JPH0740079B2 - Combustible powder oxine charcoal filter used for purification of water containing radionuclide - Google Patents

Combustible powder oxine charcoal filter used for purification of water containing radionuclide

Info

Publication number
JPH0740079B2
JPH0740079B2 JP20379289A JP20379289A JPH0740079B2 JP H0740079 B2 JPH0740079 B2 JP H0740079B2 JP 20379289 A JP20379289 A JP 20379289A JP 20379289 A JP20379289 A JP 20379289A JP H0740079 B2 JPH0740079 B2 JP H0740079B2
Authority
JP
Japan
Prior art keywords
oxine
cartridge
charcoal
purification
water containing
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
JP20379289A
Other languages
Japanese (ja)
Other versions
JPH0368900A (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 JP20379289A priority Critical patent/JPH0740079B2/en
Publication of JPH0368900A publication Critical patent/JPH0368900A/en
Publication of JPH0740079B2 publication Critical patent/JPH0740079B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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) 本発明は可燃性粉末オキシン炭フイルターに関するもの
である。
TECHNICAL FIELD The present invention relates to a combustible powder oxine charcoal filter.

(従来技術) 新型転換炉重水系で使用したイオン交換樹脂を廃棄する
場合、イオン交換樹脂からの重水の回収、トリチウムの
系外排出を目的とした軽水化と称する操作が必要とな
る。この操作を行うと、軽水で希釈された劣化重水(重
水濃度1〜99%)が生じるが、この重水は別途アップグ
レイダーと称する重水精製装置で99.8%以上に精製され
る。この劣化重水中にはCo−60が含まれるため、劣化重
水中のCo−60を除去した後、アップグレイダーに移送し
て、アップグレイダーにおけるCo−60の蓄積による線量
の上昇を防止するが、この除去装置を極力簡便化し、か
つコンパクトにまとめることが検討されている。
(Prior Art) When discarding the ion exchange resin used in the heavy water system of the new converter, it is necessary to perform operations called light water recovery for the purpose of recovering heavy water from the ion exchange resin and discharging tritium out of the system. When this operation is performed, deteriorated heavy water diluted with light water (heavy water concentration of 1 to 99%) is generated, but this heavy water is separately purified to 99.8% or more by a heavy water purification device called an upgrader. Since Co-60 is contained in this deteriorated heavy water, after removing Co-60 in the deteriorated heavy water, it is transferred to an upgrader to prevent an increase in dose due to the accumulation of Co-60 in the upgrader. It has been studied to simplify this removal device as much as possible and to make it compact.

1)一般的にはイオン交換樹脂とフイルターの組合せで
処理することが考えられ、イオン交換樹脂でCo−60イオ
ンを、フイルターでCo−60クラッド(粒子状物質)を吸
着又は濾過効果で液中から除去する。一般的性能として
でイオン、クラッドともにDFが10程度と考えられる。
1) Generally, it is considered to treat with a combination of an ion exchange resin and a filter. In the liquid, Co-60 ions are adsorbed by the ion exchange resin and Co-60 clad (particulate matter) is adsorbed or filtered by the filter. To remove from. For general performance Therefore, DF is considered to be about 10 for both ions and cladding.

2)一方、オキシンを添着した活性炭(以下オキシン炭
と略す)がCo−60の吸着除去に有効であることが知られ
ている。このオキシン炭の使用方法としては通常は粒状
のオキシン炭を使用する場合はカラムに充填して使用す
る。又粉末オキシン炭を使用する場合はフイルターにプ
リコートしてクラッド除去用として使用するが、この場
合はプリコートするためのタンクやポンプが必要とな
る。
2) On the other hand, it is known that activated carbon impregnated with oxine (hereinafter abbreviated as oxine charcoal) is effective for adsorption and removal of Co-60. As a method of using the oxine charcoal, when granular oxine charcoal is used, the column is packed and used. When powdered oxine charcoal is used, it is precoated on a filter and used for removing the clad. In this case, a tank or pump for precoating is required.

(発明により解決しようとする課題) 従来技術の問題点に鑑み、劣化重水中のCo−60の除去装
置を出来る限り簡便化し、かつコンパクト化することを
目的とする。
(Problems to be solved by the invention) In view of the problems of the prior art, it is an object of the present invention to make a device for removing Co-60 in deteriorated heavy water as simple and compact as possible.

(発明による課題の解決手段) Co−60イオン除去に有効なオキシンを活性炭に添着した
粉末オキシン炭で粒度分布を50〜200メッシュに調整し
たものをカートリッジに充填し、処理原液の入口に数十
μm程度のプレフイルタを、処理液の出口に数μmのポ
ストフイルタを装着した。
(Means for Solving the Problems According to the Invention) A cartridge was filled with powdered oxine charcoal in which oxine effective for Co-60 ion removal was impregnated with activated carbon, and the particle size distribution was adjusted to 50 to 200 mesh. A prefilter of about μm and a postfilter of several μm were attached to the outlet of the treatment liquid.

又、オキシン炭を充填するカートリッジ及び該カートリ
ッジを装填するハウジングの全部又は大部分を可燃性物
質製とし、廃棄時にハウジングごと焼却し減容可能にし
た。
Further, all or most of the cartridge filled with oxine charcoal and the housing loaded with the cartridge are made of a combustible material, and the entire housing is incinerated at the time of disposal so that the volume can be reduced.

さらに又、可燃性物質がナイロン,ABS,アクリル等であ
る。
Furthermore, the flammable substance is nylon, ABS, acrylic or the like.

(実施例) 第1図は粉末オキシン添着炭を充填したカートリッジフ
イルターエレメントAの第1実施例断面図である。1は
円筒状をなしたカートリッジで、内部に100〜150メッシ
ュの粉末オキシン炭2が乾燥状態で充填されている。3
はプレフイルタ、4はポストフイルタで、粉末オキシン
炭はこれらフイルタ間に充填されている。プレフイルタ
3は粉末オキシン炭をカートリッジ1内に保持し、流出
を防止するが、数μmのクラッドは捕捉しないよう25μ
m程度の濾過精度となっている。
(Example) FIG. 1 is a sectional view of a cartridge filter element A of Example 1 filled with powdered oxine impregnated carbon. Reference numeral 1 is a cylindrical cartridge in which 100-150 mesh powder oxine carbon 2 is filled in a dry state. Three
Is a prefilter, and 4 is a postfilter, and powdered oxine charcoal is filled between these filters. The prefilter 3 holds the powdered oxine charcoal in the cartridge 1 to prevent it from flowing out, but 25 μm so as not to capture the clad of several μm.
The filtration accuracy is about m.

又ポストフイルタ4はプレフイルタ3と同様、粉末オキ
シン炭2の流出防止及び最終濾過層としてクラッドの除
去を目的とし、数μm程度の濾過精度となっている。
Like the prefilter 3, the postfilter 4 has a filtration accuracy of about several μm for the purpose of preventing the outflow of the powdered oxine carbon 2 and removing the clad as the final filtration layer.

カートリッジフイルターエレメントAの直径及び高さ
は、約70φ×250と一般用のカートリッジフイルター
と同様で、ハウジングに組込むことができるよう互換性
をもたせている。
The cartridge filter element A has a diameter and height of about 70φ × 250, which is similar to that of a general-purpose cartridge filter and has compatibility so that it can be incorporated into a housing.

第2図はカートリッジフイルターエレメントAの第2実
施例断面図である。この例では粉末オキシン炭2はカー
トリッジ外管1aとカートリッジ内管1b間の環状空間に充
填されている。
FIG. 2 is a sectional view of a cartridge filter element A according to a second embodiment. In this example, the powdered oxine charcoal 2 is filled in the annular space between the cartridge outer tube 1a and the cartridge inner tube 1b.

この例においては処理原液はカートリッジ外管1aの上下
の原液入口5から供給され、中心部でポストフイルタ4
を介し、カートリッジ内管1bに設けた処理液出口6から
排出される。
In this example, the stock solution for treatment is supplied from the stock solution inlets 5 at the top and bottom of the cartridge outer tube 1a, and the post filter 4 is provided at the center.
Through the treatment liquid outlet 6 provided in the cartridge inner tube 1b.

第1図の第1例ではオキシン炭2の充填高さは約200mm
となるが、流路面積は断面積に相当する面積である。又
第2図の第2実施例では上部及び下部から流れるため、
流路面積は大きくとれるが、充填高さは第1実施例の1/
2となる。なお仕様は要求されるDF,流量によって任意に
決めることができる。
In the first example of FIG. 1, the filling height of the oxine charcoal 2 is about 200 mm.
However, the flow path area is an area corresponding to the cross-sectional area. Further, in the second embodiment shown in FIG. 2, since it flows from the upper and lower parts,
The flow passage area can be made large, but the filling height is 1/1 of that of the first embodiment.
It becomes 2. The specifications can be arbitrarily determined according to the required DF and flow rate.

現状では原子力発電所の廃棄物処理設備において生じる
廃水は、フイルター,イオン交換樹脂において処理され
ているが、本発明のフイルターカートリッジを従来のフ
イルターカートリッジと交換することにより、放射性Co
−60のみならず、Ni,Fe等の放射性核種の除去をより高
いDFで処理することができる。
At present, the wastewater generated in the waste treatment facility of a nuclear power plant is treated with a filter and an ion exchange resin, but by replacing the filter cartridge of the present invention with a conventional filter cartridge, radioactive Co
Not only -60, but also removal of radionuclides such as Ni and Fe can be treated with higher DF.

以上説明したようなオキシン炭カートリッジフイルター
で新型転換炉重水系の処理を行った場合、線量の上昇し
たカートリッジの取扱いが問題となる。この点を解決す
るため、カートリッジ及びハウジングをすべて可燃性の
もので製作すれば、通水処理後ドレンおよび乾燥を行っ
たカートリッジフイルターをハウジングごと焼却可能で
ある。
When the new converter heavy water system is treated with the oxine charcoal cartridge filter as explained above, handling of the cartridge with increased dose becomes a problem. In order to solve this point, if the cartridge and the housing are all made of a combustible material, it is possible to incinerate the cartridge filter, which has been drained and dried after the passage of water, together with the housing.

第3図は可燃性フイルターハウジングの一例で、ABS樹
脂で成形されている。
FIG. 3 shows an example of a flammable filter housing, which is molded from ABS resin.

以上のような構成であって次の如く作用する。With the above-mentioned configuration, it operates as follows.

処理原液は第1図の例では上部のプレフイルタ3から、
又第2図の例では上部と下部のプレフイルタ3,3を通過
しオキシン炭2の層へ流入する。このプレフイルタ3に
より粒子径が大きく(数十μm以上)、オキシン炭表面
で蓄積して閉塞(目づまり)の原因となるものが取除か
れる。
In the example of FIG. 1, the processing stock solution is supplied from the upper prefilter 3,
Further, in the example of FIG. 2, it passes through the upper and lower prefilters 3, 3 and flows into the bed of oxine coal 2. The prefilter 3 removes particles having a large particle size (several tens of μm or more) and accumulating on the surface of oxine charcoal and causing blockage (clogging).

次にオキシン炭2の層に流入した原液のうち、イオン性
のCo−60はオキシンとキレート化合物O−M/nを生成し
て吸着され、クラッド性のCo−60は粉末オキシン炭2の
濾過効果により濾過される。
Next, in the stock solution that has flowed into the layer of oxine charcoal 2, ionic Co-60 forms oxine and a chelate compound O-M / n and is adsorbed, and clad Co-60 is filtered of powdered oxine charcoal 2. It is filtered by the effect.

オキシン炭2の層でCo−60を吸着除去された処理済液は
ポストフイルタ4を通って出口6へ流出する。
The treated liquid from which Co-60 has been adsorbed and removed in the layer of oxine charcoal 2 flows out to the outlet 6 through the post filter 4.

(効果) オキシンを活性炭に添着した粉末オキシン炭をカートリ
ッジに充填し、処理原液の入口と出口にフイルターを装
着した。このような構成にしたので、 1)従来Co−60イオンとクラッドを別々の機能をもつ
(例えばイオン交換樹脂とフイルター)機器で処理され
ていたが、1つのフイルターエレメントで同時に処理で
き、かつ従来よりも高いDF(DF>100)を持たせること
ができるようになった。
(Effect) A powdered oxine charcoal in which oxine was impregnated on activated carbon was filled in a cartridge, and filters were attached to the inlet and outlet of the stock solution for treatment. With such a configuration, 1) Conventionally, Co-60 ions and the clad were treated with equipment having different functions (for example, ion exchange resin and filter), but they can be treated with one filter element at the same time, and It is now possible to have a higher DF (DF> 100).

2)プリコート型で使用しないので、プリコートタン
ク,ポンプが不要となり、設備が簡略化できる。特に処
理量が少い場合に有効である。
2) Since it is not used as a pre-coat type, a pre-coat tank and pump are unnecessary, and the equipment can be simplified. It is especially effective when the processing amount is small.

3)従来のプリコート型の場合、オキシン炭層が緻密な
ものとなるので、初期差圧及び表面濾過による閉塞から
の差圧上昇が大きく、処理流量を大きくとれないが、本
カートリッジにおいては、プリコート型に比べるとオキ
シン炭層の緻密さについては劣るものの深層濾過作用が
大きいので、Co−60クラッド除去性能として十分である
ことが実証された。
3) In the case of the conventional precoat type, since the oxine charcoal layer is dense, the differential pressure rise due to the initial differential pressure and blockage due to surface filtration is large, and the processing flow rate cannot be made large. Although it is inferior to that of oxine in terms of the denseness of the oxine coal layer, it has been proved that the Co-60 clad removal performance is sufficient because the deep layer filtration action is large.

4)カートリッジ交換時においてCo−60等の放射性核種
はカートリッジ内部のオキシン炭層に保持されており、
これらの雰囲気への飛散、作業者の吸入による被曝を防
止できる。
4) When replacing the cartridge, radionuclides such as Co-60 are retained in the oxine carbon layer inside the cartridge,
It is possible to prevent the radiation from being scattered into these atmospheres and inhaled by an operator.

5)カートリッジ及びハウジングを共に可燃性材料製と
したので、線量の上昇したカートリッジをハウジングか
ら抜き出す操作が不要となり、作業員の被曝低減を図る
ことが可能となった。
5) Since both the cartridge and the housing are made of a flammable material, it is not necessary to extract the cartridge with the increased dose from the housing, and it is possible to reduce the exposure of workers.

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

第1図は本発明に係る粉末オキシン炭フイルターの第1
実施例断面図。 第2図は同じく第2実施例断面図。 第3図(a)は可燃性ハウジングの一例を示し、第3図
(b)はその平面図である。 図において; A……カートリッジフイルターエレメント 1……カートリッジ、1a……カートリッジ外管 1b……カートリッジ内管、2……粉末オキシン炭 3……プレフイルタ、4……ポストフイルタ 5……原液入口、6……処理液出口
FIG. 1 is a first view of a powder oxine charcoal filter according to the present invention.
FIG. FIG. 2 is a sectional view of the second embodiment. FIG. 3 (a) shows an example of a flammable housing, and FIG. 3 (b) is a plan view thereof. In the figure; A ... Cartridge filter element 1 ... Cartridge, 1a ... Cartridge outer tube 1b ... Cartridge inner tube, 2 ... Powder oxine carbon 3 ... Prefilter, 4 ... Postfilter 5 ... Undiluted solution inlet, 6 ...... Processing liquid outlet

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57−144080(JP,A) 実公 昭53−38926(JP,Y1)Front Page Continuation (72) Inventor Mikiya Fujii 2-1-1 Yatocho, Tanashi City, Tokyo Metropolitan Area Sumitomo Heavy Industries, Ltd. Tanashi Factory (56) Reference JP-A-57-144080 (JP, A) 53-38926 (JP, Y1)

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】Co−60イオン除去に有効なオキシンを活性
炭に添着した粉末オキシン炭で粒度分布を50〜200メッ
シュに調整したものをカートリッジに充填し、処理原液
の入口に数十μm程度のプレフイルタを、処理液の出口
に数μmのポストフイルタを装着したことを特徴とする
放射性核種を含む水の浄化に使用する可燃性粉末オキシ
ン炭フイルター。
1. A cartridge is filled with a powdered oxine powder in which oxine effective for removing Co-60 ions is impregnated with activated carbon and the particle size distribution is adjusted to 50 to 200 mesh. A flammable powder oxine charcoal filter used for purification of water containing a radionuclide, characterized in that a prefilter is equipped with a post filter of several μm at the outlet of the treatment liquid.
【請求項2】オキシン炭を充填するカートリッジ及び該
カートリッジを装填するハウジングの全部又は大部分を
可燃性物質製とし、廃棄時にハウジングごと焼却し減容
可能にしたことを特徴とする請求項(1)記載の放射性
核種を含む水の浄化に使用する可燃性粉末オキシン炭フ
イルター。
2. A cartridge filled with oxine charcoal and a housing in which the cartridge is loaded are wholly or almost entirely made of a combustible substance, and can be incinerated together with the housing at the time of disposal to reduce the volume. ) A flammable powder oxine charcoal filter used for purification of water containing a radionuclide as described above.
【請求項3】可燃性物質がナイロン,ABS,アクリル等で
あることを特徴とする請求項(2)記載の放射性核種を
含む水の浄化に使用する可燃性粉末オキシン炭フイルタ
ー。
3. A flammable powder oxine charcoal filter used for purification of water containing a radionuclide according to claim 2, wherein the flammable substance is nylon, ABS, acrylic or the like.
JP20379289A 1989-08-08 1989-08-08 Combustible powder oxine charcoal filter used for purification of water containing radionuclide Expired - Lifetime JPH0740079B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20379289A JPH0740079B2 (en) 1989-08-08 1989-08-08 Combustible powder oxine charcoal filter used for purification of water containing radionuclide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20379289A JPH0740079B2 (en) 1989-08-08 1989-08-08 Combustible powder oxine charcoal filter used for purification of water containing radionuclide

Publications (2)

Publication Number Publication Date
JPH0368900A JPH0368900A (en) 1991-03-25
JPH0740079B2 true JPH0740079B2 (en) 1995-05-01

Family

ID=16479829

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20379289A Expired - Lifetime JPH0740079B2 (en) 1989-08-08 1989-08-08 Combustible powder oxine charcoal filter used for purification of water containing radionuclide

Country Status (1)

Country Link
JP (1) JPH0740079B2 (en)

Also Published As

Publication number Publication date
JPH0368900A (en) 1991-03-25

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