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1.发明授权Reactor for producing C2- to C8- olefins from a material flow containing oxygenate, water vapor and one or more hydrocarbons 有权用于从含有氧化物，水蒸气和一种或多种烃的物料流中生产C2-至C8-烯烃的反应器公开(公告)号：US08444940B2
公开(公告)日：2013-05-21
申请号：US12303227
申请日：2007-04-21
申请人： Hermann Bach , Lothar Brehm , Jurgen Bohle , Gunter Quass , Gunther Heinz , Katja Bartels , Heinrich Dörr , Harald Kömpel
发明人： Hermann Bach , Lothar Brehm , Jurgen Bohle , Gunter Quass , Gunther Heinz , Katja Bartels , Heinrich Dörr , Harald Kömpel
IPC分类号： B01J8/02
CPC分类号： B01J8/0496 , B01J4/002 , B01J8/0453 , B01J8/0492 , B01J19/26 , B01J19/30 , B01J19/32 , B01J2208/00176 , B01J2208/00212 , B01J2208/00362 , B01J2208/00663 , B01J2208/00672 , B01J2208/00805 , B01J2208/00814 , B01J2208/00884 , B01J2208/025 , B01J2219/185 , B01J2219/1943 , B01J2219/30207 , B01J2219/30416 , B01J2219/32286 , C07C1/20 , C07C2529/40 , C07C2529/70 , F28D9/00 , Y02P30/42 , C07C11/06 , C07C11/02
摘要： A reactor is described for the production of C2 to C8 olefins from gaseous oxygenate and H2O and one or more material flows containing C2 C4, C5, C6, C7, C8 olefin and paraffin at 400° to 470° C., wherein several reaction stages which the material flow can pass through from the top to the bottom, each consisting of a support base with a catalyst layer situated on it, are arranged in a closed, upright container. In order to be able in each case to lower the temperature of the reaction mixture leaving the reaction stages before it enters into the next reaction stage, it is provided that each support base consists of cells which are placed closely next to each other with no gaps and which are securely attached to each other and filled with catalyst, and in the space formed by two neighboring reaction stages, respectively, an assembly of nozzle tubes is installed for spraying a liquid phase containing H2O and DME and/or MEOH, using a water-saturated gas phase containing mainly DME and/or MEOH, in the direction of the following reaction stage downstream.
摘要翻译： 描述了一种用于从气态含氧化合物和H 2 O生产C 2至C 8烯烃的反应器和在400℃至470℃下含有C 2 -C 4，C 5，C 6，C 7，C 8烯烃和石蜡的一种或多种物料流，其中几个反应阶段 材料流可以从顶部到底部通过，每个由位于其上的具有催化剂层的支撑基底组成，设置在封闭的直立容器中。 为了能够在每种情况下降低在进入下一个反应阶段之前留下反应级的反应混合物的温度，条件是每个载体基底由彼此紧密相邻放置而没有间隙的细胞组成 并且彼此牢固地连接并填充有催化剂，并且在由两个相邻反应段形成的空间中分别安装喷嘴管的组件，以使用水喷射含有H 2 O和DME和/或MEOH的液相 主要含有DME和/或MEOH的饱和气相，在下游反应段的方向。
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2.发明申请REACTOR FOR PRODUCING C2- TO C8- OLEFINS FROM A MATERIAL FLOW CONTAINING OXYGENATE, WATER VAPOR AND ONE OR MORE HYDROCARBONS 有权从含有氧化物，水蒸汽和一种或多种烃的材料流中生产C2-至C8-烯烃的反应器公开(公告)号：US20100063337A1
公开(公告)日：2010-03-11
申请号：US12303227
申请日：2007-04-21
申请人： Hermann Bach , Lothar Brehm , Jürgen Bohle , Gunter Quass , Günther Heinz , Katja Bartels , Heinrich Dörr , Harald Kömpel
发明人： Hermann Bach , Lothar Brehm , Jürgen Bohle , Gunter Quass , Günther Heinz , Katja Bartels , Heinrich Dörr , Harald Kömpel
CPC分类号： B01J8/0496 , B01J4/002 , B01J8/0453 , B01J8/0492 , B01J19/26 , B01J19/30 , B01J19/32 , B01J2208/00176 , B01J2208/00212 , B01J2208/00362 , B01J2208/00663 , B01J2208/00672 , B01J2208/00805 , B01J2208/00814 , B01J2208/00884 , B01J2208/025 , B01J2219/185 , B01J2219/1943 , B01J2219/30207 , B01J2219/30416 , B01J2219/32286 , C07C1/20 , C07C2529/40 , C07C2529/70 , F28D9/00 , Y02P30/42 , C07C11/06 , C07C11/02
摘要： The invention relates to a reactor for the production of C2 to C8 olefins from gaseous oxygenate and H2O and one or more material flows containing C2 C4, C5, C6, C7, C8 olefin and paraffin at 400° to 470° C., wherein several reaction stages which the material flow can pass through from the top to the bottom, each consisting of a support base with a catalyst layer situated on it, are arranged in a closed, upright container. In order to be able in each case to lower the temperature of the reaction mixture leaving the reaction stages before it enters into the next reaction stage, it is provided that each support base consists of cells which are placed closely next to each other with no gaps and which are securely attached to each other and filled with catalyst, and in the space formed by two neighboring reaction stages, respectively, an assembly of nozzle tubes is installed for spraying a liquid phase containing H2O and DME and/or MeOH, using a water-saturated gas phase containing mainly DME and/or MeOH, in the direction of the following reaction stage downstream.
摘要翻译： 本发明涉及一种用于从气态含氧化合物和H 2 O生产C 2至C 8烯烃的反应器，以及在400°至470℃下含有C 2 -C 4，C 5，C 6，C 7，C 8烯烃和石蜡的一种或多种物料流， 材料流可以从顶部到底部通过的反应阶段，每个由位于其上的具有催化剂层的支撑基底组成，设置在封闭的直立容器中。 为了能够在每种情况下降低在进入下一个反应阶段之前留下反应级的反应混合物的温度，条件是每个载体基底由彼此紧密相邻放置而没有间隙的细胞组成 并且其彼此牢固地连接并填充有催化剂，并且在由两个相邻反应段形成的空间中分别安装喷嘴管的组件，以使用水喷射含有H 2 O和DME和/或MeOH的液相 主要含有DME和/或MeOH的饱和气相，在下游反应阶段的方向。
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公开(公告)号：US09561483B2
公开(公告)日：2017-02-07
申请号：US14116596
申请日：2012-05-07
CPC分类号： B01J7/00 , B01J4/002 , B01J8/0278 , B01J8/0285 , B01J2208/00504 , C01B3/363 , C01B3/382 , C01B2203/0244 , C01B2203/025 , C10J3/506 , C10J2200/152
摘要： For producing synthesis gas by autothermal reformation of gaseous, liquid and/or solid fuels, the fuel is reacted with an oxidizing agent in a reaction space at a pressure of 10 to 120 bar and a reaction space temperature of 800 to 2,000° C. to obtain synthesis gas, wherein the oxidizing agent is introduced centrally in the upper region of the reaction space and wherein a flame is formed in the reaction space. The oxidizing agent is introduced into the reaction space separate from the fuel.
摘要翻译： 为了通过气体，液体和/或固体燃料的自热改造来生产合成气，燃料与反应空间中的氧化剂在10至120巴的压力和800至2,000℃的反应空间温度下反应至 获得合成气，其中氧化剂中心地引入反应空间的上部区域，并且其中在反应空间中形成火焰。 将氧化剂引入到与燃料分开的反应空间中。
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