,其具有布置在会聚流体入口部分和发散流体出口部分之间的管状喉部部分和涡流产生装置。

    MERCURY COMPOUND REMOVAL AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR
    75.
    发明申请
    MERCURY COMPOUND REMOVAL AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR 审中-公开
    使用超级流动反应器的汞化合物去除和甲烷转化方法

    公开(公告)号:WO2014031324A1

    公开(公告)日:2014-02-27

    申请号:PCT/US2013/053691

    申请日:2013-08-06

    Applicant: UOP LLC

    CPC classification number: C07C7/12 C07C2/76 C07C7/005 C07C7/13 C07C7/163 C07C11/24

    Abstract: Methods and systems are provided for converting methane in a feed stream to acetylene. The method includes removing at least a portion of mercury containing compounds from a hydrocarbon stream. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. The method according to certain aspects includes controlling the level of organic, ionic or suspended mercury compounds by first converting these compounds to elemental mercury or to inorganic mercury compounds and then removing them by use of an adsorbent bed.

    Abstract translation: 提供了将进料流中的甲烷转化为乙炔的方法和系统。 该方法包括从烃流中除去至少一部分含汞化合物。 将烃流引入超音速反应器中并热解以将至少一部分甲烷转化为乙炔。 反应器流出物流可以被处理以将乙炔转化成另一个烃过程。 根据某些方面的方法包括通过首先将这些化合物转化为元素汞或无机汞化合物,然后通过使用吸附床将其去除来控制有机,离子或悬浮的汞化合物的含量。

    WATER REMOVAL AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR
    76.
    发明申请
    WATER REMOVAL AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR 审中-公开
    使用超声波流量反应器的水去除和甲烷转化过程

    公开(公告)号:WO2014031322A1

    公开(公告)日:2014-02-27

    申请号:PCT/US2013/053686

    申请日:2013-08-06

    Applicant: UOP LLC

    CPC classification number: C07C7/12 C07C2/76 C07C7/10 C07C7/11 C07C7/13 C07C11/24

    Abstract: Methods and systems are provided for converting methane in a feed stream to acetylene. The method includes removing at least a portion of water from a hydrocarbon stream. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. The method according to certain aspects includes controlling the level of water in the hydrocarbon stream.

    Abstract translation: 提供了将进料流中的甲烷转化为乙炔的方法和系统。 该方法包括从烃流中除去至少一部分水。 将烃流引入超音速反应器中并热解以将至少一部分甲烷转化为乙炔。 反应器流出物流可以被处理以将乙炔转化成另一个烃过程。 根据某些方面的方法包括控制烃流中的水的含量。

    NITROGEN REMOVAL AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR
    77.
    发明申请
    NITROGEN REMOVAL AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR 审中-公开
    使用超级流动反应器的氮去除和甲烷转化过程

    公开(公告)号:WO2014031318A1

    公开(公告)日:2014-02-27

    申请号:PCT/US2013/053547

    申请日:2013-08-05

    Applicant: UOP LLC

    Abstract: Methods and systems are provided for converting methane in a feed stream to acetylene. The method includes removing at least a portion of nitrogen from a hydrocarbon stream. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. The method according to certain aspects includes controlling the level of nitrogen in the hydrocarbon stream.

    Abstract translation: 提供了将进料流中的甲烷转化为乙炔的方法和系统。 该方法包括从烃流中除去至少一部分氮。 将烃流引入超音速反应器中并热解以将至少一部分甲烷转化为乙炔。 反应器流出物流可以被处理以将乙炔转化成另一个烃过程。 根据某些方面的方法包括控制烃流中的氮水平。

    SULFUR REMOVAL AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR
    78.
    发明申请
    SULFUR REMOVAL AND METHANE CONVERSION PROCESS USING A SUPERSONIC FLOW REACTOR 审中-公开
    使用超级流动反应器的硫去除和甲烷转化过程

    公开(公告)号:WO2014031298A1

    公开(公告)日:2014-02-27

    申请号:PCT/US2013/053138

    申请日:2013-08-01

    Applicant: UOP LLC

    CPC classification number: C07C7/12 C07C2/76 C07C7/13 C07C11/24

    Abstract: Methods and systems are provided for converting methane in a feed stream to acetylene. The method includes removing at least a portion of sulfur containing compounds from a hydrocarbon stream. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process. The method according to certain aspects includes controlling the level of sulfur containing compounds in the hydrocarbon stream.

    Abstract translation: 提供了将进料流中的甲烷转化为乙炔的方法和系统。 该方法包括从烃流中去除至少一部分含硫化合物。 将烃流引入超音速反应器中并热解以将至少一部分甲烷转化为乙炔。 反应器流出物流可以被处理以将乙炔转化成另一个烃过程。 根据某些方面的方法包括控制烃流中含硫化合物的含量。

    ГОРЕЛКА ДЛЯ ПОЛУЧЕНИЯ АЦЕТИЛЕНА
    79.
    发明申请
    ГОРЕЛКА ДЛЯ ПОЛУЧЕНИЯ АЦЕТИЛЕНА 审中-公开
    燃烧器生产乙烯

    公开(公告)号:WO2014027985A1

    公开(公告)日:2014-02-20

    申请号:PCT/UA2013/000049

    申请日:2013-05-07

    CPC classification number: C07C2/78 C10L3/02 F23D14/24 C07C11/24

    Abstract: Горелка для получения ацетилена методом термоокислительного пиролиза метана, содержит блочное газораспределительное устройство с каналами для подачи газовой смеси и каналами для подачи стабилизирующего кислорода, соединёнными с коллектором подачи стабилизирующего кислорода. Новым в изобретении является то, что газораспределительное устройство выполнено в виде совокупно направляющего газораспределительного моноблока с цельно выфрезированными в нём каналами для подачи газовой смеси, стабилизирующего кислорода и коллектора подачи стабилизирующего кислорода. Верхняя часть газораспределительного моноблока выполнена в виде конуса с образующей, имеющей форму циклоиды (брахистохроны); а входы в газовые каналы выполнены в форме плавно сужающихся участков с переходом от трапециодального сечения в трапециодальное с углом сужения а = 40-60°. Технический результат предлагаемого изобретения заключается в существенном увеличении ресурса работы горелки и её производительности.

    Abstract translation: 用于通过甲烷的热氧化热解方法生产乙炔的燃烧器包括具有用于供应气体混合物的通道和用于供应稳定氧气的通道的模块化气体分配装置,所述通道连接到用于供应稳定氧气的储存器。 本发明的新颖之处在于,气体分配装置为以下形式:联合提供指导:气体分配整体单元,其中通道在其中单个加工成用于提供气体混合物和稳定氧气,以及用于 供应稳定氧气。 气体分布整体单元的上部是具有摆线形式的母线的圆锥形(brachistochrone)的形式; 并且进入气体通道的入口是逐渐变细的部分的形式,其具有从梯形部分到具有会聚角度a = 40-60°的梯形部分的过渡。 所提出的发明的技术结果在于燃烧器的使用寿命和其效率的显着增加。

    MULTI-STAGE PLASMA CRACKING CARBONACEOUS MATERIAL REACTOR AND PROCESS FOR PRODUCING ACETYLENE BY USING THE SAME
    80.
    发明申请
    MULTI-STAGE PLASMA CRACKING CARBONACEOUS MATERIAL REACTOR AND PROCESS FOR PRODUCING ACETYLENE BY USING THE SAME 审中-公开
    多级等离子体破碎碳质材料反应器及使用它们生产乙烯的方法

    公开(公告)号:WO2013029457A1

    公开(公告)日:2013-03-07

    申请号:PCT/CN2012/079637

    申请日:2012-08-03

    Abstract: Disclosed is a multi-stage plasma reactor for cracking carbonaceous material comprising: first stage of reaction tube mainly for mixing of the carbonaceous material, carrier gas with first heating gas and pyrolysis of the carbonaceous material; second stage-N stage of reaction tube mainly for gas phase reaction of volatiles resulted from the pyrolysis, wherein N is integer of more than or equal to 2; at least one inlet of the carbonaceous material and carrier gas as feedstock located on top of the first stage of reaction tube; at least one inlet of first heating gas located on side surface of the first stage of reaction tube; at least one inlets of second-N heating gases located on side surface of the second stage-N stage of reaction tube respectively, wherein said second-N heating gases are plasma high temperature gases; at least one inlet of quench media for quenching or freezing of reaction products; at least one outlet of quenched products and gases located on bottom or lower portion of last stage of reaction tube.

    Abstract translation: 公开了一种用于裂化含碳材料的多级等离子体反应器,包括:主要用于混合碳质材料,载气与第一加热气体的反应管的第一级和碳质材料的热解; 主要用于由热解产生的挥发物气相反应的反应管的第二阶段-N阶段,其中N为大于或等于2的整数; 至少一个碳质材料入口和载气作为原料位于反应管的第一级的顶部; 位于反应管第一级侧表面上的第一加热气体的至少一个入口; 分别位于反应管的第二阶段-N阶段的侧表面上的至少一个第二-N加热气体的入口,其中所述第二N加热气体是等离子体高温气体; 用于淬灭或冷冻反应产物的至少一个骤冷介质入口; 位于反应管最后阶段的底部或下部的至少一个淬火产物和气体出口。

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