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    • 14. 发明授权
    • Hydrocarbon reforming catalyst material and configuration of the same
    • 烃重整催化剂材料及其构造
    • US5527631A
    • 1996-06-18
    • US539814
    • 1995-10-04
    • Prabhakar SinghLarry A. ShocklingRaymond A. GeorgeRichard A. Basel
    • Prabhakar SinghLarry A. ShocklingRaymond A. GeorgeRichard A. Basel
    • F02M27/02B01J23/78B01J23/89B01J35/02B01J35/04C01B3/40H01M8/06H01M8/18H01M8/10
    • C01B3/40B01J35/02B01J35/04H01M8/0625C01B2203/1041C01B2203/1052C01B2203/107C01B2203/1082Y02P20/52
    • A hydrocarbon reforming catalyst material comprising a catalyst support impregnated with catalyst is provided for reforming hydrocarbon fuel gases in an electrochemical generator. Elongated electrochemical cells convert the fuel to electrical power in the presence of an oxidant, after which the spent fuel is recirculated and combined with a fresh hydrocarbon feed fuel forming the reformable gas mixture which is fed to a reforming chamber containing a reforming catalyst material, where the reforming catalyst material includes discrete passageways integrally formed along the length of the catalyst support in the direction of reformable gas flow. The spent fuel and/or combusted exhaust gases discharged from the generator chamber transfer heat to the catalyst support, which in turn transfers heat to the reformable gas and to the catalyst, preferably via a number of discrete passageways disposed adjacent one another in the reforming catalyst support. The passageways can be slots extending inwardly from an outer surface of the support body, which slots are partly defined by an exterior confining wall. According to a preferred embodiment, the catalyst support is non-rigid, porous, fibrous alumina, wherein the fibers are substantially unsintered and compressible, and the reforming catalyst support is impregnated, at least in the discrete passageways with Ni and MgO, and has a number of internal slot passageways for reformable gas, the slot passageways being partly closed by a containing outer wall.
    • 提供了一种包含浸渍有催化剂的催化剂载体的烃重整催化剂材料,用于在电化学发生器中重整碳氢化合物燃料气体。 细长的电化学电池在氧化剂存在下将燃料转化为电力,之后废燃料再循环并与形成可重整气体混合物的新鲜烃进料燃料组合,该可重整气体混合物被供给到含有重整催化剂材料的重整室,其中 重整催化剂材料包括沿可催化气体流动方向沿催化剂载体的长度一体形成的离散通道。 从发生器室排放的乏燃料和/或燃烧的废气将热量转移到催化剂载体,催化剂载体又将热量转移到可重整气体和催化剂,优选通过在重整催化剂中彼此相邻设置的多个离散通道 支持。 通道可以是从支撑体的外表面向内延伸的槽,该狭缝部分地由外部限制壁限定。 根据优选的实施方案,催化剂载体是非刚性多孔的纤维状氧化铝,其中纤维基本上是未烧结和可压缩的,并且重整催化剂载体至少在具有Ni和MgO的离散通道中浸渍,并且具有 用于可重整气体的内槽通道的数量,槽通道由容纳的外壁部分地封闭。
    • 17. 发明授权
    • Method of manufacturing thin metal alloy foils
    • 薄金属合金箔的制造方法
    • US06315820B1
    • 2001-11-13
    • US09420620
    • 1999-10-19
    • George Steve SalokaMujeeb Ismael IjazPrabhakar Singh
    • George Steve SalokaMujeeb Ismael IjazPrabhakar Singh
    • B01D5322
    • C01B3/505B32B15/01C22C1/00C23C14/0005Y10S55/05Y10T428/12438Y10T428/12875Y10T428/12903
    • A method of manufacturing thin foil alloys through a series of steps. A carrier having a polished carrier surface is placed within a deposition chamber. The carrier surface is generally polished to a mirrored surface finish. A sacrificial layer is applied atop the carrier surface. The sacrificial layer is made of a material that may be easily dissolved or separated from the carrier surface to remove the metal foil. The carrier surface and sacrificial layer are placed within the deposition chamber. The sacrificial layer is exposed to an evaporated first metal which becomes deposited upon the sacrificial layer. An evaporated second metal is then applied concurrently or sequentially with the first metal. The first and second evaporated metals solidify on the sacrificial layer to form a multilayer foil. At this point, the multilayer foil includes discrete layers or areas of the evaporated metals.
    • 通过一系列步骤制造薄箔合金的方法。 具有抛光载体表面的载体被放置在沉积室内。 载体表面通常被抛光成镜面表面光洁度。 在载体表面上施加牺牲层。 牺牲层由可容易地从载体表面溶解或分离以除去金属箔的材料制成。 载体表面和牺牲层被放置在沉积室内。 牺牲层暴露于沉积在牺牲层上的蒸发的第一金属。 然后与第一金属同时或顺序地施加蒸发的第二金属。 第一和第二蒸发金属在牺牲层上固化以形成多层箔。 在这一点上,多层箔包括离散的层或蒸发的金属的区域。
    • 18. 发明授权
    • Protective interlayer for high temperature solid electrolyte
electrochemical cells
    • 高温固体电解质电化学电池保护层
    • US5516597A
    • 1996-05-14
    • US334990
    • 1994-11-07
    • Prabhakar SinghTheodore R. VasilowVon L. Richards
    • Prabhakar SinghTheodore R. VasilowVon L. Richards
    • H01M8/02H01M8/12
    • H01M8/0215H01M2008/1293H01M2300/0074H01M8/0217Y02P70/56
    • The invention comprises of an electrically conducting doped or admixed cerium oxide composition with niobium oxide and/or tantalum oxide for electrochemical devices, characterized by the general formula:Nb.sub.x Ta.sub.y Ce.sub.1-x-y O.sub.2where x is about 0.0 to 0.05, y is about 0.0 to 0.05, and x+y is about 0.02 to 0.05, and where x is preferably about 0.02 to 0.05 and y is 0, and a method of making the same. This novel composition is particularly applicable in forming a protective interlayer of a high temperature, solid electrolyte electrochemical cell (10), characterized by a first electrode (12); an electrically conductive interlayer (14) of niobium and/or tantalum doped cerium oxide deposited over at least a first portion (R) of the first electrode; an interconnect (16) deposited over the interlayer; a solid electrolyte (18) deposited over a second portion of the first electrode, the first portion being discontinuous from the second portion; and, a second electrode (20) deposited over the solid electrolyte. The interlayer (14) is characterized as being porous and selected from the group consisting of niobium doped cerium oxide, tantalum doped cerium oxide, and niobium and tantalum doped cerium oxide or admixtures of the same. The first electrode (12), an air electrode, is a porous layer of doped lanthanum manganite, the solid electrolyte layer (18) is a dense yttria stabilized zirconium oxide, the interconnect layer (16) is a dense, doped lanthanum chromite, and the second electrode (20), a fuel electrode, is a porous layer of nickel-zirconium oxide cermet. The electrochemical cell (10) can take on a plurality of shapes such as annular, planar, etc. and can be connected to a plurality of electrochemical cells in series and/or in parallel to generate electrical energy.
    • 本发明包括具有氧化铌和/或氧化钽用于电化学装置的导电掺杂或混合的氧化铈组合物,其特征在于以下通式:Nb x T a C e 1-x-y O 2,其中x为约0.0至0.05,y为约0.0至0.05 ,x + y为约0.02〜0.05,其中x优选为约0.02〜0.05,y为0,其制造方法。 该新型组合物特别适用于形成高温固体电解质电化学电池(10)的保护性中间层,其特征在于第一电极(12)。 在第一电极的至少第一部分(R)上沉积的铌和/或钽掺杂的氧化铈的导电中间层(14); 沉积在中间层上的互连(16); 沉积在所述第一电极的第二部分上的固体电解质(18),所述第一部分与所述第二部分不连续; 和沉积在固体电解质上的第二电极(20)。 中间层(14)的特征在于是多孔的,并且选自铌掺杂的氧化铈,掺杂钽的氧化铈,以及铌和钽掺杂的氧化铈或其掺杂物。 第一电极(12)是空气电极,是掺杂的亚锰酸镧的多孔层,固体电解质层(18)是致密的氧化钇稳定的氧化锆,互连层(16)是致密掺杂的亚铬酸镧, 第二电极(20)是燃料电极,是镍 - 锆氧化物金属陶瓷的多孔层。 电化学电池(10)可以承受多个形状,例如环形,平面等,并且可以串联和/或并联连接到多个电化学电池以产生电能。