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公开(公告)号：US20080263953A1
公开(公告)日：2008-10-30
申请号：US11630929
申请日：2005-06-28
申请人： Osamu Okada , Kota Yokoyama , Naoki Inoue
发明人： Osamu Okada , Kota Yokoyama , Naoki Inoue
CPC分类号： C01B3/382 , B01J8/0492 , B01J8/0496 , B01J19/30 , B01J2208/00061 , B01J2208/00203 , B01J2208/00415 , B01J2208/00522 , B01J2208/00849 , B01J2208/00973 , B01J2208/025 , B01J2219/0004 , B01J2219/30215 , B01J2219/30223 , C01B2203/0244 , C01B2203/085 , C01B2203/1047 , C01B2203/1058 , C01B2203/1247 , C01B2203/142 , C01B2203/143 , C01B2203/1614 , C01B2203/1619 , C01B2203/169 , C10L3/08 , H01M8/0612 , Y02E60/50 , Y02P20/52 , Y02P70/56
摘要： The invention provides a method for operating a reformed gas production apparatus with which it is possible to achieve a high reforming efficiency while preventing a drop in catalyst activity due to the deposition of carbon. The reformed gas production method uses a reforming catalyst to reform a fuel that contains a hydrocarbon having at least two carbon atoms to produce a reformed gas that includes methane, hydrogen, and carbon monoxide. With this method, a fluid that includes the fuel, at least one of steam and a carbon dioxide-containing gas, and an oxygen-containing gas, is supplied to a reforming reaction region, and with the thermal decomposition index temperature of the fuel, which is determined by the type and the concentration of the hydrocarbons having at least two carbon atoms that make up the fuel, serving as an upper limit temperature of the reforming reaction region, the fluid is brought into contact with the reforming catalyst to produce the reformed gas.
摘要翻译： 本发明提供了一种操作重整气体生产设备的方法，通过该方法可以实现高重整效率，同时防止由于碳沉积引起的催化剂活性下降。 重整气生产方法使用重整催化剂来重整含有至少两个碳原子的烃的燃料，以产生包括甲烷，氢气和一氧化碳的重整气体。 利用这种方法，将包括燃料，蒸汽和含二氧化碳的气体中的至少一种和含氧气体的流体供应到重整反应区域，并且随着燃料的热分解指数温度， 其由构成燃料的具有至少两个碳原子的烃的类型和浓度确定为重整反应区的上限温度，使流体与重整催化剂接触以产生重整的 加油站。
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公开(公告)号：US08486167B2
公开(公告)日：2013-07-16
申请号：US11630929
申请日：2005-06-28
申请人： Osamu Okada , Kota Yokoyama , Naoki Inoue
发明人： Osamu Okada , Kota Yokoyama , Naoki Inoue
IPC分类号： B01J8/04
CPC分类号： C01B3/382 , B01J8/0492 , B01J8/0496 , B01J19/30 , B01J2208/00061 , B01J2208/00203 , B01J2208/00415 , B01J2208/00522 , B01J2208/00849 , B01J2208/00973 , B01J2208/025 , B01J2219/0004 , B01J2219/30215 , B01J2219/30223 , C01B2203/0244 , C01B2203/085 , C01B2203/1047 , C01B2203/1058 , C01B2203/1247 , C01B2203/142 , C01B2203/143 , C01B2203/1614 , C01B2203/1619 , C01B2203/169 , C10L3/08 , H01M8/0612 , Y02E60/50 , Y02P20/52 , Y02P70/56
摘要： The invention provides a method for operating a reformed gas production apparatus with which it is possible to achieve a high reforming efficiency while preventing a drop in catalyst activity due to the deposition of carbon. The reformed gas production method uses a reforming catalyst to reform a fuel that contains a hydrocarbon having at least two carbon atoms to produce a reformed gas that includes methane, hydrogen, and carbon monoxide. With this method, a fluid that includes the fuel, at least one of steam and a carbon dioxide-containing gas, and an oxygen-containing gas, is supplied to a reforming reaction region, and with the thermal decomposition index temperature of the fuel, which is determined by the type and the concentration of the hydrocarbons having at least two carbon atoms that make up the fuel, serving as an upper limit temperature of the reforming reaction region, the fluid is brought into contact with the reforming catalyst to produce the reformed gas.
摘要翻译： 本发明提供了一种操作重整气体生产设备的方法，通过该方法可以实现高重整效率，同时防止由于碳沉积引起的催化剂活性下降。 重整气生产方法使用重整催化剂来重整含有至少两个碳原子的烃的燃料，以产生包括甲烷，氢气和一氧化碳的重整气体。 利用这种方法，将包括燃料，蒸汽和含二氧化碳的气体中的至少一种和含氧气体的流体供应到重整反应区域，并且随着燃料的热分解指数温度， 其由构成燃料的具有至少两个碳原子的烃的类型和浓度确定为重整反应区的上限温度，使流体与重整催化剂接触以产生重整的 加油站。
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公开(公告)号：US09162888B2
公开(公告)日：2015-10-20
申请号：US13449521
申请日：2012-04-18
申请人： Osamu Okada , Kota Yokoyama , Naoki Inoue
发明人： Osamu Okada , Kota Yokoyama , Naoki Inoue
CPC分类号： C01B3/382 , B01J8/0492 , B01J8/0496 , B01J19/30 , B01J2208/00061 , B01J2208/00203 , B01J2208/00415 , B01J2208/00522 , B01J2208/00849 , B01J2208/00973 , B01J2208/025 , B01J2219/0004 , B01J2219/30215 , B01J2219/30223 , C01B2203/0244 , C01B2203/085 , C01B2203/1047 , C01B2203/1058 , C01B2203/1247 , C01B2203/142 , C01B2203/143 , C01B2203/1614 , C01B2203/1619 , C01B2203/169 , C10L3/08 , H01M8/0612 , Y02E60/50 , Y02P20/52 , Y02P70/56
摘要： The present invention relates to a reformed gas production apparatus that includes a reaction chamber containing a reforming catalyst, a supply route to the reaction chamber, a reformed gas conduction route from the reaction chamber, and a reaction chamber temperature control means that controls a temperature of the reaction chamber. The supply route supplies a fluid that includes a fuel containing a hydrocarbon having at least two carbon atoms, at least one of steam and a carbon dioxide-containing gas, and an oxygen-containing gas. The fuel can be a mixed fuel that includes a plurality of types of hydrocarbons that each have at least two carbon atoms. The reaction chamber temperature control means relates to the thermal decomposition index temperature of the fuel, which defines an upper limit temperature of the reforming reaction region.
摘要翻译： 本发明涉及一种重整气体生产装置，其包括含有重整催化剂的反应室，到反应室的供给路径，来自反应室的重整气体传导路径，以及控制反应室温度控制装置， 反应室。 供应路线提供包含含有至少两个碳原子的烃，含蒸汽和含二氧化碳的气体中的至少一种和含氧气体的燃料的流体。 燃料可以是混合燃料，其包括各自具有至少两个碳原子的多种类型的烃。 反应室温度控制装置涉及限定重整反应区域的上限温度的燃料的热分解指数温度。
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公开(公告)号：US20120224997A1
公开(公告)日：2012-09-06
申请号：US13449521
申请日：2012-04-18
申请人： Osamu Okada , Kota Yokoyama , Naoki Inoue
发明人： Osamu Okada , Kota Yokoyama , Naoki Inoue
CPC分类号： C01B3/382 , B01J8/0492 , B01J8/0496 , B01J19/30 , B01J2208/00061 , B01J2208/00203 , B01J2208/00415 , B01J2208/00522 , B01J2208/00849 , B01J2208/00973 , B01J2208/025 , B01J2219/0004 , B01J2219/30215 , B01J2219/30223 , C01B2203/0244 , C01B2203/085 , C01B2203/1047 , C01B2203/1058 , C01B2203/1247 , C01B2203/142 , C01B2203/143 , C01B2203/1614 , C01B2203/1619 , C01B2203/169 , C10L3/08 , H01M8/0612 , Y02E60/50 , Y02P20/52 , Y02P70/56
摘要： The present invention relates to a reformed gas production apparatus that includes a reaction chamber containing a reforming catalyst, a supply route to the reaction chamber, a reformed gas conduction route from the reaction chamber, and a reaction chamber temperature control means that controls a temperature of the reaction chamber. The supply route supplies a fluid that includes a fuel containing a hydrocarbon having at least two carbon atoms, at least one of steam and a carbon dioxide-containing gas, and an oxygen-containing gas. The fuel can be a mixed fuel that includes a plurality of types of hydrocarbons that each have at least two carbon atoms. The reaction chamber temperature control means relates to the thermal decomposition index temperature of the fuel, which defines an upper limit temperature of the reforming reaction region.
摘要翻译： 本发明涉及一种重整气体生产装置，其包括含有重整催化剂的反应室，到反应室的供给路径，来自反应室的重整气体传导路径，以及控制反应室温度控制装置， 反应室。 供应路线提供包含含有至少两个碳原子的烃，含蒸汽和含二氧化碳的气体中的至少一种和含氧气体的燃料的流体。 燃料可以是混合燃料，其包括各自具有至少两个碳原子的多种类型的烃。 反应室温度控制装置涉及限定重整反应区域的上限温度的燃料的热分解指数温度。
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公开(公告)号：US20110147667A1
公开(公告)日：2011-06-23
申请号：US12999232
申请日：2009-06-11
申请人： Kota Yokoyama , Naoki Inoue , Koichiro Ikeda , Fuyuki Noguchi
发明人： Kota Yokoyama , Naoki Inoue , Koichiro Ikeda , Fuyuki Noguchi
IPC分类号： C01B3/38
CPC分类号： B01J4/002 , B01J8/0035 , B01J8/025 , B01J8/0278 , B01J8/0453 , B01J23/462 , B01J2208/00061 , B01J2208/00495 , B01J2208/00548 , B01J2208/00752 , B01J2208/00769 , B01J2208/00849 , B01J2208/00884 , B01J2208/025 , C01B3/40 , C01B2203/0244 , C01B2203/0261 , C01B2203/1064 , C01B2203/1619 , C01B2203/169 , Y02P20/52
摘要： A catalytic reactor including: a reaction container filled with a catalyst having ruthenium; and an introduction part for introducing a material fluid to the reaction container. The reaction container is supplied with a mixed gas as material fluid to produce synthetic gas containing hydrogen and carbon monoxide in the presence of the catalyst. The introduction part is connected to the reaction container in a horizontal direction or a direction inclined downward from above a horizontal plane, and a height of the catalyst filled in the reaction container is adjusted above a height at which the material fluid is fed from the introduction part to the reaction container. Also, a method of using the catalytic reactor including monitoring a molar ratio of carbon and oxygen contained in the material fluid and stopping the supply of an oxygen-containing gas to the reaction container before the molar ratio becomes excessively low.
摘要翻译： 一种催化反应器，包括：填充有具有钌的催化剂的反应容器; 以及用于将材料流体引入反应容器的引入部。 向反应容器中供给混合气体作为材料流体，以在催化剂存在下产生含有氢和一氧化碳的合成气体。 引导部分在水平方向或从水平面上方向下倾斜的方向上连接到反应容器，并且将填充在反应容器中的催化剂的高度调节到高于从引入物供给原料流体的高度 反应容器的一部分。 另外，使用催化反应器的方法包括监测材料流体中所含的碳和氧的摩尔比，并且在摩尔比变得过低之前停止向反应容器供应含氧气体。
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公开(公告)号：US08361433B2
公开(公告)日：2013-01-29
申请号：US11922032
申请日：2006-06-13
申请人： Fuyuki Noguchi , Naoki Inoue , Kota Yokoyama
发明人： Fuyuki Noguchi , Naoki Inoue , Kota Yokoyama
IPC分类号： C01B3/26
CPC分类号： B01J8/0095 , B01J4/002 , B01J8/0221 , B01J8/025 , B01J8/0278 , B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J19/0013 , B01J19/26 , B01J2208/00061 , B01J2208/00495 , B01J2208/00707 , B01J2208/00849 , B01J2208/025 , B01J2219/00198 , B01J2219/002 , B01J2219/00213 , B01J2219/00231 , B01J2219/00265 , C01B3/382 , C01B2203/0244 , C01B2203/1241 , C01B2203/1276 , C01B2203/1619 , C01B2203/1623 , C01B2203/169
摘要： There is provided a technique for manufacturing a hydrogen-containing gas. An oxygen-containing gas is mixed with a feed gas obtained by mixing steam with a hydrocarbon fuel, this mixture is introduced into a catalytic reaction chamber, and a partial oxidation reaction and a steam reforming reaction are conducted to obtain a hydrogen-containing gas. In this reforming, an antechamber of the catalytic reaction chamber is heated up to a self-ignition temperature in a first catalyst section, where the self-ignition temperature is the temperature at which a mixed gas self-ignites during the advection period required for the mixed gas to move from a mixing chamber to the catalytic reaction chamber, with this temperature being at least a minimum partial-oxidation temperature and lower than a minimum steam reforming temperature.
摘要翻译： 提供了制造含氢气体的技术。 将含氧气体与通过将蒸汽与烃燃料混合而获得的进料气体混合，将该混合物引入催化反应室中，进行部分氧化反应和蒸汽重整反应以获得含氢气体。 在这种重整中，催化反应室的前室在第一催化剂部分被加热到自燃温度，其中自燃温度是混合气体在平流期间自燃的温度 混合气体从混合室移动到催化反应室，该温度至少为最小部分氧化温度且低于最小蒸汽重整温度。
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公开(公告)号：US08945422B2
公开(公告)日：2015-02-03
申请号：US12999232
申请日：2009-06-11
申请人： Kota Yokoyama , Naoki Inoue , Koichiro Ikeda , Fuyuki Noguchi
发明人： Kota Yokoyama , Naoki Inoue , Koichiro Ikeda , Fuyuki Noguchi
CPC分类号： B01J4/002 , B01J8/0035 , B01J8/025 , B01J8/0278 , B01J8/0453 , B01J23/462 , B01J2208/00061 , B01J2208/00495 , B01J2208/00548 , B01J2208/00752 , B01J2208/00769 , B01J2208/00849 , B01J2208/00884 , B01J2208/025 , C01B3/40 , C01B2203/0244 , C01B2203/0261 , C01B2203/1064 , C01B2203/1619 , C01B2203/169 , Y02P20/52
摘要： A catalytic reactor including: a reaction container filled with a catalyst having ruthenium; and an introduction part for introducing a material fluid to the reaction container. The reaction container is supplied with a mixed gas as material fluid to produce synthetic gas containing hydrogen and carbon monoxide in the presence of the catalyst. The introduction part is connected to the reaction container in a horizontal direction or a direction inclined downward from above a horizontal plane, and a height of the catalyst filled in the reaction container is adjusted above a height at which the material fluid is fed from the introduction part to the reaction container. Also, a method of using the catalytic reactor including monitoring a molar ratio of carbon and oxygen contained in the material fluid and stopping the supply of an oxygen-containing gas to the reaction container before the molar ratio becomes excessively low.
摘要翻译： 一种催化反应器，包括：填充有具有钌的催化剂的反应容器; 以及用于将材料流体引入反应容器的引入部。 向反应容器中供给混合气体作为材料流体，以在催化剂存在下产生含有氢和一氧化碳的合成气体。 引导部分在水平方向或从水平面上方向下倾斜的方向上连接到反应容器，并且将填充在反应容器中的催化剂的高度调节到高于从引入物供给原料流体的高度 反应容器的一部分。 另外，使用催化反应器的方法包括监测材料流体中所含的碳和氧的摩尔比，并且在摩尔比变得过低之前停止向反应容器供应含氧气体。
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公开(公告)号：US20090212259A1
公开(公告)日：2009-08-27
申请号：US11922032
申请日：2006-06-13
申请人： Fuyuki Noguchi , Naoki Inoue , Kota Yokoyama
发明人： Fuyuki Noguchi , Naoki Inoue , Kota Yokoyama
CPC分类号： B01J8/0095 , B01J4/002 , B01J8/0221 , B01J8/025 , B01J8/0278 , B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J19/0013 , B01J19/26 , B01J2208/00061 , B01J2208/00495 , B01J2208/00707 , B01J2208/00849 , B01J2208/025 , B01J2219/00198 , B01J2219/002 , B01J2219/00213 , B01J2219/00231 , B01J2219/00265 , C01B3/382 , C01B2203/0244 , C01B2203/1241 , C01B2203/1276 , C01B2203/1619 , C01B2203/1623 , C01B2203/169
摘要： There is provided a technique for manufacturing a hydrogen-containing gas. An oxygen-containing gas is mixed with a feed gas obtained by mixing steam with a hydrocarbon fuel, this mixture is introduced into a catalytic reaction chamber, and a partial oxidation reaction and a steam reforming reaction are conducted to obtain a hydrogen-containing gas. In this reforming, an antechamber of the catalytic reaction chamber is heated up to a self-ignition temperature in a first catalyst section, where the self-ignition temperature is the temperature at which a mixed gas self-ignites during the advection period required for the mixed gas to move from a mixing chamber to the catalytic reaction chamber, with this temperature being at least a minimum partial-oxidation temperature and lower than a minimum steam reforming temperature.
摘要翻译： 提供了制造含氢气体的技术。 将含氧气体与通过将蒸汽与烃燃料混合而获得的进料气体混合，将该混合物引入催化反应室中，进行部分氧化反应和蒸汽重整反应以获得含氢气体。 在这种重整中，催化反应室的前室在第一催化剂部分被加热到自燃温度，其中自燃温度是混合气体在平流期间自燃的温度 混合气体从混合室移动到催化反应室，该温度至少为最小部分氧化温度且低于最小蒸汽重整温度。
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