JPH03108697A - Treatment method for radioactive liquid waste - Google Patents
Treatment method for radioactive liquid wasteInfo
- Publication number
- JPH03108697A JPH03108697A JP24514789A JP24514789A JPH03108697A JP H03108697 A JPH03108697 A JP H03108697A JP 24514789 A JP24514789 A JP 24514789A JP 24514789 A JP24514789 A JP 24514789A JP H03108697 A JPH03108697 A JP H03108697A
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- filled
- liquid waste
- radioactive liquid
- substances
- 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
Landscapes
- Water Treatment By Sorption (AREA)
Abstract
Description
【発明の詳細な説明】
[発明の目的コ
(産業上の利用分野)
本発明は、原子力施設より発生する放射性廃液の処理方
法に関し、特に衣服の洗濯水、手洗い、シャワー等の放
射能濃度の極めて低い廃液に適した処理方法に関する。[Detailed Description of the Invention] [Purpose of the Invention (Field of Industrial Application) The present invention relates to a method for treating radioactive waste fluid generated from nuclear facilities, and in particular to a method for treating radioactive waste fluid such as washing water for clothes, hand washing, showering, etc. This invention relates to a treatment method suitable for extremely low waste liquid.
(従来の技術)
原子力施設、特に原子力発電所では、作業員の使用した
衣服の洗濯水や、手洗い、シャワー等の廃水が発生する
。このような廃水の特徴は、放射能濃度が極めて低く、
洗剤成分や、糸屑、髪の毛、垢等の不溶解成分が含まれ
ていることである。これらの廃液を処理する場合、現在
はストレーナ−等により糸屑等の大きなごみを除去した
後、放射能を測定し、規定濃度以下の放射能であること
を確認して環境に放出している。(Prior Art) Nuclear facilities, especially nuclear power plants, generate wastewater such as water used by workers for washing clothes, washing hands, and showering. The characteristics of such wastewater are that the radioactivity concentration is extremely low.
Contains detergent ingredients and insoluble ingredients such as lint, hair, and dirt. Currently, when processing these waste liquids, large debris such as lint is removed using a strainer, etc., and then the radioactivity is measured and the radioactivity is confirmed to be below the specified concentration before being released into the environment. .
しかしながら、この方法では、廃液中の洗剤や垢等の各
種有機成分がそのまま放出されるので、環境保全上好ま
しくない。However, in this method, various organic components such as detergent and grime in the waste liquid are released as they are, which is not preferable from an environmental conservation perspective.
(発明が解決しようとする課題)
そこで、廃水中に含まれる溶解性物質と不溶解性物質と
を活性炭により一度に除去することを試みた。ところが
、活性炭には、粒径が3mmから10μm程度のものま
であり、粒径の大きなものでは吸着性能が低いので、洗
剤等の溶解性物質が除去し難く、一方位径の小さなもの
では吸着性能は高いが目詰まりを起こして処理能力が低
下し、頻繁に逆洗操作を行わなければならない。(Problems to be Solved by the Invention) Therefore, an attempt was made to remove soluble and insoluble substances contained in wastewater at once using activated carbon. However, activated carbon has particle sizes ranging from 3 mm to 10 μm, and those with large particle sizes have low adsorption performance, making it difficult to remove soluble substances such as detergents, and those with small diameters have poor adsorption performance. Although the efficiency is high, it can become clogged, reducing processing capacity and requiring frequent backwashing operations.
本発明はかかる状況に対処してなされたもので、低放射
性濃度の放射性廃液から溶解性物質と不溶解性物質を効
率的に除去することを目的とするものである。The present invention was made in response to such a situation, and an object of the present invention is to efficiently remove soluble and insoluble substances from a radioactive waste liquid with a low radioactive concentration.
[発明の構成]
(課題を解決するための手段および作用)上記目的は、
活性炭の粒径が上層で大きく下層で小さくなるような順
序で活性炭を容器に充填し、この容器内に放射性廃液を
通すことにより達成することができる。[Structure of the invention] (Means and effects for solving the problem) The above purpose is to
This can be achieved by filling a container with activated carbon in such an order that the particle size of the activated carbon is large in the upper layer and decreasing in particle size in the lower layer, and passing the radioactive waste liquid into the container.
本発明は活性炭を上記したような方法で容器に充填した
ので、廃水中の糸屑等の不溶解性物質は上層で除去され
、洗剤等の溶解性物質は下層の吸着能の高い活性炭で除
去される。したがって、目詰まりを起こすことなく溶解
性物質および不溶解性物質のいずれをも除去することが
でき、これらを含む放射性廃液の処理に極めて好都合で
ある。In the present invention, activated carbon is filled into a container using the method described above, so insoluble substances such as lint in wastewater are removed in the upper layer, and soluble substances such as detergent are removed by the activated carbon with high adsorption capacity in the lower layer. be done. Therefore, both soluble and insoluble substances can be removed without causing clogging, which is extremely convenient for treating radioactive waste liquid containing these substances.
(実施例) 本発明の実施例を図面を参照しながら説明する。(Example) Embodiments of the present invention will be described with reference to the drawings.
まず、本発明の処理方法を試験するために、下記第1表
に示す模擬廃液を作った。First, in order to test the treatment method of the present invention, simulated waste liquids shown in Table 1 below were prepared.
第
表
この模擬廃液を使って、第1図に示す試験装置により廃
液の濾過処理を行った。第1図において、1は給液タン
ク、2はポンプ、3は活性炭充填容器、4は活性炭、5
は圧力計、6は逆洗タンク。Table 1 Using this simulated waste liquid, the waste liquid was filtered using the testing apparatus shown in FIG. In Fig. 1, 1 is a liquid supply tank, 2 is a pump, 3 is an activated carbon filling container, 4 is activated carbon, and 5 is a pump.
is the pressure gauge, and 6 is the backwash tank.
7は圧縮空気、8は逆洗受はタンクである。7 is compressed air, and 8 is a tank for backwashing.
例 1(比較例)
粒径10pm表面積!500n−r/ g 、平均細孔
半径30〜50Aの活性炭を活性炭充填容器3に充填し
、廃水給液タンク1に模擬液を供給した。つぎにポンプ
2を作動させて模擬液を活性炭充填容器3に送り、活性
炭充填容器3の出口に設置した圧力計5で圧力を測定し
た。圧力が最初の圧力の2倍に達した時点でポンプ2を
停止し、圧縮空気7を送って逆洗タンク6を加圧し、活
性炭を逆洗受はタンク8に収容した。Example 1 (comparative example) Particle size 10pm surface area! The activated carbon filling container 3 was filled with activated carbon having a weight of 500 nr/g and an average pore radius of 30 to 50 A, and the simulated liquid was supplied to the waste water supply tank 1. Next, the pump 2 was operated to send the simulated liquid to the activated carbon filled container 3, and the pressure was measured with a pressure gauge 5 installed at the outlet of the activated carbon filled container 3. When the pressure reached twice the initial pressure, the pump 2 was stopped, compressed air 7 was sent to pressurize the backwash tank 6, and the activated carbon was stored in the backwash tank 8.
例 2(比較例)
粒径2000μm、表面積1200rrf/g、平均細
孔半径10〜+5Aの活性炭を活性炭充填容器3に充填
し、それ以外は例1と同様にして模擬液の濾過処理を行
った。Example 2 (Comparative Example) Activated carbon having a particle size of 2000 μm, a surface area of 1200 rrf/g, and an average pore radius of 10 to +5 A was filled into the activated carbon filling container 3, and the simulated liquid was filtered in the same manner as in Example 1 except for the above. .
例 3(本発明実施例)
活性炭充填容器3の下部2/3に例1と同じ活性炭を充
填し、上部1/3に例2と同じ活性炭を充填して、それ
以外は例1と同様にして模擬液の濾過処理を行った。こ
の活性炭充填容器の縦断面図を第2図に示す。この図に
おいて、4aは例2に使用した粒径の大きな活性炭であ
り、4bは例1に使用した粒径の小さな活性炭である。Example 3 (Embodiment of the present invention) The lower 2/3 of the activated carbon filling container 3 was filled with the same activated carbon as in Example 1, the upper 1/3 was filled with the same activated carbon as in Example 2, and the rest was the same as in Example 1. The simulated liquid was filtered. A longitudinal cross-sectional view of this activated carbon-filled container is shown in FIG. In this figure, 4a is the activated carbon with a large particle size used in Example 2, and 4b is the activated carbon with a small particle size used in Example 1.
また、11は廃液供給口、12は排水出口である。Further, 11 is a waste liquid supply port, and 12 is a drainage outlet.
以上の試験の結果を第2表に示す。The results of the above tests are shown in Table 2.
第 2 表
上記表に示すように、粒径の小さな活性炭のみを使った
例1では目詰まりにより圧力の上昇が著しく、逆洗に至
るまでの廃液処理量がわずか201である。また、粒径
の大きな活性炭のみを使った例2では、圧力の上昇は少
ないが出口水の水質が著しく悪くなった。Table 2 As shown in the above table, in Example 1 in which only activated carbon with a small particle size was used, the pressure increased significantly due to clogging, and the amount of waste liquid treated until backwashing was only 201 kg. In addition, in Example 2 in which only activated carbon with a large particle size was used, the increase in pressure was small, but the quality of the outlet water deteriorated significantly.
これらに対して例3では圧力の上昇が少なく、逆洗に至
るまでの廃液処理量は1001に達し、しかも出口水の
水質も良好であった。On the other hand, in Example 3, the increase in pressure was small, the amount of waste liquid treated before backwashing reached 1001, and the quality of the outlet water was also good.
[発明の効果コ
以上説明したように、本発明によれば、原子力施設から
発生する衣服の洗濯水や手洗いシャワー等の放射能濃度
が極めて低い廃液から、効率的に溶解性物質と不溶解性
物質とを除去することができる。[Effects of the Invention] As explained above, according to the present invention, soluble substances and insoluble substances can be efficiently extracted from waste liquid with extremely low radioactivity concentration, such as washing water for clothes and hand-washing showers generated from nuclear facilities. substances can be removed.
第1図は本発明の実施例に使用した装置の系統図、第2
図は本発明の実施例で使用した活性炭充填容器の縦断面
図である。
1・・・廃液給液タンク
2・・・給液ポンプ
3・・・活性炭充填容器
4・・・活性炭
4a・・・粒径の大きな活性炭
4b・・・粒径の小さな活性炭
5・・・圧力計
6・・・逆洗タンク
7・・・圧縮空気
8・・・逆洗骨はタンクFigure 1 is a system diagram of the equipment used in the embodiment of the present invention, Figure 2
The figure is a longitudinal cross-sectional view of an activated carbon-filled container used in an example of the present invention. 1... Waste liquid supply tank 2... Liquid supply pump 3... Activated carbon filling container 4... Activated carbon 4a... Activated carbon with large particle size 4b... Activated carbon with small particle size 5... Pressure Total 6... Backwash tank 7... Compressed air 8... Backwash bones are in the tank
Claims (1)
に充填した容器内に放射性廃液を通すことを特徴とする
放射性廃液の処理方法。A method for treating radioactive waste liquid, characterized by passing the radioactive waste liquid through a container filled with activated carbon having a large particle size in the upper layer and activated carbon having a small particle size in the lower layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24514789A JPH03108697A (en) | 1989-09-22 | 1989-09-22 | Treatment method for radioactive liquid waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24514789A JPH03108697A (en) | 1989-09-22 | 1989-09-22 | Treatment method for radioactive liquid waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03108697A true JPH03108697A (en) | 1991-05-08 |
Family
ID=17129322
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24514789A Pending JPH03108697A (en) | 1989-09-22 | 1989-09-22 | Treatment method for radioactive liquid waste |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03108697A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010234370A (en) * | 2010-06-03 | 2010-10-21 | Nippon Kensetsu Gijutsu Kk | Water purification method and water purification device |
| US7918923B2 (en) * | 2005-05-16 | 2011-04-05 | Saes Getters S.P.A. | Gas purification with carbon based materials |
-
1989
- 1989-09-22 JP JP24514789A patent/JPH03108697A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7918923B2 (en) * | 2005-05-16 | 2011-04-05 | Saes Getters S.P.A. | Gas purification with carbon based materials |
| JP2010234370A (en) * | 2010-06-03 | 2010-10-21 | Nippon Kensetsu Gijutsu Kk | Water purification method and water purification device |
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