JPS6262299A - Method of processing radioactive ion exchange resin - Google Patents
Method of processing radioactive ion exchange resinInfo
- Publication number
- JPS6262299A JPS6262299A JP60200486A JP20048685A JPS6262299A JP S6262299 A JPS6262299 A JP S6262299A JP 60200486 A JP60200486 A JP 60200486A JP 20048685 A JP20048685 A JP 20048685A JP S6262299 A JPS6262299 A JP S6262299A
- Authority
- JP
- Japan
- Prior art keywords
- ion exchange
- resin
- exchange resin
- radioactive ion
- nuclide
- 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
Links
- 238000000034 method Methods 0.000 title claims description 23
- 239000003456 ion exchange resin Substances 0.000 title claims description 12
- 229920003303 ion-exchange polymer Polymers 0.000 title claims description 12
- 230000002285 radioactive effect Effects 0.000 title claims description 10
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 title claims description 6
- 239000002253 acid Substances 0.000 claims description 18
- 239000003480 eluent Substances 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 8
- 238000000354 decomposition reaction Methods 0.000 claims description 7
- 238000000502 dialysis Methods 0.000 claims description 7
- 238000009792 diffusion process Methods 0.000 claims description 7
- 239000012670 alkaline solution Substances 0.000 claims description 4
- 238000007711 solidification Methods 0.000 claims description 3
- 230000008023 solidification Effects 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims 1
- 239000011347 resin Substances 0.000 description 22
- 229920005989 resin Polymers 0.000 description 22
- 239000000126 substance Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000003011 anion exchange membrane Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 210000005241 right ventricle Anatomy 0.000 description 3
- 241000218691 Cupressaceae Species 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000002144 chemical decomposition reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 210000003127 knee Anatomy 0.000 description 1
- 210000005240 left ventricle Anatomy 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000012857 radioactive material Substances 0.000 description 1
- 239000000941 radioactive substance Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- 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】
(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使用済イオン交換
樹脂の安定化処理方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for stabilizing used ion exchange resins stored in nuclear facilities.
(従来の技術)
使用済イオン交換樹脂(以下、単に@脂という)の処理
方法として、未だ長期適用例はないが、下記のような種
々の技術が提案され、ている。(Prior Art) As a method for disposing of used ion exchange resins (hereinafter simply referred to as @fat), various techniques have been proposed, such as those described below, although there are still no examples of long-term application.
(13焼却法;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、燃焼排ガス中に含まれる
放射能量も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Kなる。すなわち排ガス処
理装置が複雑大規模化する。また焼却灰の放射性濃度が
高くなルその取扱いが容易でない。(13 Incineration method: This is a method of incinerating resin, but if the radioactivity level contained in the resin is high, the amount of radioactivity contained in the combustion exhaust gas will also increase, so excessive radioactivity removal performance is required of the exhaust gas treatment equipment. In other words, the exhaust gas treatment equipment becomes complicated and large-scale.Furthermore, the radioactive concentration of the incinerated ash is high, making it difficult to handle it.
(2)熱分解法;不活性雰囲気て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。(2) Pyrolysis method; thermal decomposition at high temperature in an inert atmosphere,
This method then combusts the cracked gas.
焼却法に比べ煤塵が少ない有利性があるが熱分解工程が
余分に必要という不利益があシ、また生成物の放射能濃
度が高い点では燃焼法と同様である。This method has the advantage of producing less dust compared to the incineration method, but has the disadvantage of requiring an extra thermal decomposition step, and is similar to the combustion method in that the radioactivity concentration of the product is high.
(3)化学分解法;化学薬品との化学反応によシ樹脂を
酸分解するものであるが、強力な酸及び酸化剤を高温で
取扱うので装置構成材料の腐食が問題となる。また放射
能レベルが高くメンテナンスに困難を伴う。(3) Chemical decomposition method: This method involves acid decomposing the resin through a chemical reaction with chemicals, but since strong acids and oxidizing agents are handled at high temperatures, corrosion of the equipment constituent materials becomes a problem. Furthermore, the radioactivity level is high and maintenance is difficult.
(4)直接同化法;セメント、アスファルト、プラスチ
ッ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
を住じ、−の低下、ガスの発生を伴い、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 assimilation method: This is a method in which resin is directly solidified with cement, asphalt, or plastic, but because the resin has a high radioactivity level, the resin suffers radiation deterioration during long-term storage, resulting in a decrease in - Damage to the solidified material due to the generation of gas,
This will eventually lead to damage to the container (drum).
(発明が解決しようとする問題点)
本発明は、比較的高いレベルの樹脂を酸分解する場合に
おいて、樹脂に吸着している放射性物質を溶離(分離)
することで樹脂は低レベル物質として扱えるようにして
、樹脂を酸分解する場合、装置の汚染レベルが低く維持
でき、メンテナンスが容易となシ、引いては運転の向上
につながシ、一方樹脂から分離した核種は拡散透析槽を
経て、濃縮し、固化体としうる放射性イオン交換樹脂の
処理方法を提供しようとするものである。(Problems to be Solved by the Invention) The present invention is designed to elute (separate) radioactive substances adsorbed to the resin when acid decomposing a resin at a relatively high level.
By doing so, the resin can be treated as a low-level substance, and when the resin is subjected to acid decomposition, the contamination level of the equipment can be kept low, maintenance is easier, and operation is improved, while the resin can be treated as a low-level substance. The separated nuclides pass through a diffusion dialysis tank and are concentrated to provide a method for treating radioactive ion exchange resins that can be solidified.
(問題点を解決するための手段)
本発明は放射性イオン交換樹脂の処理にあたり、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
核種をアルカリ溶液又は酸溶液よ)なる溶離液を用いて
溶離し、該核種を溶離したイオン交換樹脂は酸分解法に
よシ処理し、該核種を溶離した溶離液は拡散透析槽に通
液し放射性核me縮液と再生溶離液とに分離し、後者は
系において再使用し、前者は濃縮固化することを特徴と
する放射性イオン交換樹脂の処理方法である。(Means for Solving the Problems) In the treatment of radioactive ion exchange resins, the present invention uses an eluent (alkaline solution or acid solution) to remove radionuclides with medium to long half-lives that are adsorbed on the radioactive ion exchange resin. The ion exchange resin from which the nuclide was eluted was treated by an acid decomposition method, and the eluent from which the nuclide was eluted was passed through a diffusion dialysis tank to form a radioactive nuclear mecondensate and a regenerated eluent. This is a method for treating radioactive ion exchange resin, which is characterized by separating the resin, reusing the latter in the system, and concentrating and solidifying the former.
すなわち、本発明では樹脂が吸着している中・長半減期
の核種(Co−60,0s−434,−137,5r−
90など)を、NaOH,KOHなどのアルカリ溶液又
はH2S04などの酸溶液のHa+、に+又は鱈のイオ
ンを利用して、樹脂よシ溶離させることによシ、樹脂を
低レベル放射能材料として取扱うことを可能とし、通常
の酸分解装置の汚染レベルを低く維持しメンテナンスを
容易にしたものである。That is, in the present invention, nuclides with medium to long half-lives (Co-60, 0s-434, -137, 5r-
90, etc.) is eluted from the resin using Ha+, Ni+, or Cod ions in an alkaline solution such as NaOH, KOH or an acid solution such as H2S04, the resin can be used as a low-level radioactive material. This makes it possible to maintain low contamination levels in conventional acid decomposition equipment and facilitate maintenance.
また溶離に使用したアルカリ溶液又は酸溶液は拡散透析
槽に通液し、その溶液中の核種を濃縮した核種濃縮液と
再生溶離液とに分離し、後者は再度樹脂からの核種の溶
離に利用し、前者は濃縮固化する。この結果、二次廃棄
物を低減させ得ることにもなる。In addition, the alkaline solution or acid solution used for elution is passed through a diffusion dialysis tank, and the nuclide in the solution is separated into a concentrated nuclide solution and a regenerated eluent, and the latter is used again to elute the nuclide from the resin. However, the former is concentrated and solidified. As a result, secondary waste can also be reduced.
拡散透析槽において使用される膜としては、一般的には
半透膜が用いられるが、溶離液が酸溶液の時は陰イオン
交換膜であるセレミオン、ネオセプタ、ユニレックス等
(いずれも商品名)を使用するのが好ましい。Semipermeable membranes are generally used as membranes in diffusion dialysis tanks, but when the eluent is an acid solution, anion exchange membranes such as Selemion, Neocepta, and Unirex (all trade names) are used. It is preferable to use
以下、本発明の一実施態様を説明する。Hereinafter, one embodiment of the present invention will be described.
第1図に本発明方法を実施するためのフローを示す。FIG. 1 shows a flow for implementing the method of the present invention.
まず樹脂は廃樹脂貯蔵タンク1より、一定量(こ工では
0.25扉37回)取シ出し、樹脂処理槽2に充填され
る。次いで一定濃度(約9%)のH2S04をポンプ4
によ)通液する。この時、樹脂処理槽2で社核種が溶離
し、鱈が吸着する。(H2S04が消費される)。First, a fixed amount of resin is taken out from the waste resin storage tank 1 (in this process, 0.25 door 37 times) and filled into the resin processing tank 2. Next, pump 4 H2S04 at a constant concentration (approximately 9%).
) Pour the liquid through. At this time, the nuclides are eluted in the resin treatment tank 2, and the cod is adsorbed. (H2S04 is consumed).
この槽2の下流には拡散透析槽3が設置してあシ、又槽
3内には、陰イオン交換膜3′が配設され檜3を左室と
右室に2分している。今、核種を含む溶離液を左室へ上
向流で通液し、一方布室には下向流で純水を流すと、こ
の間に檜3内では、溶離液中のHBOは鱈とSOニーに
解離し、SOニー 陰イオン交換膜3′を通過し、右室
へ移動する。一方、溶離した核種(Cjo”、CjB+
など)はイオン的に反ばつし合い、右室へ移動しない
。このことから酸(H2S04)と核種を分離すること
ができる。回収された酸は再度溶離液として利用される
。A diffusion dialysis tank 3 is installed downstream of this tank 2, and an anion exchange membrane 3' is provided inside the tank 3 to divide the cypress 3 into a left ventricle and a right ventricle. Now, if the eluent containing nuclides is passed in an upward flow to the left chamber, while pure water is passed in a downward flow to the cloth chamber, during this time, in the cypress 3, the HBO in the eluent is mixed with cod and SO. It dissociates into the SO knee, passes through the anion exchange membrane 3', and moves to the right ventricle. On the other hand, the eluted nuclides (Cjo”, CjB+
) are ionically repulsed by each other and do not move to the right ventricle. From this, the acid (H2S04) and the nuclide can be separated. The recovered acid is used again as an eluent.
このように核種と溶離液を分離回収利用することで、二
次廃棄物量の低減が図れる。核種を含んだ液は小型蒸発
装置6によシ濃縮後、直接同化体8とする。By separating and recovering the nuclide and the eluent in this way, it is possible to reduce the amount of secondary waste. The liquid containing the nuclide is concentrated in a small evaporator 6 and then directly converted into an assimilate 8.
一方、放射性核種が抜き取られた樹脂は、酸分解槽5へ
導かれる。ここでは、 H2O2−Fe系又はH2BO
3−HNO,系などの薬液で樹脂を化学的に分解される
。この分解液は、若干の未分解物を含んでいるが放射能
レベル的には、充分低いため既設の廃液処理系で処理す
る。つまシ、既設のエバポレーター9を経て、固化装置
10へ導かれる。この操作を行なうことで、核種の同化
体と既設固化装置からの固化体と2種の固化体が作成さ
れるが、これは分別管理として利用することもできる。On the other hand, the resin from which the radionuclides have been extracted is led to the acid decomposition tank 5. Here, H2O2-Fe system or H2BO
The resin is chemically decomposed with a chemical solution such as 3-HNO. Although this decomposed liquid contains some undecomposed substances, its radioactivity level is sufficiently low and is therefore treated with the existing waste liquid treatment system. After passing through the existing evaporator 9, it is led to the solidification device 10. By performing this operation, two types of solidified bodies are created: the assimilated body of the nuclide and the solidified body from the existing solidification equipment, which can also be used for separate management.
酸分解条件の一般的な条件を下表に示す。General acid decomposition conditions are shown in the table below.
但し、方法A : H2So4+ HNO3混合液B:
H2SO4+H2O2混合液
C: H2O+H2O2(Fe触媒)混合液以上、溶離
液として酸(H2S04)を使用した場合について説明
したが、溶離液としてアルカリを使用する時には、拡散
透析槽の隔膜を半透膜を使用することによって略々同様
な結果が得られる。However, method A: H2So4+ HNO3 mixture B:
H2SO4 + H2O2 mixture C: H2O + H2O2 (Fe catalyst) mixture Above, we have explained the case where acid (H2S04) is used as the eluent, but when using alkali as the eluent, a semipermeable membrane is used as the diaphragm of the diffusion dialysis tank. Almost the same result can be obtained by doing this.
(発明の効果) 樹脂から核種を取)除いているため、 1)酸分解装置の線量が低くおさえることができる。(Effect of the invention) Because the nuclide is removed from the resin, 1) The dose of acid decomposition equipment can be kept low.
2)シたがって装置のメンテナンスが容易となシ、ひい
ては運転性の向上につながる。2) Therefore, maintenance of the device becomes easier, which in turn leads to improved operability.
3)又固化体を高、低レベルに分けることができ、分別
管理に利用できる。3) Also, the solidified material can be divided into high and low levels, and can be used for separate management.
第1図は本発明方法を実施するための70−を示す。 復代理人 内 1) 明 復代理人 萩 原 亮 − 復代理人 安 西 篤 夫 FIG. 1 shows a 70- for carrying out the method of the invention. Among the sub-agents: 1) Akira Sub-agent Ryo Hagi Hara - Sub-agent Atsuo Annishi
Claims (1)
換樹脂に吸着している、中・長半減期の放射性核種をア
ルカリ溶液又は酸溶液よりなる溶離液を用いて溶離し、
該核種を溶離したイオン交換樹脂は酸分解法により処理
し、該核種を溶離した溶離液は拡散透析槽に通液し放射
性核種濃縮液と再生溶離液とに分離し、後者は系におい
て再使用し、前者は濃縮固化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。When treating radioactive ion exchange resins, radionuclides with medium and long half-lives adsorbed on the radioactive ion exchange resins are eluted using an eluent consisting of an alkaline solution or an acid solution.
The ion exchange resin that has eluted the nuclide is treated with an acid decomposition method, and the eluate that has eluted the nuclide is passed through a diffusion dialysis tank and separated into a radionuclide concentrate and a regenerated eluate, with the latter being reused in the system. However, the former is a method for processing radioactive ion exchange resin, which is characterized by concentration and solidification.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60200486A JPS6262299A (en) | 1985-09-12 | 1985-09-12 | Method of processing radioactive ion exchange resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60200486A JPS6262299A (en) | 1985-09-12 | 1985-09-12 | Method of processing radioactive ion exchange resin |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6262299A true JPS6262299A (en) | 1987-03-18 |
Family
ID=16425112
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60200486A Pending JPS6262299A (en) | 1985-09-12 | 1985-09-12 | Method of processing radioactive ion exchange resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6262299A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4833379B1 (en) * | 2011-07-25 | 2011-12-07 | 技研興業株式会社 | Lead plate laminating parts and lead plate laminating method |
-
1985
- 1985-09-12 JP JP60200486A patent/JPS6262299A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4833379B1 (en) * | 2011-07-25 | 2011-12-07 | 技研興業株式会社 | Lead plate laminating parts and lead plate laminating method |
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