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    • 2. 发明专利
    • Gas sampling system
    • 气体采样系统
    • JPS6141944A
    • 1986-02-28
    • JP16462184
    • 1984-08-06
    • Hitachi LtdHitachi Nuclear Eng Co Ltd
    • MORIYA KIMIAKINOJI HISASHITOTSUKA FUMIOYAMANARI SHOZOMITADERA MASASHI
    • G21C17/00G01N1/00G01N1/22G21C17/028
    • G21C17/028G01N1/24
    • PURPOSE:To improve measurement precision and reduce operation cost by providing a flow meter at the sample introduction part of a sampling pipe and nearby a gas analyzer. CONSTITUTION:Sample gas in a dry well 12 is sucked by a sampling pump 24 and guided to the sampling pipe 14, and then dehumidified by a cooler 16; almost all of the dehumidified sampling gas SG is guided to return piping 22 through a by-pass pipe 72 and the remainder enters the gas analyzer 20. An H2 concn. and O2 concn. of the SG entering the analyzer 20 are measured by a heat conduction type hydrogen gas detector and a magnetic wind type oxygen detector and the gas is admitted into the piping. The SG in the piping 22 is returned to the dry well 12 through the pump 24. Vapor condensed by the cooler 16, on the other hand, is discharged into a suppression chamber through piping 70. Thus, the H2 concn. and O2 concn. after the analysis 20 are corrected with measured values of a manometer 58, thermometer 60, differential pressure gauge 62, manometer 64, thermometer 66, and differential pressure gauge 68 to detect the H2 concn. and O2 concn. in the dry well 12.
    • 目的:通过在采样管的样品引入部分和气体分析仪附近提供流量计,提高测量精度并降低运行成本。 构成:干井12中的采样气体被采样泵24吸引并被引导到采样管14,然后由冷却器16除湿; 几乎所有的除湿取样气体SG被引导以通过旁通管72返回管道22,其余的进入气体分析器20。 和O2浓度 进入分析器20的SG由导热型氢气检测器和磁风式氧检测器测量,气体进入管道。 管道22中的SG通过泵24返回到干井12.另一方面,由冷却器16冷凝的蒸气通过配管70被排放到抑制室内。 和O2浓度 在分析20之后用压力计58,温度计60,差压计62,压力计64,温度计66和差压计68的测量值进行校正,以检测H2浓度。 和O2浓度 在干井12。
    • 6. 发明专利
    • REACTOR CONTAINMENT PROVIDED WITH HYDROGEN GAS COUNTERMEASURE EQUIPMENT
    • JPH10288695A
    • 1998-10-27
    • JP9557197
    • 1997-04-14
    • HITACHI LTD
    • ANDO KOJIYAMANARI SHOZO
    • G21C13/00G21D3/08
    • PROBLEM TO BE SOLVED: To efficiently mitigate containment internal pressure due to a plenty of hydrogen gas generation in a severe accident with the addition of minimum equipments by placing a catalystic burnable gas concentration controller in the containment and surrounding it with a vessel having a semipermeable membrane through which oxygen gas cannot pass and hydrogen gas can pass. SOLUTION: Hydrogen gas generated excessively in a containment by metal- water reaction, etc., in a pressure vessel 18 during a severe accident passes a break 19, fills the containment 13, passes a semipermeable membrane in the containment 13 and fills the vessel 1 having the semipermeable membrane. For the semipermeable membrane, polytetrafluoroethylene, for example, which let hydrogen pass but does not let oxygen pass, is used. At the beginning of a severe accident, only hydrogen gas is filled in the vessel 1 having a semipermeable membrane. When oxygen gas is injected from an oxygen supplier 3 through an oxygen injection part 4 provided at the lower part of the catalyst 2 inside the vessel 1, oxygen gas passes the catalyst 2 to combine with hydrogen and deposit in the space of the vessel 1.