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1.发明授权Method and tube bundle reactor for carrying out endothermic and exothermic gas phase reactions 有权用于进行吸热和放热气相反应的方法和管束反应器公开(公告)号：US07449037B2
公开(公告)日：2008-11-11
申请号：US11203353
申请日：2005-08-12
申请人： Manfred Lehr , Franz Egner , Michael Claussen , Markus Maly
发明人： Manfred Lehr , Franz Egner , Michael Claussen , Markus Maly
CPC分类号： B01J8/067 , B01J8/065 , B01J2208/0007
摘要： A method for carrying out endothermic or exothermic gas phase reactions by using a tube bundle reactor with a tube bundle of catalyst-filled reaction tubes comprises the following steps: a) Introducing a reaction gas mixture into the reaction tubes; b) Dividing-up of the reaction gas mixture flow flowing through each of the reaction tubes into at least two partial flows, each partial flow having the same composition; c) Feeding-in of each partial flow at a different point along the catalyst filling with an existing flow resistance; d) Determining the desired partial flow volume for each partial flow (V1, V2, V3, V4); e) Calculating the pressure at the point of the first division of the reaction gas mixture (9); f) Calculating the pressure in the catalyst filling (12) at the point of feeding-in of each partial flow (V1, V2, V3, V4); and g) Setting of flow resistance for each point of feeding-in in such a way that the flow resistance at the desired partial flow volume corresponds to the pressure difference between the pressures determined in steps e) and f).
摘要翻译： 通过使用具有催化剂填充反应管的管束的管束反应器进行吸热或放热气相反应的方法包括以下步骤：a）将反应气体混合物引入反应管中; b）将流过每个反应管的反应气体混合物流分成至少两个部分流，每个部分流具有相同的组成; c）沿着催化剂填充的不同点处的每个部分流进入现有的流动阻力; d）确定每个部分流（V 1，V 2，V 3，V 4）的期望的部分流量， SUB>）; e）计算反应气体混合物（9）的第一分馏点的压力; f）计算每个部分流（V 1，V 2，V 3）的进料点处的催化剂填充物（12）中的压力， / SUB>，V 4）; 和g）以每一个进料点设定流动阻力，使得所需部分流量下的流动阻力对应于在步骤e）和f）中确定的压力之间的压力差。
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2.发明申请Method and tube bundle reactor for carrying out endothermic and exothermic gas phase reactions 有权用于进行吸热和放热气相反应的方法和管束反应器公开(公告)号：US20060041030A1
公开(公告)日：2006-02-23
申请号：US11203353
申请日：2005-08-12
申请人： Manfred Lehr , Franz Egner , Michael Claussen , Markus Maly
发明人： Manfred Lehr , Franz Egner , Michael Claussen , Markus Maly
CPC分类号： B01J8/067 , B01J8/065 , B01J2208/0007
摘要： A method for carrying out endothermic or exothermic gas phase reactions by using a tube bundle reactor with a tube bundle of catalyst-filled reaction tubes comprises the following steps: a) Introducing a reaction gas mixture into the reaction tubes; b) Dividing-up of the reaction gas mixture flow flowing through each of the reaction tubes into at least two partial flows, each partial flow having the same composition; c) Feeding-in of each partial flow at a different point along the catalyst filling with an existing flow resistance; d) Determining the desired partial flow volume for each partial flow (V1, V2, V3, V4); e) Calculating the pressure at the point of the first division of the reaction gas mixture (9); f) Calculating the pressure in the catalyst filling (12) at the point of feeding-in of each partial flow (V1, V2, V3, V4); and g) Setting of flow resistance for each point of feeding-in in such a way that the flow resistance at the desired partial flow volume corresponds to the pressure difference between the pressures determined in steps e) and f).
摘要翻译： 通过使用具有催化剂填充反应管的管束的管束反应器进行吸热或放热气相反应的方法包括以下步骤：a）将反应气体混合物引入反应管中; b）将流过每个反应管的反应气体混合物流分成至少两个部分流，每个部分流具有相同的组成; c）沿着催化剂填充的不同点处的每个部分流进入现有的流动阻力; d）确定每个部分流（V 1，V 2，V 3，V 4）的期望的部分流量， SUB>）; e）计算反应气体混合物（9）的第一分馏点的压力; f）计算每个部分流（V 1，V 2，V 3）的进料点处的催化剂填充物（12）中的压力， / SUB>，V 4）; 和g）以每一个进料点设定流动阻力，使得所需部分流量下的流动阻力对应于在步骤e）和f）中确定的压力之间的压力差。
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