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1.发明申请Fuel reformer for hydrogen production, especially for operation of a fuel cell 审中-公开用于氢气生产的燃料重整器，特别是用于燃料电池的操作公开(公告)号：US20050097820A1
公开(公告)日：2005-05-12
申请号：US10939247
申请日：2004-09-10
申请人： Ian Faye , Rainer Saliger , Thanh-Binh Truong , Esmond Newson
发明人： Ian Faye , Rainer Saliger , Thanh-Binh Truong , Esmond Newson
CPC分类号： B01J8/0278 , B01J8/0214 , C01B3/382 , C01B3/386 , C01B2203/0244 , C01B2203/066 , C01B2203/0844 , C01B2203/12 , C01B2203/1247 , C01B2203/142 , C01B2203/82 , H01M8/0612 , H01M8/0618 , H01M8/0631 , Y02P20/52
摘要： The fuel reformer, especially for a fuel cell, produces a hydrogen-containing reformate from a fuel or hydrocarbon mixture supplied to it by partial oxidation (POX) and/or an autothermal reforming process. The reformer provides improved local reaction temperatures with increased conversion of hydrocarbons to hydrogen, decreased residual carbon monoxide formation and at the same time an increased yield of hydrogen. A gas supply member for distribution of reactants, such as air and/or oxygen, is arranged within the flow path of the fuel or hydrocarbon mixture in the reformer. The gas supply member has a plurality of gas supply outlets distributed in a flow direction along the fuel flow path for supplying the reactants to a catalyst material, which are distributed and formed so that reaction regions are more uniformly distributed along the flow path.
摘要翻译： 特别是用于燃料电池的燃料重整器由通过部分氧化（POX）和/或自热重整方法提供给它的燃料或烃混合物产生含氢重整产物。 重整器提供改进的局部反应温度，随着碳氢化合物向氢气的转化率的增加，残留的一氧化碳形成减少，同时提高了氢的产率。 用于分配反应物（例如空气和/或氧气）的气体供应构件设置在重整器中的燃料或烃混合物的流动路径内。 气体供给构件具有沿着沿着燃料流动路径的流动方向分布的多个气体供给口，用于将反应物供给到催化剂材料，催化剂材料分布形成，使得反应区域沿着流路更均匀地分布。
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公开(公告)号：US20090126274A1
公开(公告)日：2009-05-21
申请号：US11992812
申请日：2006-06-19
IPC分类号： C12P5/00
CPC分类号： B09B3/00 , C02F11/04 , C02F11/08 , C05F3/00 , C05G1/00 , C10J3/00 , C10J3/78 , C10J2200/06 , C10J2300/0916 , C10J2300/0959 , C10J2300/0979 , C10L3/08 , C10L5/44 , Y02A40/205 , Y02E50/10 , Y02E50/30 , Y02E50/343 , Y02P20/145 , Y02P20/52 , Y02P20/544 , Y02W30/47
摘要： To generate methane from biomass, a biomass pulp is produced from the biomass with a desired dry mass content being set, and the biomass pulp is placed under pressure. The biomass pulp is heated under pressure in order to liquefy the solid organic components of the biomass pulp. The pressurized and heated biomass pulp is heated further to at least the critical temperature of the biomass pulp. Solids precipitated under pressure and increased temperature are separated from the fluid phase. At least a part of the remaining fluid phase is gasified under pressure and increased temperature by means of a reactor to form a methane-rich gas.
摘要翻译： 为了从生物质产生甲烷，从生物质产生生物质纸浆，其中所需的干质量含量被设定，生物质纸浆被置于压力下。 在压力下加热生物质纸浆以使生物质纸浆的固体有机成分液化。 将加压和加热的生物质纸浆进一步加热至至少生物质纸浆的临界温度。 在压力下沉淀的固体和升高的温度与流体相分离。 剩余流体相的至少一部分通过反应器在压力和升高的温度下气化以形成富含甲烷的气体。
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公开(公告)号：US08475549B2
公开(公告)日：2013-07-02
申请号：US11992812
申请日：2006-06-19
IPC分类号： C10L3/08
CPC分类号： B09B3/00 , C02F11/04 , C02F11/08 , C05F3/00 , C05G1/00 , C10J3/00 , C10J3/78 , C10J2200/06 , C10J2300/0916 , C10J2300/0959 , C10J2300/0979 , C10L3/08 , C10L5/44 , Y02A40/205 , Y02E50/10 , Y02E50/30 , Y02E50/343 , Y02P20/145 , Y02P20/52 , Y02P20/544 , Y02W30/47
摘要： To generate methane from biomass, a biomass pulp is produced from the biomass with a desired dry mass content being set, and the biomass pulp is placed under pressure. The biomass pulp is heated under pressure in order to liquefy the solid organic components of the biomass pulp. The pressurized and heated biomass pulp is heated further to at least the critical temperature of the biomass pulp. Solids precipitated under pressure and increased temperature are separated from the fluid phase. At least a part of the remaining fluid phase is gasified under pressure and increased temperature by means of a reactor to form a methane-rich gas.
摘要翻译： 为了从生物质产生甲烷，从生物质产生生物质纸浆，其中所需的干质量含量被设定，生物质纸浆被置于压力下。 在压力下加热生物质纸浆以使生物质纸浆的固体有机成分液化。 将加压和加热的生物质纸浆进一步加热至至少生物质纸浆的临界温度。 在压力下沉淀的固体和升高的温度与流体相分离。 剩余流体相的至少一部分通过反应器在压力和升高的温度下气化以形成富含甲烷的气体。
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