JP6349166B2 - Operation method of radioactive cesium separation and concentration equipment - Google Patents

Description

  The present invention relates to a method for operating a radioactive cesium separation and concentration apparatus.

  In order to recover the natural environment such as soil, vegetation, sea and rivers that were contaminated with radioactive materials leaked from nuclear fission reaction equipment, etc. Various measures for concentrating these are being studied.

  Among radioactive materials, cesium 134 and cesium 137 have a low boiling point, a low melting point, are easily volatilized, and are highly water-soluble. Therefore, they have a great impact on health, and are said to be major trinuclear species together with iodine 131. In particular, cesium 137 has a long half-life of 30 years and cannot be easily decontaminated when adsorbed on soil.

  In patent document 1, only sodium chloride is added by adding an inorganic calcium compound and sodium chloride to the soil containing radioactive cesium, and heat-treating at a temperature of 1200 ° C. or less using a heating device such as a rotary kiln. Thus, a method for removing radioactive cesium that can increase the volatilization rate of radioactive cesium as compared with the case of heat treatment is disclosed.

  By adding inorganic calcium compounds to the soil, radioactive cesium is desorbed from the soil, and the desorbed radioactive cesium is combined with chlorine atoms derived from sodium chloride, so that the radioactive cesium contained in the soil is radioactive cesium chloride. As a result, it is estimated that the removal rate of about 90% of radioactive cesium is obtained.

  In Patent Document 2, combustible material contaminated with radioactive cesium is incinerated main ash containing cesium chloride by supplying sodium chloride or polyvinyl chloride, which is a chlorine compound, to the combustible material and incineration, or combustible material contaminated with radioactive cesium. Incineration main ash obtained by incineration of lime is mixed with sodium chloride or polyvinyl chloride, which is a chlorine compound, and any incineration main ash is melted above the boiling point of cesium chloride, and cesium chloride is concentrated in the molten fly ash Thus, a method for treating radioactive cesium contaminants that reduces the concentration of radioactive cesium in the molten solidified body has been proposed. According to the method for treating radioactive cesium contaminants, the fusion residual rate of radioactive cesium becomes 5%, and 95% of radioactive cesium is removed.

  In any of the above-mentioned patent documents, it is described that radioactive cesium can be effectively volatilized as radioactive cesium chloride by adding sodium chloride to a radioactive cesium contaminant and heating or melting it.

Japanese Patent No. 5175959 JP 2013-120146 A

  Patent Document 1 discloses that calcium oxide, calcium carbonate, calcium hydroxide, calcium phosphate, calcium silicate, and the like that cannot be used for cultivated land unless the soil after cesium removal is washed and desalted. Disclosed is a technique that suppresses the amount of sodium chloride added and eliminates the need for desalting after heat treatment by using at least one inorganic calcium compound selected from the group consisting of calcium cyanamide and calcium nitrate as a volatilization accelerator. Has been.

  However, when chlorine compounds such as sodium chloride are added to radioactive cesium contaminants and heat-treated, chlorine gas such as hydrogen chloride gas derived from the additive is generated in the exhaust gas, which causes corrosion of flue and exhaust gas treatment equipment. Therefore, it is necessary to provide a neutralizing agent addition mechanism that introduces a neutralizing agent such as slaked lime into the exhaust gas. If the amount of chlorine compound such as sodium chloride is increased in order to promote volatilization of cesium, neutralization is accompanied accordingly. There is a problem that the equipment cost and the drug cost necessary for the process are increased.

  In order to further increase the volatilization rate of radioactive cesium, it is necessary to increase the amount of chlorine compounds such as sodium chloride, which increases the cost of chemicals including chlorine compounds, and the amount of fly ash generated. There is a problem that a large bug filter with increased equipment cost is required due to the increase.

  Patent Document 2 discloses that incineration ash containing radioactive cesium has a preferable meltability by adjusting the basicity of 0.5 to 1.3, but a basicity adjusting agent necessary for this purpose is disclosed. In particular, in the case of soil contaminated with radioactive cesium, the composition varies greatly depending on the region, and in addition to the chemical cost for volatilizing radioactive cesium, the basicity required for melting There is also a problem that the cost of the adjusting agent greatly affects the processing cost.

  An object of the present invention is to provide a radioactive cesium separation and concentration apparatus that can further increase the volatilization rate of radioactive cesium while suppressing the amount of use of a chlorine-based auxiliary that promotes volatilization of radioactive cesium in view of the above-described problems. Is to provide a driving method.

To achieve the above object, a first characterizing feature of the method for operating the radioactive cesium separation and concentration apparatus according to the present invention, as described in claim 1., chlorine basicity adjustment aid to be treated And a basicity adjustment aid addition device for adding a basicity adjustment aid comprising a non-chlorine basicity adjustment aid , and heating a workpiece to which the basicity adjustment aid has been added to volatilize and separate radioactive cesium A method for operating a radioactive cesium separation and concentration device comprising a heating furnace and a dust collector that collects fly ash containing radioactive cesium volatilized and separated in the heating furnace, wherein the basicity of the object to be treated is The amount of the basicity adjusting aid added is determined so as to be a predetermined value, and the basicity of the object to be processed obtained in advance is the addition ratio of the chloric basicity adjusting agent and the cesium volatilization rate under the predetermined value. maximum volatilization rate of radioactive cesium is based on the relationship And basicity adjustment aid amount determination step of determining a Blend ratio of chlorine basicity adjusting aid and chlorine-basicity adjusting aid is a basic adjustment aid to fall range of the basicity A basicity adjustment step of adding a chlorine basicity adjustment aid and a non-chlorine basicity adjustment aid to the object to be treated according to the value determined in the adjustment aid addition amount determination step, and a chlorine basicity adjustment aid And a heat treatment step of heating the object to which the non-chlorine basicity adjusting aid is added in the heating furnace, and a recovery treatment step of collecting fly ash containing radioactive cesium collected by the dust collector, It is in the point to have.

  If a chlorine-based auxiliary agent is added to the object to be treated, including soil contaminated with radioactive cesium, and heat-treated, the radioactive cesium and chlorine combine to separate and volatilize from the melt as cesium chloride. Is done. The inventors of the present application have found that when a basicity adjusting aid is added to the object to be treated at this time, the skeletal structure of the slag becomes weak and cesium is easily liberated from the slag.

  Therefore, if a chlorine-based basicity adjusting aid is used as a basicity adjusting aid to be added to the object to be treated in the basicity adjusting step, it functions not only as a preferable basicity but also as a volatilization accelerator for radioactive cesium. As a result of diligent experimentation, a basicity adjustment aid and a non-chlorine basicity adjustment aid were added to the object to be treated at a predetermined addition amount and blending ratio. If added, it is possible to volatilize radioactive cesium with high efficiency in the separation process without adding a separate chlorine-based auxiliary agent such as sodium chloride, and the concentration of hydrogen chloride in the exhaust gas can be reduced. And gained new knowledge that radioactive cesium can be collected efficiently. The addition amount and blending ratio of the chloric basicity adjustment aid and the non-chlorine basicity adjustment aid are values determined in the basicity adjustment aid addition amount determination step, and the basicity adjustment aid addition amount determination step is: A step of determining the addition amount and blending ratio of the chlorine-based basicity adjusting aid and the non-chlorine-based basicity adjusting aid so that the volatilization rate of the radioactive cesium is within a predetermined range based on the test etc. It is.

In other words, the volatilization rate of radioactive cesium can be increased to the maximum even if the amount of chlorine-based auxiliary added is reduced, and the amount of chlorine-based corrosive gas generated can be reduced by reducing the amount of chlorine added, Thus, the cost of the chemicals including the neutralizing agent can be greatly reduced, the amount of fly ash generated is reduced, and there is no need to construct a large exhaust gas treatment facility. Here, basicity means not only the ratio of calcium oxide to silicon dioxide [CaO (%) / SiO ₂ (%)] but also an index expressing the basicity of the slag skeleton such as optical basicity. The optical basicity is an index found by Duffy and Ingram, and it is noted that the ultraviolet light absorption peak changes sensitively with respect to the glass composition. and an electronegativity of the cation constituting them, Ru indicator der derived based on a predetermined formula.

In the second characteristic configuration, as described in claim 2 , in addition to the first characteristic configuration described above, in the basicity adjusting auxiliary agent addition amount determining step, the treatment after adding the basicity adjusting auxiliary agent Single or multiple indicators selected from the basicity, optical basicity, chlorine concentration, basicity after heat treatment of the object to be processed, and optical basicity are within a predetermined range. The addition amount and the mixing ratio of the chlorine basicity adjusting aid and the non-chlorine basicity adjusting aid are determined.

  The basicity, optical basicity, and chlorine concentration of the processed material after the addition of basicity adjusting aid to determine the addition amount and blending ratio of chlorinated basicity adjusting aid and non-chlorine basicity adjusting aid The volatilization rate of radioactive cesium to the object to be treated can be indirectly controlled by adopting any combination of basicity, optical basicity or a plurality of indicators after the heat treatment step of the object to be treated. .

In the third feature configuration, as described in claim 3 , in addition to the first or second feature configuration described above, in the basicity adjustment assistant addition amount determination step, The composition is automatically measured and the addition amount of the basicity adjustment aid is automatically determined. In the basicity adjustment step, the chlorine-based basicity is added to the workpiece according to the addition amount determined in the basicity adjustment aid addition amount determination step. The adjustment assistant and the non-chlorine basicity adjustment assistant are automatically added.

  In the basicity adjustment aid addition amount determination step, the composition of the object to be treated is automatically measured, and based on the value, the addition amount of the basicity adjustment aid is automatically determined, and the basicity adjustment step according to the automatically determined addition amount Since the basicity adjustment aid is automatically added, the work load is greatly reduced compared to the case where the addition amount of the basicity adjustment aid is determined manually and the basicity adjustment aid is added. It is possible to increase the number of times the composition is measured for the processed material. As a result, it is possible to finely determine the amount of addition of the basicity adjustment aid to the variation in the composition of the object to be processed, and to reduce the variation in the actual volatilization rate relative to the volatilization rate of the target radioactive cesium. , Extremely stable operation is possible.

The fourth feature configuration is the chlorine-based basicity adjustment aid added in the basicity adjustment step in addition to any of the first to third feature configurations described above, as described in claim 4. Is a single substance or a plurality of substances selected from either inorganic chlorides or substances containing inorganic chlorides.

  Inorganic chlorides or substances containing inorganic chlorides can be suitably used as basicity adjustment aids, suppressing the increase in drug costs due to the use of a separate chlorine-based volatilization aid for volatilizing radioactive cesium can do.

In the fifth feature configuration, as described in claim 6 , in addition to the fourth feature configuration described above, the chlorine-based basicity adjusting aid added in the basicity adjusting step is calcium chloride, chloride. The substance is a single substance or a plurality of substances selected from sodium, potassium chloride, and iron chloride.

  Calcium chloride, sodium chloride, potassium chloride, or iron chloride can be suitably used as the chloric basicity adjusting aid.

The sixth characterizing feature of the can, as noted in the claim 6, in addition from the first described above in the fifth one of characteristic structure of, chlorine-base adjustment aid to be added in the basicity adjustment step The agent is selected from any of non-chlorine alkali metal compounds, non-chlorine alkaline earth metal compounds, non-chlorine magnesium compounds, non-chlorine boron compounds, non-chlorine iron compounds, and non-chlorine lead compounds. The point is that it is one or more substances.

  Non-chlorine basicity adjustment aids include non-chlorine alkali metal compounds, non-chlorine alkaline earth metal compounds, non-chlorine magnesium compounds, non-chlorine boron compounds, non-chlorine iron compounds, or non-chlorine lead compounds Can be suitably used.

The seventh characterizing feature of the can, as noted in the claim 7, in addition from the first described above in the sixth one characteristic feature of the, in the basicity adjustment aid amount determination step, the reducing agent is added The addition amount and the mixing ratio of the chlorine-based basicity adjusting aid and the non-chlorine basicity-adjusting aid are determined with respect to the treated object.

  If a reducing agent is added to the object to be treated, the oxide of radioactive cesium contained in the object to be treated is effectively reduced to cesium in the heat treatment process, and the reduced radioactive cesium is efficiently combined with chlorine. It shifts to cesium chloride, and the volatilization of radioactive cesium is further promoted.

The first characteristic configuration of the radioactive cesium separation and concentration apparatus according to the present invention includes a chlorine-based basicity adjusting aid and a non-chlorine-based basicity adjusting aid as described in claim 8. A basicity adjusting auxiliary addition device for adding basicity adjusting auxiliary, a heating furnace for heating and treating the object to which basicity adjusting auxiliary is added, and volatilizing and separating radioactive cesium, and volatilized and separated in the heating furnace. And a dust collector that collects fly ash containing radioactive cesium, and a radioactive cesium separation / concentration device comprising a basicity adjustment aid added so that the basicity of the object to be treated becomes a predetermined value The range in which the volatilization rate of radioactive cesium is maximized based on the relationship between the addition rate of the chlorine basicity adjusting agent and the cesium volatilization rate under the predetermined value is determined in advance. Chlorine is a basicity adjustment aid to enter Comprising a basicity adjustment aid amount determination device for determining a Blend ratio of basicity adjusting aid and non-chlorinated basicity adjustment aid, the basicity adjustment aid added device the basicity adjustment aid amount Chlorine basicity adjustment aid and nonchlorine basicity adjustment aid are added to the object to be treated according to the addition amount and blending ratio of chlorine basicity adjustment aid and nonchlorine basicity adjustment aid determined by the determination device. The point is to add.

  As described above, according to the present invention, the method of operating a radioactive cesium separation and concentration device that can increase the volatilization rate of radioactive cesium while suppressing the amount of chlorine-based auxiliary that promotes volatilization of radioactive cesium. Can now be provided.

Illustration of radioactive cesium separation and concentration (removal) equipment Flow chart of radioactive cesium separation and concentration (removal) method Illustration of the composition of the simulated soil that is the base material of the sample (A)-(c) is explanatory drawing of slag creation Explanatory drawing which shows the experimental conditions of Experimental Examples 1-22 The graph showing the result of having calculated the volatilization rate of cesium at the time of changing the kind and compounding ratio of the chloric basicity adjustment aid and the non-chlorine basicity adjustment aid in Experimental Examples 1 to 8 (A), (b) The graph which shows the volatilization rate of the chemical element in Experimental Examples 1-8 (A), (b) Explanatory drawing which photographed the state of the slag after the fusion in Experimental Examples 9-18 The graph showing the result of having calculated the volatilization rate of the cesium with respect to the addition amount of the chlorine basicity adjustment adjuvant in Experimental Examples 9-18 The graph showing the result of having calculated the volatilization rate of cesium, sodium, potassium, and chlorine with respect to the addition amount of the chlorine-based basicity adjustment aid in Experimental Examples 9 to 18 The graph showing the result of having calculated the cesium volatilization rate with respect to the addition amount of the reducing agent in Experimental Examples 12, 17, and 19-22. Explanatory drawing which shows the experimental conditions and results of Experimental Examples 23-25

  Hereinafter, embodiments of the method for separating and concentrating radioactive cesium, the apparatus for separating and concentrating radioactive cesium, and the method for operating the apparatus for separating and concentrating radioactive cesium according to the present invention will be described.

  FIG. 1 shows a radioactive cesium separation and concentration apparatus 1 according to the present invention. The radioactive cesium separation / concentration apparatus 1 is an apparatus for separating and concentrating radioactive cesium from an object to be processed containing soil contaminated with radioactive cesium, and an accepting unit 2 for collecting objects to be processed containing radioactive cesium, and an object to be processed A melting furnace 5 that volatilizes and separates radioactive cesium by heating and melting in a temperature range of 1200 ° C. to 1500 ° C., and a first dust collector 11 that collects fly ash containing radioactive cesium volatilized and separated from the object to be processed in the melting furnace 5. It has.

  A basicity adjusting auxiliary agent adding device that includes a conveying mechanism 3 that conveys the workpieces accumulated in the receiving unit 2 to the melting furnace 5 and adds a basicity adjusting aid to the workpieces conveyed by the conveying mechanism 3. 4 is installed. As a basicity adjustment aid, a chlorine-based basicity adjustment aid that also functions as an auxiliary for volatilizing radioactive cesium contained in the object to be treated is preferably used. A necessary amount of basicity adjusting aid is added.

  Basicity adjustment that determines the amount of basicity adjustment aid added by the basicity adjustment aid addition device 4, that is, the addition amount and blending ratio of the chlorine basicity adjustment aid and the non-chlorine basicity adjustment aid An auxiliary agent addition amount determination device 16 is further provided. The basicity adjustment assistant addition amount determination device 16 determines the addition amount and the mixing ratio so that the volatilization rate of radioactive cesium falls within a predetermined range with respect to the object to be processed.

  An object to be treated, which is melted in the melting furnace 5 and volatilized with radioactive cesium at a predetermined volatilization rate, is dropped as a molten slag into a cooling water tank 6 installed below, rapidly cooled to become a granulated slag, and the tank is discharged by a discharge mechanism 7. Discharged outside. The discharged slag is effectively used as industrial resources such as concrete aggregate, cement material, road pavement and the like. On the other hand, the exhaust gas generated in the melting process flows out from the flue 8 and is provided with a cooling device 9, a stripping agent adding device 10, a first dust collector 11, a neutralizing agent adding device 12, and a second arranged along the flue 8. It is discharged through a dust collector 13, a heater 14, a catalyst tower 15, and a chimney. The furnace chamber and the flue 8 of the melting furnace 5 are covered with a refractory material such as refractory bricks and refractory cement.

  The fly ash containing the radioactive cesium compound that has been cooled by the cooling device 9 and deposited in the exhaust gas is collected by the first dust collector 11, and acid gases such as hydrogen chloride gas and SOx contained in the exhaust gas are neutralized. Neutralized with slaked lime as a neutralizing agent added from the adding device 12 and collected as calcium chloride or calcium sulfide by the second dust collector 13. The first dust collector 11 and the second dust collector 13 are mainly composed of bag filters, and the release agent added from the release agent addition device 10 is applied to the filter cloth surface so that fly ash having deliquescence does not adhere firmly to the filter cloth. It is coated to ensure releasability during cleaning with a pulse jet or the like. In the case of neutralization by dry method, slaked lime is preferably used as a neutralizing agent, but sodium hydroxide (NaOH) is also used when, for example, a wet cleaning apparatus is used.

FIG. 2 shows a method for operating the radioactive cesium separation and concentration apparatus of the present invention, which is executed by the above-described radioactive cesium separation and concentration apparatus 1.
That is, the basicity adjusting auxiliary agent addition amount determining device 16 uses a basicity adjusting auxiliary agent and a non-chlorine basicity adjusting auxiliary agent so that the volatilization rate of radioactive cesium falls within a predetermined range with respect to the object to be processed. A basicity adjusting auxiliary agent addition amount determining step for predetermining the adding amount and blending ratio of the basicity adjusting auxiliary agent is executed, and the basicity adjusting auxiliary agent adding device 4 adds the basicity adjusting auxiliary agent to the workpiece. A degree adjustment step is executed, a separation step is performed in which the material to which the basicity adjustment aid is added is melted by the melting furnace 5 to volatilize and separate radioactive cesium from the molten slag, and is contained in the exhaust gas by the first dust collector 11 A collection step for collecting radioactive cesium is performed.

  The radioactive cesium contaminating the soil has a high adsorptivity to clay mineral components and the like in the soil, and once adsorbed, it is difficult to physically separate and remove it. In addition, since it is adsorbed to the soil in a strongly bonded state, it is difficult to volatilize and separate even if heated as it is.

  Conventionally, by adding a chlorine-based auxiliary agent such as sodium chloride as a volatilization accelerator to the object to be treated so that cesium is easily volatilized during heat treatment, it is combined with radioactive cesium and transferred to cesium chloride having a low boiling point. Although the method was adopted, hydrogen chloride gas, which is a corrosive gas derived from sodium chloride, is generated in large amounts by heat treatment, so the amount of neutralizing agent added to the exhaust gas increases, leading to an increase in drug cost, There has been a problem in that the equipment cost is increased due to the construction of a large bag filter for increasing the amount of fly ash.

  In addition, sodium chloride whose boiling point is close to the melting temperature tends to volatilize before combining with cesium, and the amount of hydrogen chloride gas generated tends to increase, so that further improvement can be achieved from the viewpoint of efficiently volatilizing cesium. There was room.

  By the way, when the basicity adjusting aid is added to the object to be treated when the chlorine-based assistant is added and the object to be treated is heated and melted, the slag skeleton structure becomes weak and cesium is easily released from the slag.

  Therefore, by using a chlorine-based basicity adjustment aid as a basicity adjustment aid added to the object to be treated in the basicity adjustment step, not only adjustment to a preferable basicity but also a volatilization accelerator for radioactive cesium It is possible to function, and even without adding a chlorine-based auxiliary agent such as sodium chloride, the radioactive cesium can be volatilized with high efficiency in the separation process, and the radioactive cesium can be efficiently collected in the collection process. Become. That is, the chlorine-based basicity adjustment aid is a high-functionality basicity adjustment aid that has both functions of adjusting basicity and promoting volatilization by chlorine.

  In addition, by adding a non-chlorine basicity adjustment aid in addition to a chlorine-based basicity adjustment aid when adjusting the basicity, while reducing the amount of chlorine to be added, while suppressing the generation of hydrogen chloride gas However, the volatilization rate of radioactive cesium can be further increased. In particular, it is useful when the volatilization rate of radioactive cesium is improved under conditions where the amount and basicity of the basicity adjusting aid added to the object to be processed are substantially constant.

  Specifically, in the basicity adjustment aid addition amount determination step, the addition amount and the blending ratio of the chlorine-based basicity adjustment aid and the non-chlorine-based basicity adjustment aid are varied with respect to a small amount of the object to be processed. Component analysis of the slag obtained by heating and melting the test sample with a test device is performed, and the volatilization rate of radioactive cesium may be within a predetermined range (here, both the lower limit value and the upper limit value, or only the lower limit value) The amount of addition and the mixing ratio may be determined.

  The addition rate of the basicity adjusting aid correlates with the volatilization rate of the radioactive cesium, that is, the decrease rate of the radioactive material before and after the heat treatment. The amount of radioactive material in the material to be treated varies depending on the region and the type of solid matter. For example, the concentration is below the legally usable value or below the disposable value, or below the voluntary regulated usable value or at the disposal. The target value of volatilization rate may be calculated according to the region and the type of solid matter so that it is below the value. Chlorine basicity adjustment aid and non-chlorine basicity adjustment aid so that the value can be achieved. What is necessary is just to determine the addition amount and compounding ratio of an agent.

If the basicity of the object to be treated as the soil (CaO (wt%) / SiO 2 _(wt%)) is low, by adding a base adjustment aid to be treated, the radioactive from molten slag The separation efficiency of cesium can be improved. Incidentally, the general soil basicity (CaO (wt%) / SiO ₂ (wt%)) is about 0.03 to 0.1, the optical basicity of the soil is about 0.50 to 0.52 .

When the basicity of the object to be treated (CaO (wt%) / SiO ₂ (wt%)) is low, strong binding of the skeletal structure composed slug cation binding SiO ₂ as the main component, combined with the skeletal structure Strong binding strength with cesium. Therefore, even if the chlorine component tries to combine with cesium, cesium cannot leave the skeletal structure, the bond between chlorine and cesium is inhibited, and as a result, there is a strong tendency for radioactive cesium to remain in the molten slag.

  Even in such a case, the basicity of the slag is increased by adding the basicity adjusting aid. The workpiece is melted at a lower temperature and the fluidity is increased. That is, the bond of the slag skeleton structure is weakened, and cesium is easily separated from the slag skeleton structure. This is because the chlorine and radioactive cesium contained in the added chlorine-based basicity adjusting aid increase the chance of ionic bonding and promote the reaction to transfer to cesium chloride. Therefore, volatilization of radioactive cesium is promoted.

Simple binary basicity as basicity (CaO (wt%) / SiO 2 _(wt%)) and has been described the case of using as an index, basicity has also various definitions in addition to this, waste Society It is disclosed in the journal (Vol.19, No19, pp17-25,2008). For example, some are represented by a plurality of components as shown in the following formula.
(CaO + MgO + Fe ₂ O ₃ + K ₂ O + Na ₂ O) / (SiO ₂ + Al ₂ O ₃ )

  Optical basicity is a basicity that can greatly increase the number of components that can be handled and can take into account almost all oxides, so it is commonly used for solids to be processed having various compositions. It is a possible basicity index.

  Optical basicity is an index found by Duffy and Ingram, focusing on the fact that the ultraviolet light absorption peak changes sensitively with respect to the glass composition. Is an index that is derived from the electronegativity of the cation constituting s based on the following formula.

Optical basicity Λ = 1−Σ (zi · ri / 2) · (1-1 / γi)
However, γi = 1.36 (χi−0.26)
Here, zi is the valence of the i-type cation, ri is the number of the i-type cation expressed per oxygen, and χi is the electronegativity of the i-type cation.

  The basicity increases in the same manner regardless of whether a chlorine-based or non-chlorine-based basicity adjusting aid is added. Therefore, the addition ratio of both chlorine and non-chlorine is adjusted using the chlorine concentration of the object to be treated as an index. Even if the basicity is the same value, the higher the chlorine concentration, the higher the ratio of the chloric basicity adjusting aid, and the lower the chlorine concentration, the higher the ratio of the non-chlorine basicity adjusting aid.

  In other words, the basicity, optical basicity, chlorine concentration, basicity after the heat treatment step of the object to be processed, and optical basicity are selected from the basicity of the object to be processed after the addition of the basicity adjusting aid. Alternatively, it is also possible to determine the addition amount and the blending ratio of the chlorine-based basicity adjusting aid and the non-chlorine basicity-adjusting aid so that a plurality of indices fall within a predetermined range.

  As the chloric basicity adjusting aid, it is preferable to employ a single substance or a plurality of substances selected from either inorganic chlorides or substances containing inorganic chlorides, such as calcium chloride, sodium chloride, potassium chloride, chloride. It is more preferable to employ a single substance or a plurality of substances selected from any one of iron, and calcium chloride or the like is preferably used as a high boiling point chloride, and calcium chloride or the like recovered by the second dust collector 13 is preferably used. It is also possible to use fly ash containing fly ash or calcium ash generated in a garbage incinerator.

  Non-chlorine basicity adjustment aids include non-chlorine alkali metal compounds, non-chlorine alkaline earth metal compounds, non-chlorine magnesium compounds, non-chlorine boron compounds, non-chlorine iron compounds, and non-chlorine lead compounds. A single substance or a plurality of substances selected from any of the above can be suitably used.

  In particular, calcium oxide, calcium hydroxide, calcium carbonate, sodium carbonate, lithium carbonate, potassium carbonate, magnesium carbonate, magnesium hydroxide, magnesium oxide, boron oxide, borax, boric acid, ferrous oxide, triiron tetroxide, A single substance or a plurality of substances selected from any one of ferric oxide, lead monoxide, lead dioxide and the like are preferably used.

  It is preferable that the basicity of the object to be treated after adding the chlorine-based basicity adjusting aid and the non-chlorine-based basicity adjusting aid added in the basicity adjusting step is substantially constant, and the basicity is made substantially constant. As long as it is maintained, the volatilization rate of radioactive cesium due to the weakening of the slag skeleton may be changed even if the type and addition ratio of the chlorine-based basicity adjusting aid or non-chlorine-based basicity adjusting aid added in the basicity adjusting step are changed. The effect of rising is always obtained. In particular, in the case of a combination of a chlorine basicity adjustment aid and a non-chlorine basicity adjustment aid of the same element, adjustment can be made without changing the basicity by changing the addition ratio in molar ratio It becomes. In addition, in order to improve the controllability of the addition amount of the basicity adjusting aid, it is possible to use a basicity adjusting aid by mixing a substance having no basicity adjusting effect. It is also possible to change the volatilization rate of radioactive cesium by changing the amount of chlorine (addition ratio of chlorine-based basicity adjusting aid and non-chlorine-based basicity adjusting aid) under the condition of constant basicity. Is possible. Even if the amount of chlorine is reduced, the volatilization rate of radioactive cesium may increase, and there is an addition ratio that maximizes the volatilization rate of radioactive cesium.

  It is preferable that the chlorine-based basicity adjusting aid added in the basicity adjusting step is calcium chloride and the non-chlorine-based basicity adjusting aid is calcium hydroxide, for a wide area of soil contaminated with radioactive cesium. In addition, it is possible to separate and remove radioactive cesium suitably, and when calcium chloride is used as a chlorine-based basicity adjustment aid added in the basicity adjustment step, basicity can be adjusted effectively and the volatilization rate of radioactive cesium can be increased. If calcium hydroxide is used as a non-chlorine basicity adjusting aid, basicity can be effectively adjusted instead of calcium chloride.

  When calcium chloride is used as the chlorine-based basicity adjusting aid and calcium hydroxide is used as the non-chlorine basicity-adjusting aid, the calcium chloride is used in an amount of 30% to 50% of the total amount of the chlorine-based basicity adjusting aid. While adding at a percentage by weight, and adjusting the addition ratio of the basicity adjustment aid to the soil to be treated as a whole from 30% to 45% by weight, while suppressing the generation of chlorine-based gas Radiocesium can be volatilized at a high volatilization rate.

  In the basicity adjusting auxiliary agent addition amount determining step, the addition amount and the mixing ratio of the chlorine basicity adjusting auxiliary agent and the non-chlorine basicity adjusting auxiliary agent are determined with respect to the object to which the reducing agent is added. It is preferable. If a reducing agent is added to the object to be treated, the oxide of radioactive cesium contained in the object to be treated is effectively reduced to cesium in the heat treatment process, and the reduced radioactive cesium is efficiently combined with chlorine. It shifts to cesium chloride, and the volatilization of radioactive cesium is further promoted.

  What is necessary is just to provide the reducing agent addition apparatus which calculates | requires the preferable addition amount of a reducing agent in a basicity adjustment adjuvant addition amount determination process, and adds a reducing agent to the to-be-processed object thrown into a melting furnace. As the reducing agent, a single substance or a plurality of substances selected from activated carbon, graphite, carbon black, coke, charcoal, plastic, vegetation, and sewage sludge are preferably used. Since sewage sludge contains a carbon component obtained by decomposing organic matter by biological treatment, it can be suitably used as a reducing agent. In addition, if waste plastic is used among plastics, economical efficiency will improve and it will be used more suitably.

  The basicity adjusting auxiliary agent addition amount determination device 16 includes a test furnace and a component analysis device for slag melted in the test furnace. Further, a predetermined amount of base is obtained by quantitatively sampling the object to be processed received in the receiving unit 2. A degree-adjusting assistant, preferably a reducing agent, is automatically added, melted in a test furnace, and the components of the obtained slag are analyzed to determine the preferred basicity-adjusting assistant addition amount and chlorine-based and non-chlorine-based It is preferable to include a control device that automatically determines the addition ratio of and outputs the determined addition amount and addition ratio to the basicity adjusting aid adding device 4.

  As described above, the method for separating and concentrating radioactive cesium according to the present invention is a method for separating and concentrating radioactive cesium contained in an object to be treated including soil by heat treatment, and is at least a chlorine-based basicity adjustment aid. A basicity adjustment step of adding a basicity adjusting aid containing an agent to the object to be treated, and heating the object to which the basicity adjusting aid is added from 1200 ° C. to 1500 ° C. to remove radioactive cesium from the object to be treated It is in the point including the separation process which volatilizes and separates, and the collection process which collects the radioactive cesium volatilized and separated by the said separation process.

  The basicity adjustment step is a step of blending a chlorine basicity adjustment aid and a non-chlorine basicity adjustment aid at a predetermined addition ratio, and the predetermined addition ratio is the object to be treated in the separation step. Although it is preferable that it is a value determined based on the volatilization rate of the radioactive cesium volatilized from, it is preferable to use a chlorine basicity adjustment aid as at least a basicity adjustment aid.

  The addition ratio of the chlorine-based basicity adjusting aid and the non-chlorine-based basicity adjusting aid added in the basicity adjusting step is 25% by weight to 85% by weight of the basic basicity adjusting aid. It is preferable to suppress the generation amount of chlorine-based corrosive gas contained in the exhaust gas while increasing the volatilization rate of radioactive cesium rather than using a chlorine-based basicity adjusting aid alone. become able to.

The addition ratio of the chlorine basicity adjusting aid and the non-chlorine basicity adjusting aid is a value determined to be 0.6 or more when the optical basicity of the object to be processed is used as an index. It is preferable that the two-component basicity CaO (wt%) / SiO ₂ (wt%) is used as an index, and it is preferably determined to be 0.7 or more. It will never be done. Further, when optical basicity is used as an index, it is more preferable to determine the optical basicity to be 0.61 or more and 0.68 or less. When the two-component basicity CaO (% by weight) / SiO ₂ (% by weight) is used as an index, it is more preferably determined to be 0.8 or more and 1.6 or less.

  Further, the addition ratio of the basicity adjusting aid added in the basicity adjusting step is preferably 25% by weight to 50% by weight, and preferably 30% by weight to 50% by weight with respect to the object to be processed. Further preferred. If such a value is employ | adopted, the usage-amount of basicity adjustment adjuvant can be adjusted to an appropriate quantity, raising the volatilization rate of radioactive cesium.

  Furthermore, the predetermined addition ratio is preferably a value determined such that the volatilization rate of radioactive cesium volatilized from the object to be processed in the separation step is 99% or more. If the volatilization rate of radioactive cesium is 99% or more, the radiation dose remaining on the object to be treated after the separation step is adjusted to an allowable value, for example, a value allowable as general waste.

  Even if the object to be processed is contaminated to a high concentration containing a radioactive substance of 5000 Bq / kg or more, radioactive cesium is efficiently separated and concentrated, so that the radioactive material remaining on the object to be processed after the separation step The amount of the substance is adjusted to an allowable value, for example, a value that can be used effectively as a civil engineering material, or, for example, the remaining radioactive material is 100 Bq / kg (clearance level) or less, and the object to be treated is treated as containing no radioactive material. Will be able to.

  Furthermore, if the volatilization rate of radioactive cesium is 99% or more, even if the radioactive material contained in the object to be processed is 10000 Bq / kg, the radioactive material after treatment becomes 100 Bq / kg (clearance level) or less and the object to be processed Can be treated as containing no radioactive material. In the above-described embodiment, an example has been described in which a chlorine-based basicity adjustment aid and a non-chlorine basicity-adjustment aid are collectively added to a workpiece using the same apparatus. The agent and the non-chlorine basicity adjusting aid may be added separately in different apparatuses.

  In the flue 8, a part of the radioactive cesium volatilized with a decrease in the temperature of the exhaust gas may be deposited and penetrate into the refractory. As described above, since the flue 8 is covered with a refractory material such as refractory bricks or refractory cement, it is also possible to pulverize the refractory material contaminated during the refractory maintenance and to treat it as a material to be treated. is there.

  In the above-described embodiment, the type of the melting furnace as the heating furnace has been described without limitation, but any of a fuel type, an electric type, a continuous type, and a batch type may be used as long as it can be heated to a necessary temperature. For example, any type such as a rotary surface melting furnace, a fixed surface melting furnace, a shaft melting furnace, a kiln melting furnace, an electric melting furnace, a high-frequency furnace, a plasma melting furnace, and the like may be used.

  In addition, the rotary surface melting furnace can stably treat even sewage sludge containing various combustible materials, various biomass, etc., and the combustible material can be used as an auxiliary fuel. Format. Moreover, as long as sufficient heating is performed as a heating furnace, not only a melting furnace but any type may be used.

  In the above description, the present invention has been described for an object to be treated including soil. However, the method for separating and concentrating radioactive cesium according to the present invention is not limited to soil, but includes sewage sludge, straw sludge, general waste, industrial waste, agriculture. It can be applied to a mixture of a single substance or a plurality of substances selected from a biomass, a woody biomass, a herbaceous biomass, or a residue from incineration thereof, and soil, and is the above-described object to be treated excluding soil. Is also applicable.

  Each of the above-described embodiments is an example of the present invention, and the present invention is not limited by the description, and the specific configuration of each part can be appropriately changed and designed within the range where the effects of the present invention are exhibited. Needless to say.

An experimental example will be described below. In the following experimental examples, “%” excluding the volatilization rate means “% by weight”.
In this experiment, simulated soil was used as the base material of the sample. This simulated soil is a mixture of 99.5% pure sand (sand component) and 0.5% cesium carbonate (Cs ₂ CO ₃ ) reagent (base material A) and soil (mass sand and bentonite in a weight ratio of 85: 15) and 70% of sewage sludge incineration ash (combustible component) 29% and cesium carbonate (Cs ₂ CO ₃ ) reagent 1% (base material B). FIG. 3 shows the compositions of the substrates A and B.

A sample is prepared by adding CaCl ₂ or NaCl as a chlorine-based basicity adjusting aid and Ca (OH) ₂ or Na ₂ CO ₃ as a non-chlorine basicity adjusting aid to the base material, and adding the added drug type and the added drug. The following experiment was conducted by changing the ratio and the conditions for maximizing the volatilization rate of radioactive cesium.

  As shown in FIGS. 4 (a), 4 (b), and 4 (c), the test method is such that a test piece is filled on one end side of a boat-shaped magnetic boat, and the magnetic boat is set so that the filling portion faces upward. With the angle inclined, the slag was left standing in an electric furnace under natural convection maintained at a predetermined temperature for a predetermined time (15 minutes), allowed to cool naturally, and slag was separated from the magnetic boat. The slag weight and element-containing concentration were analyzed, and the volatilization rate of each element was calculated. Further, in some experimental examples shown below, the state of slag was confirmed.

(Experimental Examples 1-8)
(Examination of the effect of chlorinated basicity adjusting aid and non-chlorine basicity adjusting aid depending on the type of drug)
As a chlorine-based basicity adjusting aid, a Ca-based chlorine-based basicity adjusting aid (CaCl ₂ ) and a Na-based chlorine-based basicity adjusting aid (NaCl) are used as non-chlorine-based basicity adjusting aids. Chlorine basicity adjusting aid (Ca (OH) ₂ ) and Na non-chlorine basicity adjusting aid (Na ₂ CO ₃ ) were used. The blending ratio of the chlorine-based basicity adjusting aid and the non-chlorine-based basicity adjusting aid is 15% of the non-chlorine basicity adjusting aid with respect to the entire composition including the base material and the basicity adjusting aid. Then, a chlorine basicity adjusting aid was blended so as to be 10% or 20%. A base material A is used as a treatment target, and the total of chlorine-based basicity adjustment aid and non-chlorine basicity-adjustment aid is 25% with respect to 75% of the treatment target, and 1350 ° C. And melted. The blending conditions are as shown in FIG. As shown in 1-8.

  FIG. 6 is a graph showing the results of calculating the cesium volatilization rate when the types and blending ratios of the chlorine basicity adjusting aid and the non-chlorine basicity adjusting aid are changed. In FIG. 6, the horizontal axis represents a combination of a chlorine-based basicity adjusting aid and a non-chlorine-based basicity adjusting aid as the type of basicity adjusting aid, and the vertical axis represents the cesium volatilization rate (%). In addition, the bar graph shows the cesium content due to the difference in the blending ratio of the chlorine basicity adjustment aid and the nonchlorine basicity adjustment aid for each combination of the chlorine basicity adjustment aid and the nonchlorine basicity adjustment aid. It represents the volatilization rate (%).

  In addition, the volatilization rate of cesium was calculated | required from the following formula. The volatilization rates of other elements were determined in the same manner. Cesium volatilization rate = 100 × {1− (weight of slag × concentration containing cesium in slag) / (weight of sample × concentration containing cesium in sample)}

From FIG. 6, as the chlorine-based basicity adjusting aid and the non-chlorine-based basicity adjusting aid, those using CaCl ₂ and Ca (OH) ₂ are most excellent in cesium volatilization rate (%), and then CaCl ₂ And Na ₂ CO ₃ and those using NaCl and Ca (OH) ₂ are almost equally excellent in cesium volatility (%), followed by using NaCl and Na ₂ CO _3. Recognize. From these results, it was found that as the chlorine-based basicity adjusting aid and the non-chlorine basicity-adjusting aid, it is better to use calcium-based compounds in terms of volatilization rate (%) of cesium.

  In FIG. 7A, 10% of the chlorine-based basicity adjusting aid is blended with respect to 15% of the non-chlorine basicity adjusting aid with respect to the entire composition including the base material and the basicity adjusting aid. In this case, FIG. 7 (b) is a graph showing the volatilization rate of the drug element when 20% of the chlorine-based basicity adjustment aid is blended with 15% of the non-chlorine basicity-adjustment aid. 7 (a) and (b), the horizontal axis represents the combination of a chlorine basicity adjusting aid and a non-chlorine basicity adjusting aid as the type of basicity adjusting aid, and the vertical axis represents the drug element. Indicates the volatilization rate (%). Moreover, the bar graph represents the volatilization rate (%) of Ca and Na with respect to the combination of each chlorine basicity adjusting aid and non-chlorine basicity adjusting aid.

7 (a) and 7 (b), the volatilization rate of Ca is small and the volatilization rate of Na is 30% to 72% in any combination of the chlorine-based basicity adjusting aid and the non-chlorine-based basicity adjusting aid. It can be seen that it is big. The boiling points of CaCl ₂ and NaCl are 1935 ° C. and 1413 ° C., respectively. The boiling point of NaCl is about 500 ° C. lower than the boiling point of CaCl ₂ and is close to the melting temperature. Therefore, NaCl is a saturated vapor at the melting temperature. This is probably because the pressure was high and it did not react with cesium and volatilized as it was.

(Experimental Examples 9 to 18)
(Examination of the effect of blending ratio of chlorine-based basicity adjusting aid and non-chlorine-based basicity adjusting aid)
CaCl ₂ was used as a chloric basicity adjusting aid, and Ca (OH) ₂ was used as a non-chlorine basicity adjusting aid. The mixing ratio of the chlorine-based basicity adjusting aid and the non-chlorine basicity-adjusting aid is such that the chlorine-based basicity adjusting aid and the non-chlorine base are mixed with respect to the entire composition including the base material and the basicity adjusting aid. The chlorine-based basicity adjusting aid was mixed from 0% to 35% with respect to the total amount of the degree adjusting aid of 35% and 40%. The base material B is used as the treatment object, and the total of the chlorine-based basicity adjustment aid and the non-chlorine-based basicity adjustment aid is 35% and 40% with respect to the treatment object of 65% and 60%. Blended and melted at 1400 ° C. The blending conditions are as shown in FIG. As shown in 9-18.

  In Experimental Examples 9 to 18, the state of the slag after melting was visually confirmed. 8A and 8B are photographs showing the state of the slag after melting. FIG. 8A shows the state of the slag after melting in Experimental Examples 9 to 13, and FIG. 8B shows the state of the slag after melting in Experimental Examples 14 to 18. Moreover, the part surrounded by the white circle in the photograph of each slag has shown the slag after melting. In the experimental examples (experimental examples 9 to 11 and 14 to 16) in which the concentration of calcium chloride added was 20% or more, white particles of calcium chloride were observed on the surface. This is considered that when the addition concentration of calcium chloride is high, a part of calcium chloride cannot be formed as a uniform slag melt phase with the object to be processed and is released as a calcium chloride melt phase.

FIG. 9 is a graph showing the results of calculating the cesium volatilization rate with respect to the addition amount of the chlorine-based basicity adjusting aid in Experimental Examples 9 to 18. From FIG. 9, when the addition amount of CaCl ₂ which is a chlorine-based basicity adjusting aid is 15%, the volatilization rate of cesium is maximized, and the volatilization rate of cesium when the total basicity adjusting aid is 35% is It can be seen that the cesium volatilization rate is 99.96% when 99.80% and the basicity adjusting aid total is 40%. If the total basicity adjusting aid is the same, the basicity is considered to be approximately the same value. In this case, it has been found that the volatilization rate of cesium does not increase according to the addition amount of the chloric basicity adjusting aid.

10A and 10B are graphs showing the results of calculating the volatilization rates of cesium, sodium, potassium, and chlorine with respect to the addition amount of the chlorine-based basicity adjusting aid in Experimental Examples 9-18. FIG. 10A shows the volatilization rate of each element when 35% of the basicity adjusting aid is added, and FIG. 10B shows the volatilization rate of each element when the basicity adjustment of 40% is added. 10 (a) and 10 (b), it can be seen that the volatilization rate of sodium and potassium shows the same tendency as the volatilization rate of cesium. Moreover, the volatilization rate of chlorine was found to be lower as the additive concentration of CaCl ₂ was lower, and the ratio of incorporation into slag was higher. These results are in agreement with the results of the photographs showing the slag state described above. That is, it is considered that the liberated calcium chloride melt phase did not react with cesium and conversely inhibited the volatilization of cesium.

  From the above results, when the basicity adjustment aid is the same amount or the basicity of the object containing the basicity adjustment aid is substantially constant, the greater the amount of chlorine-based basicity adjustment aid, that is, the amount of chlorine added. It can be seen that the volatilization rate of cesium does not increase. In addition, by adjusting the addition ratio of the addition amount of the chlorine-based basicity adjustment aid and the addition amount of the non-chlorine basicity adjustment aid, there may be an addition ratio at which the volatilization rate of cesium becomes a maximum value. Recognize.

(Experimental Examples 19-22)
(Examination of the effect of reducing agent addition)
CaCl ₂ was used as a chloric basicity adjusting aid, and Ca (OH) ₂ was used as a non-chlorine basicity adjusting aid. The addition ratio of the reducing agent was set to 40% and 50% of the entire object to be processed including the combustible component and the basicity adjusting aid. The blending ratio of the chloric basicity adjusting aid and the non-chlorine basicity adjusting aid to the entire composition including the base material, the basicity adjusting aid and the reducing agent, A total of 35% of chlorine-based basicity adjusting aids, 15% of chlorine-based basicity adjusting aids and 20% of non-chlorine basicity-adjusting aids, and chlorine-based basicity adjusting aids The base B is mixed with 15% chlorine basicity adjustment aid and 25% nonchlorine basicity adjustment aid to the total amount of nonchlorine basicity adjustment aid of 40%. And melted at 1400 ° C. The blending conditions are as shown in FIG. As shown in 19-22.

FIG. 11 is a graph showing the results of calculating the volatilization rate of cesium with respect to the added amount of the chloric basicity adjusting aid in Experimental Examples 12, 17, and 19-22. FIG. 11 shows that the greater the amount of reducing agent added, the higher the cesium volatilization rate. In particular, in the case of Experimental Example 22 in which a treatment object containing 50% of the reducing agent is added to the soil and 40% of the basicity adjusting aid is added, the cesium volatilization rate reaches 99.99%. It was.
From the above results, it was found that the volatilization rate of cesium can be increased by appropriately adjusting the addition conditions of the chlorine basicity adjusting aid and the addition ratio of the reducing agent.

(Experimental Examples 23 to 25)
(Experiment using plant)
Using the apparatus of FIG. 1, the cesium volatilization rate and the HCl concentration in the exhaust gas were measured. The treatment object as shown in FIG. 12 is blended with CaCl ₂ as a chloric basicity adjusting aid and Ca (OH) ₂ as a non-chlorine basicity adjusting aid at a blending ratio shown in FIG. went. The cesium volatilization rate of the slag after the treatment and the HCL concentration in the exhaust gas were measured. The HCL concentration was measured at the entrance of the second dust collector 13. The results are shown in FIG.

  From FIG. 12, in Experimental Example 23 not including the non-chlorine basicity adjusting aid, the volatilization rate of cesium was as low as 96.7%, and the HCL concentration in the exhaust gas was as high as 8,200 ppm. It can be seen that as the addition ratio of the non-chlorine basicity adjusting aid increases, the cesium volatilization rate increases and the HCL concentration in the exhaust gas also decreases.

  In Experimental Example 25, which is the same condition as Experimental Example 22 in which the highest cesium volatilization rate is obtained in Experimental Examples 9 to 22, the cesium volatilization rate is as high as 99.9%, and the HCL concentration in the exhaust gas is also high. It was found that the result similar to the experimental result in the laboratory can be obtained in the experiment using the plant at a low concentration of 1,900 ppm.

Further, the optical basicity and binary basicity (CaO (%) / SiO ₂ (%)) of the slag of Experimental Example 25 having a high cesium volatilization rate are the preferable optical basicity and binary basicity (CaO (CaO) in the present invention. (%) / SiO ₂ (%)).

Therefore, if a small amount of processing object is used and a chlorine-based basicity adjusting aid and a non-chlorine basicity-adjusting aid are added at a predetermined addition ratio determined in advance, the plant is used for the same conditions. It was found that cesium can be separated and concentrated.

1: Radiocesium separation and concentration device 2: Receiving unit 3: Conveying mechanism 4: Basicity adjusting auxiliary agent adding device 5: Melting furnace 6: Cooling water tank 7: Discharging mechanism 8: Flue 9: Cooling device 10: Stripping agent adding device 11: 1st dust collector 12: Neutralizer addition device 13: 2nd dust collector 14: Heater 15: Catalyst tower 16: Basicity adjustment auxiliary agent addition amount determination device

Claims (8)

Basicity adjusting auxiliary agent adding device for adding basicity adjusting auxiliary consisting of chlorine-based basicity adjusting auxiliary and non-chlorine basicity adjusting auxiliary to the object to be processed, and processing to which basicity adjusting auxiliary is added A heating furnace for volatilizing and separating radioactive cesium by heating an object, and a dust collector for collecting fly ash containing radioactive cesium that has been volatilized and separated in the heating furnace, and a method of operating a radioactive cesium separation and concentration device comprising: Because
The amount of basicity adjusting aid added is determined so that the basicity of the object to be processed becomes a predetermined value, and the basicity of the chlorine-based basicity adjusting agent is added under the condition that the basicity of the object to be processed is determined in advance. distribution ratio and cesium volatilization rate and chlorine basicity adjustment aid volatilization rate of radioactive cesium is basic adjustment aid to fall within the range of maximum based on the relationship of the chlorine-base adjustment aid A basicity adjusting auxiliary agent addition amount determining step for determining a combined ratio;
In accordance with the value determined in the basicity adjustment aid addition amount determination step, a basicity adjustment step of adding a chlorine-based basicity adjustment aid and a non-chlorine-based basicity adjustment aid to the workpiece,
A heat treatment step of heating the object to which the chlorine-based basicity adjusting aid and the non-chlorine basicity adjusting aid are added in the heating furnace;
A recovery process for recovering fly ash containing radioactive cesium collected by the dust collector;
The operation method of the radioactive cesium separation concentration apparatus provided with this. In the basicity adjustment aid addition amount determination step, the basicity, optical basicity, chlorine concentration, basicity after the heat treatment step of the treatment object, optical base Claims where the addition amount and the blending ratio of the chlorine-based basicity adjustment aid and the non-chlorine basicity-adjustment aid are determined so that one or a plurality of indices selected from any of the degrees falls within a predetermined range Item 3. A method for operating the radioactive cesium separation and concentration apparatus according to Item 1 . In the basicity adjustment aid addition amount determination step, the composition of the object to be processed is automatically measured to automatically determine the addition amount of the basicity adjustment aid, and in the basicity adjustment step, the basicity adjustment aid addition amount determination. The operation method of the radioactive cesium separation and concentration apparatus according to claim 1 or 2 , wherein the chlorine-based basicity adjusting aid and the non-chlorine-based basicity adjusting aid are automatically added to the object to be treated according to the addition amount determined in the process. Chlorine basicity adjustment aid is added in the basicity adjustment step, claim 1 is a single or a plurality of substances selected from any material that inorganic chlorides or inorganic chlorides contained in the 3 The operation method of the radioactive cesium separation concentration apparatus in any one. Chlorine basicity adjustment aid is added in the basicity adjustment step, calcium chloride, sodium chloride, potassium chloride, as set forth in claim 4 is a single or a plurality of substances selected from one of iron chloride Operation method of radioactive cesium separation and concentration equipment. Non-chlorine basicity adjusting aids added in the basicity adjusting step include non-chlorine alkali metal compounds, non-chlorine alkaline earth metal compounds, non-chlorine magnesium compounds, non-chlorine boron compounds, and non-chlorine compounds. The method for operating a radioactive cesium separation and concentration apparatus according to any one of claims 1 to 5 , wherein the substance is a single substance or a plurality of substances selected from any one of an iron compound and a non-chlorine lead compound. In the basicity adjustment aid addition amount determination step, the addition amount and the blending ratio of the chlorine basicity adjustment aid and the non-chlorine basicity adjustment aid are determined with respect to the object to which the reducing agent is added. A method for operating the radioactive cesium separation and concentration apparatus according to any one of claims 1 to 6 . Basicity adjusting auxiliary agent adding device for adding basicity adjusting auxiliary consisting of chlorine-based basicity adjusting auxiliary and non-chlorine basicity adjusting auxiliary to the object to be processed, and processing to which basicity adjusting auxiliary is added A radioactive cesium separation and concentration device comprising a heating furnace that volatilizes and separates radioactive cesium by heating an object, and a dust collector that collects fly ash containing radioactive cesium that has been volatilized and separated in the heating furnace. ,
The amount of basicity adjusting aid added is determined so that the basicity of the object to be processed is a predetermined value, and the basicity of the chlorine-based basicity adjusting agent is added when the basicity of the object to be processed is determined in advance distribution ratio and cesium volatilization rate and chlorine basicity adjustment aid volatilization rate of radioactive cesium is basic adjustment aid to fall within the range of maximum based on the relationship of the chlorine-base adjustment aid Equipped with a basicity adjusting auxiliary agent addition amount determining device for determining the total proportion,
The basicity adjusting auxiliary agent adding device is an object to be processed according to the addition amount and the mixing ratio of the chlorine basicity adjusting auxiliary agent and the non-chlorine basicity adjusting auxiliary agent determined by the basicity adjusting auxiliary agent addition amount determining device. Adding a chlorine-based basicity adjusting aid and a non-chlorine-based basicity adjusting aid,
Radioactive cesium separation and concentration equipment.