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PROCEDE ET DISPOSITIF POUR L'UTILIZATION D'ENERGIE THERMIQUE A HAUTE TEMPERATURE

机译:在高温下使用热能的方法和装置

摘要

1412327 Decomposing steam using potassium ; potassium oxide; potassium peroxide GAZ DE FRANCE 12 Jan 1973 [13 Jan 1972] 1816/73 Heading C1A At least part of the thermal energy available from a high temperature heat source is utilized in a reaction cycle in which potassium, K, is reacted with water vapour to give gaseous hydrogen, which is separated and recovered, and solid or liquid potassium oxide (K 2 O) which is then thermally dissociated into its components, viz oxygen which is separated and recovered and potassium which is recycled. The preferred heat source is a nuclear pile or reactor. The reaction between water vapour and potassium may be carried out at a temperature of 500‹ C. The thermal dissociation of the potassium oxide is effected by melting the oxide so as to cause its disporoportionation into potassium vapour and liquid potassium peroxide, which is then reacted with molten lead to give molten litharge PbO which is separated and potassium vapour which is recycled, the molten litharge being vapourized under reduced pressure to give molten lead which is recycled and oxygen which is recovered. The disproportionation of K 2 O may be carried out at normal pressure and a temperature of 1270‹ C., if a lower pressure is used, the required temperature is lower. The reaction between lead and potassium peroxide may be carried out at normal pressure and a temperature of 1130‹ C. The decomposition of lead oxide is preferably carried out at a pressure of 0À005 bars. The potassium vapour produced in the reaction cycle may be used as a heat carrier, being used in a heat exchanger to produce steam for the process and for operating a conventional steam turbine.
机译:1412327用钾分解蒸汽;氧化钾过氧化钾GAZ DE FRANCE 1973年1月12日[1972年1月13日] 1816/73标题C1A高温热源可利用的热能的至少一部分用于反应循环,在该循环中钾K与水蒸气反应生成产生气态氢,将其分离和回收,然后将固态或液态氧化钾(K 2 O)热分解成其组分,即分离并回收氧气,然后回收钾。优选的热源是核堆或反应堆。水蒸气与钾之间的反应可以在500°C的温度下进行。氧化钾的热分解是通过将氧化物熔化以使其歧化成钾蒸气和液态过氧化钾来进行的,然后使之反应用熔融的铅得到熔融的铅矿石PbO,将其分离出来并回收钾蒸气,将熔融的铅矿石在减压下汽化,得到熔融的铅,将其再循环并回收氧气。 K 2 O的歧化可以在常压和1270℃的温度下进行,如果使用较低的压力,则所需的温度较低。铅和过氧化钾之间的反应可以在常压和1130°C的温度下进行。氧化铅的分解最好在0-005 bar的压力下进行。反应循环中产生的钾蒸汽可用作热载体,用于热交换器中以产生用于该方法的蒸汽和用于操作常规蒸汽轮机的蒸汽。

著录项

  • 公开/公告号CA983629A

    专利类型

  • 公开/公告日1976-02-10

    原文格式PDF

  • 申请/专利权人 GAZ DE FRANCE;

    申请/专利号CA19730160829

  • 发明设计人 SOURIAU DANIEL;

    申请日0000-00-00

  • 分类号G21D9;C01B3/06;C01B3/10;C01B13/02;C01B15/043;C01G21/06;C22B26/10;F01K3/18;F01K15;F01K25;

  • 国家 CA

  • 入库时间 2022-08-23 02:26:43

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