JP2017116468A - Decontamination method for iron containing radioactive cesium - Google Patents

Decontamination method for iron containing radioactive cesium Download PDF

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JP2017116468A
JP2017116468A JP2015254178A JP2015254178A JP2017116468A JP 2017116468 A JP2017116468 A JP 2017116468A JP 2015254178 A JP2015254178 A JP 2015254178A JP 2015254178 A JP2015254178 A JP 2015254178A JP 2017116468 A JP2017116468 A JP 2017116468A
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radioactive cesium
iron
furnace
cesium
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JP6524532B2 (en
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哲一 木下
Tetsuichi Kinoshita
哲一 木下
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Shimizu Construction Co Ltd
Shimizu Corp
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Abstract

PROBLEM TO BE SOLVED: To provide a decontamination method for iron containing radioactive cesium, allowing the radioactive cesium to be separated from the iron.SOLUTION: [1] The decontamination method for iron containing radioactive cesium is provided in which an iron material containing the radioactive cesium is mixed with coke and heated in a furnace, the radioactive cesium is vaporized from steel slag melted in the furnace under a reduction atmosphere, and the radioactive cesium exhausted to the outside of the furnace is cooled and collected. [2] The decontamination method for iron containing radioactive cesium is provided which is identical to the method described in the [1] except that coal is charged into the furnace and heated. [3] The decontamination method for iron containing radioactive cesium is provided which is identical to the method described in the [1] or [2] except that a temperature in the furnace is 1500°C or higher. [4] The decontamination method for iron containing radioactive cesium is provided which is identical to the method described in any of [1] to [3] except that 20-30 pts.mass of the coke is mixed with 100 pts.mass of the iron material.SELECTED DRAWING: None

Description

本発明は、放射性セシウムを含む鉄の浄化方法に関する。   The present invention relates to a method for purifying iron containing radioactive cesium.

原子力発電所で発生した汚染水には放射性セシウムが含まれている。汚染水に対する現行の対応として、汚染水を一時的に鉄製のタンク内に貯蔵している。汚染水を処理した後には、内壁面に放射性セシウムが付着した鉄製タンクが残される。非常に高い線量が観測される鉄製タンクをそのまま他の用途に転用することはできないため、廃棄処分することが検討されている。しかし、鉄は放射化されていないので、微量の放射性セシウムを鉄から分離することができれば、鉄を放射性廃棄物として扱う必要が無くなり、一般廃棄物として処理することができる。   The contaminated water generated at nuclear power plants contains radioactive cesium. As a current response to the contaminated water, the contaminated water is temporarily stored in an iron tank. After treating the contaminated water, an iron tank with radioactive cesium attached to the inner wall surface remains. Since iron tanks where very high doses are observed cannot be used for other purposes, they are being considered for disposal. However, since iron is not activated, if it is possible to separate a small amount of radioactive cesium from iron, it is not necessary to treat iron as radioactive waste, and it can be treated as general waste.

鉄板の表面を除染する方法として、タンク内壁面を構成する鉄板の表面をはつりする(表面を削ぎ落とす)方法が検討されている。しかし、はつりによって生じる粉塵には放射性セシウムが含まれているため、粉塵の飛散が問題となりうる。   As a method of decontaminating the surface of the iron plate, a method of suspending the surface of the iron plate constituting the inner wall surface of the tank (scraping the surface) has been studied. However, since dust generated by fishing contains radioactive cesium, dust scattering can be a problem.

コンクリートや土壌等に付着した放射性セシウムについては、塩素の存在下で、高温で溶融処理することにより、塩化セシウムとして揮発させて飛灰中に回収し、溶融スラグと分離する塩化揮発法が開示されている(特許文献1,2)。しかしながら、鉄は塩化物となってセシウムと同様に揮発してガス側へ移行するため、従来の塩化揮発法を適用しても鉄から放射性セシウムを分離することは困難である。   For radioactive cesium adhering to concrete, soil, etc., a chlorination volatilization method is disclosed in which it is volatilized as cesium chloride and recovered in fly ash by melting at high temperature in the presence of chlorine and separated from molten slag. (Patent Documents 1 and 2). However, since iron becomes a chloride and volatilizes in the same manner as cesium and moves to the gas side, it is difficult to separate radioactive cesium from iron even if a conventional chlorination volatilization method is applied.

特開2013−120136号公報JP 2013-120136 A 特開2013−134085号公報JP2013-134085A

本発明は、上記事情に鑑みてなされたものであり、鉄から放射性セシウムを分離することが可能な、放射性セシウムを含む鉄の浄化方法を提供する。   This invention is made | formed in view of the said situation, and provides the purification method of the iron containing radioactive cesium which can isolate | separate radioactive cesium from iron.

上記の目的を達するために、本発明は以下の手段を提供する。
[1] 放射性セシウムを含む鉄材とコークスを混合して炉内で加熱し、還元雰囲気の炉内で溶融した鉄鋼スラグから前記放射性セシウムを気化させ、炉外へ排気された前記放射性セシウムを冷却して捕集することを特徴とする、放射性セシウムを含む鉄の浄化方法。
[2] 前記炉内に石灰を投入して加熱することを特徴とする前記[1]に記載の放射性セシウムを含む鉄の浄化方法。
[3] 前記炉内の温度が1500℃以上であることを特徴とする前記[1]又は[2]に記載の放射性セシウムを含む鉄の浄化方法。
[4] 前記鉄材100質量部に対して20〜30質量部のコークスを混合することを特徴とする前記[1]〜[3]の何れか一項に記載の放射性セシウムを含む鉄の浄化方法。
[5] 前記炉内に塩素を導入しないことを特徴とする前記[1]〜[4]の何れか一項に記載の放射性セシウムを含む鉄の浄化方法。
In order to achieve the above object, the present invention provides the following means.
[1] Iron material containing radioactive cesium and coke are mixed and heated in a furnace, the radioactive cesium is vaporized from steel slag melted in a reducing atmosphere furnace, and the radioactive cesium exhausted outside the furnace is cooled. A method for purifying iron containing radioactive cesium, wherein
[2] The method for purifying iron containing radioactive cesium according to [1], wherein lime is charged into the furnace and heated.
[3] The method for purifying iron containing radioactive cesium according to [1] or [2], wherein the temperature in the furnace is 1500 ° C. or higher.
[4] The method for purifying iron containing radioactive cesium according to any one of [1] to [3], wherein 20 to 30 parts by mass of coke is mixed with 100 parts by mass of the iron material. .
[5] The method for purifying iron containing radioactive cesium according to any one of [1] to [4], wherein chlorine is not introduced into the furnace.

本発明にかかる放射性セシウムを含む鉄の浄化方法によれば、鉄から放射性セシウムを分離することができる。放射性セシウムが除去された鉄を含む溶融スラグは一般廃棄物として処理することができる。除去した放射性セシウムは比較的少量の飛灰として回収されるため、放射性廃棄物を減容化することができる。   According to the method for purifying iron containing radioactive cesium according to the present invention, radioactive cesium can be separated from iron. Molten slag containing iron from which radioactive cesium has been removed can be treated as general waste. Since the removed radioactive cesium is recovered as a relatively small amount of fly ash, the volume of radioactive waste can be reduced.

本発明にかかる放射性セシウムを含む鉄の浄化方法の一例を示す模式図である。It is a schematic diagram which shows an example of the purification method of iron containing the radioactive cesium concerning this invention.

本発明にかかる放射性セシウムを含む鉄の浄化方法の第一実施形態は、以下の加熱工程、捕集工程、及び固化工程を有する。以下に各工程の詳細を説明するが、これらの工程以外の工程又は処理を含んでいてもよい。   1st embodiment of the purification method of iron containing the radioactive cesium concerning this invention has the following heating processes, a collection process, and a solidification process. Details of each step will be described below, but steps or processes other than these steps may be included.

<加熱工程>
本実施形態の加熱工程は、放射性セシウムを含む鉄材とコークスを混合して炉内で加熱する工程である。鉄材をコークスと共に加熱することによって炉内を還元雰囲気にすることができる。
<Heating process>
The heating process of this embodiment is a process of mixing the iron material containing radioactive cesium and coke and heating in a furnace. The inside of the furnace can be made a reducing atmosphere by heating the iron material together with the coke.

前記鉄材とコークスの混合物を加熱する温度は、鉄材が溶融する温度以上であれば特に限定されず、通常、鉄の融点1538℃に近い1500℃以上が好ましい。鉄材に酸化鉄が含まれていたとしても、還元雰囲気で鉄になるため、1500℃程度で溶融させることができる。鉄の融点を低下させるために、石灰を添加して加熱することが好ましい。
なお、鉄の表面の酸化被膜を形成する四酸化三鉄の融点は1597℃である。
The temperature at which the mixture of iron material and coke is heated is not particularly limited as long as it is equal to or higher than the temperature at which the iron material melts, and usually 1500 ° C. or higher, which is close to the melting point of iron 1538 ° C., is preferable. Even if the iron material contains iron oxide, it becomes iron in a reducing atmosphere and can be melted at about 1500 ° C. In order to lower the melting point of iron, it is preferable to add lime and heat.
The melting point of triiron tetroxide that forms an oxide film on the surface of iron is 1597 ° C.

セシウム単体の沸点は670℃、水酸化セシウムの沸点は990℃、塩化セシウムの沸点は1295℃であるため、前記混合物を1500℃以上で加熱すると、溶融した鉄から放射性セシウムを充分に気化させることができる。
加熱温度の上限値は、鉄の沸点2862℃以下であることが好ましく、加熱炉の耐久性を考慮して、例えば1700℃〜2000℃程度であることがより好ましい。
The boiling point of cesium alone is 670 ° C, the boiling point of cesium hydroxide is 990 ° C, and the boiling point of cesium chloride is 1295 ° C. Can do.
The upper limit of the heating temperature is preferably not more than the boiling point of iron of 2862 ° C., and more preferably, for example, about 1700 ° C. to 2000 ° C. in consideration of the durability of the heating furnace.

上記の温度で加熱する時間は特に限定されず、鉄材の分量に応じて適宜設定され、例えば、前記放射性セシウムを充分に気化させる観点から、溶融状態を0.5時間〜3時間程度継続するように加熱することが好ましい。   The time for heating at the above temperature is not particularly limited and is appropriately set according to the amount of the iron material. For example, from the viewpoint of sufficiently vaporizing the radioactive cesium, the molten state is continued for about 0.5 hours to 3 hours. It is preferable to heat it.

本実施形態の加熱工程においては、従来の塩化揮発法とは異なり、前記炉内に塩素を導入しないことが好ましい。塩素を導入すると、塩化セシウムとともに大量の塩化鉄が形成される。塩化鉄(II)の沸点は677℃であり、塩化鉄(III)の沸点は351℃であるため、塩化セシウム(沸点1295℃)と共に塩化鉄が揮発してしまい、鉄とセシウムとを分離することが困難になる。   In the heating process of the present embodiment, unlike the conventional chlorination volatilization method, it is preferable not to introduce chlorine into the furnace. When chlorine is introduced, a large amount of iron chloride is formed together with cesium chloride. Since the boiling point of iron (II) chloride is 677 ° C. and the boiling point of iron (III) chloride is 351 ° C., iron chloride volatilizes together with cesium chloride (boiling point 1295 ° C.), and iron and cesium are separated. It becomes difficult.

炉内で加熱する前記鉄材とコークスの混合比としては、例えば、前記鉄材100質量部に対して、5〜80質量部のコークスが好ましく、10〜50質量部のコークスがより好ましく、20〜30質量部のコークスがさらに好ましい。
上記範囲であると、炉内を充分に還元雰囲気にすることができ、酸化鉄を鉄に還元して充分に溶融させることができる。
As a mixing ratio of the iron material and coke heated in the furnace, for example, 5 to 80 parts by mass of coke is preferable with respect to 100 parts by mass of the iron material, and 10 to 50 parts by mass of coke is more preferable. More preferred are parts by mass of coke.
Within the above range, the inside of the furnace can be sufficiently reduced and iron oxide can be reduced to iron and sufficiently melted.

炉内で加熱する前記鉄材とコークスに石灰を混合する場合の混合比としては、例えば、前記鉄材100質量部に対して、5〜80質量部の石灰が好ましく、10〜50質量部の石灰がより好ましく、20〜30質量部の石灰がさらに好ましい。
上記範囲であると、鉄材の融点を下げて、溶融に必要な加熱温度を低く設定することができる。
As a mixing ratio in the case of mixing lime with the iron material and coke heated in the furnace, for example, 5 to 80 parts by mass of lime is preferable with respect to 100 parts by mass of the iron material, and 10 to 50 parts by mass of lime. More preferably, 20-30 mass parts lime is further more preferable.
Within the above range, the melting point of the iron material can be lowered and the heating temperature required for melting can be set low.

炉内に投入する鉄材は加熱前に予め粗く(大雑把に)切断された状態であることが好ましい。加熱による溶融が容易になり、コークスや石灰との混合も容易になるため、放射性セシウムの気化を促進することができる。   The iron material to be put into the furnace is preferably in a state of being roughly (roughly) cut in advance before heating. Since melting by heating becomes easy and mixing with coke and lime becomes easy, vaporization of radioactive cesium can be promoted.

鉄材を加熱して溶融する炉は、還元雰囲気で鉄材を溶融し、気化した放射性セシウムを含む排気ガスや飛灰を捕集可能な密閉型の炉がより好ましい。このような炉としては、例えば、コークスベッド式溶融炉が挙げられる。   The furnace that heats and melts the iron material is more preferably a closed type furnace that melts the iron material in a reducing atmosphere and collects vaporized radioactive cesium and exhaust ash. An example of such a furnace is a coke bed type melting furnace.

<捕集工程>
本実施形態の捕集工程は、溶融した鉄材から放射性セシウムを気化させ、炉外へ排気された放射性セシウムを冷却して捕集する工程である。
<Collection process>
The collection step of the present embodiment is a step of vaporizing radioactive cesium from a molten iron material and cooling and collecting the radioactive cesium exhausted outside the furnace.

揮発した放射性セシウムは、炉内の燃焼ガスによって炉外に排出される。排出された放射性セシウムを含む排気ガスは、排気経路上で冷却される。凝縮又は凝固した放射性セシウムの捕集は、排気経路上に設置された所定の捕集器で行うことが好ましい。捕集器としては、例えば、バグフィルター、セラミックフィルタ等の公知の集塵装置が挙げられる。公知の集塵装置の前段には、高温の排気ガスを例えば200℃程度に冷却するための冷却機構が備えられていることが多い。このような冷却機構は本実施形態においても有用である。捕集された放射性セシウムは法令に則った公知方法により処分される。   Volatilized radioactive cesium is discharged outside the furnace by the combustion gas in the furnace. The exhaust gas containing the discharged radioactive cesium is cooled on the exhaust path. It is preferable to collect the condensed or solidified radioactive cesium with a predetermined collector installed on the exhaust path. Examples of the collector include known dust collectors such as a bag filter and a ceramic filter. A pre-stage of a known dust collector is often provided with a cooling mechanism for cooling high-temperature exhaust gas to about 200 ° C., for example. Such a cooling mechanism is also useful in this embodiment. The collected radioactive cesium is disposed of by a publicly known method in accordance with laws and regulations.

<固化工程>
本実施形態の固化工程は、鉄材の溶融物を冷却し、固化した溶融スラグを得る工程である。充分に加熱及び溶融することにより、溶融スラグには放射性セシウムが実質的に含まれない程度まで処理することができる。得られた溶融スラグは法令に則った公知方法により処分される。この処分方法には再利用も含まれる。
<Solidification process>
The solidification process of this embodiment is a process of cooling the molten iron material to obtain a solidified molten slag. By sufficiently heating and melting, the molten slag can be processed to such an extent that radioactive cesium is not substantially contained. The obtained molten slag is disposed of by a known method in accordance with laws and regulations. This disposal method includes reuse.

本実施形態の浄化方法の概要を図1に示す。放射性セシウムで汚染された鉄材(例えば、鉄板)を大雑把に切断し、適量のコークス及び石灰と混合して、加熱炉10へ投入する。炉内に空気を供給し、1500℃程度に加熱することにより、鉄材を溶融させる。数時間加熱する間に放射性セシウムは気化する、放射性セシウムのガスは炉外へ排気され、バグフィルター12で捕集される。放射性セシウムが除かれた排気ガスは大気放出される。その後、溶融スラグは炉外へ排出される。   An outline of the purification method of the present embodiment is shown in FIG. An iron material (for example, an iron plate) contaminated with radioactive cesium is roughly cut, mixed with an appropriate amount of coke and lime, and charged into the heating furnace 10. Air is supplied into the furnace and heated to about 1500 ° C. to melt the iron material. The radioactive cesium vaporizes during heating for several hours. The radioactive cesium gas is exhausted to the outside of the furnace and collected by the bag filter 12. Exhaust gas from which radioactive cesium has been removed is released into the atmosphere. Thereafter, the molten slag is discharged out of the furnace.

セシウム及び鉄を含む廃棄物の焼却灰10gを、1500℃で30分間、還元雰囲気下で加熱し、その後ゆっくりと冷却して、処理済み焼却灰(スラグ)を得た。
焼却灰と処理済み焼却灰に含まれるセシウム及び鉄の各元素量をAgilent社製のICP-MSで測定したところ、加熱前の焼却灰に含まれていたセシウムのうち、約85%のセシウムが焼却灰から除去され、約15%のセシウムが処理済み焼却灰に残っていた。一方、鉄の殆どは処理済み焼却灰に残ったことが分かった。この結果は、セシウムが焼却灰から揮発し、鉄から分離されたことを示している。揮発したセシウムを冷却することによって回収できることは別途確認した。本実験では、実験を簡便な装置で実施するためにセシウム及び鉄を含む焼却灰を処理したが、セシウムを含む鉄材を処理する場合にも同様の結果が得られる。
したがって、放射性セシウムを含む鉄材を本発明の方法によって処理すれば、揮発した放射性セシウムを冷却して捕集するとともに、放射能が十分に低減された溶融スラグを得られることが明らかである。
10 g of waste incineration ash containing cesium and iron was heated in a reducing atmosphere at 1500 ° C. for 30 minutes, and then slowly cooled to obtain treated incineration ash (slag).
When the amount of each element of cesium and iron contained in incineration ash and treated incineration ash was measured by ICP-MS made by Agilent, about 85% of the cesium contained in the incineration ash before heating was about 85%. It was removed from the incineration ash, and about 15% of cesium remained in the treated incineration ash. On the other hand, it was found that most of the iron remained in the treated incineration ash. This result shows that cesium was volatilized from incineration ash and separated from iron. It was confirmed separately that volatile cesium could be recovered by cooling. In this experiment, incineration ash containing cesium and iron was treated in order to carry out the experiment with a simple apparatus, but similar results are also obtained when treating iron materials containing cesium.
Therefore, it is clear that when the iron material containing radioactive cesium is treated by the method of the present invention, the volatilized radioactive cesium is cooled and collected, and a molten slag having a sufficiently reduced radioactivity can be obtained.

以上で説明した各実施形態における各構成及びそれらの組み合わせ等は一例であり、本発明の趣旨を逸脱しない範囲で、公知の構成の付加、省略、置換、およびその他の変更が可能である。   The configurations and combinations thereof in the embodiments described above are examples, and additions, omissions, substitutions, and other modifications of known configurations are possible without departing from the spirit of the present invention.

本発明は、放射性セシウムを取り扱う分野に広く適用できる。   The present invention can be widely applied in the field of handling radioactive cesium.

10…加熱炉、12…バグフィルター 10 ... heating furnace, 12 ... bag filter

Claims (5)

放射性セシウムを含む鉄材とコークスを混合して炉内で加熱し、還元雰囲気の炉内で溶融した前記鉄材から前記放射性セシウムを気化させ、炉外へ排気された前記放射性セシウムを冷却して捕集することを特徴とする、放射性セシウムを含む鉄の浄化方法。   Iron material containing radioactive cesium and coke are mixed and heated in a furnace, the radioactive cesium is vaporized from the iron material melted in a reducing atmosphere furnace, and the radioactive cesium exhausted outside the furnace is cooled and collected A method for purifying iron containing radioactive cesium, comprising: 前記炉内に石灰を投入して加熱することを特徴とする請求項1に記載の放射性セシウムを含む鉄の浄化方法。   The method for purifying iron containing radioactive cesium according to claim 1, wherein lime is charged into the furnace and heated. 前記炉内の温度が1500℃以上であることを特徴とする請求項1又は2に記載の放射性セシウムを含む鉄の浄化方法。   The method for purifying iron containing radioactive cesium according to claim 1 or 2, wherein the temperature in the furnace is 1500 ° C or higher. 前記鉄材100質量部に対して20〜30質量部のコークスを混合することを特徴とする請求項1〜3の何れか一項に記載の放射性セシウムを含む鉄の浄化方法。   The method for purifying iron containing radioactive cesium according to any one of claims 1 to 3, wherein 20 to 30 parts by mass of coke is mixed with 100 parts by mass of the iron material. 前記炉内に塩素を導入しないことを特徴とする請求項1〜4の何れか一項に記載の放射性セシウムを含む鉄の浄化方法。   The method for purifying iron containing radioactive cesium according to any one of claims 1 to 4, wherein chlorine is not introduced into the furnace.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03293599A (en) * 1990-04-12 1991-12-25 Nippon Steel Corp Melting of scraps akin to ion contaminated by radioactive substances
JP2004239693A (en) * 2003-02-04 2004-08-26 Japan Nuclear Cycle Development Inst States Of Projects Method for melting treatment of radioactive contaminated metal
JP2015215219A (en) * 2014-05-09 2015-12-03 新日鐵住金株式会社 Purification method of radioactive contaminated soil

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03293599A (en) * 1990-04-12 1991-12-25 Nippon Steel Corp Melting of scraps akin to ion contaminated by radioactive substances
JP2004239693A (en) * 2003-02-04 2004-08-26 Japan Nuclear Cycle Development Inst States Of Projects Method for melting treatment of radioactive contaminated metal
JP2015215219A (en) * 2014-05-09 2015-12-03 新日鐵住金株式会社 Purification method of radioactive contaminated soil

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