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JPS6023863B2 - Method for producing cesium selective separator - Google Patents
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JPS6023863B2 - Method for producing cesium selective separator - Google Patents

Method for producing cesium selective separator

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Publication number
JPS6023863B2
JPS6023863B2 JP52127270A JP12727077A JPS6023863B2 JP S6023863 B2 JPS6023863 B2 JP S6023863B2 JP 52127270 A JP52127270 A JP 52127270A JP 12727077 A JP12727077 A JP 12727077A JP S6023863 B2 JPS6023863 B2 JP S6023863B2
Authority
JP
Japan
Prior art keywords
cesium
resin
seawater
concentration
ammonium
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.)
Expired
Application number
JP52127270A
Other languages
Japanese (ja)
Other versions
JPS5461014A (en
Inventor
章 中岡
速一 横山
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.)
Central Research Institute of Electric Power Industry
Original Assignee
Central Research Institute of Electric Power Industry
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 Central Research Institute of Electric Power Industry filed Critical Central Research Institute of Electric Power Industry
Priority to JP52127270A priority Critical patent/JPS6023863B2/en
Publication of JPS5461014A publication Critical patent/JPS5461014A/en
Publication of JPS6023863B2 publication Critical patent/JPS6023863B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は分離能力の著しい向上などを図りうる、燐モリ
ブデン酸アンモンを利用したセシウム選択分離体の製造
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a selective cesium separator using ammonium phosphomolybdate, which can significantly improve separation performance.

原子力発電プラントから排出される液体廃棄物、即ち核
分裂生成によって生じた各種半減期の核種を含む液体廃
棄物の処理に当っては、半減期の短かし、核種と、廃棄
処理に特別の考慮を必要とする半減期の長い核種とを分
離処理できることが極めて望ましい。しかし従来主とし
てとられている方法は、蒸発凝縮法のように長おび短半
減期の核種を同時に処理する方法であるため、特に半減
期の長いセシウム例えば134Cs,137Csなどが
含まれる。従って廃棄処理に当っては長、短半減期の核
種が含まれている大量の廃棄物を、長い半減期のものに
必要とすると同様な慎重な配慮のもとに廃棄処理するこ
とが必要である。このため従釆から大量の液体廃棄物か
ら特に半減期が長いセシウムを選択分離できる方法の開
発が要望されている。一方上記のような核種や分離され
た液体は、環境中例えば海水中に放出されるが、この中
には分離できなかった核種が含まれている。
In the treatment of liquid waste discharged from nuclear power plants, that is, liquid waste containing nuclides with various half-lives resulting from nuclear fission production, special consideration must be given to short half-lives, nuclides, and waste treatment. It is extremely desirable to be able to separate nuclides with long half-lives that require However, the conventional methods mainly used, such as the evaporation condensation method, simultaneously process nuclides with long and short half-lives, and therefore include cesium, which has a particularly long half-life, such as 134Cs and 137Cs. Therefore, when disposing of large quantities of waste containing long and short half-life nuclides, it is necessary to dispose of them with the same careful consideration as that required for long half-life nuclides. be. Therefore, there is a demand for the development of a method that can selectively separate cesium, which has a particularly long half-life, from a large amount of liquid waste. On the other hand, the above-mentioned nuclides and separated liquid are released into the environment, for example, into seawater, but they contain the nuclides that could not be separated.

このため公衆の被曝線量の評価上、行政指導によって海
水中における放射線セシウムの量および放射能の測定監
視が要求されている。しかし従来主として用いられてい
る代表的な方法例えば科学技術庁法といわれるものは、
採取された海水中にセシウム選択補集性を有する微粉末
状の燐モリブデン酸アンモンその他複数種類の試薬を添
加し、かっこの間損梓猿過などを繰返したのち煮沸して
、蒸発凝集によりセシウムを選択分離するものである。
従って分離処理に長い時間を要するばかりでなく、採取
された海水中に含まれるセシウムを100%回収するた
めには操作に高度の熟練を必要とする。従ってこの方法
は測定の迅速簡便性に欠け、十分なものとはいえない。
またこの方法は小量の液体中のセシウムの分離回収に適
当する方法であって、原子力発電プラント周辺の環境放
射能測定のように大量の液体からのセシウム分離に適用
できにくいことも明らかである。そこで例えばセシウム
の選択分離性をもつことが周知である燐モリブデン酸ア
ンモンの徴粉体をアスベストなどの担体に担持させ、こ
れに海水などを通して選択分離する方法が提案されてい
る。しかしこれでは燐モリブデン酸アンモン.を確実に
担特できないため大きなカラムを作ることができないば
かりか、カラム内の空隙容積が大きくなって分離性能を
低下するなどの欠点がある。本発明は上記のような欠点
を排除しうるセシウZム選択分離体の製造方法を提供す
るものであって、その特徴とするところは次の点にある
For this reason, in order to evaluate the public's exposure dose, administrative guidance requires measurement and monitoring of the amount of radioactive cesium and radioactivity in seawater. However, the representative methods mainly used in the past, such as the Science and Technology Agency method,
Finely powdered ammonium phosphomolybdate and other reagents that have cesium selective and scavenging properties are added to the collected seawater, and after repeated filtration and filtration, the water is boiled to collect cesium by evaporation and coagulation. It is selective separation.
Therefore, not only does the separation process take a long time, but it also requires a high degree of skill in order to recover 100% of the cesium contained in the collected seawater. Therefore, this method lacks quickness and ease of measurement and cannot be said to be sufficient.
It is also clear that this method is suitable for separating and recovering cesium from small amounts of liquid, but is difficult to apply to separating cesium from large amounts of liquid, such as when measuring environmental radioactivity around nuclear power plants. . Therefore, for example, a method has been proposed in which a powder of ammonium phosphomolybdate, which is well known to selectively separate cesium, is supported on a carrier such as asbestos, and then seawater is passed through the carrier to selectively separate the ammonium phosphomolybdate. However, this is ammonium phosphomolybdate. Not only is it impossible to make a large column because it cannot reliably support the particles, but it also has drawbacks such as increasing the void volume within the column and reducing separation performance. The present invention provides a method for producing a cesium Z selective separator that can eliminate the above-mentioned drawbacks, and is characterized by the following points.

即ち本発明においては燐モリブデン酸アンモンの担持体
として多孔質樹脂を用いると同時に、これに鱗モリブデ
ン酸溶液を含浸させたのち硝酸アZンモン溶液を作用さ
せる。そしてこれにより樹脂中の紐孔内によく行き亘る
ように隣モリブデン酸アンモンの沈澱物(固体)を生じ
させ、その生成時の膨張により樹脂のもつ弾性に抗して
その紬孔を押広げるようにして燐モリブデン酸アンモン
の大きな担持力を発生させるようにしたものである。そ
してこれにより空隙容積を低くして分離性能の向上を図
ると同時に所要の大きさのカラムを容易に作りうるよう
にして、従釆の燐モリブデン酸アンモンによるセシウム
選択分離体の欠点の除去を図ったことを特徴とするもの
である。
That is, in the present invention, a porous resin is used as a support for ammonium phosphomolybdate, and at the same time, this is impregnated with a scale molybdic acid solution and then treated with an ammonium nitrate solution. As a result, a precipitate (solid) of ammonium molybdate is formed so that it spreads well into the string holes in the resin, and when it expands, it pushes out the string holes against the elasticity of the resin. It is designed to generate a large supporting capacity for ammonium phosphomolybdate. As a result, the void volume is lowered to improve separation performance, and at the same time, columns of the required size can be easily manufactured, thereby eliminating the drawbacks of the conventional cesium selective separator using ammonium phosphomolybdate. It is characterized by:

このようにすれば原子力発電プラントの液体廃棄物を通
液することによりセシウムの選択分離を簡単迅速に行う
ことができる。
In this way, selective separation of cesium can be easily and quickly carried out by passing liquid waste from a nuclear power plant.

また被分離液例えばセシウムを含む海水を通液して樹脂
に分離されたセシウムを渚雛回収することにより簡単迅
速かつ正確に海水中における放射性セシウムの定量測定
を行うことができる。次に本発明の製造方法および定量
測定例について図面によって説明する。第1図は本発明
を海水中の放射性セシウムの定量測定に適用した例を示
す系統図である。本発明はまず■交換器を持たない多孔
質樹脂、例えばェポキシ、フェノール、ポリカーボネィ
トなどの従来公知の樹脂により作られた多孔質樹脂1を
、燐モリブデン酸溶液2を満した槽3中に浸潰しよく損
拝して、樹脂中に液を浸透させる。次に■槽3の上燈液
を除去したのち、硝酸アンモン溶液4を添加し濁拝して
、樹脂1中の燐モリブデン酸溶液2とよく反応させ、周
知の作用により多孔質樹脂1の細孔中に、燐モリブデン
酸アンモンの沈澱物を生成させて樹脂中に閉じ込める。
しかるのち■この樹脂5を塩酸溶液6を充填した糟7中
に浸潰し洗浄して、樹脂5の全表面に生じた鱗モリブデ
ン酸アンモンの沈澱物を除去して、測定における通液時
セシウムを捕集した隣モリブデン酸アンモンが流出して
測定誤差を生じないようにする当然行われる周知の洗浄
を行って、セシウム選択分離樹脂を調製する。次に■調
製樹脂5を液流入口と流出口を有するカラム7に充填し
、これに放射性セシウムを含有する海水8を通液してセ
シウムを樹脂5に楠集したのち、■セシウム溶離作用を
もつことが公知である、例えば水酸化ナトリウム9を通
液して樹脂5からセシウム10を溶雛する。しかるのち
従来と全く同様に■回収率の測定、■1クマリネリ容器
に移したのち、■放射能計測を行って、海水中への放射
性セシウムの定量測定を行う。以上説明した本発明によ
れば分離性能を著しく向上できるので、調製樹脂に被分
離液を通液し、水酸化ナトリウム溶液により溶離するの
みでセシウムを著しく高い分離度で回収できる。
Further, by passing a liquid to be separated, such as seawater containing cesium, and collecting the cesium separated into resin from the beach, it is possible to easily, quickly and accurately quantitatively measure radioactive cesium in seawater. Next, the manufacturing method and quantitative measurement examples of the present invention will be explained with reference to the drawings. FIG. 1 is a system diagram showing an example in which the present invention is applied to quantitative measurement of radioactive cesium in seawater. The present invention first involves (1) immersing a porous resin 1 made of a conventionally known resin such as epoxy, phenol, or polycarbonate into a tank 3 filled with a phosphomolybdic acid solution 2; Crush it well and let the liquid penetrate into the resin. Next, after removing the top liquid from tank 3, ammonium nitrate solution 4 is added and stirred to react well with phosphomolybdic acid solution 2 in resin 1. In the pores, a precipitate of ammonium phosphomolybdate is formed and trapped in the resin.
After that, ■ This resin 5 is washed by immersing it in a pot 7 filled with a hydrochloric acid solution 6 to remove the precipitate of ammonium molybdate scales formed on the entire surface of the resin 5, and to remove cesium during the measurement. A cesium selective separation resin is prepared by performing a well-known cleaning process to prevent the collected ammonium molybdate from flowing out and causing measurement errors. Next, (1) the prepared resin 5 is packed into a column 7 having a liquid inlet and an outlet, and seawater 8 containing radioactive cesium is passed through this column to collect cesium in the resin 5. For example, sodium hydroxide 9 is passed through the resin 5 to dissolve cesium 10. Then, in exactly the same manner as before, 1. Measure the recovery rate, 2. Transfer to a Kumarinelli container, and 2. Measure the radioactivity to quantitatively measure the amount of radioactive cesium in the seawater. According to the present invention described above, the separation performance can be significantly improved, so that cesium can be recovered with a significantly high degree of separation simply by passing the liquid to be separated through the prepared resin and eluting with a sodium hydroxide solution.

また使用する樹脂量の選定により、大量の液体廃棄物か
らのセシウム分離除去にも、定量測定における小量の液
体からのセシウムの分離除去にも適用できる。従って例
えば本発明方法により原子力発電プラントからの液体廃
棄物中からセシウムを分離したのち蒸発凝縮法を適用す
れば、蒸発凝縮によって得られた廃棄物の処理が容易と
なる。また本発明を海水中のセシウムの定量測定に適用
すれば、前記した従来方法のように長い時間と熟練した
操作技術を全く必要とすることなくセシウムを分離回収
できるので、測定の簡単迅速化を図ることができる。次
に本発明を実施例について説明する。実施例 1人工海
水則ち天然海水と同一塩分量、同一pHとなるように人
工的に調製した海水に、海水中のセシウムイオン濃度に
応じて、キャリア用セシウムイオンを1〜30仰m加え
たのち、0.1N程度の塩酸溶液としたものを、樹脂中
の燐モリブデン酸ァンモン濃度を92の9/の‘樹脂と
した米国ロームアンドハース社製アンバーライトXAD
−7樹脂に通液した。
Furthermore, by selecting the amount of resin used, it can be applied to the separation and removal of cesium from large amounts of liquid waste as well as from small amounts of liquid in quantitative measurements. Therefore, for example, if cesium is separated from liquid waste from a nuclear power plant by the method of the present invention and then the evaporative condensation method is applied, the waste obtained by evaporative condensation can be easily disposed of. Furthermore, if the present invention is applied to the quantitative measurement of cesium in seawater, cesium can be separated and recovered without the need for a long time and skilled operation techniques unlike the conventional method described above, making the measurement simple and quick. can be achieved. Next, the present invention will be explained with reference to examples. Example 1 To artificial seawater, that is, seawater that was artificially prepared to have the same salinity and pH as natural seawater, 1 to 30 m of cesium ions for carrier were added depending on the cesium ion concentration in the seawater. Afterwards, the solution was made into a hydrochloric acid solution of about 0.1N, and the ammonium phosphomolybdate concentration in the resin was made into a resin of 9/92 (Amberlite XAD manufactured by Rohm and Haas Co., Ltd. in the United States).
-7 resin was passed through.

この結果第2図にようにキャリアセシウム濃度1脚にお
いて、1.7×10‐3meg/の‘の貫流容量が得ら
れ、本発明樹脂の有効性が実証された。また樹脂中に捕
集されたセシウムイオンは、INの水酸化ナトリウムを
樹脂量の2倍量で通液することによりほぼ100%回収
できた。また流速の貫流容量への影響を検討した結果、
SV30〜120の範囲では認められなかった。また交
換容量は隣モリブデン酸アンモンの濃度が高い程大とな
った。なお上記樹脂中における燐モリブデン酸アンモン
濃度92爪9/私樹脂は多孔性樹脂30の上を5〜20
多燐モリブデン酸の10の‘溶液に浸潰したのち、同濃
度の硝酸アンモニウム溶液を添加し、最後に0.1N塩
酸で洗浄して得られたもので、30の上樹脂に対する機
モリブデン酸、硝酸アンモン溶液濃度(夕/10の‘)
と燐モリブデン酸アンモン濃度(雌/の‘)との関係は
第3図の通りである。実施例 2 天然海水60〜80〆用い、これにセシウムイオンを加
えてキャリア濃度を1脚としたものを、機モリブデン酸
ァンモン濃度が92の9/私となるように調製された4
00の‘の樹脂にSVIOOで通液した。
As a result, as shown in Fig. 2, a flow capacity of 1.7 x 10-3 meg/' was obtained at a single carrier cesium concentration, demonstrating the effectiveness of the resin of the present invention. Furthermore, almost 100% of the cesium ions trapped in the resin could be recovered by passing IN sodium hydroxide in an amount twice the amount of the resin. In addition, as a result of examining the influence of flow velocity on throughflow capacity,
It was not observed in the range of SV30-120. In addition, the exchange capacity increased as the concentration of ammonium dextrose molybdate increased. Note that the concentration of ammonium phosphomolybdate in the above resin is 92 9/I resin, and the concentration of ammonium phosphomolybdate on the porous resin 30 is 5 to 20.
After soaking in a 10' solution of polyphosphorous molybdic acid, adding an ammonium nitrate solution of the same concentration, and finally washing with 0.1N hydrochloric acid, it was obtained by soaking in a 10' solution of polyphosphorous molybdic acid and nitric acid. Ammonium solution concentration (evening/10')
The relationship between the concentration of ammonium phosphomolybdate and the ammonium phosphomolybdate concentration (female/') is shown in Figure 3. Example 2 Natural seawater with a concentration of 60 to 80% was used, and cesium ions were added to it to make the carrier concentration 1.
00' resin was passed through SVIOO.

しかるのちINの水酸化ナトリウムによりセシウムの溶
機を行い、1そ中の回収率を原子吸光法により限定した
ところ、第1表に示すように93〜102%にも及ぶ極
めてよい結果を得ることができた。また1クマリネリ容
器に充填して高能率y線計測装置により1『秒間放射能
第1表 註くは表記濃度以下である事を示す の計測を行ったところ、第1表の結果が得られ、従来の
報告値例えば137Csの場合0.1〜0.斑Ci/そ
とより一致を示した。
After that, cesium was dissolved in IN sodium hydroxide, and the recovery rate of the cesium was limited by atomic absorption spectroscopy, and as shown in Table 1, extremely good results of 93 to 102% were obtained. was completed. In addition, when we filled one Kumarinelli container and measured the radioactivity per second using a high-efficiency Y-ray measuring device, the results shown in Table 1 were obtained. Conventionally reported values, for example, 0.1 to 0.1 for 137Cs. The spots Ci/ showed more agreement.

また本発明を海水セシウムの定量に適用した場合、樹脂
の調製カラムへの充填作業に0.虫時間、カラムへの通
液に2時間、溶離に0.5時間の計3時間を要した。こ
れは従来の定量法所謂科学技術庁法の約3畑時間に対し
て1/10、また最も速い方法に対しても、1/2の時
間である。また本発明ではカラムに通液するのみで、従
来方法のように各試薬の添加、蝿過、煮沸など数種類に
及ぶ操作を必要としない。従って従来方法に比べて測定
操作を著しく簡便迅速化できる。なお以上の実施例にお
いては、セシウムイオンを加えて被分離液のセシウム濃
度を調製したが、セシウム濃度が所定値以上のときには
調製を必要としない。また以上では樹脂の調製と分離を
連続的に行う場合について説明したが、予め樹脂を調製
しておき、必要に応じて使用するようにすることもでき
る。以上の説明から明らかなように、本発明によれば液
中におけるセシウムの分離除去、分離回収を簡便迅速に
行えるすぐれた利点が得られるもので、環境中における
放射性セシウムの定量測定などに極めて著しい貢献をな
すものである。
Furthermore, when the present invention is applied to the determination of seawater cesium, 0.00% is required to fill the resin preparation column. It took a total of 3 hours, 2 hours to pass the liquid through the column, and 0.5 hours to elute. This is 1/10 of the time required for conventional quantitative determination, which is about 3 hours for the so-called Science and Technology Agency method, and is also 1/2 of the time required for the fastest method. In addition, in the present invention, only the liquid is passed through the column, and there is no need for several operations such as addition of each reagent, filtration, and boiling, as in conventional methods. Therefore, the measurement operation can be made much simpler and faster than the conventional method. In the above embodiments, the cesium concentration of the liquid to be separated was adjusted by adding cesium ions, but this adjustment is not required when the cesium concentration is equal to or higher than a predetermined value. Moreover, although the case where the preparation and separation of the resin are carried out continuously has been described above, the resin can also be prepared in advance and used as needed. As is clear from the above explanation, the present invention provides an excellent advantage of being able to easily and quickly separate and remove cesium in a liquid, and separate and recover it, which is extremely useful for quantitative measurement of radioactive cesium in the environment. It makes a contribution.

図面の箇単な説明 第1図は本発明樹脂の調製工程を示す系統図、第2図は
海水中におけるセシウムイオン濃度と貫流容量の関係図
、第3図は30凧‘樹脂に対する燐モリブデン酸、硝酸
アンモン溶液(夕/10奴)と樹脂中の隣モリブデン濃
度(倣/の‘樹脂)の関係図である。
Brief explanation of the drawings Figure 1 is a systematic diagram showing the preparation process of the resin of the present invention, Figure 2 is a diagram showing the relationship between cesium ion concentration in seawater and flow capacity, and Figure 3 is a diagram showing the relationship between cesium ion concentration and flow capacity in seawater. , is a relationship diagram between the ammonium nitrate solution (Y/10) and the molybdenum concentration in the resin (Imitation/'s resin).

第1図 弟2図 第5図Figure 1 younger brother 2 Figure 5

Claims (1)

【特許請求の範囲】[Claims] 1 燐モリブデン酸溶液を含浸さた交換基をもたない多
孔質樹脂に硝酸アンモン液を添加して上記樹脂の細孔中
に燐モリブデン酸アンモンの沈澱物を生成することを特
徴とするセシウム選択分離体の製造方法。
1 Cesium selection characterized by adding an ammonium nitrate solution to a porous resin having no exchange group impregnated with a phosphomolybdic acid solution to form a precipitate of ammonium phosphomolybdate in the pores of the resin. Method for producing a separator.
JP52127270A 1977-10-25 1977-10-25 Method for producing cesium selective separator Expired JPS6023863B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52127270A JPS6023863B2 (en) 1977-10-25 1977-10-25 Method for producing cesium selective separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52127270A JPS6023863B2 (en) 1977-10-25 1977-10-25 Method for producing cesium selective separator

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JPS5461014A JPS5461014A (en) 1979-05-17
JPS6023863B2 true JPS6023863B2 (en) 1985-06-10

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JP5849342B2 (en) * 2011-04-26 2016-01-27 株式会社化研 Decontamination equipment and decontamination method for radioactive substances from radioactive contaminated water mixed with seawater
JP5733703B2 (en) * 2011-06-20 2015-06-10 国立研究開発法人日本原子力研究開発機構 Cloth-like radioactive material adsorbent and method for producing the same

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JPS5229480A (en) * 1975-09-01 1977-03-05 Kanebo Ltd Method of producing heavy metal adsorbent
JPS5229479A (en) * 1975-09-01 1977-03-05 Kanebo Ltd Uranium adsorbent and method of producing thereof

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