首页> 外国专利> seen that during the discharge of a metal klorackumulator regulate the generation and matandet of chlorine from a lagringsrum for klorhydrat to accumulator

seen that during the discharge of a metal klorackumulator regulate the generation and matandet of chlorine from a lagringsrum for klorhydrat to accumulator

机译:可以看到,在排出金属碳酸钾蓄积器期间,调节​​了从滞后渣渣中产生氯的水和氯的残留量,以便将碳酸氢钾溶出至蓄积器中

摘要

1452199 Metal-chlorine storage battery ENERGY DEVELOPMENT ASSOCIATES 2 July 1974 [2 July 1973] 29279/74 Heading H1B A storage battery 11 essentially as disclosed in Specification 1339060 having metal electrodes, preferably of zinc, and graphite electrodes to which chlorine is supplied, the chlorine being dissolved in an aqueous electrolyte, preferably of zinc chloride, and flowing through a circuit 15, 23, 13 including a pump 21, adjustable valve 27, and a dissolver 25 for dissolving the chlorine, has an additional flow circuit 29, 33 including a non- return valve 35, the chlorine hydrate store 31 and an adjustable valve 37. The temperature of the store 31 is maintained at a lower temperature than that of the electrolyte which enters from line 29, the electrolyte temperature being such, e.g. 15- 50‹C, that it decomposes the hydrate to form chlorine and water, the increase of pressure in the store caused by the generation of the products shutting the valve 35. The electrolyte flow through the store 31 thus ceases and no more chlorine is generated. On discharge, the battery 11 consumes chlorine causing a reduction in pressure to the lines 13, 33 whereby electrolyte flows through the store 31 to generate chlorine and make up the deficiency. The valves 27, 37 are set to give pressure drops such that the system is selfregulating in relation to the chlorine demands of the battery and operates to maintain the electrolyte saturated with chlorine. A small venting orifice 19 is provided in line 15.
机译:1452199金属-氯蓄电池能源开发协会1974年7月2日[1973年7月2日] 29279/74标题H1B一种基本上如规范1339060中所公开的蓄电池11,具有金属电极(最好是锌)和供有氯的石墨电极,氯溶解在最好是氯化锌的水性电解液中,并流经回路15、23、13,回路15、23、13包括泵21,可调阀27和用于溶解氯的溶解器25,该回路还有一个附加的流量回路29、33,包括止回阀35,水合氯气储存器31和可调阀37。储存器31的温度保持在比从管线29进入的电解质的温度低的温度,电解质温度例如为在图15-50℃中,它分解水合物形成氯和水,由于关闭阀门35的产物的产生而导致储存器中压力的增加。因此,通过储存器31的电解质流停止并且不再有氯被释放。产生。放电时,电池11消耗氯气,导致对管线13、33的压力降低,由此电解质流过储存器31以产生氯气并弥补不足。阀27、37被设置为给出压降,使得系统相对于电池的氯需求量是自调节的,并且用于维持电解质被氯饱和。管路15中设有一个小的排气孔19。

著录项

  • 公开/公告号SE409781B

    专利类型

  • 公开/公告日1979-09-03

    原文格式PDF

  • 申请/专利权人 * ENERGY DEVELOPMENT ASSOCIATES;

    申请/专利号SE19740008659

  • 发明设计人 P C * SYMONS;

    申请日1974-07-01

  • 分类号H01M12/02;H01M12/08;H01M10/44;

  • 国家 SE

  • 入库时间 2022-08-22 20:30:00

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