JPS6041320B2 - Processing method for waste ion exchange resin in heavy water-moderated nuclear reactors - Google Patents
Processing method for waste ion exchange resin in heavy water-moderated nuclear reactorsInfo
- Publication number
- JPS6041320B2 JPS6041320B2 JP5623780A JP5623780A JPS6041320B2 JP S6041320 B2 JPS6041320 B2 JP S6041320B2 JP 5623780 A JP5623780 A JP 5623780A JP 5623780 A JP5623780 A JP 5623780A JP S6041320 B2 JPS6041320 B2 JP S6041320B2
- Authority
- JP
- Japan
- Prior art keywords
- heavy water
- water
- waste
- resin
- ion exchange
- 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
Links
- 239000002699 waste material Substances 0.000 title claims description 29
- 239000003456 ion exchange resin Substances 0.000 title claims description 8
- 229920003303 ion-exchange polymer Polymers 0.000 title claims description 8
- 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
- 238000003672 processing method Methods 0.000 title 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N Heavy water Chemical compound [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 claims description 78
- 239000011347 resin Substances 0.000 claims description 41
- 229920005989 resin Polymers 0.000 claims description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- 238000000746 purification Methods 0.000 claims description 15
- YZCKVEUIGOORGS-NJFSPNSNSA-N Tritium Chemical compound [3H] YZCKVEUIGOORGS-NJFSPNSNSA-N 0.000 claims description 11
- 229910052722 tritium Inorganic materials 0.000 claims description 11
- 239000010795 gaseous waste Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 8
- 239000002910 solid waste Substances 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Description
【発明の詳細な説明】
本発明は重水減速型原子炉で使用された廃イオン交換処
理方法に関するものであって、その目的とするところは
、トリチウムの系外放出を防止し、併せて廃イオン交灘
樹脂の滅容化を図って貯蔵に便ならしめることにある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a waste ion exchange treatment method used in a heavy water-moderated nuclear reactor. The aim is to sterilize the resin and make it convenient for storage.
重水減速型原子炉に於ては、重水中に漆出した金属を取
り除いて重水を浄化する目的で、イオン交換樹脂が使用
されるが、重水との接触によってイオン交手製樹脂の金
属除去能は次第に低下するため、原子炉の重水浄化設備
では、金属除去能が衰微した廃イオン交≠剣樹脂(以下
、廃樹脂と略記する)が、新しいイオン交換樹脂(以下
、新樹脂と略記する)と交換され、廃樹脂は廃棄処分に
付されている。ところで廃樹脂を処分する場合、従来は
廃樹脂が保有する重水を軽水で置換させて廃樹脂を軽水
化した後、これを樹脂移送水と共に系外に放出し、廃樹
脂についてはこれをそのまま適当なタンクに収容して貯
蔵する方法が採用されている。In heavy water-moderated nuclear reactors, ion exchange resins are used to purify heavy water by removing metals that have been lacquered in the heavy water, but the ability of ion exchange resins to remove metals is affected by contact with heavy water. As a result, in heavy water purification equipment of nuclear reactors, waste ion exchange resin (hereinafter abbreviated as waste resin) whose metal removal ability has declined is replaced with new ion exchange resin (hereinafter abbreviated as new resin). It has been replaced and the waste resin has been disposed of. By the way, when disposing of waste resin, conventionally, the heavy water held by the waste resin is replaced with light water to make the waste resin lighter water, and then this is discharged outside the system along with the resin transfer water, and the waste resin is left as it is as it is. A method of storing it in a tank is adopted.
しかし、この方法では軽水化後の廃樹脂及び樹脂移送水
に含まれるトリチウムが系外に放出されてしまう点で問
題があるばかりでなく、廃樹脂がそのままの形状で貯蔵
される関係上、嵩張ってしまう点でも好ましくない。本
発明は廃樹脂を焼却することによって上記した従来法の
欠点を一挙に解消した廃樹脂の新しい処理方法を提案す
るものであって、その方法は重水減速型原子炉の重水浄
化設備で使用された廃イオン交モ期間脂に軽水を加え、
樹脂が保有するトリチゥム含有重水を軽水と置換させて
樹脂を軽水化すると共に劣化重水を回収し、この劣化重
水を重水精製設備でトリチゥム含有重水と軽水に分離後
、トリチウム含有重水を前記の重水浄化設備に循環させ
、軽水化された樹脂を焼却して気体廃棄物と固体廃棄物
を生成させ、この固体廃棄物はこれを任意の形状に成型
して貯蔵し、一方、前記の気体廃棄物はこれを凝縮器に
送って気体廃棄物中の水蒸気を凝縮させ、得られた凝縮
水を廃樹脂の軽水化用軽水の一部及び/又は廃樹脂の移
送水の一部として使用し、前記の凝縮器から排出される
非凝縮性気体をフィルターに通した後系外に放出するこ
とからなる。However, this method not only has a problem in that the tritium contained in the waste resin and resin transfer water after lightening is released outside the system, but also because the waste resin is stored in its original form, which makes it bulky. I also don't like it because it makes it tense. The present invention proposes a new method for treating waste resin that eliminates all the drawbacks of the conventional methods described above by incinerating the waste resin, and this method is used in heavy water purification equipment for heavy water-moderated nuclear reactors. Add light water to the waste ionized fat,
The tritium-containing heavy water held by the resin is replaced with light water to make the resin lighter, and the degraded heavy water is recovered. After separating this degraded heavy water into tritium-containing heavy water and light water using heavy water purification equipment, the tritium-containing heavy water is purified as described above. The resin is circulated through the equipment and the lightened resin is incinerated to produce gaseous waste and solid waste, which is molded into any shape and stored. This is sent to a condenser to condense the water vapor in the gaseous waste, and the resulting condensed water is used as part of the light water for converting waste resin into water and/or as part of the waste resin transfer water. It consists of passing non-condensable gas discharged from the condenser through a filter and then releasing it outside the system.
以下、添付図面にそって本発明の方法をさらに具体的に
説明すると、原子炉の重水浄化設備1では重水の浄化に
使用された廃樹脂に軽水が注加され、廃樹脂が保有する
重水を軽水に置換させることを内容とする擬樹脂の軽水
化が行なわれる。Hereinafter, the method of the present invention will be explained in more detail with reference to the attached drawings. In the heavy water purification equipment 1 of a nuclear reactor, light water is poured into waste resin used for purification of heavy water, and the heavy water held by the waste resin is removed. Water-lightening of pseudo-resin is carried out by replacing it with light water.
この際、重水に軽水が混入した劣化重水が得られるが、
この劣化重水は従来法通り、ライン7を介して重水精製
設備5に送り、例えば分別蒸留などの手段によってトリ
チウム含有重水と軽水とに分離後、トリチゥム含有重水
はライン8を介して重水浄化設備1に戻し、軽水はライ
ン9から系外に放出することができる。重水浄化設備1
で軽水化された廃樹脂は、樹脂移送水(軽水)と共にラ
イン10を経て焼却設備2に送られる。At this time, degraded heavy water is obtained, which is a mixture of heavy water and light water.
As in the conventional method, this degraded heavy water is sent to the heavy water purification facility 5 via line 7, and after being separated into tritium-containing heavy water and light water by means such as fractional distillation, the tritium-containing heavy water is sent via line 8 to the heavy water purification facility 1. The light water can be discharged out of the system through line 9. Heavy water purification equipment 1
The waste resin that has been reduced to light water is sent to the incineration facility 2 through a line 10 together with resin transfer water (light water).
この間、重水浄化設備1には新樹脂がライン16から補
給され、新樹脂が保有する軽水を重水で置換させること
を内容とする新樹脂の重水化が行なわれることは勿論で
ある。尚、新樹脂の重水化に際しては、廃樹脂を軽水化
する場合と同様、劣化重水が生ずるが、この劣化重水は
上記したところと全く同様に処理することができる。焼
却設備2に供V給された廃樹脂は、ここで焼却され、気
体廃棄物と固体廃棄物が生成される。During this time, new resin is supplied to the heavy water purification equipment 1 from the line 16, and it goes without saying that the new resin is converted into heavy water by replacing the light water held by the new resin with heavy water. Incidentally, when converting new resin into heavy water, degraded heavy water is produced as in the case where waste resin is converted into light water, but this degraded heavy water can be treated in exactly the same manner as described above. The waste resin supplied to the incineration facility 2 is incinerated here to generate gaseous waste and solid waste.
固体廃棄物は灰などの焼却残律からなるが、これらはラ
イン11を経て固形化設備3に送られ、ここで任意の形
状に成型された後、貯蔵設備などに収容される。一方、
競却設備2からライン12に取り出される気体廃棄物は
、凝縮器4に導かれ、トリチウムを含有する水蒸気はこ
こで凝縮された後、ライン13を経て重水浄化設備1に
戻され、廃樹脂の軽水化用水及び/又は樹脂の移送水と
して再使用される。凝縮器4で凝縮しない非凝縮気体は
、ライン14からフィルター6に送られ、ここで爽雑物
を猿別した後、ライン15を介して系外に放出される。
以上の通り、本発明の方法によれば、廉樹脂は焼却処理
によって減客化が図れるため、廃樹脂を貯蔵するタンク
の容量を大幅に減少させることができる。The solid waste consists of incineration residue such as ash, which is sent to the solidification facility 3 via the line 11, where it is formed into an arbitrary shape and then stored in a storage facility or the like. on the other hand,
The gaseous waste taken out from the competition equipment 2 to the line 12 is led to the condenser 4, where the water vapor containing tritium is condensed, and then returned to the heavy water purification equipment 1 via the line 13, where the waste resin is It is reused as water for lightweighting and/or resin transfer water. Non-condensable gases that are not condensed in the condenser 4 are sent to the filter 6 through a line 14, where impurities are separated, and then discharged to the outside of the system through a line 15.
As described above, according to the method of the present invention, it is possible to reduce the number of customers by incinerating the waste resin, so that the capacity of the tank for storing the waste resin can be significantly reduced.
これに加えて、廃樹脂中の水分、樹脂移送水は、擬樹脂
の承却に際して蒸発せしめられた後、気体廃棄物の凝縮
によって系内に回収されるため、これらに同伴されるト
リチウムが系外に放出される危険を回避することができ
る。In addition, the moisture in the waste resin and the resin transfer water are evaporated when the pseudo-resin is accepted and then recovered into the system by condensation of the gaseous waste, so the tritium entrained in these is collected in the system. The danger of release to the outside can be avoided.
図面は本発明の一実施例を示すブロックダイアグラムで
ある。
1;垂水浄化設備、2;焼却設備、3:固形化設備、4
;凝縮器、5:重水精製設備、6;フィルター。The drawing is a block diagram showing one embodiment of the invention. 1; Tarumi purification equipment, 2; Incineration equipment, 3: Solidification equipment, 4
; Condenser; 5; Heavy water purification equipment; 6; Filter.
Claims (1)
オン交換樹脂に軽水を加え、樹脂が保有するトリチウム
含有重水を軽水と置換させて樹脂を軽水化すると共に劣
化重水を回収し、この劣化重水を重水精製設備でトリチ
ウム含有重水と軽水に分離後、トリチウム含有重水を前
記の重水浄化設備に循環させ、軽水化された樹脂を焼却
して気体廃棄物と固体廃棄物を生成させ、この固体廃棄
物はこれを任意の形状に成型して貯蔵し、一方、前記の
気体廃棄物はこれを凝縮器に送つて気体廃棄物中の水蒸
気を凝縮させ、得られた凝縮水を廃イオン交換樹脂の軽
水化用軽水の一部及び/又は廃イオン交換樹脂移送水の
一部として使用し、前記の凝縮器から排出される非凝縮
性気体をフイルターに通した後系外に放出することから
なる重水減速型原子炉に於ける廃イオン交換樹脂の処理
方法。1 Light water is added to the waste ion exchange resin used in the heavy water purification equipment of a heavy water-moderated nuclear reactor, and the tritium-containing heavy water held in the resin is replaced with light water, making the resin lighter and recovering the degraded heavy water. After heavy water is separated into tritium-containing heavy water and light water using heavy water purification equipment, the tritium-containing heavy water is circulated through the heavy water purification equipment, and the light water resin is incinerated to produce gaseous waste and solid waste. The waste is molded into any shape and stored, while the gaseous waste is sent to a condenser to condense the water vapor in the gaseous waste, and the resulting condensed water is poured into waste ion exchange resin. The non-condensable gas discharged from the condenser is passed through a filter and then released outside the system. A method for treating waste ion exchange resin in a heavy water-moderated nuclear reactor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5623780A JPS6041320B2 (en) | 1980-04-30 | 1980-04-30 | Processing method for waste ion exchange resin in heavy water-moderated nuclear reactors |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5623780A JPS6041320B2 (en) | 1980-04-30 | 1980-04-30 | Processing method for waste ion exchange resin in heavy water-moderated nuclear reactors |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56153297A JPS56153297A (en) | 1981-11-27 |
| JPS6041320B2 true JPS6041320B2 (en) | 1985-09-14 |
Family
ID=13021482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5623780A Expired JPS6041320B2 (en) | 1980-04-30 | 1980-04-30 | Processing method for waste ion exchange resin in heavy water-moderated nuclear reactors |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6041320B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0631868B2 (en) * | 1984-06-08 | 1994-04-27 | 株式会社日立製作所 | Method and apparatus for treating used ion exchange resin |
| JPS6159299A (en) * | 1984-08-31 | 1986-03-26 | 株式会社日立製作所 | Radioactive waste processing method and processing equipment |
| JP4620546B2 (en) * | 2005-08-18 | 2011-01-26 | 中部電力株式会社 | Low level radioactive waste treatment method and treatment plant |
| CN109524143B (en) * | 2018-11-21 | 2020-10-20 | 中国核电工程有限公司 | Nuclear power plant radioactive waste liquid treatment method and system |
-
1980
- 1980-04-30 JP JP5623780A patent/JPS6041320B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56153297A (en) | 1981-11-27 |
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