• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention concerns a procedure and a bioreactor for treating low activity wastes from nuclear power plants with the aid of anaerobic fermentation. The waste (11,28) is subjected to desired pretreatment, such as e.g. comminution (12) and suspending (13), or a special treatment (30), such as e.g. hydrolysis and/or physical dispersion, such as e.g. irradiation, heat treatment or equivalent. The pretreated waste is conducted into a bioreactor (15), where anaerobic decomposition takes place in two steps, the first step being an acid step (15a) and the second step, a methane step (15b). The gases produced in the decomposition process are conducted from the methane step (15b) to gas burning (27), and the undecomposed waste is removed from the process to concentration (20) and packed in barrels (21) or equivalent.
    公开号:SU1627098A3
    申请号:SU884355492
    申请日:1988-04-07
    公开日:1991-02-07
    发明作者:Туса Эско；Мяття Раймо；Руусканен Антти
    申请人:Иматран Войма Ой (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to atomic technology and technology, and more specifically to the treatment of low-level solid radioactive waste generated in nuclear power plants using anaerobic fermentation.
    The aim of the invention is to improve the environmental safety of the environment, as well as simplify the processing of solid radioactive waste.
    FIG. 1 shows a bioreactor for anaerobic treatment of solid radioactive, low activity waste, side view, FIG. 2 is the same, front view, in FIG. 3 - the same, side view, with connected containers with water and chemicals: new radioactive waste, old radioactive waste, as well as a collection of undecomposed waste and a non-decomposing waste circulation line, fig. 4 is a technological scheme for treating low activity solid radioactive waste using anaerobic fermentation, i
    The bioreactor contains the covering
    1 and the lower 2 parts, which can be separated from one another and mounted on the supporting structure 3. B. The lower part 2 of the bioreactor has a circulation pump 4. The covering 1 and the lower 2 parts of the bioreactor form the gas 5 and liquid 6 chambers. A suspending device 7 is installed on the lower part 2 of the bioreactor, and the covering part 1 of the bioreactor has a ventilating pipe 8, and the lower part 2 of the bioreactor is divided into blocks 9-11 using partitions 12 and 13. After decomposition of the bottom of the bioreactor 2 With the help of 15 circulation pump 4 it is transported to the collection of undecomposed waste 14, or through the circulation pipe 15 through the suspending device 7 to re-enter the lower 20 part 2 of the bioreactor.
    The bioreactor works as follows.
    Pre-treated by grinding, suspending or special treatment, such as hydrolysis, and / or physical dispersion (nulling, heat treatment), radioactive waste is fed to the bottom 2 of the bioreactor, which is divided into blocks 9-11. In addition, each unit is designed for a specific type of waste, characterized by the time required for its decomposition .35
    The capacity of each unit is selected in accordance with the time that the material must spend in it, i.e. according to the decomposition rate .40
    Water and chemicals are supplied to the lower part 2 of the boreactor.
    During anaerobic fermentation, the resulting gas is accumulated in the gas chamber 5 and removed through the vent tube 8 from the bioreactor.
    Undecomposed radioactive waste from the bottom 2 of the bioreactor. Through a circulation pump 4, CQ collection 14 of undecomposed or, if necessary, repeated anaerobic fermentation through the circulation tube 15 is fed through the suspending device 7 and fed again. . The second part of the bioreactor.
    The method of anaerobic fermentation of solid radioactive waste is carried out as follows (Fig.4).
    Initially, waste is collected and emptied by waste barrels (in figure 4, new waste is indicated by block 16, barrels with old waste by block 17 and emptying of barrels by block 18). Then the waste is crushed (block 19) and the crushed waste is suspended (block 20). Suspended waste is fed to the separator 21, from where decomposed waste is fed to the proposed bioreactor 22, in which a two-stage anaerobic decomposition takes place: in the first stage - acidic (22a), and the second - methane (226).
    Undecomposed wastes are removed from separator 21 and fed to block 23, from bioreactor 22, undecomposed wastes are fed to block 24, and the anaerobically decomposed wastes are sent to separator 25, where the decomposition of the unintegrated substance and water occurs. Undecomposed waste is fed to block 26, and water returns through the circulation pipe 27 to the water tank 28. Replaced water is supplied from block 29 to block 28. Undecomposed waste which has been removed from the process is fed from blocks 23, 24 and 26 to collector 30, from where the treated waste is placed in barrels 31, which are fed to storage 32. Chemicals are added to unit 22 in bioreactor 22. The products of the methane reaction stage (22c) of the bioreactor 22 in the form of -gas are fed to block 34 and further to the gas burner 35.
    The proposed method may also include special processing (figure 4, block 36). In this case, the waste may be treated with chemicals (block 37), subjected to heat treatment (block 38), and irradiated with ultraviolet light (block 39).
    At the acid stage (22a) and / or methane stage (22c) of bioreactor 22, chemicals necessary for the decomposition process are added: feed salts, trace amounts of additives, chemicals that regulate pH, thickeners, etc. Moevine, phosphoric acid, mmonium phosphate, ammonia are mainly used as soy nutrients, cobalt, nickel or olibdenum salts are used as small soybeans, and loquates (iron salts, aluminum, zvest or bentonite) are used as thickeners.
    3 1
    Undeposable waste (Fig. 4) can be fed through circulation pipe 27 back to bioreactor 22. If necessary, undecomposed waste can be supplied from blocks 23, 24 and 26 through tubes 27 and special treatment block 36, where they are subjected to special treatment with hydrolysis. and / or physical dispersion and then return through the circulation pipe 27 to the bioreactor 22.
    The gas obtained in the proposed method is used to maintain the temperature of the process.
    The proposed method can be performed within a wide temperature range: 5-65 ° C. However, the recommended range is 20-35 ° C. When operating in an elevated temperature range, the method can be carried out faster.
    The corresponding dry matter content of the process is 5-107-. In the proposed method, the required water is about 7-, depending on the amount of waste being processed. The proposed method can be further enhanced by developing a bacterial strain that is most suitable for use in the process.
    The decomposition process in the proposed method is divided into two, three or more stages. In this case, in the first stage, decomposing difficultly decomposing wastes, such as rubber, is subjected. In the second stage, the treatment is directed towards easily decomposable waste, such as paper, wood, cotton fabric, cardboard, wool, etc. The bioreactor in this case is equipped with partitions, which divide it into separate blocks in proportion to the number of stages.
    Example. Solid radioactive waste of low levels of radioactivity of the following composition: paper, mixed materials, plastic, rubber,. The wood, refractory cloth, wiping ends and cardboard are processed by the proposed method at 5-65 ° C in two or more stages by anaerobic digestion.
    As a result of the operations performed, the volume of solid radioactive waste is reduced to 5-10% of the initial
    70 () 86
    volume 1 waste, stacked l barrels. After reprocessing, the solid i.iuq-type wastes of mrenstls are a material that is in a stable state, which prevents the possibility of environmental pollution. The pre-tagging method is characterized by simplicity, relatively high pro-JQ efficiency and is effective for most of the components.
    waste. The proposed method is a closed technological process and therefore does not cause damage to the surrounding environment.
    Thanks to the proposed method, a variety of different wastes can be processed.
    The design of the bioreactor is distinguished by its simplicity, as well as the ability to process at the same time several types of solid wastes of low radioactivity that require different time required for their decomposition.
    权利要求:
    Claims (4)
    [1]
    1. An anaerobic treatment of solid radioactive waste, including pre-grinding and subsequent oxidative decomposition of waste, characterized in that, in order to ensure the environmental safety of the environment, as well as to simplify the treatment process, solid radioactive waste is suspended or hydrolyzed and / or irradiated with ultraviolet radiation, and or is heat treated and fed to a bioreactor, where anaerobic digestion is carried out in two stages — acidic and methane, and the undecomposed waste l was deposited.
    [2]
    2. A method according to claim 1, characterized in that the anaerobic digestion is carried out using urea, phosphoric acid, ammonium phosphate, ammonia, additions of cobalt salts, nickel, molybdenum, and thickeners - iron salts or aluminum, or lime, or bentonite .
    [3]
    3. The method according to claim 1, characterized in that the anaerobic digestion process is carried out in the temperature range of 5-65 ° C.
    [4]
    4. The method according to claim 3, characterized in that the anaerobic process 1 /
    eight
    -2
    eleven
    2
    ten
    "
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    同族专利:
    公开号 | 公开日
    EP0286358B1|1992-08-26|
    DE3873957D1|1992-10-01|
    DE3873957T2|1993-03-18|
    FI871550A0|1987-04-08|
    JPS63279200A|1988-11-16|
    FI871550A|1988-10-09|
    FI89581B|1993-07-15|
    FI89581C|1993-10-25|
    CA1329278C|1994-05-03|
    EP0286358A2|1988-10-12|
    US4861519A|1989-08-29|
    JPH0711596B2|1995-02-08|
    EP0286358A3|1989-01-11|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI871550A|FI89581C|1987-04-08|1987-04-08|FOERFARANDE FOER BEHANDLING AV AVFALL SOM INNEHAOLLER LAOGAKTIVA ORGANISKA AVFALLSSAMMANSAETTNINGAR FRAON KAERNKRAFTVERK MED HJAELP AV ANAEROBISK JAESNING|
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