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    • 41. 发明专利
    • Method and device for electrolytic decontamination for waste material from reprocessing facility
    • JP2004117149A
    • 2004-04-15
    • JP2002280693
    • 2002-09-26
    • Hitachi Ltd株式会社日立製作所
    • SAWA TOSHIOKONDO YOSHIKAZUUEDA KIYOTAKA
    • G21F9/28C25D11/26C25F3/00
    • PROBLEM TO BE SOLVED: To provide a method and a device for the electrolytic decontamination which make it possible to efficiently and simultaneously decontaminate numerous objects to be decontaminated which are waste materials from reprocessing facilities such as end pieces of fuel cladding tubes and whose shapes are different. SOLUTION: A basket 4 made of a titanium material which can be uniformly energized so as to use numerous objects 1 to be decontaminated as anodes and is given a passivation treatment is used in an electrolytic cell 2, and cathodes 5 and 6 are set up on the outer periphery including the bottom and an upper part of the objects 1 to be decontaminated. Oxalic acid which has high solvency power and is excellent in electrical conductivity is used as a decontamination liquid. An ultrasonic vibrator 10 is located in the electrolytic cell 2 to intermittently facilitate the exfoliation of the attachment to the objects 1 to be decontaminated during electrolytic decontamination. Since the titanium basket 4 which is given the passivation treatment is used as an anode conductive material, the differentially-shaped objects to be decontaminated can be uniformly decontaminated through the electrolytic manipulation of the oxalic acid decontamination liquid without the work for electrically connecting the anode to each of the objects 1 to be decontaminated. The impartation of ultrasonic vibration during the electrolytic manipulation enables the decontamination for the back sides and intricately-shaped parts of the differentially-shaped objects 1 to be decontaminated. COPYRIGHT: (C)2004,JPO
    • 42. 发明专利
    • METHOD FOR MANUFACTURING WASTE OF SOLIDIFIED CHLORIDE
    • JPH11258389A
    • 1999-09-24
    • JP5769298
    • 1998-03-10
    • HITACHI LTDCENTRAL RES INST ELECT
    • ITO SHUICHISAWA TOSHIOMATSUBARA CHIAKIKOYAMA MASASHI
    • G21C19/44G21F9/16
    • PROBLEM TO BE SOLVED: To improve leach resistance by mixing a plastic material with an ingredient of a solidified aluminosilicate, sintering the mixture at the synthesizing temperature of the aluminosilicate and then sintering it at the softening temperature or higher of the plastic material. SOLUTION: A skeletal material 1 of solidified aluminosilicate and waste 2 of a molten salt are supplied to mixing process 4. Then, much the same quantity of a plastic ingredient 3 as that of the mixture is supplied and they are mixed evenly. The mixed materials are put into a cylindrical stainless container in a molding process 5 and pressure molding is carried out under the pressure of about 2,000 kg/cm exerted from the upper part of the container. With the mixed materials kept in the container, they are sintered at nearly 700 deg.C for about 200 hours under the atmosphere in the first sintering process 6. In the second sintering process 7, subsequently, the mixture is sintered at the softening temperature of 1,000 deg.C of the plastic ingredient 3 for about 10 hours to obtain waste 8 of solidified chloride. Consequently, the solidified waste is in contact with a liquid with a small contact when the waste is immersed in the water and such a simple process also makes it possible to manufacture a solidified waste with a less quantity of unimmobilized waste of the molten salt 2.
    • 43. 发明专利
    • MOISTURE REMOVING METHOD OF RADIOACTIVE GAS WASTE PROCESSING SYSTEM
    • JPH11202091A
    • 1999-07-30
    • JP217698
    • 1998-01-08
    • HITACHI LTDHITACHI ENG CO LTD
    • YOKOSE KENJIKAWABE KENICHIKONNO MASANOBUKUMASAKA MASAKISAWA TOSHIO
    • G21F9/02
    • PROBLEM TO BE SOLVED: To prevent secondary side contamination of a permeable film and improve safety and reliability of a nuclear plant by using a steam permeable film on a dehumidifier, providing temperature difference of a medium in a primary system and a secondary system of the steam permeable film and selectively permeating steam. SOLUTION: An exhaust gas of a primary side fluid introduced to a dehumidifier 1 from an exhaust gas condenser enters inside of a drum side of the dehumidifier via an exhaust gas inlet 4. A circulation water of a secondary side fluid is introduced to an upper water chamber 8 of the dehumidifier 1 via a circulation water inlet 6, flowed in the inside of a steam permeable film 11 downward, and introduced to the outside of the dehumidifier 1 via a lower water chamber 9 and a circulation water outlet 7. Thus, the steam of the exhaust gas is removed in a process in which circulation water leads to the lower water chamber 9 from the upper water chamber 8 of the dehumidifier 1. In addition, the condensed water of the exhaust gas side of the steam permeable film 11 is moved up to the upper part of the lower water chamber 9 by gravity, and discharged to the outside via a condensed water outlet 10. As a result, since radioactive waste can be prevented from mixing in the circulation water side of the steam permeable film 11, safety and reliability of a radioactive gas waste processing facility can be improved.
    • 44. 发明专利
    • METHOD AND FACILITY FOR DISPOSING OF WASTE LIQUID
    • JPH10311897A
    • 1998-11-24
    • JP11943397
    • 1997-05-09
    • HITACHI LTDHITACHI KYOWA ENG KK
    • KIDO YOSHIHIROYOSHIKAWA RYOZOSAWA TOSHIO
    • G21F9/06C02F1/04C02F1/44G21F9/08
    • PROBLEM TO BE SOLVED: To solve problems with enrichment or dry pulverization and solidification processes by removing, at the first step of processing, univalent ion which is harmful to these processes from waste liquid to be disposed of. SOLUTION: Solids are removed by a filter 2 from waste liquid, i.e., the subject of enrichment or drying pulverization process which is put into a waste liquid tank 1, and then the waste liquid is supplied to an electrodialyzer 11 to separate the same into univalent ion and bivalent or more ions; the liquid from which the univalent ion has been removed and the liquid enriched with univalent ions are separately collected into a processing liquid tank 12 and a separate liquid collecting tank 13, respectively. The waste liquid collected in the processing liquid tank 12, when it is subjected to enrichment process by an enriching device 14, can be enriched until the concentration of the enriched liquid reaches a reference value. Also, when the waste liquid is dry pulverized by a drier, pulverization can be continued well under stable conditions without a decrease in pulverization performance; in a solidification process, malfunctions such as the delay of polymerization reactions do not occur, and normal solidification is made possible.
    • 46. 发明专利
    • ABSORPTION FREEZER
    • JPH06307735A
    • 1994-11-01
    • JP9741693
    • 1993-04-23
    • HITACHI LTD
    • YOKOSE KENJINISHINO YOSHITAKASAWA TOSHIONAKAO TAKESHIAIZAWA MICHIHIKOOUCHI TOMIHISA
    • F25B37/00F25B43/04
    • PURPOSE:To reduce the occurrence of fluid resistance of steam in the absorber of an absorption freezer and to facilitate discharge of non-condensed gas in an absorber. CONSTITUTION:In a section where alignment of the heat transfer pipes of an absorber is seen from the longitudinal direction of the heat transfer pipe, a space is formed between a pipe group and a wall surface to form a steam flow passage 2. The width of a flow passage is decreased because of a wall surface in the middle of the steam flow passage 2 being continuously inclined in the direction of a steam flow. A bleed port 7 is installed outside a pipe group and non-condensable gas is discharged with high efficiency simultaneously with reduction of a pressure loss. Steam generated at a vaporizer flows through a steam inflow part 3 and flows through a steam flow passage 2 over the whole interior of an absorber. Simultaneously, the steam is absorbed by means of absorption liquid 5 sprayed over the outer surface of each transfer pipe by means of an absorption liquid spraying device 4. Through the effect of the steam flow passage 2 between a pipe group region, where heat transfer pipes 1 are densly arranged, and a wall surface, and flow resistance of steam can be reduced. Rectification is effected in a manner to form a bleed port 6 additionally functioning as an absorption liquid discharge port or the bleed port 7, and non-condensable gas can be discharged with high efficiency.
    • 49. 发明专利
    • ULTRAPURE WATER MANUFACTURING DEVICE
    • JPH0699165A
    • 1994-04-12
    • JP24950192
    • 1992-09-18
    • HITACHI LTD
    • KUROKAWA HIDEAKIMATSUMOTO TAKAYUKISAWA TOSHIO
    • B01D53/22B01D1/22C02F1/04
    • PURPOSE:To reduce water manufacturing cost and improve the quality of generated ultrapure water by adopting a multiple-effect system which uses a distillation part structure incorporating an extratubular descending flow liquid membrane in a method for obtaining ultrapure water by condensation after distillation of untreated water and removal of generated mist. CONSTITUTION:The subject ultrapure water consists of a deaeration part 104, distillers 105, 111, 112, a condenser 113 and hydrophobic multi-porous membranes 110, 120, 121. The distillers 105, 111, 112 are of an extratubular descending flow liquid membrane type. The liquid running outside a heat conducting pipe in a first distiller 105 is sent to the untreated water inlet 115 of a second distiller 111 from an untreated water outlet 114. The same procedures are taken with the second and a third distiller 111, 112. Vapor generated from the third distiller 112 is filtered by the hydrophobic multi-porous membrane 121, then is condensated by a condenser 102, and the condensed water obtained by the second and the third distiller 111, 112 and the condenser 102 is supplied as ultrapure water. In the extratubular descending flow liquid membrane system, generated water runs through a welded part between the heat conducting pipe and a terminal plate, thus causing no fear about contamination.