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    • 1. 发明授权
    • Sulfuric acid electrolysis process
    • 硫酸电解过程
    • US08211287B2
    • 2012-07-03
    • US12459161
    • 2009-06-26
    • Masaaki KatoYusuke OgawaHiroki DomonNaoya HayamizuMakiko TangeYoshiaki KurokawaNobuo Kobayashi
    • Masaaki KatoYusuke OgawaHiroki DomonNaoya HayamizuMakiko TangeYoshiaki KurokawaNobuo Kobayashi
    • C25B1/28
    • 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 (1) 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; 供给所述阳极室的含有硫酸的电解质的流量F1(L / min)被控制为形成的气体的流量Fa(L / min)的1.5倍以上(F1 /Fa≥1.5) 在阳极侧,由下述式(1)计算,含有供给阴极室的硫酸的电解质的流量F2(L / min)被控制为1.5倍以上(F2 /Fc≥1.5 )由如下所示的等式(2)计算的在阴极侧形成的气体的流速Fe(L / min)。 Fa =(I×S×R×T)/(4×法拉第常数)等式(1)Fe =(I×S×R×T)/(2×法拉第常数)等式(2)I:电解电流 )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 / mol)
    • 4. 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)
    • 5. 发明授权
    • Water-cooled heat-accumulating type drink cooling system
    • 水冷蓄热式饮料冷却系统
    • US4365486A
    • 1982-12-28
    • US278857
    • 1981-06-29
    • Masao IwanamiYusuke Ogawa
    • Masao IwanamiYusuke Ogawa
    • F25D21/02F25D31/00B67D5/62
    • F25D31/003F25D21/02
    • A system for controlling the temperature of the drink cooling coil of a drink cooling system is disclosed. The system is a water-cooled heat-accumulating type drink cooling system having a water tank filled with water, a cooler in said tank, a drink cooling coil formed in an intermediate portion of a drink supply pipeline and an electric water agitator. The cooler is operated to cool the water in the tank by forming an ice bank around the cooler to accumulate heat in the tank, in order to cool a drink in the cooling coil. An agitator stopping means is provided which senses the temperature of the water in the tank and stops the agitator when said temperature is about 0.degree. C., so that an over-cooling of water in the tank occurs generally only at the cooler, and not at the cooling coil, thereby preventing ice from forming inside the cooling coil.
    • 公开了一种用于控制饮料冷却系统的饮料冷却盘管的温度的系统。 该系统是具有填充有水的水箱,所述罐中的冷却器,形成在饮料供应管线的中间部分中的饮料冷却盘管和电动水搅拌器的水冷蓄热型饮料冷却系统。 操作冷却器以通过在冷却器周围形成冰块以在罐中积聚热量来冷却罐中的水,以冷却冷却盘管中的饮料。 提供了一种搅拌器停止装置,其在所述温度约为0℃时感测到罐中的水的温度并停止搅拌器,使得罐中的水过度通常仅在冷却器处发生,而不是冷却器 在冷却盘管处,从而防止在冷却盘管内形成冰。
    • 8. 发明申请
    • Water electrolysis system
    • 水电解系统
    • US20080264780A1
    • 2008-10-30
    • US12149036
    • 2008-04-25
    • Masaaki KatoYusuke Ogawa
    • Masaaki KatoYusuke Ogawa
    • C25B9/10
    • C25B1/04C25B11/035C25B11/0489H01M4/8605H01M4/90H01M4/926Y02E60/366
    • In a water electrolysis system having an anode catalyst layer containing anode catalyst and a cathode catalyst layer containing cathode catalyst tightly attached, respectively, to each surface of a solid polymer electrolyte membrane comprising a cation exchange membrane, wherein at least one catalyst layer of said anode catalyst layer and cathode catalyst layer comprises a porous structure of anode catalyst or cathode catalyst dispersed in fluorine resin containing resin, featuring the surface of the anode catalyst layer or the cathode catalyst layer being hydrophobized and the water contact angle with the surface of the anode catalyst layer or the cathode catalyst layer of said porous structure being 90 degrees or more, whereby the transfer of gas to the counter electrode can be significantly suppressed, gas purity and current efficiency be improved, and safety operation of the electrolysis system be secured, without a major change in configuration of the water electrolysis system.
    • 在具有阳极催化剂层的阳极催化剂层和含有阴极催化剂层的阴极催化剂层的水电解系统分别紧密地连接在包含阳离子交换膜的固体高分子电解质膜的各表面上,其中所述阳极的至少一个催化剂层 催化剂层和阴极催化剂层包括分散在含氟树脂的树脂中的阳极催化剂或阴极催化剂的多孔结构,阳极催化剂层的表面或阴极催化剂层被疏水化,并且与阳极催化剂的表面的水接触角 所述多孔结构的层或阴极催化剂层为90度以上,由此可以显着地抑制气体向对置电极的转移,提高气体纯度和电流效率,并且可以确保电解系统的安全运行,而不需要 水电解系统配置发生重大变化。
    • 9. 发明授权
    • Powder inhaler
    • 粉末吸入器
    • US08875703B2
    • 2014-11-04
    • US12994064
    • 2009-05-22
    • Tetsuya SatoToru NishibayashiYusuke OgawaTakaaki NakaoShintaro Adachi
    • Tetsuya SatoToru NishibayashiYusuke OgawaTakaaki NakaoShintaro Adachi
    • B05D7/14A61M15/00A61M11/00
    • A61M15/0065A61M11/002A61M15/0026A61M15/0075A61M2202/064
    • A powder inhaler includes: a housing having a port; a storage member located in the housing for storing a powder medicament; and a medicament-delivery member provided in the housing. The medicament-delivery member includes at least one concave portion for receiving medicament, and is capable of taking, relative to the storage member, a receiving position wherein the concave portion receives a predetermined amount of powder medicament from the storage member, and an inhalation position wherein the powder medicament can be inhaled through the admission port; and a stirring member for stirring the powder medicament stored in the storage member. An operation button is provided in the housing and is capable of moving between the initial position and a depressed position, while the operation button reciprocates between the initial position and the depressed position, the concave portion in the medicament-delivery member moves from the receiving position to the inhalation position and the stirring member operates.
    • 粉末吸入器包括:具有端口的壳体; 位于所述壳体中的用于储存粉末药物的存储构件; 以及设置在所述壳体中的药物输送构件。 所述药物输送构件包括至少一个用于接收药物的凹部,并且能够相对于所述存储构件获取接收位置,其中所述凹部从所述存储构件接收预定量的粉末药物,并且吸入位置 其中所述粉末药物可以通过所述入口口吸入; 以及用于搅拌存储在所述存储部件中的粉末药剂的搅拌部件。 操作按钮设置在壳体中,并且能够在初始位置和踩下位置之间移动,同时操作按钮在初始位置和踩下位置之间往复运动,药物输送构件中的凹部从接收位置移动 到吸入位置并且搅拌部件工作。