首页> 外国专利> METHOD FOR PRODUCING strontium-90 without a carrier and strontium-89 without a carrier using nuclear WATER-solution reactor and apparatus for implementing the method

METHOD FOR PRODUCING strontium-90 without a carrier and strontium-89 without a carrier using nuclear WATER-solution reactor and apparatus for implementing the method

机译:使用核水溶液反应堆生产无载体锶90和无载体锶89的方法及实施该方法的装置

摘要

1.method of manufacturing u0441u0442u0440u043eu043du0446u0438u00a0 90 without u043du043eu0441u0438u0442u0435u043bu00a0 and u0441u0442u0440u043eu043du0446u0438u00a0 - 89 without u043du043eu0441u0438u0442u0435u043bu00a0 using u00a0u0434u0435u0440u043du043eu0433u043e water u0440u0430u0441u0442u0432u043eu0440u043du043eu0433u043e reactor u0437u0430u043au043bu044eu0447u0430u044eu0449u0438u0439u0441u00a0 is, gaseous wednesday, u043eu0431u0440u0430u0437u0443u044eu0449u0443u044eu0441u00a0 in active zone of a u00a0u0434u0435u0440u043du043eu0433u043e water u0440u0430u0441u0442u0432u043eu0440u043du043eu0433u043e reactor and u0432u044bu0445u043eu0434u00a0u0449u0443u044e in compensation.components of the gaseous products which u00a0u0432u043bu00a0u044eu0442u0441u00a0 u0434u0435u043bu0435u043du0438u00a0 u00a0u0434u0435u0440u043du043eu0433u043e fuel and volatile u0441u043eu0435u0434u0438u043du0435u043du0438u00a0 radionuclides u043fu0440u043eu043au0430u0447u0438u0432u0430u044eu0442 through the first and second devices u0434u043bu00a0 extracts the gaseous environment, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 so that gaseous environment in the first and second sets u0434u043bu00a0 extracts the gaseous environment u043fu0440u043eu043au0430u0447u0438u0432u0430u044eu0442 together with u043du0430u0445u043eu0434u00a0u0449u0438u043c u0441u00a0 in solvent u0441u0442u0440u043eu043du0446u0438u00a0,in the process of u043fu0440u043eu043au0430u0447u043au0438 and gaseous environment to its u043fu043eu0441u0442u0443u043fu043bu0435u043du0438u00a0 second apparatus u0434u043bu00a0 extracts the gaseous environment during the time t, u043eu043fu0440u0435u0434u0435u043bu00a0u0435u043cu043eu0433u043e on forms ule;where: t is u0432u0440u0435u043cu00a0 extracts the gaseous environment to its u043fu043eu0441u0442u0443u043fu043bu0435u043du0438u00a0 second apparatus u0434u043bu00a0 extracts the gaseous environment.;- u043eu0431u044au0435u043cu043du0430u00a0 activity of krypton - 89 before the first machine u0434u043bu00a0 extracts the gaseous environment, bq / m3;;- u043eu0431u044au0435u043cu043du0430u00a0 activity of krypton - 90 to the first apparatus u0434u043bu00a0 extracts the gaseous environment, bq / m3;;is the ratio of specific activity u0441u0442u0440u043eu043du0446u0438u00a0 - 90 to the specific activity u0441u0442u0440u043eu043du0446u0438u00a0 - 89 in the final product u0441u0442u0440u043eu043du0446u0438u00a0 - 89 without u043du043eu0441u0438u0442u0435u043bu00a0;;- u043fu043eu0441u0442u043eu00a0u043du043du0430u00a0 the krypton - 89, - 1.;- u043fu043eu0441u0442u043eu00a0u043du043du0430u00a0 the krypton - 90, - 1;accumulate strontium - 90 without u043du043eu0441u0438u0442u0435u043bu00a0 solvent u0441u0442u0440u043eu043du0446u0438u00a0, u043du0430u0445u043eu0434u00a0u0449u0435u043cu0441u00a0 first the u0434u043bu00a0 extracts the gaseous environment, accumulate strontium - 89 without u043du043eu0441u0438u0442u0435u043bu00a0 in solvent u0441u0442u0440u043eu043du0446u0438u00a0, u043du0430u0445u043eu0434u00a0u0449u0435u043cu0441u00a0 second apparatus u0434u043bu00a0 extracts the gaseous environmentrecombine with the accumulated amount of solvent u0441u0442u0440u043eu043du0446u0438u00a0 u0441u0442u0440u043eu043du0446u0438u00a0 90 without u043du043eu0441u0438u0442u0435u043bu00a0 and solvent u0441u0442u0440u043eu043du0446u0438u00a0 with the accumulated amount of u0441u0442u0440u043eu043du0446u0438u00a0 - 89 without u043du043eu0441u0438u0442u0435u043bu00a0 in sys he u043au043eu043du0434u0438u0446u0438u043eu043du0438u0440u043eu0432u0430u043du0438u00a0 finished product.;2. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that a u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0 u0441u0442u0440u043eu043du0446u0438u00a0 use water of at least 0.1 m solution of nitric acid.;3. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the gaseous environment at a second machine u0434u043bu00a0 extracts the gaseous environment during at least one period u043bu0443u0440u0430u0441u043fu0430u0434u0430 krypton - 89.;4. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the strontium - 90 without u043du043eu0441u0438u0442u0435u043bu00a0 accumulate in the solvent u0441u0442u0440u043eu043du0446u0438u00a0 for at least seven days.;5. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the strontium - 89 without u043du043eu0441u0438u0442u0435u043bu00a0 accumulate in the solvent u0441u0442u0440u043eu043du0446u0438u00a0 within one day.;6. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, however, that govern the u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0 u0441u0442u0440u043eu043du0446u0438u00a0 at joint a tune up with the gaseous environment.;7.the device u0434u043bu00a0 production u0441u0442u0440u043eu043du0446u0438u00a0 90 without u043du043eu0441u0438u0442u0435u043bu00a0 and u0441u0442u0440u043eu043du0446u0438u00a0 - 89 without u043du043eu0441u0438u0442u0435u043bu00a0, of which u0432u0445u043eu0434u00a0u0442 established in line u0446u0438u0440u043au0443u043bu00a0u0446u0438u0438 gaseous environment u00a0u0434u0435u0440u043d five water u0440u0430u0441u0442u0432u043eu0440u043du044bu0439 reactor located on the active area of the compensation chamber, u043fu043eu0434u0432u043eu0434u00a0u0449u0438u0439 pipeline, a compressor, a first apparatus u0434u043bu00a0 extracts gas creative environment, connecting pipelinethe second apparatus u0434u043bu00a0 extracts the gaseous environment and u043eu0442u0432u043eu0434u00a0u0449u0438u0439 u043eu0442u043bu0438u0447u0430u044eu0449u0435u0435u0441u00a0 pipeline, so that the first and second devices u0434u043bu00a0 extracts the gaseous environments s u0432u0445u043eu0434u00a0u0442 hydraulic pump u0434u043bu00a0 u043fu0440u043eu043au0430u0447u043au0438 u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0 u0441u0442u0440u043eu043du0446u0438u00a0, u043du0430u043fu043eu0440u043du044bu0439 vessel, pipeline u0434u043bu00a0 joint u043fu0440u043eu043au0430u0447u043au0438 gaseous environment and u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0 u0441u0442u0440u043eu043du0446u0438 u00a0 and expansion vessel with a compensation chamber in its upper part.both sets u0434u043bu00a0 extracts the gaseous environment u043du0430u043fu043eu0440u043du044bu0439 receptacle is connected to a compensation chamber of the u0434u043bu00a0 pipeline expansion joint u043fu0440u043eu043au0430u0447u043au0438 gaseous environment and u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0 u0441u0442u0440u043eu043du0446u0438u00a0, u043au043eu043cu043fu0435u043du0441u0430u0446u0438u043eu043du043du0430u00a0 luggage u00a0u0434u0435u0440u043du043eu0433u043e water u0440u0430u0441u0442u0432u043eu0440u043du043eu0433u043e reactor is connected with the first pressure pipe apparatus of vessel u043bu00a0 extracts the gaseous environment u043fu043eu0434u0432u043eu0434u00a0u0449u0438u043c lineu043au043eu043cu043fu0435u043du0441u0430u0446u0438u043eu043du043du0430u00a0 chamber widening of the first apparatus u0434u043bu00a0 extracts the gaseous environment of pressure pipe is connected with the second apparatus u0434u043bu00a0 extracts gas vessel creative environment, the connecting line u043au043eu043cu043fu0435u043du0441u0430u0446u0438u043eu043du043du0430u00a0 chamber widening of the second apparatus u0434u043bu00a0 extracts the gaseous environment is offset by u0441u0430u0446u0438u043eu043du043du043eu0439 camera u00a0u0434u0435u0440u043du043eu0433u043e water u0440u0430u0441u0442u0432u043eu0440u043du043eu0433u043e reactor u043eu0442u0432u043eu0434u00a0u0449u0438u043c pipeline.;8. device for u043eu0442u043bu0438u0447u0430u044eu0449u0435u0435u0441u00a0 p.7, so that the pipeline u0434u043bu00a0 joint u043fu0440u043eu043au0430u0447u043au0438 gaseous environment and u0440u0430u0441u0442u0432u043eu0440u0438u0442u0435u043bu00a0 u0441u0442u0440u043eu043du0446u0438u00a0 is equipped with a regulating valve and u0440u0430u0441u0445u043eu0434u043eu043cu0435 rum.;9. device for u043eu0442u043bu0438u0447u0430u044eu0449u0435u0435u0441u00a0 p.7, so that u043fu043eu0434u0432u043eu0434u00a0u0449u0438u0439 and connecting pipelines are equipped with u043cu0430u043du043eu0432u0430u043au0443u0443u043cu043cu0435u0442u0440u043eu043c, back valve and u0434u0438u0441u043fu0435u0440u0433u0430u0442u043eu0440u043eu043c gaseous environments s.;10. device for u043eu0442u043bu0438u0447u0430u044eu0449u0435u0435u0441u00a0 p.7, so that the connecting pipeline is equipped with a compressor.
机译:1.制造方法 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0 90不具有 u043d u043e u0441 u0438 u0442 u0435 u043b u00a0和 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0-89不带有 u043d u043e u0441 u0438 u0442 u0435 u043b u043b u00b0使用 u00a0 u0434 u0435 u0435 u0440 u043d u043e u0433 u0433 u043e水u0442 u0432 u043e u0440 u043d u043e u0433 u043e反应堆 u0437 u0430 u043a u043b u044e u0447 u0430 u044e u0449 u0438 u0439 u0439 u0441 u00a0是气态星期三u043a u0440 u0430 u0437 u0443 u044e u0449 u0443 u044e u0441 u00a0在 u00a0 u0434 u0435 u0440 u043d u043e u0433 u043e水的活动区域中 u0440 u0430 u0430 u0441 u0442 u0432 u043e u0440 u043d u043e u0433 u043e反应器和 u0432 u044b u0445 u043e u0434 u00a0 u0449 u0443 u044e补偿气态产物的成分,其中 u00a0 u0432 u043b u00a0 u044e u0442 u0441 u00a0 u0434 u0435 u043b u0435 u043d u043d u0438 u00a0 u00a0 u0434 u0435 u0440 u043d u043e u043e u0433 u043e燃油和挥发物 u0441 u043e 0435 u0434 u0438 u043d u0435 u043d u0438 u00a0放射性核素 u043f u0440 u043e u043a u0430 u0447 u0438 u0432 u0430 u044e u0442通过第一和第二个设备 u0434 u043b u00a提取气体环境 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0,以便第一和第二组 u0434 u043b u00a0提取气体环境 u043f u0440 u043e u043a u0430 u0447 u0438 u0432 u0430 u044e u043e u0432 u043d u0430 u0445 u043e u0434 u00a0 u0449 u0438 u043c u043c u0441 u00a0 u0442 u0440 u043e u043d u0446 u0438 u00a0,在 u043f u0440 u043e u043a u0430 u0447 u043a u0438的过程中,以及向其 u043f u043e u043e u0441 u0442 u0443 u043f u043b u0435 u043d u0438 u00a0第二设备 u0434 u043b u00a0在时间t内提取气体环境, u043e u043f u0440 u0435 u0434 u0435 u043b u043b u00a0 u0435 u043c u043e u0433 u043e在形式ule上;其中:t是 u0432 u0440 u0435 u043c u00a0 ext向第二设备 u043f u043e u0441 u0442 u0443 u043f u043b u0435 u043d u0438 u00a0抽取气体环境。;- u043e u0431 u044a u0435 u043c u043d u0430 u00a0 activity的活动-在第一台机器 u0434 u043b u00a0提取气态环境bq / m3之前;;- u043e u0431 u044a u043a u0435 u043c u043d u0430 to的活动-90对第一个设备的活性 u0434 u043b u00a0提取气体环境bq / m3;是比活度的比率 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0 -90至特定活动 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0-最终产品 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0-89无 u043d u043e u0441 u0438 u0442 u0435 u043b u00a0 ;;--u003e u043e u043e u0441 u0442 u043e u00a0 u043d u043d u043d u0430 u00a0 k-89,-1。;- u043f u043e u0441 u0442 u043e u00a0 u043d u043d u0430 u00a0 rypto-90,-1;累积锶-90机智hout u043d u043e u0441 u0438 u0442 u0435 u043b u00a0溶剂 u0441 u0442 u0440 u043e u043d u043d u0446 u0438 u00a0, u043d u0430 u0445 u043e u0434 u00a0 u0435 u043c u0441 u00a0首先提取 u0434 u043b u00a0的气态环境,积累锶-89在溶剂 u0441 u0442 u0442 u0442 u04a u0445 u043b u043b u0040 u043e u043d u0446 u0438 u00a0, u043d u0430 u0445 u043e u043c u0441 u00a0第二设备 u0434 u043b u00a0将溶剂的气态环境与累积的量混合 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0 90不具有 u043d u043e u0441 u0441 u0438 u0442 u0435 u043b和溶剂 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0,其累计量为 u0441 u0442 u0440 u043e u043d u043d u0446 u0438 u00a0-89无 u043d u043e u0441 u0438 u0442 u0435 u043b u00a0在系统中的 u043a u043e u043d u0434 u0438 u0446 u0438 u043e u043d u043 8 u0440 u043e u0432 u0430 u043d u0438 u00a0成品; 2。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,这样 u0440 u0430 u0441 u0442 u0432 u0432 u043e u0440 u0438 u0442 u0435 u043b u00a0 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0使用至少0.1 m硝酸溶液的水; 3。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,以便至少在第二台机器上的气体环境在至少期间提取气体环境一个周期 u043b u0443 u0440 u0430 u0441 u043f u0430 u0434 u0430 k-89.; 4。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,这样锶-90不包含 u043d u043e u0441 u0438 u0442 u0435 u043b u00a0在溶剂 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0中累积至少七天; 5。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此锶-89不含 u043d u043e u0441 u0438 u0442 u0435 u0432 u04b u00a0的锶在一天之内就会累积在溶剂 u0441 u0442 u0440 u043e u043d u0446 u0446 u0438 u00a0中。 。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,但是,它控制 u0440 u0430 u0441 u0442 u0432 u0432 u043e u0440 u0438 u0442 u0435 u043b u00a0 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0结合气体环境进行调整; 7。设备 u0434 u043b u00a0生产 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0 90不具有 u043d u043e u0441 u0438 u0442 u0435 u043b u00a0和 u0441 u0442 u0440 u04340 u043e u043d u0446 u0438 u00a0-89不具有u043d u043e u0441 u0438 u0442 u0435 u043b u00a0,其中 u0432 u0445 u043e u0434 u00a0 u0442位于 u0446 u0438 u0440 u0440 u043a u0443 u043b u00a0 u0446 u0438 u0438气态环境 u00a0 u0434 u0435 u0440 u043d五水 u0440 u0430 u0441 u0442 u0432 u043e u0440 u043d u044b u0439反应堆位于补偿室的活动区域 u043f u043e u0434 u0432 u043e u0434 u00a0 u0449 u0438 u0439管道,压缩机,第一台设备 u0434 u043b u00a0提取气体创意环境,连接管道第二个设备 u0434 u043b u00a0提取气体环境,并且 u043e u0442 u0432 u043e u0434 u00a0 u0449 u0438 u0439 u043e u0442 u0432 u043b u0438 u0447 u0430 u044e u0449 u0435 u0435 u0441 u00a0管道,以便第一台设备和第二台设备 u0434 u043b u00a0提取气体环境s u0432 u0445 u043e u0434 u00a0 u0442液压泵 u0434 u043b u00a0 u043f u0440 u043e u043a u0430 u0447 u043a u0438 u0440 u0430 u0441 u0442 u0432 u043e u0440 u0438 u0442 u0435 u0435 u043b u00a0 u0441 u0442 u04340 u04340 u043 u0446 u0438 u00a0, u043d u0430 u043f u043e u0440 u043d u044b u0439容器,管道 u0434 u043b u00a0接头 u043f u0440 u043e u043e u043a u0430 u0447 u043a u043a u0438eous环境和 u0440 u0430 u0441 u0442 u0432 u043e u0440 u0438 u0442 u0432 u0435 u043b u00a0 u0441 u0442 u0440 u043e u043d u0446 u0438 u00a0和带有补偿腔的扩展容器两者都设置 u0434 u043b u00a0提取气体环境 u043d u0430 u043f u043e u0440 u043d u044b u0439插座已连接到 u0434 u043b u00a0管道膨胀接头 u043f u0440 u043e u043a u04a u0430 u0447 u043a u0438气体环境和 u0440 u0430 u0441 u0442 u0432 u043e u0440 u0438 u0442 u0435 u043b u00a0 u0441 u0442 u0440 u043e u043d u043d u0446 u0438 u00a0, u043a 043 u043c u043f u0435 u043d u0441 u0430 u0446 u0438 u043e u043d u043d u043d u0430 u00a0行李箱 u00a0 u0434 u0435 u0440 u043d u043e u043e u0433 u043e水 u0440 u0430 u043e u0442 u0432 u043e u0440 u043d u043e u0433 u043e反应器与容器的第一压力管设备相连 u043b u00a0提取气态环境 u043f u043e u0434 u0432 u043e u043e u0434 u00a0 u0449 u0438 u043c行 u043a u043e u043c u043f u0435 u043d u0441 u0430 u0446 u0438 u043e u043d u043d u043d u0430 u00a0扩大第一台设备的室 u0434 u043b u00a0提取气体压力管的环境与第二台设备连接 u0434 u043b u00a0提取天然气容器的创作环境,第二设备的连接线 u043a u043e u043c u043f u0435 u043d u0431 u0430 u0446 u0438 u043e u043d u043d u04d u0430 u00a0 u0434 u043b u00a0提取的气体环境被 u0441 u0430 u0446 u0438 u043e u043d u043d u043e u0439相机 u00a0 u0434 u0435 u0440 u043d u043e u0433 u043e水 u0440 u0430 u0441 u0442 u0432 u043e u0440 u043d u043e u0433 u043e反应堆 u043e u0442 u0432 u043e u0434 u00a0 u0449 u0438 u043c管道。; 8。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0435 u0435 u0441 u00a0 p.7的设备,以便管道 u0434 u043b u00a0接头 u043f u0440 u043e u043a u0430 u0447 u043a u0438气态环境和 u0440 u0430 u0441 u0442 u0432 u043e u0440 u0438 u0442 u0435 u043b u043b u00a0 u0441 u0442 u0440 u04340 u043e u043d u0446 u0438 ;装有调节阀和朗姆酒; 9。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0435 u0435 u0441 u00a0 p.7的设备,因此 u043f u043e u0434 u0432 u0432 u043e u0434 u0434 u00a0 u0449 u0438 u0439和连接管道配有 u043c u0430 u043d u043e u0432 u0430 u043a u0443 u0443 u043c u043c u0435 u0442 u0440 u043e u043c,背阀和 u0434 u0438 u0441 u043f u0435 u0440 u0433 u0430 u0442 u043e u0440 u043e u043c气体环境s。; 10。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0435 u0435 u0441 u00a0第7页的设备,因此连接管道装有压缩机。

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