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公开(公告)号:US07563292B2
公开(公告)日:2009-07-21
申请号:US10789219
申请日:2004-02-27
IPC分类号: B01J7/00
CPC分类号: B01J8/0492 , B01J8/0465 , B01J8/0496 , B01J2208/00309 , B01J2208/00495 , B01J2208/0053 , C01B3/382 , C01B3/386 , C01B3/48 , C01B2203/0244 , C01B2203/0283 , C01B2203/0288 , C01B2203/044 , C01B2203/0455 , C01B2203/0465 , C01B2203/047 , C01B2203/0485 , C01B2203/066 , C01B2203/0844 , C01B2203/0877 , C01B2203/0883 , C01B2203/1041 , C01B2203/1064 , C01B2203/107 , C01B2203/1082 , C01B2203/1205 , C01B2203/1241 , C01B2203/1247 , C01B2203/1276 , C01B2203/1282 , C01B2203/1294 , C01B2203/142 , C01B2203/143 , C01B2203/146 , C01B2203/169 , C01B2203/82
摘要: A method of producing a H2 rich gas stream includes supplying an O2 rich gas, steam, and fuel to an inner reforming zone of a fuel processor that includes a partial oxidation catalyst and a steam reforming catalyst or a combined partial oxidation and stream reforming catalyst. The method also includes contacting the O2 rich gas, steam, and fuel with the partial oxidation catalyst and the steam reforming catalyst or the combined partial oxidation and stream reforming catalyst in the inner reforming zone to generate a hot reformate stream. The method still further includes cooling the hot reformate stream in a cooling zone to produce a cooled reformate stream. Additionally, the method includes removing sulfur-containing compounds from the cooled reformate stream by contacting the cooled reformate stream with a sulfur removal agent. The method still further includes contacting the cooled reformate stream with a catalyst that converts water and carbon monoxide to carbon dioxide and H2 in a water-gas-shift zone to produce a final reformate stream in the fuel processor.
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公开(公告)号:US06713040B2
公开(公告)日:2004-03-30
申请号:US09816676
申请日:2001-03-23
IPC分类号: C01B326
CPC分类号: B01J8/0492 , B01J8/0465 , B01J8/0496 , B01J2208/00309 , B01J2208/00495 , B01J2208/0053 , C01B3/382 , C01B3/386 , C01B3/48 , C01B2203/0244 , C01B2203/0283 , C01B2203/0288 , C01B2203/044 , C01B2203/0455 , C01B2203/0465 , C01B2203/047 , C01B2203/0485 , C01B2203/066 , C01B2203/0844 , C01B2203/0877 , C01B2203/0883 , C01B2203/1041 , C01B2203/1064 , C01B2203/107 , C01B2203/1082 , C01B2203/1205 , C01B2203/1241 , C01B2203/1247 , C01B2203/1276 , C01B2203/1282 , C01B2203/1294 , C01B2203/142 , C01B2203/143 , C01B2203/146 , C01B2203/169 , C01B2203/82
摘要: A method of producing a H2 rich gas stream includes supplying an O2 rich gas, steam, and fuel to an inner reforming zone of a fuel processor that includes a partial oxidation catalyst and a steam reforming catalyst or a combined partial oxidation and stream reforming catalyst. The method also includes contacting the O2 rich gas, steam, and fuel with the partial oxidation catalyst and the steam reforming catalyst or the combined partial oxidation and stream reforming catalyst in the inner reforming zone to generate a hot reformate stream. The method still further includes cooling the hot reformate stream in a cooling zone to produce a cooled reformate stream. Additionally, the method includes removing sulfur-containing compounds from the cooled reformate stream by contacting the cooled reformate stream with a sulfur removal agent. The method still further includes contacting the cooled reformate stream with a catalyst that converts water and carbon monoxide to carbon dioxide and H2 in a water-gas-shift zone to produce a final reformate stream in the fuel processor.
摘要翻译: 一种生产富H2气体流的方法包括将富O2的气体,蒸汽和燃料供应到包括部分氧化催化剂和蒸汽重整催化剂或组合的部分氧化和物流重整催化剂的燃料处理器的内部重整区。 该方法还包括使富氧气体,蒸汽和燃料与内部重整区中的部分氧化催化剂和蒸汽重整催化剂或组合的部分氧化和物流重整催化剂接触以产生热重整产物流。 该方法还包括在冷却区中冷却热重整物流以产生冷却的重整产物流。 此外,该方法包括通过将冷却的重整产物流与除硫剂接触来从冷却的重整产物流中除去含硫化合物。 该方法还包括将冷却的重整产物流与在水煤气转移区中将水和一氧化碳转化为二氧化碳和H 2的催化剂接触,以在燃料处理器中产生最终的重整产物流。
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公开(公告)号:US06670305B2
公开(公告)日:2003-12-30
申请号:US09851843
申请日:2001-05-09
IPC分类号: B01J2104
CPC分类号: B01J37/0244 , B01J23/42 , B01J23/63 , B01J35/04 , B01J37/0018 , B01J37/0219 , C01B3/382 , Y02P20/52
摘要: A monolithic catalyst with micro-scale flow channels and methods of making such a monolithic catalyst are provided. The monolithic catalyst includes a plurality of thin catalyst walls. The walls have a set thickness in a range from 1 to 150 &mgr;m. The thin catalyst walls define a plurality of flow channels. A fugitive material is used to form the flow channels. The flow channels have a set width in a range from 1 to 200 &mgr;m. The flow channels are formed by an organic fugitive material, which burns off during processing. By using the thin catalyst walls and flow channels having a set width in a range from 1 to 200 &mgr;m, a reduced diffusion path length that molecules travel between the bulk gas and the active site is provided. Accelerating the mass transport thus improves the overall reaction rate, which allows processing of more reactants. Thus, the volume of the required catalyst is reduced, allowing more compact reactors. Fabrication methods involve simple, low-cost and scaleable procedures, allowing the flow channel and catalyst dimensions to be easily scaled to a requisite size for a given application. One fabrication method involves tape casting successive layers of fugitive and catalyst materials, and then firing to remove the organic binders and partially sinter the catalyst particles. The slurries can also be cast into thin layers using various processes, including screen printing, wet spraying and spin casting. Another fabrication method for fabricating a supported catalyst involves dipping a pre-shaped metal foil into a slurry containing an active catalyst powder, allowing the catalyst slurry to coat the foil evenly and allowing the catalyst slurry coated foil to dry. The catalyst slurry coated foil is dipped into a solution to form a fugitive coating layer, next the coated metal foil is cut into strips and formed into a selected shape.
摘要翻译: 提供了具有微尺度流动通道的整体式催化剂和制造这种整体式催化剂的方法。 整体式催化剂包括多个薄的催化剂壁。 墙壁的厚度范围为1至150 mum。 薄催化剂壁限定多个流动通道。 使用逃逸材料形成流动通道。 流道的设定宽度范围为1〜200μm。 流动通道由加工过程中燃烧的有机短暂物质形成。 通过使用具有1至200μm范围内的设定宽度的薄催化剂壁和流动通道,提供分子在大气体和活性位点之间行进的减小的扩散路径长度。 因此,加速质量传递提高了整体反应速率,这允许加工更多的反应物。 因此,所需催化剂的体积减小,允许更紧凑的反应器。 制造方法涉及简单,低成本和可扩展的程序,允许流动通道和催化剂尺寸容易地缩放到给定应用的必要尺寸。 一种制造方法包括将连续的挥发性和催化剂材料层进行带铸,然后焙烧以除去有机粘合剂并部分烧结催化剂颗粒。 浆料也可以使用各种方法浇铸成薄层,包括丝网印刷,湿式喷涂和旋转浇铸。 用于制造负载型催化剂的另一种制造方法包括将预形金属箔浸入含有活性催化剂粉末的浆料中,使催化剂浆料均匀地涂覆箔片,并使涂覆有催化剂浆料的箔片干燥。 将催化剂浆料涂覆的箔浸入溶液中以形成短暂的涂层,接下来将涂覆的金属箔切成条并形成选定的形状。
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公开(公告)号:US5248566A
公开(公告)日:1993-09-28
申请号:US796973
申请日:1991-11-25
申请人: Romesh Kumar , Shabbir Ahmed , Michael Krumpelt , Kevin M. Myles
发明人: Romesh Kumar , Shabbir Ahmed , Michael Krumpelt , Kevin M. Myles
IPC分类号: H01M8/06
CPC分类号: H01M8/0612
摘要: A propulsion system for a vehicle having pairs of front and rear wheels and a fuel tank. An electrically driven motor having an output shaft operatively connected to at least one of said pair of wheels is connected to a fuel cell having a positive electrode and a negative electrode separated by an electrolyte for producing dc power to operate the motor. A partial oxidation reformer is connected both to the fuel tank and to the fuel cell receives hydrogen-containing fuel from the fuel tank and water and air and for partially oxidizing and reforming the fuel with water and air in the presence of an oxidizing catalyst and a reforming catalyst to produce a hydrogen-containing gas. The hydrogen-containing gas is sent from the partial oxidation reformer to the fuel cell negative electrode while air is transported to the fuel cell positive electrode to produce dc power for operating the electric motor.
摘要翻译: 一种用于具有一对前后轮和一个燃料箱的车辆的推进系统。 具有可操作地连接到所述一对车轮中的至少一个的输出轴的电动马达连接到具有由用于产生直流电力以产生电动机的电解质分离的正极和负极的燃料电池。 部分氧化重整器连接到燃料箱,燃料电池从燃料箱和水和空气接收含氢燃料,并在氧化催化剂存在下用水和空气部分氧化和重整燃料, 重整催化剂以产生含氢气体。 将含氢气体从部分氧化重整器输送到燃料电池负极,同时将空气输送到燃料电池正极,以产生用于操作电动机的直流电力。
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公开(公告)号:US06244367B1
公开(公告)日:2001-06-12
申请号:US09110425
申请日:1998-07-06
申请人: Shabbir Ahmed , Romesh Kumar , Michael Krumpelt
发明人: Shabbir Ahmed , Romesh Kumar , Michael Krumpelt
IPC分类号: B60K100
CPC分类号: B01J8/0285 , B01J8/025 , B60K1/04 , B60K15/10 , B60K17/356 , B60L11/1881 , B60L11/1892 , B60L11/1894 , C01B3/386 , C01B2203/0261 , C01B2203/044 , C01B2203/0445 , C01B2203/047 , C01B2203/066 , C01B2203/085 , C01B2203/1023 , C01B2203/1076 , C01B2203/1082 , C01B2203/1223 , C01B2203/1258 , C01B2203/1288 , C01B2203/1604 , C01B2203/1619 , C01B2203/1676 , C01B2203/169 , H01M8/0612 , H01M8/0631 , Y02T90/34
摘要: A partial oxidation reformer comprising a longitudinally extending chamber having a methanol, water and an air inlet and an outlet. An igniter mechanism is near the inlets for igniting a mixture of methanol and air, while a partial oxidation catalyst in the chamber is spaced from the inlets and converts methanol and oxygen to carbon dioxide and hydrogen. Controlling the oxygen to methanol mole ratio provides continuous slightly exothermic partial oxidation reactions of methanol and air producing hydrogen gas. The liquid is preferably injected in droplets having diameters less than 100 micrometers. The reformer is useful in a propulsion system for a vehicle which supplies a hydrogen-containing gas to the negative electrode of a fuel cell.
摘要翻译: 一种部分氧化重整器,其包括具有甲醇,水和空气入口以及出口的纵向延伸室。 点火器机构靠近用于点燃甲醇和空气的混合物的入口,而室中的部分氧化催化剂与入口间隔开并将甲醇和氧转化为二氧化碳和氢气。 控制氧气与甲醇的摩尔比提供甲醇和产生氢气的空气的连续轻微的放热部分氧化反应。 液体优选以直径小于100微米的液滴注入。 重整器可用于向燃料电池的负极供给含氢气体的车辆的推进系统。
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公开(公告)号:US06303098B1
公开(公告)日:2001-10-16
申请号:US09382737
申请日:1999-08-24
申请人: Kurt W. Kramarz , Ira D. Bloom , Romesh Kumar , Shabbir Ahmed , Rolf Wilkenhoener , Michael Krumpelt
发明人: Kurt W. Kramarz , Ira D. Bloom , Romesh Kumar , Shabbir Ahmed , Rolf Wilkenhoener , Michael Krumpelt
IPC分类号: C01B316
CPC分类号: B01J35/0006 , C01B3/386 , C01B3/40 , C01B2203/0261 , C01B2203/085 , C01B2203/1047 , C01B2203/1052 , C01B2203/1064 , C01B2203/107 , C01B2203/1082 , C01B2203/1241 , C01B2203/1247 , C01B2203/1619 , C04B35/453 , C04B35/486 , C04B35/495 , C04B35/50 , H01M8/0612 , Y02P20/52
摘要: A method of forming a hydrogen rich gas from a source of hydrocarbon fuel. A vapor of the hydrocarbon fuel and steam is brought in contact with a two-part catalyst having a dehydrogenation powder portion and an oxide-ion conducting powder portion at a temperature not less than about 770°C. for a time sufficient to generate the hydrogen rich. The H2 content of the hydrogen gas is greater than about 70 percent by volume. The dehydrogenation portion of the catalyst includes a group VIII metal, and the oxide-ion conducting portion is selected from a ceramic oxide from the group crystallizing in the fluorite or perovskite structure and mixtures thereof. The oxide-ion conducting portion of the catalyst is a ceramic powder of one or more of ZrO2, CeO2, Bi2O3, (BiVO)4, and LaGaO3.
摘要翻译: 从碳氢燃料源形成富氢气体的方法。 在不低于约770℃的温度下使烃燃料和蒸汽的蒸气与具有脱氢粉末部分和氧化物离子传导粉末部分的两部分催化剂接触。 足以产生富氢的时间。 氢气的H 2含量大于约70体积%。 催化剂的脱氢部分包括VIII族金属,氧化物离子传导部分选自以萤石或钙钛矿结构结晶的基团的陶瓷氧化物及其混合物。 催化剂的氧化物离子传导部分是ZrO 2,CeO 2,Bi 2 O 3,(BiVO)4和LaGaO 3中的一种或多种的陶瓷粉末。
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公开(公告)号:US6110861A
公开(公告)日:2000-08-29
申请号:US867556
申请日:1997-06-02
申请人: Michael Krumpelt , Shabbir Ahmed , Romesh Kumar , Rajiv Doshi
发明人: Michael Krumpelt , Shabbir Ahmed , Romesh Kumar , Rajiv Doshi
IPC分类号: B01J23/63 , B01J35/00 , C01B3/38 , C01B3/40 , C04B35/453 , C04B35/486 , C04B35/495 , C04B35/50 , H01M8/06 , B01J23/40 , C04B35/48 , G01N27/26 , H01M4/86
CPC分类号: H01M8/0612 , B01J35/0006 , C01B3/386 , C01B3/40 , C04B35/453 , C04B35/486 , C04B35/495 , C04B35/50 , C01B2203/0261 , C01B2203/085 , C01B2203/1047 , C01B2203/1052 , C01B2203/1064 , C01B2203/107 , C01B2203/1082 , C01B2203/1241 , C01B2203/1247 , C01B2203/1619 , Y02P20/52 , Y02P70/56
摘要: A two-part catalyst comprising a dehydrogenation portion and an oxide-ion conducting portion. The dehydrogenation portion is a group VIII metal and the oxide-ion conducting portion is selected from a ceramic oxide crystallizing in the fluorite or perovskite structure. There is also disclosed a method of forming a hydrogen rich gas from a source of hydrocarbon fuel in which the hydrocarbon fuel contacts a two-part catalyst comprising a dehydrogenation portion and an oxide-ion conducting portion at a temperature not less than about 400.degree. C. for a time sufficient to generate the hydrogen rich gas while maintaining CO content less than about 5 volume percent. There is also disclosed a method of forming partially oxidized hydrocarbons from ethanes in which ethane gas contacts a two-part catalyst comprising a dehydrogenation portion and an oxide-ion conducting portion for a time and at a temperature sufficient to form an oxide.
摘要翻译: 包含脱氢部分和氧化物离子传导部分的两部分催化剂。 脱氢部分是VIII族金属,氧化物离子传导部分选自以萤石或钙钛矿结构结晶的陶瓷氧化物。 还公开了一种从烃燃料源形成富氢气体的方法,其中烃燃料在不低于约400℃的温度下与包含脱氢部分和氧化物离子传导部分的两部分催化剂接触 足以产生富氢气体同时保持CO含量小于约5体积%的时间。 还公开了一种从乙烷形成部分氧化的烃的方法,其中乙烷气体接触包含脱氢部分和氧化物离子传导部分的两部分催化剂一段时间并在足以形成氧化物的温度下进行。
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公开(公告)号:US5942346A
公开(公告)日:1999-08-24
申请号:US110373
申请日:1998-07-06
申请人: Shabbir Ahmed , Romesh Kumar , Michael Krumpelt
发明人: Shabbir Ahmed , Romesh Kumar , Michael Krumpelt
CPC分类号: B60L11/1892 , B01J19/10 , B01J19/2415 , B01J19/26 , B01J23/80 , B01J8/065 , B60L11/1881 , B60L11/1894 , C01B3/323 , H01M8/0612 , H01M8/0631 , B01J2208/00716 , B01J2219/00063 , B01J2219/00069 , B01J2219/00132 , B01J2219/00159 , B01J2219/00186 , H01M2250/20 , Y02P20/52 , Y02T90/32 , Y02T90/34
摘要: A partial oxidation reformer comprising a longitudinally extending chamber having a methanol, water and an air inlet and an outlet. An igniter mechanism is near the inlets for igniting a mixture of methanol and air, while a partial oxidation catalyst in the chamber is spaced from the inlets and converts methanol and oxygen to carbon dioxide and hydrogen. Controlling the oxygen to methanol mole ratio provides continuous slightly exothermic partial oxidation reactions of methanol and air producing hydrogen gas. The liquid is preferably injected in droplets having diameters less than 100 micrometers. The reformer is useful in a propulsion system for a vehicle which supplies a hydrogen-containing gas to the negative electrode of a fuel cell.
摘要翻译: 一种部分氧化重整器,其包括具有甲醇,水和空气入口以及出口的纵向延伸室。 点火器机构靠近用于点燃甲醇和空气的混合物的入口,而室中的部分氧化催化剂与入口间隔开并将甲醇和氧转化为二氧化碳和氢气。 控制氧气与甲醇的摩尔比提供甲醇和产生氢气的空气的连续轻微的放热部分氧化反应。 液体优选以直径小于100微米的液滴注入。 重整器可用于向燃料电池的负极供给含氢气体的车辆的推进系统。
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公开(公告)号:US5939025A
公开(公告)日:1999-08-17
申请号:US518541
申请日:1995-08-23
申请人: Shabbir Ahmed , Romesh Kumar , Michael Krumpelt
发明人: Shabbir Ahmed , Romesh Kumar , Michael Krumpelt
IPC分类号: B01J8/06 , B01J19/10 , B01J19/24 , B01J19/26 , B01J23/80 , B60L11/18 , C01B3/32 , H01M8/06 , B01J8/04
CPC分类号: B60L11/1892 , B01J19/10 , B01J19/2415 , B01J19/26 , B01J23/80 , B01J8/065 , B60L11/1881 , B60L11/1894 , C01B3/323 , H01M8/0612 , H01M8/0631 , B01J2208/00716 , B01J2219/00063 , B01J2219/00069 , B01J2219/00132 , B01J2219/00159 , B01J2219/00186 , H01M2250/20 , Y02P20/52 , Y02T90/32 , Y02T90/34
摘要: A partial oxidation reformer comprising a longitudinally extending chamber having a methanol, water and an air inlet and an outlet. An igniter mechanism is near the inlets for igniting a mixture of methanol and air, while a partial oxidation catalyst in the chamber is spaced from the inlets and converts methanol and oxygen to carbon dioxide and hydrogen. Controlling the oxygen to methanol mole ratio provides continuous slightly exothermic partial oxidation reactions of methanol and air producing hydrogen gas. The liquid is preferably injected in droplets having diameters less than 100 micrometers. The reformer is useful in a propulsion system for a vehicle which supplies a hydrogen-containing gas to the negative electrode of a fuel cell.
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公开(公告)号:US06967063B2
公开(公告)日:2005-11-22
申请号:US09860851
申请日:2001-05-18
申请人: Michael Krumpelt , John P. Kopasz , Shabbir Ahmed , Richard Li-chih Kao , Sarabjit Singh Randhava
发明人: Michael Krumpelt , John P. Kopasz , Shabbir Ahmed , Richard Li-chih Kao , Sarabjit Singh Randhava
CPC分类号: C01B3/38 , C01B3/40 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0844 , C01B2203/1247 , C01B2203/127 , C01B2203/142 , C01B2203/82 , Y02P20/129
摘要: A method for reforming a sulfur-containing carbonaceous fuel in which the sulfur-containing carbonaceous fuel is mixed with H2O and an oxidant, forming a fuel/H2O/oxidant mixture. The fuel H2O/oxidant mixture is brought into contact with a catalyst composition comprising a dehydrogenation portion, an oxidation portion and a hydrodesulfurization portion, resulting in formation of a hydrogen-containing gas stream.
摘要翻译: 一种用于重整含硫碳质燃料的方法,其中含硫碳质燃料与H 2 O 2和氧化剂混合,形成燃料/ H 2 O / 氧化剂混合物。 使燃料H 2 O /氧化剂混合物与包含脱氢部分,氧化部分和加氢脱硫部分的催化剂组合物接触,导致含氢气流的形成。
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