JPS58161898A - Chemical decomposition of radioactive ion exchange resin - Google Patents

Chemical decomposition of radioactive ion exchange resin

Info

Publication number
JPS58161898A
JPS58161898A JP57044375A JP4437582A JPS58161898A JP S58161898 A JPS58161898 A JP S58161898A JP 57044375 A JP57044375 A JP 57044375A JP 4437582 A JP4437582 A JP 4437582A JP S58161898 A JPS58161898 A JP S58161898A
Authority
JP
Japan
Prior art keywords
ion exchange
exchange resin
radioactive ion
chemical decomposition
hydrogen peroxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP57044375A
Other languages
Japanese (ja)
Inventor
利夫 市橋
晃 長谷川
中山 康敬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Nippon Genshiryoku Jigyo KK
Nippon Atomic Industry Group Co Ltd
Original Assignee
Nippon Genshiryoku Jigyo KK
Tokyo Shibaura Electric Co Ltd
Nippon Atomic Industry Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Genshiryoku Jigyo KK, Tokyo Shibaura Electric Co Ltd, Nippon Atomic Industry Group Co Ltd filed Critical Nippon Genshiryoku Jigyo KK
Priority to JP57044375A priority Critical patent/JPS58161898A/en
Publication of JPS58161898A publication Critical patent/JPS58161898A/en
Pending legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は使用済み放射性イオン交換樹脂を化学分解する
方法に係り、特に硫酸第二鉄水溶液中において過酸化水
素により前記樹脂を酸化分解する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for chemically decomposing a used radioactive ion exchange resin, and more particularly to a method for oxidatively decomposing the resin with hydrogen peroxide in an aqueous ferric sulfate solution. .

〔発明の技術的背景〕[Technical background of the invention]

原子力発電所婢においては種々の固体廃棄物が発生する
が、現在のところその多くは最終処分方法が未だ確立せ
ず流動的であるため、そのまま主としてタンク等に貯蔵
保管されている。従って、廃棄物の発生量を滅らすこと
は貯蔵管理の上で重要なことであり、緊急の課題である
。このよう表固体廃棄物の中で4使用済み放射性イオン
交換樹脂は主要なものであり、これを減容化することは
発生廃棄物量の減少に大きく貢献する。
A variety of solid wastes are generated at nuclear power plants, but as the final disposal method for most of them has not yet been established and the waste is in flux, it is mainly stored in tanks and the like. Therefore, reducing the amount of waste generated is an important and urgent issue in storage management. Among these solid wastes, used radioactive ion exchange resins are the main ones, and reducing their volume will greatly contribute to reducing the amount of waste generated.

イオン交換樹脂を化学構造的に分解して減容処理する方
法としては、焼却法、熱分解法、化学分解法等が考えら
れている。焼却法は文字通り焼く方法で、多くの方式が
開発中である。しかしながら、焼却炉にて焼却する場合
には熱菫のコントロールが必要なため、乾燥等の前処理
や樹脂の供給方法の工夫が必要で、操作や設備が複雑と
なる。
As a method for chemically decomposing an ion exchange resin to reduce its volume, there are incineration methods, thermal decomposition methods, chemical decomposition methods, and the like. Incineration is literally a method of burning, and many methods are under development. However, when incinerating in an incinerator, thermal violet control is required, so pretreatment such as drying and a method for supplying resin must be devised, making operations and equipment complicated.

また、焼却ガスとして80x、 NOx等の有害ガスが
発生するので、廃ガス処理という後処理が必要であるこ
と、及びこれらのガスは腐食性が強く、装置材料の選定
が難しいとと等の問題点があり、さらシ(は高温の環境
で処理されるために、放射能成分が揮発してガス側に移
行する、いわゆる核種の移行という放射能取扱いに特有
な問題もある。
In addition, harmful gases such as 80x and NOx are generated as incineration gas, so post-treatment called waste gas treatment is required, and these gases are highly corrosive, making it difficult to select equipment materials. However, since raw materials are processed in a high-temperature environment, there is a problem unique to the handling of radioactivity: radioactive components volatilize and migrate to the gas side, so-called nuclide migration.

熱分解法は、酸素の供給を遮断して加熱分解させる方法
で、不活性ガス雰囲気下で高温で樹脂成分を熱分解する
ため、焼却法に比較して発生する煤塵O量が少ないとい
う利点を有する。しかしながら、分解ガスの燃焼工程が
余計に必要である上に、焼却法の場合と同様に、有害ガ
スの発生、装置材料の腐食、放射性核穫の移行嬌の問題
がある。
The thermal decomposition method is a method of thermally decomposing the resin by cutting off the supply of oxygen, and because the resin component is thermally decomposed at high temperatures in an inert gas atmosphere, it has the advantage of generating less soot and dust compared to the incineration method. have However, this method requires an extra step of burning the decomposed gas, and, like the incineration method, there are problems with the generation of harmful gases, corrosion of equipment materials, and transferability of radioactive nuclear harvest.

化学分解法は薬剤との化学反応により樹脂を酸化分解さ
せるもので、主として熱濃硫酸(130℃〜300℃)
で樹脂を炭化させた優、硝酸を九は過酸化水素で酸化分
解する方法が知られているが、この方法の量大の問題点
は強力な酸及び酸化剤を非常な高温で取扱うために、!
i!箇材料の選定が非常に厳しいことである。現状では
実験室規模−t″はガラス、実際の設備ではタンタルが
用いられているが、タンタルについても材料的な問題が
全てクリアーになっているわけではない。
The chemical decomposition method oxidizes and decomposes the resin through a chemical reaction with a chemical, mainly using hot concentrated sulfuric acid (130°C to 300°C).
It is known to oxidize and decompose nitric acid with hydrogen peroxide by carbonizing the resin, but the major problem with this method is that the strong acid and oxidizing agent must be handled at extremely high temperatures. ,!
i! The selection of materials is extremely difficult. At present, glass is used for laboratory scale -t'', and tantalum is used in actual equipment, but not all material issues have been resolved with tantalum as well.

濃硫酸と硝酸または過酸化水素を用いる方法の他には、
硝酸第二鉄#液中で過酸化水素で酸化分ン交換64 )
1! Lか処理できないことが確認されている。
In addition to methods using concentrated sulfuric acid and nitric acid or hydrogen peroxide,
Oxide exchange with hydrogen peroxide in ferric nitrate # solution64)
1! It has been confirmed that L cannot be processed.

またこの他に、有機分析試薬として、硫酸第一鉄水溶液
中に過酸化水素水を添加して有機物を分解するツエント
ン試薬法やアルカリ性の溶液中で儂酸化水素を用いて加
熱しながら溶剤成分を分解する方法が報告されているが
、これらはイオン交換樹脂を分解できるかどうかについ
ては触れられていない。
In addition, as an organic analysis reagent, there is also the Tzenton reagent method, in which hydrogen peroxide is added to an aqueous ferrous sulfate solution to decompose organic substances, and the solvent component is dissolved in an alkaline solution while heating with hydrogen oxide. Although decomposition methods have been reported, there is no mention of whether these methods can decompose ion exchange resins.

〔発明の目的〕[Purpose of the invention]

本発明は上記の点に鑑みてなされたもので、放射性イオ
ン交換樹脂を硫酸第二鉄水溶液中で過酸化水素と接触さ
せることにより、カチオン交換樹脂のみならずアニオン
交換樹脂をも、従来技術に比して低温で容易に酸化分解
できる放射性イオン交換樹脂の化学分解法を提供しよう
とするもので゛ある。
The present invention has been made in view of the above points, and by contacting a radioactive ion exchange resin with hydrogen peroxide in an aqueous ferric sulfate solution, it is possible to improve not only a cation exchange resin but also an anion exchange resin using conventional techniques. In contrast, the present invention aims to provide a chemical decomposition method for radioactive ion exchange resins that can be easily oxidized and decomposed at low temperatures.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の一実施例について説明する。 An embodiment of the present invention will be described below.

硫酸第二鉄水溶液に分解すべきイオン交換wIAWIを
加え、ついで過酸化水素水を添力pして攪拌しながら室
温で放置することによ鰺、欄7を酸イヒしガス状生成物
と液状残留物に分解する。この場合、Fes+濃度が約
0.03mol/1以上で、過酸イし水素濃度が8%以
上の反応#11で乾燥したイオン交換樹脂を約501に
9以上分解すること力;できる。
Add the ion exchange wIAWI to be decomposed to the ferric sulfate aqueous solution, then add hydrogen peroxide solution and leave it at room temperature while stirring. Decomposes into residues. In this case, it is possible to decompose the ion exchange resin dried in reaction #11 in which the Fes+ concentration is about 0.03 mol/1 or more and the hydrogen peroxide concentration is 8% or more into about 501 parts or more.

上記の例は回分方式を採用したが、この例に限らず半回
分方式や連続方式で分解処理を行うことも可能である。
Although the above example adopted a batch method, the decomposition process is not limited to this example, and it is also possible to perform the decomposition process in a semi-batch method or a continuous method.

この場合、過酸化水素水を一定流量で時間をかけて滴下
しながら連続的に添カロする方法、硫酸第二1鉄水溶液
を同様に滴下する方法、または過酸化水素水と硫酸第二
鉄水浴液の両方を連続的に滴下する方法などが考えられ
゛る。過酸イヒ水素水を連続的に供給する方法では11
分式の場合よりも少ない電で樹11酋を分解できること
力ζ実鰐的に確認されている。
In this case, a method of continuously adding potassium while dropping hydrogen peroxide solution at a constant flow rate over time, a method of dropping a ferric sulfate aqueous solution in the same way, or a method of adding hydrogen peroxide solution and ferric sulfate water bath One possible method is to drop both liquids continuously. In the method of continuously supplying hydrogen peroxide solution, 11
It has been experimentally confirmed that the tree can be disassembled using less electricity than in the case of a split method.

また、反応液の硫#!第二鉄及び過酸イヒ水素の濃度は
実施例の一度条件に限定されるものではなく、より広い
範囲のfIk度をとることができる。
Also, sulfur # in the reaction solution! The concentrations of ferric iron and dihydrogen peroxide are not limited to the one-time conditions of the example, but can take a wider range of fIk degrees.

、また、酸化反応は室温でも進行するが、若干の加熱(
反応液の温度としては100℃以下)によシN応速度を
大きくシ、分w4操作をより迅速イヒすることもできる
、 次表に、本煽明と同様に過酸化水素を用いた従来法と本
発明q)方法とを比較して、良好なものにi:j(’)
、そうでない本のにはX印を記してその違い登示す。
In addition, although the oxidation reaction proceeds at room temperature, slight heating (
The temperature of the reaction solution is 100°C or lower), which increases the N reaction rate and allows for faster oxidation. and the method q) of the present invention, the better one is i:j(')
, mark the book with an X to indicate the difference.

〔発明の効果〕〔Effect of the invention〕

以上の説明からも明らかなように、本発明の化学分解法
は従来法と比較して次のような利点を示す。
As is clear from the above explanation, the chemical decomposition method of the present invention has the following advantages compared to conventional methods.

イ)反応開始時の温度は室温でも充分であるため、分解
操作が容易であシ、かつ設備や装置材料の面でも負担が
少ない。
b) Since room temperature is sufficient at the start of the reaction, the decomposition operation is easy and there is less burden on equipment and equipment materials.

−)分解生成物は着千の硫酸が生じるだけなので、後処
理としては塩の回収及び硫酸の回収のみで(場合によっ
ては回収せずに)樹脂の分解処理が可能表ため、設備を
単純化できる。
-) Since the only decomposition product is 1,000 sulfuric acid, the resin can be decomposed by recovering the salt and sulfuric acid (in some cases, without recovery), which simplifies the equipment. can.

ハ)同一の反応条件でカチオン交換樹脂もアニオン交換
樹脂も分解口■能なため、条件の設定が容易である。
c) Since both cation exchange resin and anion exchange resin can be decomposed under the same reaction conditions, it is easy to set the conditions.

二)反応は発熱反応であるため、反応温度を強制的に維
持する必要はない。
2) Since the reaction is exothermic, there is no need to forcibly maintain the reaction temperature.

ホ)反応液の温度を監視することにより、反応の。e) of the reaction by monitoring the temperature of the reaction solution.

終了点を確望することができる。You can be sure of the ending point.

へ)硫酸第一鉄水溶液は不安定で長期間の保存には適さ
ないが、硫酸第二鉄水溶液は安定であるためvI!際の
使用には適している。
f) Ferrous sulfate aqueous solution is unstable and not suitable for long-term storage, but ferric sulfate aqueous solution is stable, so vI! Suitable for occasional use.

代理人弁理士  須 山 佐 − 591−Representative Patent Attorney Su Yamasa - 591-

Claims (1)

【特許請求の範囲】 1、放射性イオン交換樹脂を硫酸第二鉄水溶液中で過酸
化水素と接触させ、前記樹脂を酸化させることにより分
解することを特徴とする放射性イオン交換樹脂の化学分
解法。 2、 酸化は室温にて行なわれる特許請求の範囲第1項
記載の放射性イオン交換樹脂の化学分解法。
[Scope of Claims] 1. A method for chemically decomposing a radioactive ion exchange resin, which comprises bringing the radioactive ion exchange resin into contact with hydrogen peroxide in an aqueous ferric sulfate solution to oxidize and decompose the resin. 2. A method for chemically decomposing a radioactive ion exchange resin according to claim 1, wherein the oxidation is carried out at room temperature.
JP57044375A 1982-03-19 1982-03-19 Chemical decomposition of radioactive ion exchange resin Pending JPS58161898A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57044375A JPS58161898A (en) 1982-03-19 1982-03-19 Chemical decomposition of radioactive ion exchange resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57044375A JPS58161898A (en) 1982-03-19 1982-03-19 Chemical decomposition of radioactive ion exchange resin

Publications (1)

Publication Number Publication Date
JPS58161898A true JPS58161898A (en) 1983-09-26

Family

ID=12689748

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57044375A Pending JPS58161898A (en) 1982-03-19 1982-03-19 Chemical decomposition of radioactive ion exchange resin

Country Status (1)

Country Link
JP (1) JPS58161898A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997012647A1 (en) * 1995-10-04 1997-04-10 Leonhard Weiss Gmbh & Co. Process for processing acid resins sludge
JP2012005996A (en) * 2010-06-28 2012-01-12 Jgc Corp Method for treating organic compound by fenton reaction
JP2013242291A (en) * 2012-03-07 2013-12-05 Daiki Ataka Engineering Co Ltd Method for removing radioactive cesium from drainage water containing radioactive cesium
EP2819125A1 (en) 2013-06-21 2014-12-31 Hitachi-GE Nuclear Energy, Ltd. Radioactive organic waste treatment method and system

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53123556A (en) * 1977-04-05 1978-10-28 Toa Gosei Chem Ind Method of treating nighttsoil treated water
JPS54112556A (en) * 1978-02-22 1979-09-03 Kankyo Eng Disposal method of organic waste water
JPS571446A (en) * 1980-06-05 1982-01-06 Japan Atom Energy Res Inst Decomposition of ion exchange resin
JPS5872099A (en) * 1981-10-27 1983-04-28 日揮株式会社 Treatment of radioactive organic waste

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53123556A (en) * 1977-04-05 1978-10-28 Toa Gosei Chem Ind Method of treating nighttsoil treated water
JPS54112556A (en) * 1978-02-22 1979-09-03 Kankyo Eng Disposal method of organic waste water
JPS571446A (en) * 1980-06-05 1982-01-06 Japan Atom Energy Res Inst Decomposition of ion exchange resin
JPS5872099A (en) * 1981-10-27 1983-04-28 日揮株式会社 Treatment of radioactive organic waste

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997012647A1 (en) * 1995-10-04 1997-04-10 Leonhard Weiss Gmbh & Co. Process for processing acid resins sludge
JP2012005996A (en) * 2010-06-28 2012-01-12 Jgc Corp Method for treating organic compound by fenton reaction
JP2013242291A (en) * 2012-03-07 2013-12-05 Daiki Ataka Engineering Co Ltd Method for removing radioactive cesium from drainage water containing radioactive cesium
EP2819125A1 (en) 2013-06-21 2014-12-31 Hitachi-GE Nuclear Energy, Ltd. Radioactive organic waste treatment method and system
US9336913B2 (en) 2013-06-21 2016-05-10 Hitachi-Ge Nuclear Energy, Ltd. Radioactive organic waste treatment method

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