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    • 63. 发明专利
    • DEVICE FOR PRODUCING OXIDE POWDER
    • JPS6321228A
    • 1988-01-28
    • JP16277886
    • 1986-07-10
    • NIPPON NUCLEAR FUELS
    • OMURA NAOTAKAYAMATO KEIJI
    • B02C21/00C01B13/14C01G43/01C03B13/14G21C21/02
    • PURPOSE:To produce the title oxide powder from sintered pellets in a short time by coarsely crushing the pellets, oxidizing the material in a heat-treating furnace, pulverizing the material, and screening the material with a classifier at the time of producing the oxide powder from sintered pellets. CONSTITUTION:The sintered pellets in a raw material supply can 1 hung from a balance loader 2 are supplied into a supply hopper 3, and the pellets are charged in a coarse crusher 5 through a feeder 4 and crushed. The crushed pellets are dropped onto a belt conveyor 7 in a heat-treating device 6 and oxidized while being traveled in the heat-treating device 6. The oxidized powder is supplied into a pulverizer 8 and pulverized, and then supplied to the classifier 9 wherein product powder having coarser particle size an the powder having specified particle size are separated. The powder having specified particle size is supplied to a product can 11 by a feeder 10, and weighed by a weighing device 12 to a specified weight. The powder coarser than the specified size is supplied to a storage can 13. Oxide powder can be produced in a short time from sintered pellets by this device.
    • 70. 发明专利
    • Process for recovering anhydrous hydrogen fluoride from deteriorated uf6 and reutilizing thereof
    • 从去除的UF6中回收氢氟酸的方法及其回收
    • JPS6186402A
    • 1986-05-01
    • JP20556684
    • 1984-10-02
    • Mitsubishi Metal CorpPower Reactor & Nuclear Fuel Dev Corp
    • SASAO NOBUYUKITANAKA AKIRAUMEMURA AKIO
    • C01G43/01C01B7/19C01B9/08C01G43/06
    • PURPOSE: To recover HF having high purity inexpensively without producing almost no secondary wastes by transforming deteriorated UF
      6 to U≥3O
      8 by the gaseous phase reaction by the dry process and recovering by-produced dil. HF in the form of anhydrous HF by the sulfuric acid extraction process.
      CONSTITUTION: Waste deteriorated UF
      6 is vaporized in a vaporizer 1, introduced into a fluidized bed reaction furnace 2. A gaseous phase reaction is caused by the steam 11 from the bottom of the reactor generating particles of UO
      2 F
      2 and a fluidized bed is formed. The UO
      2 F
      2 particles are overflowed over the top of the fluidized bed, into a second fluidized bed reaction furnace 3 where it is transformed to U
      3 O
      8 by the steam contained in the waste gas from a third fluidized bed reaction furnace 4, overflowed to the third fluidized bed reaction furnace 4, defluorinated by the steam 12, and the product is received in a U
      3 O
      8 eceiver 5. By-produced HF discharged from the reaction furnace 2, 3 is collected in a condenser 6 to form dil. HF having high concn., and is transferred to an extraction distillation tower 7. H
      2 SO
      4 14 is fed to the tower, and anhydrous HF is recovered from the top of the tower by the extraction distillation, condensed in a condenser 8 and received by a receiver 9. Dil. H
      2 SO
      4 13 is recovered from the bottom of the tower, and recycled to the extraction distillation tower 7 through a concentration tower 10.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:通过干法处理气相反应并回收副产的稀释剂,通过将劣化的UF6转化为U> = 3O8来回收廉价的高纯度的HF,几乎不产生二次废物。 HF以无水HF的形式通过硫酸提取过程。 构成:废气劣化UF6在蒸发器1中蒸发,引入流化床反应炉2.气相反应由反应器底部的蒸汽11引起,产生UO2F2颗粒,形成流化床。 UO2F2颗粒在流化床的顶部溢出,进入第二流化床反应炉3,在其中通过包含在来自第三流化床反应炉4的废气中的蒸汽转化成U3O8,溢流到第三流化床 反应炉4,由蒸汽12脱氟,产物被接收在U3O8收发器5中。从反应炉2,3排出的副产HF被收集在冷凝器6中以形成稀释。 高浓度的HF,并被转移到提取蒸馏塔7.将H 2 SO 4 14进料到塔中,通过萃取蒸馏从塔的顶部回收无水HF,在冷凝器8中冷凝并被接收器 戴尔 从塔底回收H 2 SO 4 13,并通过浓缩塔10再循环至萃取蒸馏塔7。