专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US08629191B2 Process and plant for producing methanol 有权
标题翻译：生产甲醇的工艺和装置
公开(公告)号：US08629191B2
公开(公告)日：2014-01-14
申请号：US13121562
申请日：2009-07-29
申请人： Hans Kopetsch , Philipp Marius Hackel , Veronika Gronemann , Rainer Morgenroth
发明人： Hans Kopetsch , Philipp Marius Hackel , Veronika Gronemann , Rainer Morgenroth
IPC分类号： C07C27/00
CPC分类号： C07C29/152 , B01J8/067 , B01J2208/00274 , B01J2219/0004 , C07C31/04
摘要： For producing methanol from a synthesis gas containing hydrogen and carbon oxides the synthesis gas is passed through a first, water-cooled reactor in which a part of the carbon oxides is catalytically converted to methanol. The resulting mixture containing synthesis gas and methanol vapor is supplied to a second, gas-cooled reactor in which a further part of the carbon oxides is converted to methanol. Subsequently, methanol is separated from the synthesis gas, and synthesis gas is recirculated to the first reactor. The cooling gas flows through the second reactor cocurrent to the mixture withdrawn from the first reactor.
摘要翻译：为了从含有氢和碳氧化物的合成气生产甲醇，合成气通过第一个水冷反应器，其中一部分碳氧化物被催化转化成甲醇。将所得到的含有合成气和甲醇蒸汽的混合物供应到第二个气冷反应器中，其中另外一部分碳氧化物转化为甲醇。随后，从合成气中分离出甲醇，合成气再循环至第一反应器。冷却气体流过第二反应器并流至从第一反应器排出的混合物。

2. 发明申请

US20110178188A1 PROCESS AND PLANT FOR PRODUCING METHANOL 有权
标题翻译：生产甲醇的工艺和设备
公开(公告)号：US20110178188A1
公开(公告)日：2011-07-21
申请号：US13121562
申请日：2009-07-29
申请人： Hans Kopetsch , Philipp Marius Hackel , Veronika Gronemann , Rainer Morgenroth
发明人： Hans Kopetsch , Philipp Marius Hackel , Veronika Gronemann , Rainer Morgenroth
IPC分类号： C07C29/152
CPC分类号： C07C29/152 , B01J8/067 , B01J2208/00274 , B01J2219/0004 , C07C31/04
摘要： For producing methanol from a synthesis gas containing hydrogen and carbon oxides the synthesis gas is passed through a first, water-cooled reactor in which a part of the carbon oxides is catalytically converted to methanol. The resulting mixture containing synthesis gas and methanol vapor is supplied to a second, gas-cooled reactor in which a further part of the carbon oxides is converted to methanol. Subsequently, methanol is separated from the synthesis gas, and synthesis gas is recirculated to the first reactor. The cooling gas flows through the second reactor cocurrent to the mixture withdrawn from the first reactor.
摘要翻译：为了从含有氢和碳氧化物的合成气生产甲醇，合成气通过第一个水冷反应器，其中一部分碳氧化物被催化转化成甲醇。将所得到的含有合成气和甲醇蒸汽的混合物供应到第二个气冷反应器中，其中另外一部分碳氧化物转化为甲醇。随后，从合成气中分离出甲醇，合成气再循环至第一反应器。冷却气体流过第二反应器并流至从第一反应器排出的混合物。

3. 发明申请

US20110178187A1 PROCESS AND PLANT FOR PRODUCING METHANOL 有权
标题翻译：生产甲醇的工艺和设备
公开(公告)号：US20110178187A1
公开(公告)日：2011-07-21
申请号：US13121553
申请日：2009-07-29
申请人： Hans Kopetsch
发明人： Hans Kopetsch
IPC分类号： C07C29/152
CPC分类号： C07C29/1516 , B01D5/009 , B01D5/0093 , B01J8/067 , B01J2208/00274 , B01J2219/0004 , C07C31/04
摘要： For producing methanol from a synthesis gas containing hydrogen and carbon oxides the synthesis gas is passed through a first, preferably water-cooled reactor in which a part of the carbon oxides is catalytically converted to methanol, and the resulting mixture containing synthesis gas and methanol vapor is supplied to a second, preferably gas-cooled reactor in which a further part of the carbon oxides is converted to methanol. The mixture withdrawn from the first reactor is guided through a gas/gas heat exchanger in which the mixture is cooled to a temperature below its dew point. Subsequently, methanol is separated from the gas stream in a methanol separator and withdrawn, while the remaining gas stream is supplied to the second reactor.
摘要翻译：为了从含有氢和碳氧化物的合成气中生产甲醇，合成气通过第一个，优选水冷却的反应器，其中一部分碳氧化物被催化转化成甲醇，所得混合物含有合成气和甲醇蒸汽被供应到第二，优选气冷反应器，其中另外部分的碳氧化物转化成甲醇。从第一反应器排出的混合物被引导通过气体/气体热交换器，其中将混合物冷却至低于其露点的温度。随后，在甲醇分离器中将甲醇从气流中分离出并取出，同时将剩余的气流供应到第二反应器。

4. 发明授权

US08629190B2 Process and plant for producing methanol 有权
标题翻译：生产甲醇的工艺和装置
公开(公告)号：US08629190B2
公开(公告)日：2014-01-14
申请号：US13121553
申请日：2009-07-29
申请人： Hans Kopetsch
发明人： Hans Kopetsch
IPC分类号： C07C27/00
CPC分类号： C07C29/1516 , B01D5/009 , B01D5/0093 , B01J8/067 , B01J2208/00274 , B01J2219/0004 , C07C31/04
摘要： For producing methanol from a synthesis gas containing hydrogen and carbon oxides the synthesis gas is passed through a first, preferably water-cooled reactor in which a part of the carbon oxides is catalytically converted to methanol, and the resulting mixture containing synthesis gas and methanol vapor is supplied to a second, preferably gas-cooled reactor in which a further part of the carbon oxides is converted to methanol. The mixture withdrawn from the first reactor is guided through a gas/gas heat exchanger in which the mixture is cooled to a temperature below its dew point. Subsequently, methanol is separated from the gas stream in a methanol separator and withdrawn, while the remaining gas stream is supplied to the second reactor.
摘要翻译：为了从含有氢和碳氧化物的合成气中生产甲醇，合成气通过第一个，优选水冷却的反应器，其中一部分碳氧化物被催化转化成甲醇，所得混合物含有合成气和甲醇蒸汽被供应到第二，优选气冷反应器，其中另外部分的碳氧化物转化成甲醇。从第一反应器排出的混合物被引导通过气体/气体热交换器，其中将混合物冷却至低于其露点的温度。随后，在甲醇分离器中将甲醇从气流中分离出并取出，同时将剩余的气流供应到第二反应器。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式