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    • 4. 发明申请
    • FUEL CONSUMING AGENT
    • 燃油消耗剂
    • WO2006001789A1
    • 2006-01-05
    • PCT/US2004/018360
    • 2004-06-09
    • THE GILLETTE COMPANYDAVIS, Stuart, M.
    • DAVIS, Stuart, M.
    • H01M8/04
    • H01M8/22H01M8/04089H01M8/04186H01M8/04208H01M8/1009H01M8/222H01M8/2475
    • Electrochemical cell system (36) comprising: a fuel cell (10) comprising: a fuel cell housing (12) having a first external surface and a first internal surface defining a first internal volume of the fuel cell housing, and a cathode, an anode, and an electrolyte disposed within the first internal volume, a fuel cartridge (38) connected to the fuel cell, the cartridge comprising: a cartridge housing (44) having a second external surface and a second internal surface defining a second internal volume (39) of the cartridge housing, wherein the second internal volume (39) includes a fuel; and a fuel consuming agent (28,45) disposed on at least one of the first external surface and the second external surface.
    • 电化学电池系统(36)包括:燃料电池(10),包括:燃料电池壳体(12),具有第一外表面和限定燃料电池壳体的第一内部容积的第一内表面,以及阴极,阳极 以及设置在所述第一内部容积内的电解质,连接到所述燃料电池的燃料盒(38),所述盒包括:具有第二外部表面的盒壳体(44)和限定第二内部容积(39 ),其中所述第二内部容积(39)包括燃料; 以及设置在所述第一外表面和所述第二外表面中的至少一个上的燃料消耗剂(28,45)。
    • 8. 发明申请
    • PROCESS FOR MANUFACTURE AND IMPROVED MANGANESE DIOXIDE FOR ELECTROCHEMICAL CELLS
    • 电化学电池制造和改进二氧化锰的方法
    • WO2002066707A2
    • 2002-08-29
    • PCT/US2002/004861
    • 2002-02-19
    • THE GILLETTE COMPANYDAVIS, Stuart, M.MOSES, Peter, R.MILLER, Gary
    • DAVIS, Stuart, M.MOSES, Peter, R.MILLER, Gary
    • C25B1/00
    • C01G45/02C01P2006/10C01P2006/12C01P2006/40C01P2006/80C25B1/21H01M4/50
    • A process for manufacture of manganese dioxide comprising subjecting an aqueous bath comprising manganese sulfate (MnSO 4 ) and sulfuric acid (H2S04) to electrolysis in a closed cell wherein the electrolysis bath is maintained at an elevated temperature above 110°C, preferably above 115°C and at superatmospheric pressure. Desirably the bath can be maintained at an elevated temperature between about 115°C and 155°C. The electrolysis is carried out preferably at elevated current density of between about 12.5 and 37 Amp/sq.ft (135 and 400 Amp/sq.meter) of the anode surface which allows for smaller or fewer electrolysis units. An MnO 2 product having a specific surface area (SSA) within desired range of between 18-45 m 2 /g can be obtained. A doping agent, preferably a soluble titanium dopant can also be employed to help obtain the desired specific surface area (SSA) of the MnO¿2¿ product. The manganese dioxide product when used as cathode active material in zinc/MnO 2 alkaline cells results in excellent service life, particularly when the cell is used in high power application.
    • 一种制造二氧化锰的方法,包括使包含硫酸锰(MnSO 4)和硫酸(H 2 SO 4)的水浴在封闭的电池中进行电解,其中电解浴保持在高于110℃,优选高于115℃的高温 并在超大气压下。 理想地,浴可以保持在约115℃和155℃之间的升高的温度。电解优选在升高的电流密度下进行,电流密度在约12.5和37安培/平方英尺之间(135和400安培/平方米) ),其允许更小或更少的电解单元。 可以获得具有在18-45m 2 / g之间的期望范围内的比表面积(SSA)的MnO 2产物。 还可以使用掺杂剂,优选可溶性钛掺杂剂来帮助获得所需的MnO 2产物的比表面积(SSA)。 当用作锌/锰氧化物碱性电池中的阴极活性材料时,二氧化锰产品具有优异的使用寿命,特别是当电池用于大功率应用时。