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    • 4. 发明授权
    • Fuel cell stack and hydrogen supply including a positive temperature coefficient ceramic heater
    • 燃料电池堆和氢气供应包括正温度系数陶瓷加热器
    • US07955740B2
    • 2011-06-07
    • US11467574
    • 2006-08-28
    • Franz WinterStefan Nettesheim
    • Franz WinterStefan Nettesheim
    • H01M8/04
    • H01M8/0267H01M4/0407H01M8/2465
    • A fuel cell system that employs one or more PTC ceramic heaters that do not need to be self-regulated, and thus will not require various control components, such as temperature sensors. The PTC ceramic heaters include a ceramic material that is designed for a particular temperature depending on the particular application. An electrical current is applied to the ceramic heater that generates heat as long as the temperature of the ceramic heater is below the designed temperature. If the ceramic heater reaches the designed temperature, then the resistance of the ceramic material goes up, and the current through the ceramic material goes down, so that the heater does not provide significant heating. Therefore, it does not need to be regulated.
    • 一种燃料电池系统,其采用一个或多个不需要自调节的PTC陶瓷加热器,因此不需要诸如温度传感器的各种控制部件。 PTC陶瓷加热器包括根据特定应用设计用于特定温度的陶瓷材料。 只要陶瓷加热器的温度低于设计温度,就可以向陶瓷加热器施加电流,产生热量。 如果陶瓷加热器达到设计温度,则陶瓷材料的电阻上升,并且通过陶瓷材料的电流下降,使得加热器不提供显着的加热。 因此,它不需要受到管制。
    • 6. 发明授权
    • Vehicle mounted fuel cell assembly
    • 车载燃料电池组件
    • US09333845B2
    • 2016-05-10
    • US11534329
    • 2006-09-22
    • Franz WinterReiner EssingerThomas VogelMichael J. Gorman
    • Franz WinterReiner EssingerThomas VogelMichael J. Gorman
    • H01M8/02B60L11/18H01M8/24B60K1/04
    • B60K1/04H01M2250/20Y02T90/32
    • A power distribution unit for a vehicle includes a fuel cell stack, a bracket connected to the fuel cell stack and including at least one mount adapted to be connected directly to a vehicle to directly interconnect the fuel cell stack to the vehicle, a connection feature, and a traction system communicated with the fuel cell stack and carried by at least one of the fuel cell stack and the bracket with the connection feature disposed between the traction system and said at least one of the fuel cell stack and the bracket so that the traction system is indirectly connected to the vehicle. In one implementation, the connection feature includes an elastomeric pad disposed between a housing of the traction system and a mount or the vehicle frame. The pad provides a so-called “soft mount” of the traction system to the vehicle.
    • 用于车辆的配电单元包括燃料电池堆,连接到燃料电池堆的支架,并且包括适于直接连接到车辆以将燃料电池堆直接互连到车辆的至少一个安装座,连接特征, 牵引系统与所述燃料电池堆连通并由所述燃料电池堆和所述支架中的至少一个承载,所述牵引系统具有布置在所述牵引系统和所述至少一个所述燃料电池堆和所述支架之间的连接特征,使得所述牵引 系统间接连接到车辆。 在一个实施方式中,连接特征包括设置在牵引系统的壳体和安装座或车架之间的弹性垫。 该垫将该牵引系统的所谓“软安装”提供给车辆。
    • 9. 发明申请
    • Oxychlorination of olefins and aromatics by a novel concept of fluidized bed reaction
    • 通过流化床反应的新概念对烯烃和芳烃进行氧氯化
    • US20060149102A1
    • 2006-07-06
    • US10525419
    • 2003-08-08
    • Andreas VoightFranz WinterMartin Kozek
    • Andreas VoightFranz WinterMartin Kozek
    • C07C17/15C07C17/152
    • C07C17/156C07C19/045
    • A continuous process to oxychlorinate olefins and aromatics is described, comprising the conversion of olefins and aromatics as component (a) with oxygen and hydrogen chloride as component (b) in the presence of a solid cuprous/cupric salt catalyst in a reactor, characterized in that components (a) and (b) are fed separately from each other in spatial terms into reaction zones and regeneration zones of the reactor, where the reaction zone shows a higher concentration of the catalyst in its oxidized form at the solids entry point than at the solids exit point, and the regeneration zone shows a higher concentration of the catalyst in its reduced form at the solids entry point than at its solids exit point, and where component (a) is fed into the reaction zones and component (b) is fed into the regeneration zones.
    • 描述了烯烃和芳族化合物的含氯氯化物的连续方法,包括在反应器中在固体亚铜/铜盐催化剂存在下,将作为组分(a)的烯烃和芳族化合物与氧和氯化氢作为组分(b)的转化,其特征在于 组分(a)和(b)在空间上彼此分开地进料到反应区域和反应器的再生区域中,其中反应区在固体入口点显示比在氧化形式的更高浓度的催化剂在固体入口点比在 固体出口点和再生区域在固体入口处显示出比在其固体出口点处还原形式的催化剂浓度高的浓度,并且其中组分(a)进料到反应区域中,组分(b)为 进入再生区。