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    • 55. 发明公开
    • REMOVAL DEVICE FOR RADIOACTIVE CESIUM
    • VORRICHTUNG ZUR ENTFERNUNG VON RADIOAKTIVEMCÄSIUM
    • EP2869308A1
    • 2015-05-06
    • EP13810086.2
    • 2013-06-19
    • Taiheiyo Cement Corporation
    • TANAKA, YoshihisaOGIRI, TetsuoHONMA, KenichiOKAMURA, SoichiroSHINDO, Takuya
    • G21F9/32G21F9/28G21F9/30
    • G21F9/32B01D53/508B01D53/8625B01D2257/302B01D2257/404B01D2258/02B09B3/0083C04B7/4423F23G5/0276F23G5/033F23G5/04F23J7/00G21F9/02G21F9/06G21F9/28G21F9/30G21F9/34Y02P40/126
    • [OBJECT] To provide a device for removing radioactive cesium from waste material containing radioactive cesium, doing so at low energy and in a dependable manner.
      [MEANS OF REALIZING THE OBJECT] The removal device 1 for radioactive cesium is provided with: a rotary kiln 41 which is provided with a burner 41b supplying from the kiln outlet an organic matter 03 contaminated with radioactive cesium, and an inorganic matter charging port 41a supplying from the kiln inlet inorganic matter S4 contaminated with radioactive cesium, and which is employed to burn the organic matter 03 together with the inorganic matter S4; and a recovery device cooling tower 51, a cyclone 52, a bag filter 53 for recovering cesium that has volatilized in the rotary kiln. A drying/crushing device (dryer 21, crusher 22) for drying and crushing the organic matter O1 prior to charging the radioactive cesium-contaminated organic matter to the rotary kiln can be provided. Additionally, a reforming/drying/crushing device (reformer 31, dryer 32, crusher 23) for reforming, drying, and crushing the inorganic matter S1 can be provided. During burning of the organic matter 03 together with the inorganic matter S4, a calcium source can be added as a reaction accelerant A to the rotary kiln.
    • [目的]提供一种用于从含有放射性铯的废料中除去放射性铯的装置,以低能量和可靠的方式进行。 [实现对象的手段]放射性铯去除装置1设置有回转窑41,该回转窑41具有从窑出口供给被放射性铯污染的有机物质03的燃烧器41b和无机物填充口41a 从窑入口的无机物质S4供给,被放射性铯污染,用于与无机物质S4一起燃烧有机物质03; 回收装置冷却塔51,旋风分离器52,回收窑内挥发的铯的袋式过滤器53。 可以提供用于在将放射性铯污染的有机物质装入旋转窑之前将有机物质O1干燥并粉碎的干燥/破碎装置(干燥机21,破碎机22)。 此外,可以提供用于重整,干燥和粉碎无机物质S1的重整/干燥/破碎装置(重整器31,干燥器32,破碎机23)。 在与无机物质S4一起燃烧有机物质03时,可以将钙源作为反应促进剂A添加到回转窑中。
    • 57. 发明公开
    • METHOD AND DEVICE FOR TREATING CHLORINE BYPASS DUST AND DISCHARGE GAS
    • VERFAHREN UND VORRICHTUNG ZUR BEARBEITUNG VON CHLOR-BYPASSSTAUB UND ENTLADUNGSGAS
    • EP2604586A1
    • 2013-06-19
    • EP11816357.5
    • 2011-08-04
    • Taiheiyo Cement Corporation
    • Terasaki JunichiSAITO Shinichiro
    • C04B7/60B01D53/50B01D53/77
    • B01D53/501B01D2258/0233C04B7/436C04B7/60C04B18/162F27D17/008F27D2017/009Y02W30/95
    • [Problems] To treat chlorine bypass dust while preventing increases in chemical cost and concentrations of heavy metals in clinker, and ensuring stability in quality of cement, and to treat chlorine bypass exhaust gas while avoiding coating troubles in a cement kiln etc., and preventing heat losses in a preheater etc., without degradation of clinker production amount.
      [Means for Solving Problems] In a chlorine bypass facility 1 extracting a part G of combustion gas, while cooling it, from a kiln exhaust gas passage, which runs from an inlet end of a cement kiln to a bottom cyclone, and recovering a chlorine bypass dust D6 from the extracted gas, the recovered chlorine bypass dust is slurried, and is contacted with the exhaust gas G4 from the chlorine bypass facility. The recovered chlorine bypass dust can be slurried after classified, and the slurry can be contacted with the exhaust gas from the chlorine bypass facility, and a coarse powder D1 that is classified before recovering the chlorine bypass dust from the extracted gas can be further classified, and a fine powder obtained by the second classification can be slurried together with the chlorine bypass dust, and the slurry can be contacted with the exhaust gas from the chlorine bypass facility.
    • [问题]在防止熟料中化学成本和重金属浓度升高,确保水泥质量稳定性和氯旁路废气处理同时避免水泥窑等中的涂层问题的同时防治氯旁路粉尘,防止 预热器中的热损失等,而不降低熟料生产量。 [解决问题的方法]在氯旁路设备1中,在从水泥窑的入口端到底部旋风器的窑尾废气通道中抽出燃烧气体一部分的同时进行冷却,并回收氯 从抽出的气体旁边除尘D6,回收的氯旁路粉尘浆化,并与来自氯旁路设备的废气G4接触。 回收的氯旁路粉尘可以分级后浆化,并且浆料可以与氯旁路设备的废气接触,并且可以进一步分类在从提取的气体中回收氯旁路粉尘之前分类的粗粉末D1, 并且通过第二分级获得的细粉末可以与氯旁路粉尘一起浆化,并且浆料可以与氯旁路设备的废气接触。