JPH0672957B2 - Treatment method of radioactive ion exchange resin - Google Patents

Treatment method of radioactive ion exchange resin

Info

Publication number
JPH0672957B2
JPH0672957B2 JP61242122A JP24212286A JPH0672957B2 JP H0672957 B2 JPH0672957 B2 JP H0672957B2 JP 61242122 A JP61242122 A JP 61242122A JP 24212286 A JP24212286 A JP 24212286A JP H0672957 B2 JPH0672957 B2 JP H0672957B2
Authority
JP
Japan
Prior art keywords
resin
acid
nuclide
ion exchange
exchange resin
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 - Lifetime
Application number
JP61242122A
Other languages
Japanese (ja)
Other versions
JPS6396600A (en
Inventor
豊孝 音田
崇史 三宅
均 宮本
俊夫 船越
亘 川村
雄三 稲垣
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP61242122A priority Critical patent/JPH0672957B2/en
Publication of JPS6396600A publication Critical patent/JPS6396600A/en
Publication of JPH0672957B2 publication Critical patent/JPH0672957B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Treatment Of Water By Ion Exchange (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は原子力施設に貯蔵されている放射性イオン交換
樹脂(以下単に樹脂という)の無機安定化処理方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a method for inorganic stabilization treatment of a radioactive ion exchange resin (hereinafter simply referred to as a resin) stored in a nuclear facility.

〔従来の技術〕[Conventional technology]

樹脂の処理方法として、現在実機への適用の例はまだ無
く、従つて種々開発中の技術について述べる。
As a resin treatment method, there is no example of application to an actual machine at present, and therefore various technologies under development will be described.

1)焼却法;文字通り樹脂を焼却する方法であるが、樹
脂の含有放射能レベルが高い場合は、焼却排ガス中に含
まれる放射能量を増大するので排ガス処理装置には過大
な放射能除去性能が要求されることになる。すなわち、
排ガス処理装置が、複雑、大規模化する。また焼却灰の
放射能濃度が高くなり、その取扱が容易でない。
1) Incineration method: This is literally a method of incinerating resin, but if the level of radioactivity contained in the resin is high, the amount of radioactivity contained in the incinerator exhaust gas will increase, so the exhaust gas treatment device will have an excessive amount of radioactivity removal performance. Will be required. That is,
Exhaust gas treatment equipment becomes complicated and large-scale. In addition, the radioactivity concentration of incinerated ash is high, and its handling is not easy.

2)熱分解;不活性雰囲気で高温で加熱分解させ、その
後分解ガスを燃焼させる方法である。焼却法に比べ、煤
塵が少ないが、熱分解工程が余分に必要であり、また生
成物の放射能濃度が高い。
2) Pyrolysis: This is a method of thermally decomposing at a high temperature in an inert atmosphere, and then burning the decomposed gas. Compared to the incineration method, it has less soot and dust, but requires an additional thermal decomposition step, and the product has a high radioactivity concentration.

3)化学分解法;化学薬品との化学反応により樹脂を酸
分解するものであるが、強力な酸及び酸化剤を高温で取
り扱うため装置構成材料の腐食が問題となる。
3) Chemical decomposition method: A resin is acid-decomposed by a chemical reaction with a chemical agent, but since a strong acid and an oxidizer are handled at high temperatures, corrosion of equipment constituent materials becomes a problem.

4)直接固化法;セメント、アスフアルト、プラスチツ
クで樹脂を直接固化する方法であるが、樹脂の放射能レ
ベルが高いため、長期間の保管中に樹脂が放射線劣化を
生じ、pHの低下、ガス発生等を伴ない、固化体の損傷ひ
いては容器(ドラム缶)の損傷につながる。
4) Direct solidification method: This is a method of directly solidifying the resin with cement, asphalt, or plastic, but the high radioactivity level of the resin causes the resin to deteriorate due to radiation during long-term storage, lowering the pH and generating gas. As a result, damage to the solidified body and eventually damage to the container (drum can) will occur.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

比較的高レベルの樹脂を固化(アスフアルト、プラスチ
ツク、セメント等による)、又はHIC充填する場合にお
いて、 1)樹脂中の放射能濃度を低減させる。
When solidifying a relatively high level of resin (using asphalt, plastic, cement, etc.) or HIC filling, 1) reduce the radioactivity concentration in the resin.

2)この結果、保管中に樹脂自体が受ける放射線損傷を
低下する。
2) As a result, the radiation damage to the resin itself during storage is reduced.

3)このことから固化体の樹脂の劣化を防止し、ひいて
は固化体及び容器の健全性を維持させる。
3) From this, deterioration of the resin of the solidified body is prevented, and the soundness of the solidified body and the container is maintained.

又、樹脂を旋却する場合においては 1)樹脂中の放射能濃度を低減させることにより、排ガ
スへの放射能量を低下させる。
In addition, in the case of rotating the resin, 1) the radioactivity concentration in the exhaust gas is reduced by reducing the radioactivity concentration in the resin.

2)ひいては既設の焼却炉での焼却が可能となり、新設
設備が不要となる。
2) As a result, it is possible to incinerate in an existing incinerator, and no new equipment is required.

3)溶離液中の酸を高収率で回収することにより核種を
高濃縮し、セメント固化体の量を減少させる。
3) The acid in the eluent is recovered in high yield to highly concentrate the nuclide and reduce the amount of the cement solidified product.

本発明は上述したような目的を達成できる放射性イオン
交換樹脂の処理方法提供しようとするものである。
The present invention is intended to provide a method for treating a radioactive ion exchange resin capable of achieving the above-mentioned object.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は放射性イオン交換樹脂に吸着している中・長半
減期の放射性核種を酸溶液を用いて溶離し、該溶離液を
第一の拡散透析槽へ通液して酸を回収し、核種を含む酸
廃液は濃縮器で濃縮した後、第二の拡散透析槽へ通液し
て再度酸回収を行い、この酸廃液を濃縮したのち拡散透
析槽を通して酸回収する工程を少なくとも1回行うよう
にし、これにより溶離液から核種を高濃縮で回収し固化
体とし、また酸は高収率で回収して再利用し、二次廃棄
物の低減をはかり、核種が取り除かれた樹脂は焼却処分
することを特徴とする放射性イオン交換樹脂の処理方法
である。
The present invention is to elute a medium- or long-half-life radionuclide adsorbed on a radioactive ion exchange resin using an acid solution, and pass the eluate through a first diffusion dialysis tank to recover the acid, After the acid waste liquid containing is concentrated in the concentrator, it is passed through the second diffusion dialysis tank to recover the acid again, and the acid waste solution is concentrated, and then the step of recovering the acid through the diffusion dialysis tank is performed at least once. As a result, nuclides are collected from the eluent with high concentration to form a solidified product, and acids are collected and reused in high yield to reduce secondary waste, and the resin from which nuclides have been removed is incinerated. The method for treating a radioactive ion exchange resin is characterized by

本発明においては、先ず中・長半減期核種(Co,Csな
ど)を吸着している樹脂に、酸溶液、例えばH2SO4溶液
を通液し、樹脂より該核種を溶離させ、これにより樹脂
を低放射能レベル材料として扱うことを可能とさせて低
放射能レベル用焼却炉の適用を可能とする。一方、溶離
液は2段以上に設けられた拡散透析槽へ通液することに
より、核種と溶離液中の酸を高い効率で分離する。この
ようにすることにより溶離液中の酸は再利用が可能とな
り二次廃棄物を低減させることができる。核種は拡散透
析槽によつて高濃縮され、比較的少量のセメント固化体
として無機物状態で保管される。
In the present invention, first, an acid solution, for example, a H 2 SO 4 solution is passed through a resin that has adsorbed medium-long half-life nuclides (Co, Cs, etc.) to elute the nuclide from the resin. The resin can be treated as a low activity level material and the application of an incinerator for low activity level is possible. On the other hand, the eluent is passed through a diffusion dialysis tank provided in two or more stages to separate the nuclide and the acid in the eluent with high efficiency. By doing so, the acid in the eluent can be reused and secondary waste can be reduced. The nuclide is highly concentrated by a diffusion dialysis tank and stored in a relatively small amount as a cement solidified body in an inorganic state.

〔作用〕[Action]

樹脂と放射性核種を分離することで、樹脂は焼却、核種
は無機材に封び込めるという既知の技術の組み合せのみ
で、実質上樹脂を無機体とすることができる。
By separating the resin and the radionuclide, the resin can be practically made into an inorganic substance only by a combination of known techniques in which the resin is incinerated and the nuclide is sealed in the inorganic material.

〔実施例〕〔Example〕

本発明の一実施態様を第1図によつて説明し、その物質
収支を第1表に示す。
One embodiment of the present invention will be described with reference to FIG. 1, and its mass balance is shown in Table 1.

第1図において、先ず樹脂は廃樹脂貯蔵タンク1より定
量取り出し樹脂処理槽2に充填される。次いで一定濃度
(2規定程度)のH2SO4をライン8より圧送し通液す
る。この時、樹脂処理槽2では樹脂より核種(Cs+、Co
2+など)が溶離しH+が吸着する。(H2SO4が消費され
る) この槽2の下流には第一段拡散透析槽3が設置されてい
る。該槽3には陰イオン交換膜10が配置されており、こ
れにより該槽3は室を二つに分けられている。こゝで純
水と上記工程からの溶離液とを陰イオン交換膜10を介し
て図示のようにカウンターフローで流すと、H2SO4は右
室へ移動し、核種はそのまま同室に残りつづいて槽外へ
出て行く。
In FIG. 1, first, a fixed amount of resin is taken out from a waste resin storage tank 1 and filled in a resin processing tank 2. Next, H 2 SO 4 having a constant concentration (about 2 N) is pressure-fed through the line 8 to pass the liquid. At this time, in the resin treatment tank 2, nuclides (Cs + , Co
2+ ) elutes and H + adsorbs. (H 2 SO 4 is consumed) A first stage diffusion dialysis tank 3 is installed downstream of this tank 2. An anion exchange membrane 10 is arranged in the tank 3 so that the tank 3 is divided into two chambers. When pure water and the eluent from the above process are flown through the anion exchange membrane 10 in a counter flow as shown in the figure, H 2 SO 4 moves to the right chamber, and the nuclide remains in the same chamber. Go out of the tank.

この核種を含んだ液は次に濃縮器5で濃縮され、液量は
極端に減少させられる。又、この液中には、第一拡散透
析槽3で右室へ移動しなかつたH2SO4があり、これも同
様に濃縮器5で濃縮される。
The liquid containing this nuclide is then concentrated in the concentrator 5, and the liquid amount is extremely reduced. Further, in this solution, there is H 2 SO 4 that has not moved to the right chamber in the first diffusion dialysis tank 3, and this is also concentrated in the concentrator 5.

そこでこの濃縮液を、第1段拡散透析槽3と同一構造の
第2段拡散透析槽4へ導き、更にここでH2SO4を右室へ
移動させ回収する。第2段拡散透析槽4でも同じく左室
の核種はそのまま槽4より流出して行く。この操作を繰
り返すことにより核種を含んだ液は、その容積を極めて
減少させることができる。
Therefore, this concentrated liquid is guided to the second-stage diffusion dialysis tank 4 having the same structure as the first-stage diffusion dialysis tank 3, and further, H 2 SO 4 is moved to the right chamber and collected. In the second-stage diffusion dialysis tank 4, the nuclide in the left ventricle also flows out from the tank 4 as it is. By repeating this operation, the volume of the liquid containing the nuclide can be extremely reduced.

なお表−1の物質収支差は、使用樹脂10m3/年のデータ
で、表中の〇印についた符号は、第1図の〇印のついた
符号の位置を示し、拡散透析槽を2段とした例でああ
る。
The material balance difference in Table-1 is the data of resin used 10 m 3 / year, and the symbol marked with ◯ in the table indicates the position of the symbol marked with ◯ in FIG. This is a tiered example.

第2段拡散透析槽4より排出した核種を含む液は若干
のH2SO4を含むため、NaOHで中和槽6で中和され更に濃
縮器7でNa2SO4の溶解度(25wt%)まで濃縮され、その
ままセメント固化される。
Since the liquid containing the nuclide discharged from the second-stage diffusion dialysis tank 4 contains a small amount of H 2 SO 4 , it is neutralized in the neutralization tank 6 with NaOH and the solubility of Na 2 SO 4 in the concentrator 7 (25 wt%) It is concentrated until it is solidified with cement.

一方、核種の無くなつた樹脂は焼却炉9で焼却され灰分
として回収される。
On the other hand, the nuclide-free resin is incinerated in the incinerator 9 and collected as ash.

又、消費及び回収しきれなかつたH2SO4に相当する量はH
2SO4メークアツプライン8より補給される。
Also, the amount equivalent to H 2 SO 4 that could not be consumed and recovered was H
2 SO 4 Makeup line 8 is supplied.

なお、Na2SO4はこのままセメント固化される。セメント
固化の本数はこの例では78/バツチ×20バツチ/年=
1560/年であるのでドラム缶1本に100入れるとす
ると1560/年/100/本=15.6/年≒16本/年とな
り、樹脂10m3/年をそのまま200容器に入れると50本/
年必要であつたのに対し、かなりの減容効果が得られ
る。
Note that Na 2 SO 4 is cemented as it is. In this example, the number of cement solidifications is 78 / batch x 20 batch / year =
Since it is 1560 / year, if we put 100 in one drum, it will be 1560 / year / 100 / piece = 15.6 / year ≈ 16 / year, and if we put resin 10m 3 / year in 200 containers as it is, 50 /
Although it was necessary for a year, a considerable volume reduction effect can be obtained.

〔発明の効果〕 本発明は、放射性イオン交換樹脂の処理において、酸溶
液により核種と樹脂を分離させ、核種を分離除去された
樹脂は焼却処理を行ない、核種を含む酸は2段に組まれ
た拡散透析槽で高い効率で核種と酸を分離し、酸は再利
用し、核種は少数のセメント固化体として無機安定化す
るため、放射性イオン交換樹脂を著しくく減容化させる
ことができる。
EFFECTS OF THE INVENTION In the treatment of the radioactive ion exchange resin, the present invention separates the nuclide and the resin by an acid solution, the resin from which the nuclide is separated and removed is incinerated, and the acid containing the nuclide is assembled in two stages. In the diffusion dialysis tank, the nuclide and the acid are separated with high efficiency, the acid is reused, and the nuclide is inorganic-stabilized as a small amount of cement solidified product, so that the radioactive ion exchange resin can be significantly reduced in volume.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の一実施態様の説明図である。 FIG. 1 is an explanatory diagram of an embodiment of the present invention.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 船越 俊夫 兵庫県高砂市荒井町新浜2丁目1番1号 三菱重工業株式会社高砂研究所内 (72)発明者 川村 亘 兵庫県高砂市荒井町新浜2丁目1番1号 三菱重工業株式会社高砂研究所内 (72)発明者 稲垣 雄三 兵庫県神戸市兵庫区小松通5丁目1番16号 株式会社神菱ハイテツク内 (56)参考文献 特開 昭59−51399(JP,A) 特開 昭61−155898(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Toshio Funakoshi 2-1-1, Niihama, Arai-cho, Takasago, Hyogo Prefecture Mitsubishi Heavy Industries, Ltd. Takasago Laboratory (72) Inventor Wataru Kawamura 2--1, Niihama, Arai-cho, Takasago, Hyogo Prefecture No. 1 Mitsubishi Heavy Industries, Ltd. Takasago Research Institute (72) Inventor Yuzo Inagaki 5-16 Komatsudori, Hyogo-ku, Kobe, Hyogo Prefecture (56) Shinryo High-Tech Co., Ltd. (56) Reference JP-A-59-51399 A) JP-A-61-155898 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】放射性イオン交換樹脂に吸着している中・
長半減期の放射性核種を酸溶液を用いて溶離し、該溶離
液を第一の拡散透析槽へ通液して酸を回収し、核種を含
む酸廃液は濃縮器で濃縮した後、第二の拡散透析槽へ通
液して再度酸回収を行い、この酸廃液を濃縮したのち拡
散透析槽を通して酸回収する工程を少なくとも1回行う
ようにし、これにより溶離液から核種を高濃縮で回収し
固化体とし、また酸は高収率で回収して再利用し、二次
廃棄物の低減をはかり、核種が取り除かれた樹脂は焼却
処分することを特徴とする放射性イオン交換樹脂の処理
方法。
1. Adsorbed on a radioactive ion exchange resin
The long half-life radionuclide is eluted with an acid solution, the eluate is passed through a first diffusion dialysis tank to recover the acid, and the acid waste solution containing the nuclide is concentrated in a concentrator, The acid is recovered again by passing it through the diffusion dialysis tank, and the step of concentrating the acid waste solution and then recovering the acid through the diffusion dialysis tank is carried out at least once, whereby highly concentrated nuclides are recovered from the eluent. A method for treating a radioactive ion exchange resin, which is characterized in that the resin is solidified, the acid is recovered in high yield and reused, secondary waste is reduced, and the resin from which the nuclide has been removed is incinerated.
JP61242122A 1986-10-14 1986-10-14 Treatment method of radioactive ion exchange resin Expired - Lifetime JPH0672957B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61242122A JPH0672957B2 (en) 1986-10-14 1986-10-14 Treatment method of radioactive ion exchange resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61242122A JPH0672957B2 (en) 1986-10-14 1986-10-14 Treatment method of radioactive ion exchange resin

Publications (2)

Publication Number Publication Date
JPS6396600A JPS6396600A (en) 1988-04-27
JPH0672957B2 true JPH0672957B2 (en) 1994-09-14

Family

ID=17084624

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61242122A Expired - Lifetime JPH0672957B2 (en) 1986-10-14 1986-10-14 Treatment method of radioactive ion exchange resin

Country Status (1)

Country Link
JP (1) JPH0672957B2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5951399A (en) * 1982-09-17 1984-03-24 株式会社荏原製作所 Method of heating and volume-decreasing ion exchanging resinhaving radioactivity material
JPS61155898A (en) * 1984-12-28 1986-07-15 株式会社日立製作所 Treater for regenerated waste liquor of ion exchnage resin

Also Published As

Publication number Publication date
JPS6396600A (en) 1988-04-27

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