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1. 发明授权

US08961909B2 Shell-and-tube reactor for carrying out catalytic gas phase reactions 有权
标题翻译：用于进行催化气相反应的壳 - 管反应器
公开(公告)号：US08961909B2
公开(公告)日：2015-02-24
申请号：US13823525
申请日：2011-10-12
申请人： Manfred Lehr , Josef Dachs , Franz Egner , Rolf Bank , Bernd Stürmer , Volkmar Frick , Michael Specht
发明人： Manfred Lehr , Josef Dachs , Franz Egner , Rolf Bank , Bernd Stürmer , Volkmar Frick , Michael Specht
IPC分类号： B01J8/06 , C10G2/00 , C10L3/08 , F28F13/08
CPC分类号： B01J8/067 , B01J8/065 , B01J2208/0023 , B01J2208/00238 , B01J2208/0053 , C10G2/32 , C10G2/341 , C10L3/08 , F28F13/08
摘要： A tube bundle reactor for carrying out catalytic gas phase reactions, particularly methanation reactions, has a bundle of catalyst-filled reaction tubes through which reaction gas flows and around which heat carrier flows during operation. In the region of the catalyst filling, the reaction tubes run through at least two heat carrier zones which are separated from one another, the first of which heat carrier zones extends over the starting region of the catalyst filling. The reaction tubes each have a first reaction tube portion with a first hydraulic diameter of the catalyst filling and, downstream thereof in flow direction of the reaction gas, at least a second reaction tube portion with a second hydraulic diameter of the catalyst filling that is greater than the first hydraulic diameter of the catalyst filling.
摘要翻译：用于进行催化气相反应，特别是甲烷化反应的管束反应器具有一束催化剂填充的反应管，反应气体在其中流动并在运行期间使热载体流过。在催化剂填充的区域中，反应管穿过至少两个彼此分离的热载体区，其中第一个热载体区在催化剂填充物的起始区域上延伸。反应管各自具有第一反应管部分，其具有催化剂填充物的第一水力直径，并且在反应气体的流动方向上在其下游，至少第二反应管部分具有催化剂填充物的第二水力直径更大比第一液压直径的催化剂填充。

2. 发明申请

US20130287652A1 SHELL-AND-TUBE REACTOR FOR CARRYING OUT CATALYTIC GAS PHASE REACTIONS 有权
标题翻译：用于携带催化气相反应的壳管反应器
公开(公告)号：US20130287652A1
公开(公告)日：2013-10-31
申请号：US13823525
申请日：2011-10-12
申请人： Manfred Lehr , Josef Dachs , Franz Egner , Rolf Bank , Bernd Stürmer , Volkmar Frick , Michael Specht
发明人： Manfred Lehr , Josef Dachs , Franz Egner , Rolf Bank , Bernd Stürmer , Volkmar Frick , Michael Specht
IPC分类号： B01J8/06
CPC分类号： B01J8/067 , B01J8/065 , B01J2208/0023 , B01J2208/00238 , B01J2208/0053 , C10G2/32 , C10G2/341 , C10L3/08 , F28F13/08
摘要： A tube bundle reactor for carrying out catalytic gas phase reactions, particularly methanation reactions, has a bundle of catalyst-filled reaction tubes through which reaction gas flows and around which heat carrier flows during operation. In the region of the catalyst filling, the reaction tubes run through at least two heat carrier zones which are separated from one another, the first of which heat carrier zones extends over the starting region of the catalyst filling. The reaction tubes each have a first reaction tube portion with a first hydraulic diameter of the catalyst filling and, downstream thereof in flow direction of the reaction gas, at least a second reaction tube portion with a second hydraulic diameter of the catalyst filling that is greater than the first hydraulic diameter of the catalyst filling.
摘要翻译：用于进行催化气相反应，特别是甲烷化反应的管束反应器具有一束催化剂填充的反应管，反应气体在其中流动并在运行期间使热载体流过。在催化剂填充的区域中，反应管穿过至少两个彼此分离的热载体区，其中第一个热载体区在催化剂填充物的起始区域上延伸。反应管各自具有第一反应管部分，其具有催化剂填充物的第一水力直径，并且在反应气体的流动方向上在其下游，至少第二反应管部分具有催化剂填充物的第二水力直径更大比第一液压直径的催化剂填充。

3. 发明申请

US20060024222A1 Method and apparatus for carrying out exothermic gas phase reactions 审中-公开
标题翻译：进行放热气相反应的方法和装置
公开(公告)号：US20060024222A1
公开(公告)日：2006-02-02
申请号：US11193972
申请日：2005-07-29
申请人： Josef Dachs , Wolfgang Schuster , Rolf Bank , Manfred Lehr
发明人： Josef Dachs , Wolfgang Schuster , Rolf Bank , Manfred Lehr
IPC分类号： F28D7/00 , C01B15/013
CPC分类号： F28F1/40 , B01J8/06 , B01J8/067 , B01J19/002 , B01J2208/00238 , B01J2208/0084 , B01J2208/00849 , B01J2219/00263
摘要： With a method for operating a tube bundle reactor for exothermic gas phase reactions having a tube bundle with catalyst-filled reaction tubes (2), wherein the one ends of the reaction tubes are spanned by a gas inlet hood and the other ends are spanned by a gas outlet hood and wherein around the outside of the reaction tubes a heat transfer medium flows to carry off reaction heat. An explosive gas mixture (G) is introduced into the reaction tubes (2) via the gas inlet hood and after reaction the gas mixture (G), that may still be explosive, it is led off from the reaction tubes via the gas outlet hood. A limit temperature in the reaction tubes (2) is specified that lies above the normal operating temperatures in the reaction tubes (2) but at most equals the ignition temperature of the explosive gas mixture (G) Each non-operating high temperature region (7) forming in the reaction tubes (2) whose temperature is at least equal to the limit temperature and which migrates in the respective reaction tube (2) in the longitudinal direction thereof is stopped while still in the reaction tube (2) so that the high temperature region (7) is prevented from advancing into the gas inlet hood or the gas outlet hood.
摘要翻译：使用具有管束的放出气相反应管管式反应器的方法，其中催化剂填充的反应管（2），其中反应管的一端由气体入口罩跨过，另一端被气体出口罩，并且其中在反应管的外部，传热介质流动以携带反应热。爆炸性气体混合物（G）通过进气口引入反应管（2），反应后气体混合物（G）可能仍然是爆炸性的，通过气体出口罩从反应管中引出。规定反应管（2）中的极限温度高于反应管（2）的正常工作温度，但最多等于爆炸性气体混合物（G）的点火温度。每个非工作高温区域（7））在反应管（2）中形成，其温度至少等于极限温度，并且在反应管（2）的纵向方向上迁移到反应管（2）中，同时停留在反应管（2）中，使得高温度区域（7）被阻止进入气体入口罩或气体出口罩。

4. 发明授权

US07988927B2 Method of varying the temperature of a tube bundle reactor 有权
标题翻译：改变管束反应器温度的方法
公开(公告)号：US07988927B2
公开(公告)日：2011-08-02
申请号：US11782741
申请日：2007-07-25
申请人： Manfred Lehr , Josef Dachs , Wolfgang Schuster
发明人： Manfred Lehr , Josef Dachs , Wolfgang Schuster
IPC分类号： F28D7/00
CPC分类号： B01J8/067 , B01J2208/00053 , B01J2208/00061 , B01J2208/00212 , B01J2208/00221 , B01J2208/00256 , B01J2208/00646 , B01J2208/00716 , F28D7/16 , F28F27/00
摘要： A method of varying the temperature of a tube bundle reactor for catalytic gas phase reactions upon start-up and shut-down, the tube bundle reactor comprising a major reactor portion which includes a bundle of vertically disposed reactor tubes, upper and lower tubesheets tightly connected to the upper and lower ends, respectively, of the reactor tubes, and a reactor shell enclosing the tube bundle, a heat transfer medium having a melting temperature in the range of from 100° C. to 450° C. flowing around the outer surfaces of the reactor tubes during normal operation and being circulated in at least one circuit through the major reactor portion, comprising the steps: (a) varying the heat transfer medium temperature during circulation of the heat transfer medium; and (b) passing a temperature gas through the reactor tubes at least when the heat transfer medium is not yet or no longer circulated.
摘要翻译：一种在启动和关闭时改变用于催化气相反应的管束反应器的温度的方法，所述管束反应器包括主反应器部分，其包括一束垂直设置的反应器管，上管和下管紧密连接反应器管的上端和下端以及包围管束的反应器壳体，具有在外表面流动的熔点在100℃至450℃范围内的传热介质的反应器管，并且通过主反应器部分在至少一个回路中循环，包括以下步骤：（a）改变传热介质循环期间的传热介质温度; 和（b）至少当传热介质尚未或不再循环时，使温度气体通过反应器管。

5. 发明申请

US20080023175A1 METHOD OF VARYING THE TEMPERATURE OF A TUBE BUNDLE REACTOR 有权
标题翻译：改变管组件反应器温度的方法
公开(公告)号：US20080023175A1
公开(公告)日：2008-01-31
申请号：US11782741
申请日：2007-07-25
申请人： Manfred Lehr , Josef Dachs , Wolfgang Schuster
发明人： Manfred Lehr , Josef Dachs , Wolfgang Schuster
IPC分类号： B01J8/06
CPC分类号： B01J8/067 , B01J2208/00053 , B01J2208/00061 , B01J2208/00212 , B01J2208/00221 , B01J2208/00256 , B01J2208/00646 , B01J2208/00716 , F28D7/16 , F28F27/00
摘要： A method of varying the temperature of a tube bundle reactor for catalytic gas phase reactions upon start-up and shut-down, the tube bundle reactor comprising a major reactor portion which includes a bundle of vertically disposed reactor tubes, upper and lower tubesheets tightly connected to the upper and lower ends, respectively, of the reactor tubes, and a reactor shell enclosing the tube bundle, a heat transfer medium having a melting temperature in the range of from 100° C. to 450° C. flowing around the outer surfaces of the reactor tubes during normal operation and being circulated in at least one circuit through the major reactor portion, comprising the steps: (a) varying the heat transfer medium temperature during circulation of the heat transfer medium; and (b) passing a temperature gas through the reactor tubes at least when the heat transfer medium is not yet or no longer circulated.
摘要翻译：一种在启动和关闭时改变用于催化气相反应的管束反应器的温度的方法，管束反应器包括主反应器部分，其包括一排垂直设置的反应器管，上管和下管紧密连接反应器管的上端和下端以及包围管束的反应器壳体，具有在外表面流动的熔点在100℃至450℃范围内的传热介质的反应器管，并且通过主反应器部分在至少一个回路中循环，包括以下步骤：（a）改变传热介质循环期间的传热介质温度; 和（b）至少当传热介质尚未或不再循环时，使温度气体通过反应器管。

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