会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明授权
    • Electrochemical cell having improved pressure vent
    • 电化学电池具有改进的压力通风口
    • US5258242A
    • 1993-11-02
    • US14965
    • 1993-02-08
    • Kevin DeanArthur HollandDonn Fillmore
    • Kevin DeanArthur HollandDonn Fillmore
    • H01M2/12
    • H01M2/1276H01M2/1223H01M2/1205
    • The electrochemical cell of the instant invention includes a case having a gas outlet, one or more positive electrodes positioned within the case, one or more negative electrodes positioned within the case electrode separators positioned between the positive and negative electrodes, electrolyte positioned within the case, and a pressure vent for releasing internal pressure occurring in the case to the surrounding atmosphere. The pressure vent is affixed to the case covering the gas outlet, the pressure vent includes a vent housing having a hollow interior area in gaseous communication with the surrounding atmosphere and the interior of the case via the gas outlet, a pressure release piston positioned within the hollow interior area, the pressure release piston sized to surround the gas outlet and having a seal groove configured to encapsulate all but one surface of a seal mounted within the seal groove, leaving the non-encapsulated surface of the seal exposed, and a compression spring positioned to urge the pressure release piston to compress the seal in the seal groove and block the gas outlet in the case.
    • 本发明的电化学电池包括具有气体出口的壳体,位于壳体内的一个或多个正极,位于正极和负极之间的壳体电极分离器内的一个或多个负极,位于壳体内的电解质, 以及用于将外壳中发生的内部压力释放到周围大气的压力通风口。 压力通风口固定到覆盖气体出口的壳体上,压力通风口包括通气口壳体,其具有与周围大气气体连通的中空内部区域和通过气体出口的壳体内部,位于 中空内部区域,压力释放活塞的尺寸设置成围绕气体出口并具有密封槽,该密封槽构造成将安装在密封槽内的密封件的除了一个表面之外的所有表面封装,使密封件未封装的表面露出, 定位成促使压力释放活塞压缩密封槽中的密封并阻塞气体出口。
    • 9. 发明授权
    • Compositionally and structurally disordered multiphase nickel hydroxide
positive electrode for alkaline rechargeable electrochemical cells
    • 用于碱性可再充电电化学电池的组成和结构上无序的多相氢氧化镍正极
    • US5637423A
    • 1997-06-10
    • US232782
    • 1994-04-20
    • Stanford R. OvshinskyMichael A. FetcenkoSrinivasan VenkatesanArthur Holland
    • Stanford R. OvshinskyMichael A. FetcenkoSrinivasan VenkatesanArthur Holland
    • H01M4/26H01M4/28H01M4/32H01M4/52H01M4/80H01M10/34
    • H01M10/345H01M4/26H01M4/28H01M4/32H01M4/52H01M4/80
    • A positive electrode for use in alkaline rechargeable electrochemical cells comprising: a material comprising a compositionally and structurally disordered multiphase nickel hydroxide host matrix which includes at least one modifier. A process for forming a high loading uniformly distributed multiphase substantially nitrate free sintered positive electrode for use in an alkaline rechargeable electrochemical cell, the process comprising: (1) fabricating sintered electrode material by forming a slurry of nickel powder, water, carboxy methyl cellulose binder, methyl cellulose binder, and a poly(ethylene oxide) polymer; spreading the slurry on a preoxidized perforated nickel substrate; drying the slurry; and sintering the slurry; (2) impregnating the sintered electrode material using multiple impregnation cycles to attain high loading; and (3) forming the impregnated sinter into positive electrode material by presoaking the impregnated sinter in NaOH presoak tanks to substantially eliminate nitrates; brushing the presoaked impregnated sinter in a surface brushing station; charging the brushed impregnated sinter; discharging the charged impregnated sinter; rinsing the discharged impregnated sinter; and drying the rinsed impregnated sinter to complete the formation of positive electrode material.
    • 一种用于碱性可再充电电化学电池的正电极,包括:包含组成和结构上无序的多相氢氧化镍主体基质的材料,其包含至少一种改性剂。 一种用于形成用于碱性可再充电电化学电池的高负载均匀分布的多相基本上无硝酸盐的烧结正电极的方法,所述方法包括:(1)通过形成镍粉,水,羧甲基纤维素粘合剂的浆料来制造烧结的电极材料 ,甲基纤维素粘合剂和聚(环氧乙烷)聚合物; 将浆料铺展在预氧化的穿孔镍基底上; 干燥浆料; 并烧结浆料; (2)使用多次浸渍循环浸渍烧结电极材料以达到高负荷; 和(3)通过将浸渍的烧结体预浸泡在NaOH预浸罐中以基本上除去硝酸盐,将浸渍的烧结物形成为正极材料; 在表面刷洗站中刷涂预浸渍的浸渍烧结物; 对刷洗过的烧结矿进行充电; 对带电的浸渍烧结物进行放电; 冲洗排出的浸渍烧结物; 并干燥漂洗的浸渍烧结物,以完成正极材料的形成。
    • 10. 发明授权
    • Compositionally and structurally disordered multiphase nickel hydroxide
positive electrode containing modifiers
    • US5948564A
    • 1999-09-07
    • US782863
    • 1997-01-13
    • Stanford R. OvshinskyMichael A. FetcenkoSrinivasan VenkatesanArthur Holland
    • Stanford R. OvshinskyMichael A. FetcenkoSrinivasan VenkatesanArthur Holland
    • H01M4/26H01M4/28H01M4/32H01M4/52H01M4/80H01M10/34
    • H01M10/345H01M4/26H01M4/28H01M4/32H01M4/52H01M4/80
    • A positive electrode for use in alkaline rechargeable electrochemical cells comprising: a material comprising a compositionally and structurally disordered multiphase nickel hydroxide host matrix which includes at least one modifier chosen from the group consisting of F, Li, Na, K, Mg, Ba, La, Se, Nd, Pr, Y, Co, Al, Cr, Mn, Fe, Cu, Zn, Sc, Sn, Sb, Te, Bi, Ru, and Pb. A process for forming a high loading uniformly distributed multiphase substantially nitrate free sintered positive electrode for use in an alkaline rechargeable electrochemical cell, the process comprising: (1) fabricating sintered electrode material by forming a slurry of nickel powder, water, carboxymethylcellulose binder, methyl cellulose binder, and a poly(ethylene oxide) polymer; spreading the slurry on a preoxidized perforated nickel substrate; drying the slurry; and sintering the slurry; (2) impregnating the sintered electrode material using multiple impregnation cycles to attain high loading, where each impregnation cycle comprises the steps of: placing the sintered electrode material on a rack; dipping the rack into nickel nitrate; allowing the rack to drip dry; dipping the dried rack into NaOH solution; spraying the rack in a first tank with deionized water overflowing from a second tank; dipping the rack in the second tank filled with deionized water overflowing from a third tank; dipping the rack in the third tank filling with deionized water at a rate of 8-10 gpm; drying the rack; and flipping the rack to attain uniform deposition of material; where in the median dip cycle and in the final dip cycle of the multiple impregnation cycles, the step of dipping the rack into nickel nitrate is replaced by a step of dipping the rack into cobalt nitrate to produce an enriched cobalt surface; and (3) forming the impregnated sinter into positive electrode material by presoaking the impregnated sinter in NaOH presoak tanks to substantially eliminate nitrates; brushing the presoaked impregnated sinter in a surface brushing station; charging the brushed impregnated sinter; discharging the charged impregnated sinter; rinsing the discharged impregnated sinter; and drying the rinsed impregnated sinter to complete the formation of positive electrode material.