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51. 发明申请

US20090199475A1 Reformer and Method of Startup 审中-公开
标题翻译：改革者和启动方法
公开(公告)号：US20090199475A1
公开(公告)日：2009-08-13
申请号：US12369210
申请日：2009-02-11
申请人： Peter David DeVries , Todd Healey
发明人： Peter David DeVries , Todd Healey
IPC分类号： C10J1/20 , C10L3/00
CPC分类号： C01B3/386 , C01B3/48 , C01B2203/0261 , C01B2203/0283 , C01B2203/0405 , C01B2203/043 , C01B2203/044 , C01B2203/0445 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/085 , C01B2203/0866 , C01B2203/107 , C01B2203/1223 , C01B2203/1288 , C01B2203/146 , Y02P20/128
摘要： A linear reformer for liberating hydrogen from a hydrogen containing feedstock, operable on both gaseous and liquid fuels, has a linear burner distributor with at least two fuel distribution apertures for distribution of fuel, a supply of air, where the fuel and air mix in a linear mixing cavity to form a catalytically combustible mixture, a catalytic burner element, an electric heater in heat transferring relation to at least one of the burner distributor and the catalytic burner element, a catalyst bed, a boiler for boiling and heating the feedstock, and an exhaust heat exchanger effective for pre-heating the supply of air to the burner. The burner distributor, catalyst bed, feedstock boiler, and exhaust heat exchanger are all linear elements with a common parallel axis, such that heat exchange gases from the burner travel transversely to the common parallel axis, and where the burner distributor receives heat from the electric heater such that incoming fuel may be at least partially vaporized, and the electric heater heats the catalytic burner element to sufficient temperature such that the vaporized fuel and air mixture initiates catalytic combustion.
摘要翻译：用于从含氢原料释放氢的线性重整器可在气体和液体燃料两者上运行，具有线性燃烧器分配器，其具有至少两个燃料分配孔，用于分配燃料，空气供应，其中燃料和空气在线性混合腔以形成催化燃烧混合物，催化燃烧器元件，与燃烧器分配器和催化燃烧器元件中的至少一个传热关系的电加热器，催化剂床，用于沸腾和加热原料的锅炉，以及排气热交换器，其有效地预加热到燃烧器的空气供应。燃烧器分配器，催化剂床，原料锅炉和排气热交换器都是具有共同平行轴线的线性元件，使得来自燃烧器的热交换气体横向于公共平行轴线行进，并且燃烧器分配器从电气接收热量加热器，使得进入的燃料可以至少部分蒸发，并且电加热器将催化燃烧器元件加热到足够的温度，使得汽化的燃料和空气混合物开始催化燃烧。

52. 发明申请

US20080307707A1 PARTIAL OXIDATION REACTOR 有权
标题翻译：部分氧化反应器
公开(公告)号：US20080307707A1
公开(公告)日：2008-12-18
申请号：US12125411
申请日：2008-05-22
申请人： Luc NOUGIER , Stephane Bertholin , Willy Nastoll
发明人： Luc NOUGIER , Stephane Bertholin , Willy Nastoll
IPC分类号： C10J1/20
CPC分类号： B01J8/0221 , B01J8/0285 , B01J19/006 , B01J19/244 , B01J2208/00495 , B01J2208/0053 , B01J2208/00557 , B01J2219/00085 , B01J2219/00094 , B01J2219/00155 , B01J2219/00768 , B01J2219/182 , B01J2219/185 , B01J2219/187 , C01B3/36 , C01B2203/0255 , C01B2203/0883 , C01B2203/1241 , C01B2203/1247 , C01B2203/1282 , Y02P20/129
摘要： A reactor intended to carry out partial oxidation reactions starting from liquid feedstocks that can go from GPL to gas oil for the purpose of producing synthesis gas is characterized by finely controlled hydrodynamics and a high degree of thermal integration, and comprises an elongated jacket along an axis of any orientation, means (12) for supplying a preheated gas that contains oxygen and optionally water vapor, means (9) for supplying a hydrocarbon feedstock, means (11) for evacuation of a hydrogen-rich effluent, a first internal chamber (5) inside of which is carried out an essentially isothermal partial oxidation reaction that is connected to means (9) for supplying the hydrocarbon feedstock and to means (12) for supplying preheated gas, gas turbulizing means that are suitable for creating a perfect mixing flow, means (8) for linking first chamber (5) to a second chamber (7) with a suitable volume for carrying out a piston flow, linking means (8) that comprise at least one orifice, and second chamber (7) exchanging heat in an indirect manner over at least a portion of its length with means (12) for supplying said thus preheated gas, whereby the second chamber is connected to said means (11) for evacuating the hydrogen-rich effluent, and in which gas supply means (12) comprise an annular chamber that is essentially coaxial with the reactor jacket, and second chamber (7) is essentially coaxial with said jacket.
摘要翻译：旨在进行部分氧化反应的反应器，其特征在于精细控制的流体动力学和高度的热积分，其特征在于可以从GPL到瓦斯油从液态原料开始的部分氧化反应，并且包括沿轴线的细长夹套任何方向的装置（12），用于提供含氧气和任选的水蒸气的预热气体，用于供应烃原料的装置（9），用于抽空富氢流出物的装置（11），第一内室（5 ），其中进行基本上等温的部分氧化反应，其连接到用于供应烃原料的装置（9）和用于供应预热气体的装置（12），适于产生完美混合流的气体湍流装置，用于将第一室（5）与第二室（7）连接的装置（8），其具有用于进行活塞流的合适体积，连接装置（8），其包括至少一个 e和第二室（7）以间接方式在其长度的至少一部分上与用于供应所述如此预热的气体的装置（12）进行热交换，由此第二室连接到所述装置（11）以抽空氢其中气体供应装置（12）包括基本上与反应器夹套同轴的环形室，而第二室（7）基本上与所述夹套同轴。

53. 发明申请

US20080127554A1 APPARATUS AND METHOD FOR PRODUCING HYDROGEN 失效
标题翻译：用于生产氢的装置和方法
公开(公告)号：US20080127554A1
公开(公告)日：2008-06-05
申请号：US12027587
申请日：2008-02-07
申请人： Dean A. Kenefake , W. Spencer Wheat , Hongqiao Sun , Bhaskar Balasubramanian , Vesna R. Mirkovic , Daniel G. Casey
发明人： Dean A. Kenefake , W. Spencer Wheat , Hongqiao Sun , Bhaskar Balasubramanian , Vesna R. Mirkovic , Daniel G. Casey
IPC分类号： C10J1/20
CPC分类号： C01B3/38 , C01B3/501 , C01B3/56 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0405 , C01B2203/043 , C01B2203/044 , C01B2203/0455 , C01B2203/047 , C01B2203/0485 , C01B2203/066 , C01B2203/1241 , C01B2203/16 , C01B2203/1604 , C01B2203/1628
摘要： An apparatus and method for producing a hydrogen-enriched reformate. The apparatus includes a fuel processor for converting a fuel to a reformate having fluctuations in pressure and or flow rate, means for reducing the fluctuations, a compression unit for compressing the reformate and one or more of a purification unit and a storage unit downstream of a compression unit. Means for reducing the fluctuations in the reformate can include one or more of a buffer and a conduit for providing a controlled flow of a supplemental fluid to an inlet of the compression unit. The supplemental fluid can include the compressed reformate, a hydrogen-enriched reformate, and mixtures thereof. The apparatus can include means for regulating power to the compression unit that can incrementally increase power to the compression unit particularly during start up. The purification unit can include one or more of a hydrogen selective membrane and a pressure swing adsorption unit. Methods for producing hydrogen are also disclosed.
摘要翻译：一种生产富氢重整产品的装置和方法。该装置包括用于将燃料转化为具有压力和/或流速波动的重整产品的燃料处理器，用于减少波动的装置，用于压缩重整产品的压缩单元和净化单元和存储单元下游的一个或多个压缩单元。用于减少重整产品波动的方法可以包括一个或多个缓冲器和用于向压缩单元的入口提供受控流动的补充流体的导管。补充流体可以包括压缩的重整油，富氢重整油及其混合物。该装置可以包括用于调节压缩单元的功率的装置，其可以增量地增加对压缩单元的功率，特别是在启动期间。净化单元可以包括氢选择性膜和变压吸附单元中的一种或多种。还公开了生产氢的方法。

54. 发明授权

US07045231B2 Direct hydrocarbon reforming in protonic ceramic fuel cells by electrolyte steam permeation 有权
标题翻译：通过电解质蒸汽渗透在质子陶瓷燃料电池中直接烃转化
公开(公告)号：US07045231B2
公开(公告)日：2006-05-16
申请号：US10353215
申请日：2003-01-27
申请人： W. Grover Coors
发明人： W. Grover Coors
IPC分类号： H01M8/04 , C01B3/24 , C10J1/20
CPC分类号： H01M8/1246 , C01B3/38 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/067 , C01B2203/12 , C01B2203/1241 , C01B2203/148 , H01M8/0618 , H01M8/0637 , H01M8/126 , Y02E60/525 , Y02E60/566 , Y02P70/56
摘要： A process for converting hydrocarbons and water vapor into hydrogen, carbon monoxide, and carbon dioxide; a fuel cell device; and a process of utilizing the fuel cell to convert chemical energy to electrical energy is described. The fuel cell comprises a metallic and/or mixed conducting anode, a metallic and/or mixed conducting cathode, a proton-conducting ceramic electrolyte between the anode and the cathode, and an external load connecting the anode and the cathode. The fuel cell also includes systems for bringing gaseous hydrocarbon fuels into contact with the anode and for bringing oxygen and water vapor into contact with the cathode. Water vapor in the fuel cell passes through the ceramic electrolyte membrane from the cathode side to the anode side by ambipolar diffusion, called “steam permeation” without conducting current, under the influence of a water vapor concentration gradient.
摘要翻译：将烃和水蒸气转化为氢气，一氧化碳和二氧化碳的方法; 燃料电池装置; 并描述了利用燃料电池将化学能转化为电能的过程。燃料电池包括金属和/或混合的导电阳极，金属和/或混合的导电阴极，在阳极和阴极之间的质子传导陶瓷电解质，以及连接阳极和阴极的外部负载。燃料电池还包括用于使气态烃燃料与阳极接触并使氧气和水蒸汽与阴极接触的系统。在水蒸汽浓度梯度的影响下，燃料电池中的水蒸气通过双极扩散（称为“蒸汽渗透”）通过陶瓷电解质膜从阴极侧到阳极侧。

55. 发明授权

US5912198A Staged catalytic ammonia decomposition in integrated gasification combined cycle systems 失效
标题翻译：综合气化联合循环系统分阶段催化氨分解
公开(公告)号：US5912198A
公开(公告)日：1999-06-15
申请号：US691084
申请日：1996-08-01
申请人： Alan S. Feitelberg , Raul Eduardo Ayala , Stephen Lan-Sun Hung , David Joseph Najewicz
发明人： Alan S. Feitelberg , Raul Eduardo Ayala , Stephen Lan-Sun Hung , David Joseph Najewicz
IPC分类号： B01D53/58 , B01D53/86 , C01B3/58 , C10J3/00 , C10J1/20
CPC分类号： C01B3/583 , B01D53/58 , B01D53/8634 , C10J3/00 , C10K1/004 , C10K1/101 , C10K1/16 , C10K3/02 , C10K3/04 , C01B2203/044 , C01B2203/047 , C10J2300/165 , C10J2300/1662 , C10J2300/1687 , C10J2300/1861 , Y02E20/16 , Y02E20/18
摘要： The ammonia content of fuel gas in an IGCC power generation system is reduced through ammonia decomposition, thereby reducing the NO.sub.x emissions from the plant. The power generation system includes a gasifier, a gas turbine and at least one catalytic reactor arranged between the gasifier and the gas turbine. The catalytic reactor may be either a three stage or two stage device. The three stage reactor includes a first catalyst which promotes water-gas-shift, a second catalyst which promotes CO methanation, and a third catalyst which promotes ammonia decomposition. The two stage reactor includes a first catalyst which promotes water-gas-shift and CO methanation and a second catalyst which promotes ammonia decomposition. The plural catalytic stages may be disposed in a single vessel or successively disposed in individual vessels, and the catalysts may be in a pelletized form or coated on honeycomb structures. Alternatively, fluidized bed reactors may be used. The reactions are carried out either adiabatically or non-adiabatically. Heat from the water-gas-shift and CO methanation reactions may be used to generate steam, which can be injected downstream or sent to a steam turbine. Preferably, a second catalytic reactor is provided in parallel with the first reactor so that the two reactors can alternately receive fuel gas from the gasifier.
摘要翻译： IGCC发电系统中燃气的氨含量通过氨分解而降低，从而减少了工厂的NOx排放。发电系统包括气化器，燃气轮机和布置在气化器和燃气轮机之间的至少一个催化反应器。催化反应器可以是三级或二级装置。三级反应器包括促进水煤气转移的第一催化剂，促进CO甲烷化的第二催化剂和促进氨分解的第三催化剂。两级反应器包括促进水煤气变换和CO甲烷化的第一催化剂和促进氨分解的第二催化剂。多个催化级可以设置在单个容器中或相继设置在各个容器中，并且催化剂可以是颗粒形式或涂覆在蜂窝结构上。或者，可以使用流化床反应器。反应是绝热的或非绝热的。来自水煤气变换和CO甲烷化反应的热量可用于产生蒸汽，其可以向下游喷射或送到蒸汽轮机。优选地，与第一反应器平行地设置第二催化反应器，使得两个反应器可以交替地从气化器接收燃料气体。

56. 发明授权

US4369107A Separation of super-acid in a coal liquification process 失效
标题翻译：在煤液化过程中分离超酸
公开(公告)号：US4369107A
公开(公告)日：1983-01-18
申请号：US275497
申请日：1981-06-19
申请人： Steven C. Amendola
发明人： Steven C. Amendola
IPC分类号： C10G1/00 , C10G1/06 , C10G47/02 , C10J1/20 , C10J3/00
CPC分类号： C10G1/00
摘要： This invention relates to an improved process for rapidly converting essentially solid carbonaceous material to essentially liquid and gaseous hydrocarbon products wherein a rapid and economical method of separating the components of the super-acid system from the liquified hydrogenated products is used.
摘要翻译：本发明涉及用于将基本上固体碳质材料快速转化成基本上液体和气态烃产物的改进方法，其中使用从液化氢化产物中分离超酸体系的组分的快速且经济的方法。

57. 发明授权

US3924648A Method and means for applying additives to industrial gas 失效
标题翻译：将添加剂加入工业气体的方法和手段
公开(公告)号：US3924648A
公开(公告)日：1975-12-09
申请号：US55894575
申请日：1975-03-17
申请人： ETTER BERWYN E
发明人： ETTER BERWYN E
IPC分类号： B23K7/08 , C10J1/20
CPC分类号： B23K7/08 , Y10T137/0329 , Y10T137/7404
摘要： A device for applying additives to industrial gas comprises a container, and first, second and third conduits providing communication from outside the container to the interior thereof. One of the conduits introduces a fluid gas additive to the interior of the container and another of the conduits introduces fuel gas into the interior of the chamber. The gas is introduced into the container at a point below the level of the fluid gas additive so that the gas percolates upwardly through the additive, thereby causing mixing of the additive with the gas. The third conduit includes an inlet positioned at the upper end of the chamber above the level of the gas additive. This third conduit receives the vapor mixture of fuel gas and fuel additive and carries this vapor mixture to the cutting torch. A valve is associated with the first conduit so as to limit the level of liquid within the container at a predetermined height. A safety valve is also associated with the third conduit to close the third conduit in the event the liquid level rises higher than the opening of the third conduit.

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