首页> 外国专利> METHOD AND APPARATUS FOR REGENERATING COLD TRAPS WITHIN LIQUID-METAL CIRCULATORY SYSTEMS

METHOD AND APPARATUS FOR REGENERATING COLD TRAPS WITHIN LIQUID-METAL CIRCULATORY SYSTEMS

机译:在液循环系统中再生冷阱的方法和装置

摘要

1489329 Recovery of sodium hydroxide values from liquid sodium UNITED STATES ENERGY RESEARCH & DEVELOPMENT ADMINISTRATION 12 April 1976 [29 May 1975] 14805/76 Heading ClA [Also in Division C7] Liquid sodium or sodium alloys circulating in a system have the impurities Na 2 O and Na hydride removed by depositing the impurities in a cold trap and by heating the trap to react the oxide and hydride to form NaOH, monitoring the hydrogen partial pressure to determine the efficiency of the reaction, and by draining the molten NaOH from the system. Liquid metal is drawn from a circulatory system via pipe 11, through pump 13 to an econimizer 15 wherein the heat of the metal is recovered. The cooled metal feeds through pipe 17 to a cold trap pressure vessel 27, filled with metallic packing material 37 on which the impurities crystallize when the vessel 27 is cooled by blower 39 to say 100-200‹ C. A pressure gauge 30 monitors the hydrogen partial pressure within the tank 27, which may be adjusted as required by either venting or adding hydrogen from supply 65. Tank 27 is also fitted with a drain outlet 31, connected by valve 32 to a second tank 45, which again may be heated or cooled by resistance 53 and blower 55. A level indicator 57 is installed in each 45. In operation, liquid metal withdrawn from the system enters tank 27, passing through economizer 15, to fill the tank, passing outside baffle 35 through packing 37 to the upper tank outlet 19, thence back to the circulatory system, having been cooled to 100-200‹C. in its passage through tank 27, so that the oxide and hydride impurities precipitate out on packing 37. When tank 27 is filled with impurities, it is isolated from the circulatory system by valve 23, and any liquid metal drained via outlet 31 to reservoir 67. The tank 27 is then heated to cause the reaction to occur (temperature of 412-550‹ C.), and the molten NaOH is drained into tank 45. indicator 57 showing when reaction is complete. The partial pressure of hydrogen in tank 27 is then measured to see if excess NaH or NaO is present in tank 27 which may be corrected by altering the H 2 pressure until the level in tank 45 is constant indicating that all the impurities have been removed. The cold trap is then reconnected to the circulatory system for further use.
机译:1489329从液态钠中回收氢氧化钠值1976年4月12日[1975年5月29日]美国能源研究与开发署[标题CLA] [C7分部中也存在]在系统中循环的液态钠或钠合金含有Na 2 O杂质通过在冷阱中沉积杂质并加热阱以使氧化物和氢化物反应形成NaOH,监测氢分压以确定反应效率,并从系统中排出熔融的NaOH,从而除去氢化钠。液态金属通过管道11从循环系统中抽出,通过泵13到达节能器15,在回收器中回收金属的热量。冷却后的金属通过管道17进入冷阱压力容器27,该容器中装有金属填充材料37,当容器27被鼓风机39冷却至100-200°C时,杂质会在该金属上结晶。压力表30监测氢气罐27内的分压,可以根据需要通过排放或添加来自供应源65的氢气进行调节。罐27还装有排出口31,该排出口通过阀32连接到第二个罐45,第二个罐45可以再次加热或由电阻53和鼓风机55冷却。在每个45中安装了液位指示器57。在操作中,从系统中抽出的液态金属进入储罐27,通过省煤器15填充储罐,使外部挡板35通过填料37到达储罐。上箱出口19已冷却至100-200°C,从此回到循环系统。在其通过罐27的过程中,氧化物和氢化物杂质沉淀在填料37上。当罐27中充满杂质时,它通过阀23与循环系统隔离,所有液态金属通过出口31排到储液罐67然后加热罐27以引起反应发生(温度为412-550℃),并且将熔融的NaOH排入罐45中,指示器57显示反应何时完成。然后测量罐27中氢的分压以查看罐27中是否存在过量的NaH或NaO,这可以通过改变H 2压力直至罐45中的液位恒定以表明已除去所有杂质来校正。然后将冷阱重新连接到循环系统以进一步使用。

著录项

  • 公开/公告号GB1489329A

    专利类型

  • 公开/公告日1977-10-19

    原文格式PDF

  • 申请/专利权人 UNITED STATES ENERGY RES & DEV ADMINISTRATION;

    申请/专利号GB19760014805

  • 发明设计人

    申请日1976-04-12

  • 分类号C22B9/02;C22B26/10;

  • 国家 GB

  • 入库时间 2022-08-22 23:38:43

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