JPH0368900A - Burnable powder oxine carbon filter being used for purification of water containing radioactive nuclides - Google Patents
Burnable powder oxine carbon filter being used for purification of water containing radioactive nuclidesInfo
- Publication number
- JPH0368900A JPH0368900A JP20379289A JP20379289A JPH0368900A JP H0368900 A JPH0368900 A JP H0368900A JP 20379289 A JP20379289 A JP 20379289A JP 20379289 A JP20379289 A JP 20379289A JP H0368900 A JPH0368900 A JP H0368900A
- Authority
- JP
- Japan
- Prior art keywords
- oxine
- cartridge
- filter
- carbon
- charcoal
- 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.)
- Granted
Links
- MCJGNVYPOGVAJF-UHFFFAOYSA-N quinolin-8-ol Chemical compound C1=CN=C2C(O)=CC=CC2=C1 MCJGNVYPOGVAJF-UHFFFAOYSA-N 0.000 title claims abstract description 44
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 17
- 239000000843 powder Substances 0.000 title claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 8
- 230000002285 radioactive effect Effects 0.000 title description 4
- 238000000746 purification Methods 0.000 title description 2
- 238000011045 prefiltration Methods 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims abstract description 9
- 239000002245 particle Substances 0.000 claims abstract description 6
- 239000003610 charcoal Substances 0.000 claims description 20
- 239000000463 material Substances 0.000 claims description 6
- 150000002500 ions Chemical class 0.000 claims description 5
- 239000011550 stock solution Substances 0.000 claims description 4
- 239000004677 Nylon Substances 0.000 claims description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 2
- 229920001778 nylon Polymers 0.000 claims description 2
- XLYOFNOQVPJJNP-ZSJDYOACSA-N Heavy water Chemical compound [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 abstract description 22
- 238000001914 filtration Methods 0.000 abstract description 7
- 239000013522 chelant Substances 0.000 abstract description 2
- 150000001875 compounds Chemical class 0.000 abstract description 2
- 238000001179 sorption measurement Methods 0.000 abstract description 2
- 239000003456 ion exchange resin Substances 0.000 description 5
- 229920003303 ion-exchange polymer Polymers 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 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 description 4
- 238000005253 cladding Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- YZCKVEUIGOORGS-NJFSPNSNSA-N Tritium Chemical compound [3H] YZCKVEUIGOORGS-NJFSPNSNSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000011118 depth filtration Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000010908 plant waste Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910052722 tritium Inorganic materials 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
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ィルターに関するもの
である。DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a combustible powder oxine carbon 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。(Prior art) When disposing of the ion exchange resin used in the heavy water system of a new converter reactor, an operation called light water conversion is required to recover the heavy water from the ion exchange resin and discharge tritium from the system. When this operation is performed, degraded heavy water (heavy water concentration 1 to 99%) diluted with light water is produced, but this heavy water is purified to 99.8% or more using a heavy water purification device called an upgrader.
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。This degraded heavy water contains Co-60, so after removing Co-60 from the degraded heavy water, it is transferred to the upgrader to prevent the dose from increasing due to the accumulation of Co-60 in the upgrader. However, studies are underway to make this removal device as simple and compact as possible.
1)−殻内にはイオン交換樹脂とフィルターの組合せで
処理することが考えられ、イオン交換樹脂でCo−6Q
イオンを、フィルターでCo−60クラツド(粒子状物
質)を吸着又は濾過効果で液中でイオン、クラッドとも
にDFが10程度と考えられる。1) - It is possible to treat the inside of the shell with a combination of an ion exchange resin and a filter.
It is thought that the DF of both ions and cladding in the liquid is about 10 due to the adsorption or filtration effect of ions and Co-60 cladding (particulate matter) in the filter.
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Go−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ィルター
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 carbon) is effective in adsorbing and removing Go-60. When using granular oxine charcoal, the oxine charcoal is usually used by filling it in a column. When powdered oxine charcoal is used, the filter is precoated and used for removing crud, but in this case a tank and pump for precoating are 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 from degraded heavy water as simple and compact as possible.
(発明による課題の解決手段)
Go−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メツシュ
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μ園程度のプレフィルタを、処理液の出口に数
μlのポストフィルタを装着した。(Means for solving problems by the invention) A cartridge is filled with powdered oxine charcoal, which is made by impregnating activated carbon with oxine, which is effective for removing Go-60 ions, and whose particle size distribution is adjusted to 50 to 200 mesh. A pre-filter with a capacity of about 1 μl was installed at the outlet of the processing solution, and a post-filter with a capacity of several μl was installed at the outlet of the processing solution.
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。In addition, all or most of the cartridge filled with oxine charcoal and the housing in which the cartridge is loaded are made of flammable material, so that the housing can be incinerated together with the housing to reduce its volume when disposed of.
さらに又、可燃性物質がナイロン、ABS、アクリル等
である。Furthermore, flammable materials include nylon, ABS, acrylic, and 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
ィルターエレメントAの第I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
メツ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はプレフィルタ、4はポストフィルタで、粉末オ
キシン炭はこれらフィルタ間に充填されている。プレフ
ィルタ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μ通のクラッドは捕捉しないよ
う25μm程度の濾過精度となっている。(Example) FIG. 1 is a sectional view of the first example of a cartridge filter element A filled with powdered oxine-impregnated carbon. 1 is a cylindrical cartridge with 100 to 150 particles inside.
Metush's powdered oxine charcoal 2 is filled in a dry state. 3 is a pre-filter, 4 is a post-filter, and powdered oxine charcoal is filled between these filters. The pre-filter 3 holds the powdered oxine charcoal in the cartridge 1 and prevents it from flowing out, but has a filtration accuracy of about 25 μm so as not to capture several micrometers of crud.
又ポストフィルタ4はプレフィルタ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μ通程度の濾過精度となっている。Similarly to the pre-filter 3, the post-filter 4 is intended to prevent the powdered oxine carbon 2 from flowing out and to remove crud as a final filtration layer, and has a filtration accuracy of several microns.
カートリッジフィルターエレメントAの直径及び高さは
、約70φX250flと一般用のカートリッジフィル
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 diameter and height of the cartridge filter element A are approximately 70 φ x 250 fl, which are similar to a general cartridge filter, and are compatible with each other so that they can be incorporated into the housing.
第2図はカートリッジフィルターエレメント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 second embodiment of the cartridge filter element A. In this example, 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
下の原液人口5から供給され、中心部でポストフィルタ
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 processing solution is supplied from the upper and lower solution ports 5 of the cartridge outer pipe 1a, passes through the post filter 4 in the center, and passes through the processing solution outlet 6 provided in the cartridge inner pipe 1b.
is discharged from.
第1図の第1例ではオキシン炭2の充填高さは約200
mとなるが、流路面積は断面積に相当する面積である。In the first example of Fig. 1, the filling height of oxine charcoal 2 is approximately 200 mm.
m, and the flow path area is an area corresponding to the cross-sectional area.
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。Further, in the second embodiment shown in FIG. 2, since the flow flows from the upper and lower parts, the flow path area can be increased, but the filling height is 1/2 that of the first embodiment. Note that the specifications can be arbitrarily determined depending on 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、フィルター、イオン交換樹脂において処理され
ているが、本発明のフィルターカートリッジを従来のフ
ィルターカートリッジと交換することにより、放射性C
o−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。Currently, wastewater generated in nuclear power plant waste treatment equipment is treated with filters and ion exchange resins, but by replacing the filter cartridge of the present invention with the conventional filter cartridge, radioactive C
Not only O-60 but also radioactive nuclides such as Ni and Fe can be removed at a higher DF.
以上説明したようなオキシン炭カートリッジフィルター
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
たカートリッジフィルターをハウジングごと焼却可能で
ある。When processing the heavy water system of a new converter reactor using the oxine charcoal cartridge filter as described above, handling of the cartridge with increased dose becomes a problem. To solve this problem, if the cartridge and housing are all made of flammable materials, the cartridge filter, which has been drained and dried after water treatment, can be incinerated together with the housing.
第3図は可燃性フィルターハウジングの一例で、ABS
樹脂で成形されている。Figure 3 shows an example of a flammable filter housing, with ABS
Molded from resin.
以上のような構成であって次の如く作用する。The configuration described above operates as follows.
処理原液は第1図の例では上部のプレフィルタ3から、
又第2図の例では上部と下部のプレフィルタ3,3を通
過しオキシン炭2の層へ流入する。In the example shown in Fig. 1, the processing stock solution is supplied from the upper prefilter 3.
In the example shown in FIG. 2, the water passes through the upper and lower prefilters 3, 3 and flows into the oxine carbon layer 2.
このプレフィルタ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。This pre-filter 3 removes particles that have a large particle size (several tens of micrometers or more) and accumulate on the surface of the oxine charcoal, causing 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Go−60はオキシンとキレート化合物0− M /
nを生成して吸着され、クラッド性のCo−60は粉
末オキシン炭層の濾過効果により濾過される。Next, among the stock solutions that flowed into the layer of oxine charcoal 2, ionic Go-60 was mixed with oxine and chelate compound 0-M/
The cladding Co-60 is filtered by the filtration effect of the powdered oxine carbon layer.
オキシン炭2の層でCo−60を吸着除去された処理済
液はポストフィルタ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 by the layer of oxine carbon 2 passes through the post filter 4 and flows out to the outlet 6.
(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ィルターを装
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ィルター)機器で処理さ
れていたが、1つのフィ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。(Effects) A cartridge was filled with powdered oxine charcoal in which oxin was impregnated with activated carbon, and filters were installed at the inlet and outlet of the processing stock solution. With this configuration, 1) Conventionally, Co-60 ions and cladding were treated with equipment with separate functions (for example, ion exchange resin and filter), but now it is possible to treat them simultaneously with one filter element, 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, there is no need for a pre-coat tank or pump, and the equipment can be simplified. This is particularly effective when the amount of processing 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、Go−60クラツ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 pre-coated type, the oxine carbon layer is dense, so the initial differential pressure and the differential pressure increase from blockage due to surface filtration are large, and a large processing flow rate cannot be obtained.However, in this cartridge, the pre-coated type Although the density of the oxine coal layer is inferior to that of the oxine carbon layer, the depth filtration effect is greater, so it has been demonstrated that the performance is sufficient for removing Go-60 crud.
4)カートリッジ交換時においてGo−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, radioactive nuclides such as Go-60 are retained in the oxine carbon layer inside the cartridge, which prevents them from scattering into the atmosphere and from being inhaled by workers.
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 combustible materials, there is no need to remove the cartridge with increased radiation dose from the housing, making it possible to reduce the radiation exposure of workers.
第1図は本発明に係る粉末オキシン炭フィルターの第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 カートリッジフィルターエレメント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 粉末オキシン炭プレフィルタ 4 ポスト
フィルタS yK液人口 6 処理液出口以上FIG. 1 shows a first diagram of a powdered oxine charcoal filter according to the present invention.
Example sectional view. FIG. 2 is a sectional view of the second embodiment. FIG. 3(a) shows an example of a combustible 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 Powdered oxine charcoal prefilter 4 Post filter SyK liquid population 6 Processing liquid outlet or above
Claims (3)
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のポストフィ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
シン炭フィルター。(1) Powdered oxine carbon, which is effective in removing Co-60 ions, is impregnated with activated carbon and the particle size distribution is adjusted to 50 to 200 mesh, and the cartridge is filled with a pre-filter of several tens of μm at the inlet of the processing stock solution. A flammable powder oxine charcoal filter used for purifying water containing radionuclides, characterized in that a post filter of several μm is attached to the outlet of the treatment liquid.
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ィルタ
ー。(2) Claim (1) characterized in that the cartridge filled with oxine charcoal and the housing in which the cartridge is loaded are all or most made of a combustible material, and the volume can be reduced by incinerating the entire housing at the time of disposal. combustible powder oxine charcoal filter used to purify water containing radionuclides.
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ィルター
。(3) The flammable powder oxine charcoal filter for use in purifying water containing radionuclides according to claim (2), wherein the flammable material is nylon, ABS, acrylic, or the like.
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 true JPH0368900A (en) | 1991-03-25 |
JPH0740079B2 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) |
-
1989
- 1989-08-08 JP JP20379289A patent/JPH0740079B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH0740079B2 (en) | 1995-05-01 |
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