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JPH0740078B2 - Radionuclide removal equipment in degraded heavy water - Google Patents
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JPH0740078B2 - Radionuclide removal equipment in degraded heavy water - Google Patents

Radionuclide removal equipment in degraded heavy water

Info

Publication number
JPH0740078B2
JPH0740078B2 JP20379189A JP20379189A JPH0740078B2 JP H0740078 B2 JPH0740078 B2 JP H0740078B2 JP 20379189 A JP20379189 A JP 20379189A JP 20379189 A JP20379189 A JP 20379189A JP H0740078 B2 JPH0740078 B2 JP H0740078B2
Authority
JP
Japan
Prior art keywords
heavy water
cartridge filter
deteriorated
oxine
water
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 - Fee Related
Application number
JP20379189A
Other languages
Japanese (ja)
Other versions
JPH0368899A (en
Inventor
聡 森田
泰三 加藤
幹也 藤井
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo 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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP20379189A priority Critical patent/JPH0740078B2/en
Publication of JPH0368899A publication Critical patent/JPH0368899A/en
Publication of JPH0740078B2 publication Critical patent/JPH0740078B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は劣化重水中の放射性核種除去装置に関するもの
である。
TECHNICAL FIELD The present invention relates to a radionuclide removing apparatus for deteriorating heavy water.

(従来技術) 新型転換炉等冷却材又は減速材として重水を使用した原
子力発電所において、その重水を浄化するためにイオン
交換樹脂が使用される。イオン交換樹脂を重水系内で使
用する場合、使用前に重水化と称する商品中の軽水分を
重水と置換する操作及び廃棄時には軽水化と称するトリ
チウムを含む重水を軽水に置換する操作が必要となる。
廃棄時の操作において重水と軽水の混った劣化重水が生
じるが、この劣化重水中にはトリチウムの他に浄化時に
吸着した放射性核種が混入する。劣化重水中は、アップ
グレイダーと称する同位体濃縮装置で99.8%程度に濃縮
され回収される。
(Prior Art) In a nuclear power plant using heavy water as a coolant or moderator such as a new converter, an ion exchange resin is used to purify the heavy water. When using the ion exchange resin in a heavy water system, it is necessary to perform an operation of replacing light water in the product with heavy water, which is called deuteration before use, and an operation of replacing heavy water containing tritium with light water, which is called dewatering when discarded. Become.
Deteriorated heavy water, which is a mixture of heavy water and light water, is generated during the operation at the time of disposal, and in addition to tritium, radioactive nuclides adsorbed during purification are mixed in this deteriorated heavy water. Deteriorated heavy water is concentrated to about 99.8% and collected by an isotope concentrator called an upgrader.

従来アップグレイダーの前処理系は劣化重水中のCo−60
イオンを除去し、さらにフイルターで固形状のCo−60を
除去する構成となっている。この装置では使用するイオ
ン交換樹脂は重水分を含んだまゝ廃棄することができな
いので、軽水化操作を実施する必要があり、この時イオ
ン交換樹脂の2〜3倍量の劣化重水が生じる。
The conventional pretreatment system for the upgrader is Co-60 in deteriorated heavy water.
Ion is removed, and further, solid Co-60 is removed by a filter. Since the ion exchange resin used in this apparatus cannot be discarded while containing heavy water, it is necessary to carry out a lightening operation, and at this time, the amount of deteriorated heavy water 2-3 times that of the ion exchange resin is generated.

更に使用済みイオン交換樹脂の移送は通常水移送で行な
われるので、5〜6倍量の放射性核種を含む廃水が生じ
る。
Further, since the used ion exchange resin is usually transferred by water, waste water containing 5 to 6 times the amount of radionuclide is produced.

又廃棄イオン交換樹脂は通常雑固体の焼却炉で焼却する
ことが困難であり、貯蔵タンクに貯蔵される。なお、フ
イルターは乾燥処理後雑固体として貯蔵される。即ちイ
オン交換樹脂による従来の方式では、使用済イオン交換
樹脂及び使用前後の処理時の大量の放射性の廃水が生じ
るという問題がある。
Further, it is usually difficult to incinerate the waste ion exchange resin in an incinerator of miscellaneous solids, and it is stored in a storage tank. The filter is stored as a crude solid after the drying process. That is, in the conventional method using the ion exchange resin, there is a problem that a large amount of radioactive waste water is generated in the used ion exchange resin and before and after the treatment.

(発明により解決しようとする課題) 本発明は上記アップグレイダーにおける線量の蓄積防止
を目的として行う劣化重水中のCo−60等の放射性核種の
除去装置をコンパクト化し、かつ取扱い易くすることを
目的とするものである。
(Problems to be solved by the invention) The present invention aims to make a device for removing radionuclides such as Co-60 in deteriorated heavy water compact for the purpose of preventing dose accumulation in the upgrader, and to make it easy to handle. To do.

(発明による課題の解決手段) 劣化重水中のCo−60金属性の放射性核種の除去におい
て、オキシンを添着した活性炭を充填したカートリッジ
フイルタを通して劣化重水中のイオン及び固形物を除去
する回路と、該回路内の前記カートリッジフイルタ内の
重水分を含んだ活性炭を乾燥させるため脱湿器及び加熱
器を備えた乾燥回路とを有することを特徴とする。
(Means for Solving the Problems According to the Invention) In removing Co-60 metallic radionuclide in deteriorated heavy water, a circuit for removing ions and solid matter in the deteriorated heavy water through a cartridge filter filled with activated carbon impregnated with oxine, and And a drying circuit having a dehumidifier and a heater for drying the activated carbon containing heavy water in the cartridge filter in the circuit.

(実施例) 図に基いて説明する。劣化重水1を配管aから粉末オキ
シン添着活性炭のカートリッジフイルタ2に通水し、こ
ゝでCo−60の放射性核種を除去し、配管bでアップグレ
イダー3に移送する。
(Example) It demonstrates based on a figure. Deteriorated heavy water 1 is passed from a pipe a to a cartridge filter 2 of powdered oxine-impregnated activated carbon to remove Co-60 radionuclides, and is transferred to an upgrader 3 by a pipe b.

粉末オキシン添着活性炭のカートリッジフイルタ2は本
出願と同時に本出願人が出願したもので、第2図又は第
3図に示すように、Co−60イオン除去に有効なオキシン
を活性炭に添着した可燃性の粉末オキシン炭12で粒度分
布を50〜200メッシュに調整したものをカートリッジ11
内又は11aと11bとの間に充填し、処理原液の入口15に10
0μm程度のプレフイルタ13を、処理液の出口に数μm
のポストフイルタ14a,14bを装着したものである。
The powder oxine impregnated activated carbon cartridge filter 2 was filed by the present applicant at the same time as the present application. As shown in FIG. 2 or FIG. Cartridge 11 with particle size distribution adjusted to 50-200 mesh with 12 powdered oxine charcoal
Filled inside or between 11a and 11b.
A prefilter 13 of about 0 μm is placed at the outlet of the processing liquid for several μm.
The post filters 14a and 14b are attached.

オキシン添着炭カートリッジフイルタ2の使用後、弁を
開いてカートリッジフイルタ2内の重水を配管cを経て
劣化重水回収タンク4にドレインする。
After the use of the oxine impregnated carbon cartridge filter 2, the valve is opened and the heavy water in the cartridge filter 2 is drained to the deteriorated heavy water recovery tank 4 via the pipe c.

しかるのち、圧縮機10を起動して脱湿器(例えばモレキ
ュラーシーブ充填器)5により乾燥した空気を加熱器6
により加熱して配管d,e系によりカートリッジフイルタ
2に送気して、オキシン添着活性炭の重水分を空気側に
移す。この空気中の重水分は脱湿器5に吸着され、再び
乾燥空気としてカートリッジフイルタ2に送気する。
After that, the compressor 10 is started, and the air dried by the dehumidifier (for example, the molecular sieve filling device) 5 is heated by the heater 6.
It heats up and it sends air to the cartridge filter 2 through the piping d and e system, and the heavy moisture of the oxine impregnated activated carbon is moved to the air side. The heavy moisture in the air is adsorbed by the dehumidifier 5 and is again sent to the cartridge filter 2 as dry air.

次に脱湿器5にて吸着された重水は、圧力差又は温度差
を利用して再生される。重水を含む再生ガスは配管fを
へて凝縮器7に送られ、こゝで冷却されて、劣化重水と
して劣化重水タンク4に回収される。8はブラインチリ
ングユニットである。脱湿器5は2塔用意して交互に使
用することにより、連続してオキシン炭カートリッジフ
イルタ2を乾燥することができる。これらの脱湿器5は
公知のものを使用するので、詳細は省く。
Next, the heavy water adsorbed by the dehumidifier 5 is regenerated by utilizing the pressure difference or the temperature difference. The regenerated gas containing heavy water is sent to the condenser 7 through the pipe f, cooled there, and collected in the deteriorated heavy water tank 4 as deteriorated heavy water. Reference numeral 8 is a blinch ring unit. By preparing the two dehumidifiers 5 and using them alternately, the oxine charcoal cartridge filter 2 can be dried continuously. Since these dehumidifiers 5 are known ones, their details are omitted.

乾燥空気による乾燥が終了すると、オキシン炭カートリ
ッジフイルタ2は取り外し、その全て又は大部分を交換
する。そして取り外したオキシン炭カートリッジフイル
タ2の全て、又は大部分は焼却して減容される。
When the drying with the dry air is completed, the oxine charcoal cartridge filter 2 is removed and all or most of it is replaced. All or most of the removed oxine charcoal cartridge filter 2 is incinerated to reduce the volume.

劣化重水回収タンク4に回収された劣化重水はポンプ9
によりオキシン炭カートリッジフイルタ2に再び通水し
た後、アップグレイダーに移送される。
The deteriorated heavy water collected in the deteriorated heavy water recovery tank 4 is pump 9
After that, water is again passed through the oxine charcoal cartridge filter 2 and then transferred to the upgrader.

以上説明したように、オキシン炭カートリッジフイルタ
2によって劣化重水中のCo−60等の金属性放射性核種の
イオン及び固形物(クラッド)を除去し、次に放射性核
種を吸着し、重水分を含むオキシン炭カートリッジフイ
ルタを乾燥し、乾燥完了後にカートリッジフイルタを取
外し、全て又はその大部分を焼却して減容処理するよう
にした。
As explained above, the ions and solids (clad) of metallic radionuclides such as Co-60 in the deteriorated heavy water are removed by the oxine charcoal cartridge filter 2, then the radionuclide is adsorbed, and the oxine containing heavy water The charcoal cartridge filter was dried, and after the drying was completed, the cartridge filter was removed, and all or most of it was incinerated for volume reduction.

(効果) 1)従来Co−60等金属性核種のイオン及び固形物を各々
の機能を持つ別々の装置で処理していたが、これをオキ
シン炭カートリッジフイルタ1つで両機能を持たせて処
理できるようにしたので、装置の簡略化が可能となっ
た。
(Effects) 1) Conventionally, ions and solids of metallic nuclides such as Co-60 were treated by separate devices with each function, but this was treated by one oxine charcoal cartridge filter with both functions. Since this is possible, the device can be simplified.

2)オキシン炭カートリッジフイルタを乾燥処理するこ
とにより、更に低濃度で多量の劣化重水の発生をなくす
ることができる。
2) By drying the oxine charcoal cartridge filter, it is possible to prevent the generation of a large amount of deteriorated heavy water at a lower concentration.

3)乾燥後、焼却減容することにより廃棄物の発生を低
減できる。
3) The amount of waste can be reduced by incineration and volume reduction after drying.

4)従来の如く使用済吸着剤の移送によって生じていた
放射性核種を含む廃水の発生をなくすることができる。
4) It is possible to eliminate the generation of waste water containing a radionuclide, which has been conventionally caused by the transfer of the used adsorbent.

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

第1図は本発明装置を示す。 第2図と第3図はカートリッジフイルタの2つの例を示
す。 図において; 1……劣化重水 2……カートリッジフイルタ 3……アップグレイダー 4……劣化重水回収タンク 5……脱湿器、6……加熱器 7……凝縮器 8……ブラインチリングユニット 9……ポンプ、10……圧縮機 11……カートリッジ、12……粉末オキシン炭 13……プレフイルタ 14a,14b……ポストフイルタ 15……(原液処理液の)入口
FIG. 1 shows the device of the present invention. 2 and 3 show two examples of cartridge filters. In the figure; 1 ... Deteriorated heavy water 2 ... Cartridge filter 3 ... Upgrader 4 ... Deteriorated heavy water recovery tank 5 ... Dehumidifier, 6 ... Heater 7 ... Condenser 8 ... Blinch ring unit 9 ...... Pump, 10 ...... Compressor 11 …… Cartridge, 12 …… Powdered oxine charcoal 13 …… Pre-filter 14a, 14b …… Post-filter 15 …… (stock solution) inlet

───────────────────────────────────────────────────── フロントページの続き (72)発明者 藤井 幹也 東京都田無市谷戸町2丁目1番1号 住友 重機械工業株式会社田無製造所内 (56)参考文献 特開 昭57−162642(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Mikiya Fujii 2-1-1 Yado-cho, Tanashi-shi, Tokyo Metropolitan area Sumitomo Heavy Industries, Ltd. Tanashi Factory (56) Reference JP-A-57-162642 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】劣化重水中のCo−60等金属性の放射性核種
の除去装置において、オキシンを添着した活性炭を充填
したカートリッジフイルタを通して劣化重水中のイオン
及び固形物を除去する回路と、該回路内の前記カートリ
ッジフイルタ内の重水分を含んだ活性炭を乾燥させるた
め脱湿器及び加熱器を備えた乾燥回路とを有することを
特徴とする劣化重水中の放射性核種除去装置。
1. A device for removing metallic radionuclides such as Co-60 in deteriorated heavy water, which removes ions and solids in deteriorated heavy water through a cartridge filter filled with activated carbon impregnated with oxine, and the circuit. A drying circuit equipped with a dehumidifier and a heater for drying the activated carbon containing heavy water in the cartridge filter therein.
JP20379189A 1989-08-08 1989-08-08 Radionuclide removal equipment in degraded heavy water Expired - Fee Related JPH0740078B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20379189A JPH0740078B2 (en) 1989-08-08 1989-08-08 Radionuclide removal equipment in degraded heavy water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20379189A JPH0740078B2 (en) 1989-08-08 1989-08-08 Radionuclide removal equipment in degraded heavy water

Publications (2)

Publication Number Publication Date
JPH0368899A JPH0368899A (en) 1991-03-25
JPH0740078B2 true JPH0740078B2 (en) 1995-05-01

Family

ID=16479814

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20379189A Expired - Fee Related JPH0740078B2 (en) 1989-08-08 1989-08-08 Radionuclide removal equipment in degraded heavy water

Country Status (1)

Country Link
JP (1) JPH0740078B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100451058B1 (en) * 2002-02-16 2004-10-02 (주)세영엔디씨 Radon removal apparatus
CN115497650B (en) * 2022-09-19 2025-08-12 华能核能技术研究院有限公司 Combined regeneration method of high-temperature gas cooled reactor molecular sieve bed and low-temperature activated carbon bed

Also Published As

Publication number Publication date
JPH0368899A (en) 1991-03-25

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