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    • 1. 发明授权
    • Remaining capacity meter and detection method for electric vehicle
battery
    • 电动汽车电池剩余容量计及检测方法
    • US5561362A
    • 1996-10-01
    • US334018
    • 1994-11-02
    • Nobuyuki KawamuraNaotake KumagaiTomiji OwadaHisamitsu KogaMasaaki KatoNobuya Furukawa
    • Nobuyuki KawamuraNaotake KumagaiTomiji OwadaHisamitsu KogaMasaaki KatoNobuya Furukawa
    • B60L3/00G01R31/00G01R31/36H02J7/00H02J7/04H02J7/16
    • G01R31/3624G01R31/3648G01R31/006G01R31/3675Y10S320/21
    • A remaining capacity meter is provided for an electric vehicle battery. This meter is suited for use in the detection of a remaining capacity of the electric vehicle battery. The meter includes a full charge detection device for detecting whether the battery has been brought into a fully-charged state, a remaining capacity setting device for setting, as a full-charge-time capacity, the remaining capacity of the battery at the time of detection of the fully-charged state by the full charge detection device, a discharge/charge-based correction device for correcting the remaining capacity, which has been set by the remaining capacity setting device, while integrating, with respect to time, a current discharged from or charged into the battery, and a deterioration-based correction device for correcting the fully-charged capacity, which has been set by the remaining capacity setting device, by a deterioration-based correction quantity corresponding to the number of chargings and battery temperatures at the time of the respective chargings. A method for the detection of the remaining capacity of such an electric vehicle battery is also described.
    • 为电动汽车电池提供剩余容量计。 该仪表适用于检测电动汽车电池的剩余容量。 仪表包括用于检测电池是否已经处于完全充电状态的完全充电检测装置,剩余电量设定装置,用于将充电时间容量设定为电池的剩余容量 通过完全充电检测装置检测完全充电状态,用于校正由剩余容量设定装置设定的剩余容量的放电/电荷校正装置,同时相对于时间积分放电电流 以及用于校正由剩余容量设定装置设定的完全充电容量的劣化型校正装置,通过与充电次数和电池温度对应的基于劣化的校正量, 各自充电的时间。 还描述了用于检测这种电动车辆电池的剩余容量的方法。
    • 5. 发明授权
    • Braking control system for electric automobile
    • 电动汽车制动控制系统
    • US5775784A
    • 1998-07-07
    • US682748
    • 1996-09-19
    • Hisamitsu KogaNaotake KumagaiTomiji OwadaNobuya FurukawaMasaaki KatoNobuyuki Kawamura
    • Hisamitsu KogaNaotake KumagaiTomiji OwadaNobuya FurukawaMasaaki KatoNobuyuki Kawamura
    • B60L3/00B60L7/10B60L7/24
    • B60L7/26B60L3/0023B60L3/0076B60L3/0092B60L2240/36Y02T10/7258
    • This invention relates to a braking control system for an electric automobile that runs by driving wheels with an electric motor. The braking control system controls braking of a vehicle through regenerative braking by the motor. Upon application of brakes, the braking control system can make combined use of mechanical braking by a mechanical brake system (11) and regenerative braking by a drive motor (2). The braking control system is designed to control regenerative braking of the motor (2) by a regenerative braking control device (12) so that greater braking force is produced when a failure in the mechanical brake system (11) is detected by a failure detection device (22) than when the mechanical brake system (11) is detected to be normal. This has made it possible to stop the vehicle surely by appropriately using regenerative braking in the event of a failure in the mechanical brake system while also making it possible to avoid or reduce an energy loss, which is caused by regenerative braking, when the mechanical brake system is normal.
    • PCT No.PCT / JP95 / 02423 Sec。 371日期1996年9月19日 102(e)日期1996年9月19日PCT提交1995年11月28日PCT公布。 公开号WO96 / 16831 日期1996年6月6日本发明涉及一种用电动机驱动车轮运行的电动汽车的制动控制系统。 制动控制系统通过电动机的再生制动来控制车辆的制动。 在制动时,制动控制系统可以通过机械制动系统(11)和驱动马达(2)的再生制动组合使用机械制动。 制动控制系统被设计成通过再生制动控制装置(12)来控制电动机(2)的再生制动,使得当故障检测装置检测到机械制动系统(11)的故障时,产生更大的制动力 (22)比检测到机械式制动系统(11)正常时。 这使得可以通过在机械制动系统发生故障的情况下适当地使用再生制动来可靠地停止车辆,同时还可以避免或减少由再生制动引起的能量损失,当机械制动 系统正常
    • 9. 发明申请
    • OPERATION METHOD OF OZONIZER AND OZONIZER APPARATUS USED THEREFOR
    • 其使用的臭氧和臭氧设备的操作方法
    • US20100084259A1
    • 2010-04-08
    • US12573156
    • 2009-10-05
    • Masaaki KatoRie Kawaguchi
    • Masaaki KatoRie Kawaguchi
    • C01B13/11C25B9/10
    • C25B1/13C01B13/115C01B2201/12C01B2201/22C01B2201/24C01B2201/32C01B2201/34C01B2201/62C25B9/10C25B15/02H01M4/8605Y02E60/366
    • The present invention offers an operation method of an ozonizer and an ozonizer apparatus to improve ozone gas purity and to achieve long and safety electrolysis operation in such manner that, during normal operation of the ozonizer, ozone gas is generated at the anode in the anode compartment and hydrogen gas is generated at the cathode in the cathode compartment; and only when the ozonizer is stopped and operation is switched to protective current operation during which minute electric current is supplied to protect said anode, oxygen-containing gas is supplied to said cathode compartment after electrolyte and hydrogen gas in said cathode compartment are all drained out, so that said cathode is made function as a gas electrode for oxygen reduction reaction, using said cathode as a reversible electrode with two functions as a gas generation electrode and a gas electrode, thereby during normal operation, ozone is generated efficiently, and during the protective current operation, when safety is a key issue, hydrogen gas is not generated at the cathode and mingling of hydrogen gas into ozone gas generated at the anode is prevented.
    • 本发明提供一种臭氧发生器和臭氧发生装置的操作方法,以改善臭氧气体的纯度并实现长时间和安全的电解操作,使得在臭氧发生器的正常操作期间,在阳极室的阳极处产生臭氧气体 在阴极室的阴极产生氢气; 并且只有当臭氧发生器停止并且操作切换到保护电流操作时,在该保护电流操作期间供应微小的电流以保护所述阳极,则在所述阴极室中的电解液和氢气全部被排出之后,含氧气体被供应到所述阴极室 使得所述阴极被用作用于氧还原反应的气体电极,使用所述阴极作为具有两个功能的可逆电极作为气体发生电极和气体电极,从而在正常操作期间有效地产生臭氧,并且在 保护电流操作,当安全是关键问题时,在阴极处不产生氢气,并且防止氢气混入阳极产生的臭氧气体中。
    • 10. 发明申请
    • Sulfuric acid electrolysis process
    • 硫酸电解过程
    • US20090321272A1
    • 2009-12-31
    • US12459161
    • 2009-06-26
    • Masaaki KatoYusuke OgawaHiroki DomonNaoya HayamizuMakiko TangeYoshiaki KurokawaNobuo Kobayashi
    • Masaaki KatoYusuke OgawaHiroki DomonNaoya HayamizuMakiko TangeYoshiaki KurokawaNobuo Kobayashi
    • C25B15/00
    • C25B1/285
    • Sulfuric acid electrolysis process wherein; a temperature of electrolyte containing sulfuric acid to be supplied to an anode compartment and a cathode compartment is controlled to 30 degree Celsius or more; a flow rate F1 (L/min.) of the electrolyte containing sulfuric acid to be supplied to said anode compartment is controlled to 1.5 times or more (F1/Fa≧1.5) a flow rate Fa (L/min.) of gas formed on an anode side as calculated from Equation (1) shown below and a flow rate F2(L/min.) of said electrolyte containing sulfuric acid to be supplied to said cathode compartment is controlled to 1.5 times or more (F2/Fc≧1.5) a flow rate Fe (L/min.) of gas formed on a cathode side as calculated from Equation (2) shown below. Fa=(I×S×R×T)/(4×Faraday constant)   Equation (I) Fe=(I×S×R×T)/(2×Faraday constant)   Equation (2) I: Electrolytic current (A)S: Time: 60 second (Fixed)R: Gas constant (0.082 1·atm/K/mol)K: Absolute temperature (273.15 degree Celsius+T degree Celsius)T: Electrolysis temperature (degree Celsius)Faraday constant: (C/mol)
    • 硫酸电解法其中; 供给阳极室和阴极室的含有硫酸的电解质的温度控制在30摄氏度以上; 将供给到阳极室的含有硫酸的电解质的流量F1(L / min)控制为气体的流量Fa(L / min)的1.5倍以上(F1 / Fa> 1.5) 形成在阳极侧,由下述式(1)算出,将含有供给阴极室的硫酸的电解质的流量F2(L / min)控制在1.5倍以上(F2 / Fc> = 1.5)由下面所示的等式(2)计算的在阴极侧形成的气体的流速Fe(L / min)。 Fa =(IxSxRxT)/(4xFaraday常数)等式(I)Fe =(IxSxRxT)/(2xFaraday常数)等式(2)I:电解电流(A)S:时间:60秒(固定)R:气体常数(0.082 1.atm / K / mol)K:绝对温度(273.15摄氏度+ T摄氏度)T:电解温度(摄氏度)法拉第常数:(C / mol)