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    • 4. 发明专利
    • PROCESSING METHOD FOR RADIOACTIVE WASTE LIQUID
    • JPH08271692A
    • 1996-10-18
    • JP6951795
    • 1995-03-28
    • TOSHIBA CORP
    • TOYOHARA NAOMIMIKURA MICHITAKAFUJIHATA KENJIKANEKO MASAAKIWADA MIKIOOKANO TOSHIAKI
    • G21F9/06B01D61/44B01J20/18C02F1/469G21F9/10G21F9/12
    • PURPOSE: To enable reusing neutral salt in a radioactive material treatment facility by decomposing the neutral salt in waste liquid after removing radioactive nuclides into acid and alkali by electric dialysis and recovering them. CONSTITUTION: Waste liquid containing radioactive nuclides is contained in a pH controlling tank 1, acid is supplied from an acid supply tank 2 and pH of the waste liquid is controlled with a pH meter at 5 or less, and the liquid is transported to a coprecipitation reaction tank 4. To this tank, coprecipitation agents, phosphoric acid ion, lanthanum and alkali, 5 to 7, are supplied. At this moment, the supply amount of alkali is monitored with a pH meter 8 to control the waste liquid after adding the coprecipitation agent at pH3 or higher to let the coprecipitation agent precipitate and let the deposition take in TRU nuclides. The waste liquid containing the deposition is filtered with a filter 9 to make the deposition condensed sludge. The waste liquid removed of TRU nuclides together with the deposition is transported to an ion exchanging tower 11 charged with zeolite to remove Cs and tentatively stored in a reservoir tank 12. Then part of the waste liquid is transported to a waste liquid circulation tank 13 and the salt in the waste liquid is decomposed into acid and alkali with an electric dialyzer 14.
    • 7. 发明专利
    • RADIOACTIVE LIQUID WASTE TREATING APPARATUS
    • JPS63289497A
    • 1988-11-25
    • JP12375787
    • 1987-05-22
    • NIPPON ATOMIC IND GROUP COTOSHIBA CORP
    • SEKI HIDEJISHIRAI TAKAMORIWADA MIKIO
    • G21F9/12G21F9/00
    • PURPOSE:To suppress generation of a waste while enabling reuse of a radioactive nuclide adsorbent, by connecting a reaction tank, a pump for transferring a liquid treated and a filter for separating the adsorbent in series with a piping. CONSTITUTION:A reaction tank 1, a pump 2 and a filter 3 are arranged in series and the tank 1 is provided with a pipe 4 for introducing a radioactive waste liquor, an agitating device 5 and a pipe 6 for draining and transferring a treated liquid. The radioactive waste liquor is collected to the tank 1 with the pipe 4 and stirred up with the agitating device 5. Under such a condition, a hexacyanoferrate powder is added to the mixture and mixed for a fixed time. The waste liquor thus treated is transferred with the pump 2 to the filter 3 passing through the pipe 6 to separate solid from liquid. The hexacyanoferrate adheres to the surface of the filter of the device 3 to separate and trap a radioactive nuclide therewith and after a treatment thereof at an outlet, water quality is monitored to judge separating and trapping capacity. The hexacyanoferrate with lost separating/trapping capacity is backwashed and returned to the tank 1 for re-use.
    • 9. 发明专利
    • LIQUID TREATMENT DEVICE
    • JPS62213812A
    • 1987-09-19
    • JP5859886
    • 1986-03-17
    • TOSHIBA CORPISHIKAWAJIMA HARIMA HEAVY IND
    • WADA MIKIONAKAMURA MITSUSHIGEMIYATA YASUOABE TSUNEO
    • G21F9/06B01D61/10B01D61/58B01D63/06B01D65/02B01D65/04G21F9/00
    • PURPOSE:To remove suspending matters and solutes in one flow with a simple structure and small power by providing a power-rotating brush washing the inner wall in a mechanized way in a membrane tube of a tube-shaped separator. CONSTITUTION:In operating a liquid treatment device equipped with a membrane separator 2 constituted with a membrane module consisting of a plurality of brush-washing membrane tubes, high pressure gas in high pressure gas bomb 9 is stored in a gas supply tank 11 to be supplied to a concentration liquid receiving tank 12 through a pressure regulating valve 13 and pressurizes the inside of said tank 12 with operating pressure of the membrane separator 2. Raw liquid in a raw liquid tank 5 is sent to the membrane separator 2 by operating a high pressure pump 7. Water permeating the semi-permeable membrane in the membrane separator 2 is recovered in a treating water tank 4, and concentrated liquid containing suspending matters and solutes are flowed into the concentrated liquid receiving tank 12. In brush-washing, a continuous washing by rotation of brush is carried out to lower the flow speed in the membrane tube, and the number of membrane tubes in parallel can be reduced as the water passes through the steps of membrane tubes to enable the water to be concentrated in one flow.