JPH04221799A - Treating method for radioactive sludge - Google Patents
Treating method for radioactive sludgeInfo
- Publication number
- JPH04221799A JPH04221799A JP40590390A JP40590390A JPH04221799A JP H04221799 A JPH04221799 A JP H04221799A JP 40590390 A JP40590390 A JP 40590390A JP 40590390 A JP40590390 A JP 40590390A JP H04221799 A JPH04221799 A JP H04221799A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- treatment
- container
- radioactive
- cement
- 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.)
- Withdrawn
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 50
- 238000000034 method Methods 0.000 title claims abstract description 20
- 230000002285 radioactive effect Effects 0.000 title claims abstract description 14
- 238000003860 storage Methods 0.000 claims abstract description 11
- 239000002901 radioactive waste Substances 0.000 claims description 4
- 239000000941 radioactive substance Substances 0.000 claims 1
- 239000004568 cement Substances 0.000 abstract description 7
- 239000003795 chemical substances by application Substances 0.000 abstract description 6
- 239000011521 glass Substances 0.000 abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 239000000843 powder Substances 0.000 abstract description 4
- 230000000087 stabilizing effect Effects 0.000 abstract description 3
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract description 2
- 230000005855 radiation Effects 0.000 abstract 3
- 239000000126 substance Substances 0.000 abstract 2
- 239000007787 solid Substances 0.000 abstract 1
- 208000005156 Dehydration Diseases 0.000 description 11
- 230000018044 dehydration Effects 0.000 description 11
- 238000006297 dehydration reaction Methods 0.000 description 11
- 239000012528 membrane Substances 0.000 description 10
- 238000012545 processing Methods 0.000 description 8
- 239000012510 hollow fiber Substances 0.000 description 6
- 238000005370 electroosmosis Methods 0.000 description 5
- 206010073306 Exposure to radiation Diseases 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 230000006641 stabilisation Effects 0.000 description 4
- 238000011105 stabilization Methods 0.000 description 4
- 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 3
- 239000003456 ion exchange resin Substances 0.000 description 3
- 229920003303 ion-exchange polymer Polymers 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000001027 hydrothermal synthesis Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000005341 cation exchange Methods 0.000 description 1
- 238000005253 cladding Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000002915 spent fuel radioactive waste Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[発明の目的][Object of the invention]
【産業上の利用分野】本発明は、原子力発電所等の施設
から発生する放射性スラッジの処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating radioactive sludge generated from facilities such as nuclear power plants.
【0002】0002
【従来の技術】原子力発電所等の施設から発生する放射
性スラッジのうち比較的放射能レベルの高いものはいま
だ処理・処分方法が確立されておらず、現在各施設内の
貯蔵タンクに貯蔵されている。[Prior Art] Among the radioactive sludge generated from facilities such as nuclear power plants, treatment and disposal methods have not yet been established for sludge with a relatively high radioactivity level, and it is currently stored in storage tanks within each facility. There is.
【0003】0003
【発明が解決しようとする課題】しかしながら、運転期
間が長くなるにつれて放射性廃棄物の貯蔵量が増大して
きており、貯蔵スペースも限られていることから、比較
的放射能濃度の高い放射性スラッジの処理方法を早急に
確立する必要がある。[Problem to be solved by the invention] However, as the operating period becomes longer, the amount of radioactive waste stored increases, and storage space is limited, so it is difficult to treat radioactive sludge with relatively high radioactivity concentration. A method needs to be established as soon as possible.
【0004】本発明は上記の事情に対処してなされたも
ので、比較的放射能濃度の高い放射性スラッジを固化体
にして長期間安定した状態で保存する方法であって、保
存容器内で前処理および安定化処理の各操作を行って放
射性スラッジの移送を少なくすることにより、放射線被
曝を極力低減した比較的放射能レベルの高いスラッジの
処理方法を提供することを目的とする。The present invention was made in response to the above-mentioned circumstances, and is a method for solidifying radioactive sludge with a relatively high radioactivity concentration and storing it in a stable state for a long period of time. The object of the present invention is to provide a method for treating sludge with a relatively high radioactivity level, which minimizes radiation exposure by performing treatment and stabilization operations to reduce transport of radioactive sludge.
【0005】[発明の構成][Configuration of the invention]
【課題を解決するための手段】すなわち、本発明の放射
性スラッジの処理方法は、該放射性スラッジを貯蔵槽か
ら直接最終保存容器内に移送して前処理し、しかる後安
定化処理して固化体にすることを特徴とする。[Means for Solving the Problems] That is, the radioactive sludge treatment method of the present invention involves transferring the radioactive sludge directly from a storage tank to a final storage container, pre-treating it, and then stabilizing it to solidify it. It is characterized by making it.
【0006】[0006]
【作用】本発明によれば、前処理と安定化処理を同一容
器内で行うので、工程の単純化を図ることができるとと
もに、前処理用の容器および前処理と安定化処理の間の
放射性スラッジの移送ラインが省略されることにより、
放射能汚染物質の発生量を最低限に抑え作業員の被曝の
危険性を低減することができる。[Operation] According to the present invention, since the pretreatment and stabilization treatment are performed in the same container, the process can be simplified, and the radioactivity between the pretreatment container and the pretreatment and stabilization treatment can be By eliminating the sludge transfer line,
It is possible to minimize the amount of radioactive contaminants generated and reduce the risk of radiation exposure for workers.
【0007】[0007]
【実施例】以下、図面に基づいて本発明の実施例につい
て説明する。図1は本発明による放射性スラッジの処理
工程の一実施例を示すものであり、図中、符号1は原子
炉冷却材浄化系(CUW)で発生する使用済イオン交換
樹脂や使用済燃料貯蔵プール浄化系で発生する使用済濾
過助材フィルタ等の比較的放射能濃度の高いスラッジ2
を貯蔵するスラッジ貯蔵槽である。このスラッジ貯蔵槽
1からボンプ輸送できる範囲の濃度(通常5wt%濃度
、最大10 wt%濃度)のスラッジ2が処理容器3に
移送される。このときセメントやガラス粉末等の固形化
剤4も添加され均一に攪拌混合され(工程A)、ついで
この処理容器3内で連続的に脱水処理される(工程B)
。このような容器内脱水方法としては、電極・膜などを
一体化したモジュール5を容器中に差し入れて行う電気
浸透法と、中空糸膜フィルタに代表されるような膜フィ
ルタを投入して脱水を行う方法が考えられる。どちらを
選択するかはスラッジ液の性状に基づき、濾過し易いス
ラッジでは前者を、濾過し難いものは後者を選択する。
濾過のし易さの指標としては濾過比抵抗がある。このよ
うな方法による脱水処理(工程B)は処理容器3内が満
たされるまでスラッジ2を供給しながら連続的に行われ
る。Embodiments Hereinafter, embodiments of the present invention will be described based on the drawings. Figure 1 shows an example of the radioactive sludge treatment process according to the present invention, and in the figure, reference numeral 1 indicates spent ion exchange resin and spent fuel storage pool generated in the reactor coolant cleaning system (CUW). Sludge with relatively high radioactivity concentration such as used filter aids generated in purification systems 2
This is a sludge storage tank that stores sludge. From this sludge storage tank 1, sludge 2 having a concentration within a range that can be transported by pump (normally 5 wt% concentration, maximum 10 wt% concentration) is transferred to a processing container 3. At this time, a solidifying agent 4 such as cement or glass powder is also added and stirred and mixed uniformly (Step A), and then continuously dehydrated in this processing container 3 (Step B).
. Such in-container dehydration methods include the electroosmosis method, which is carried out by inserting a module 5 that integrates electrodes and membranes into the container, and the dehydration method, which is carried out by inserting a membrane filter such as a hollow fiber membrane filter. There are ways to do this. Which one to select is based on the properties of the sludge liquid; the former is selected for sludge that is easy to filter, and the latter is selected for sludge that is difficult to filter. As an index of ease of filtration, there is filtration specific resistance. The dehydration treatment (step B) by such a method is performed continuously while supplying the sludge 2 until the inside of the treatment container 3 is filled.
【0008】脱水処理後、固形化剤4がセメントの場合
はそのまま放置しておけばセメント固化体が形成される
。しかしながら、スラッジの主成分がイオン交換樹脂の
ような場合はセメントが適さないこともあり、ガラス粉
末を添加して水熱固化する方法が有効に用いられる。
水熱固化する場合には、処理容器3に肉厚容器が用いら
れ、脱水処理後例えばヒータ6およびプレス7による水
熱合成反応(ホットプレス)の安定化処理工程(工程C
)を経て、ガラスマトリックス中に樹脂を閉じ込めた均
質固化体8に形成される。この場合、肉厚容器は遮蔽容
器としての機能も有するという効果がある。[0008] After the dehydration treatment, if the solidifying agent 4 is cement, if it is left as it is, a cement solidified body will be formed. However, if the main component of the sludge is an ion exchange resin, cement may not be suitable, and a method of adding glass powder and hydrothermally solidifying the sludge is effectively used. In the case of hydrothermal solidification, a thick walled container is used as the processing container 3, and after the dehydration treatment, for example, a stabilization treatment step (step C) of the hydrothermal synthesis reaction (hot press) using a heater 6 and a press 7
) to form a homogeneous solidified body 8 in which the resin is confined in a glass matrix. In this case, the thick-walled container has the effect of also functioning as a shielding container.
【0009】ここで、実験として粉末イオン交換樹脂の
模擬スラッジを用いて容器内脱水および水熱反応による
固化処理を行った。その結果について次ぎに説明する。
実験例1
図2に示すように、80mm径の処理容器に中空糸膜フ
ィルタ11を設けて、減圧度−510mmHgにおいて
クラッドを0 、5 、20重量%それぞれ含有する模
擬スラッジ12について脱水処理を行った。それぞれの
脱水処理後の含水率を図3に、縦軸に処理容器内の高さ
方向位置をとってクラッドの少ないものから順に実線a
、b、cで示す。
なお、図2に含水率を測定した測定ポイントを×印で示
した。この図から明らかなように、中空糸膜フィルタに
より十分容器内脱水することができた。[0009] As an experiment, a simulated sludge of powdered ion exchange resin was dehydrated in a container and solidified by hydrothermal reaction. The results will be explained next. Experimental Example 1 As shown in FIG. 2, a hollow fiber membrane filter 11 was installed in a processing container with a diameter of 80 mm, and a dehydration treatment was performed on simulated sludge 12 containing 0, 5, and 20% by weight of cladding at a reduced pressure of -510 mmHg. Ta. The water content after each dehydration process is shown in Figure 3, with the height direction position in the processing container taken as the vertical axis, and the solid line a in order from the one with the least amount of crud.
, b, and c. In addition, in FIG. 2, the measurement points at which the water content was measured are indicated by x marks. As is clear from this figure, the hollow fiber membrane filter was able to sufficiently dehydrate the container.
【0010】実験例2
図4に示す装置を用いて電気浸透法による容器内脱水を
行った。この図に示すように、陽極21、陰極22、電
極液23、陽イオン交換膜24、多孔膜25からなる一
体化されたモジュールを処理容器内に挿入してなる試験
装置にて、模擬スラッジ26を脱水したところ、脱水液
27が処理容器の中央に集められ、処理後のスラッジは
図5に示すような含水率となった。図中、実線dは容器
内のスラッジ中心部の、実線eはスラッジ外側の測定値
をそれぞれ示す。また、鎖線fは図4の容器内のスラッ
ジ上面に相当する高さ位置を示す。この試験結果からも
明らかなように、電気浸透法によっても十分脱水できる
ことが分かる。Experimental Example 2 Dehydration in a container was carried out by electroosmosis using the apparatus shown in FIG. As shown in this figure, a simulated sludge 26 When the sludge was dehydrated, a dehydrated liquid 27 was collected in the center of the treatment container, and the sludge after treatment had a moisture content as shown in FIG. In the figure, the solid line d indicates the measured value at the center of the sludge in the container, and the solid line e indicates the measured value at the outside of the sludge. Further, a chain line f indicates a height position corresponding to the upper surface of the sludge in the container in FIG. As is clear from this test result, it can be seen that sufficient dehydration can be achieved by electroosmosis.
【0011】実験例3次表に示す配合比でスラッジの水
熱固化を直径2cmの小規模装置で試みたところ、表に
示すように、十分圧縮強度の大きい固化体を形成するこ
とができた。Experimental Example 3 When hydrothermal solidification of sludge was attempted using a small-scale device with a diameter of 2 cm using the blending ratio shown in the following table, it was possible to form a solidified material with sufficiently high compressive strength as shown in the table. .
【0012】以上の説明からも明らかなように、比較的
放射能レベルの高いスラッジを容器内で脱水処理して減
容化した後、その同一容器内で速やかに固化処理するこ
とができるので、別途脱水処理装置、その脱水処理装置
と固化処理装置間のスラッジの移送ラインおよびそれに
付随するポンプ等の付属機器を用意する必要がなく、二
次放射性廃棄物の発生を抑えるとともに作業員の被曝量
の低減を図ることができる。[0012] As is clear from the above explanation, sludge with a relatively high radioactivity level can be dehydrated and reduced in volume in a container, and then solidified quickly in the same container. There is no need to prepare a separate dewatering device, a sludge transfer line between the dehydrating device and the solidification device, and associated equipment such as pumps, which reduces the generation of secondary radioactive waste and reduces the amount of radiation exposure for workers. It is possible to reduce the
【0013】[0013]
【発明の効果】以上説明したように本発明によれば、比
較的高レベルのスラッジを単純な工程で長期間安定した
状態で保存可能な形態に処理することができ、作業員の
被曝量の低減を図ることができる。Effects of the Invention As explained above, according to the present invention, relatively high level sludge can be processed into a form that can be stored stably for a long period of time through a simple process, thereby reducing the radiation exposure of workers. It is possible to reduce the
【図1】 本発明にかかる放射性廃スラッジの処理シ
ステムの一実施例を示す説明図[Fig. 1] An explanatory diagram showing an embodiment of the radioactive waste sludge treatment system according to the present invention.
【図2】 中空糸膜フィルタを設置した処理容器の断
面図[Figure 2] Cross-sectional view of a processing container equipped with a hollow fiber membrane filter
【図3】 図2の中空糸膜フィルタによる脱水処理後
のスラッジの含水率を示すグラフ[Figure 3] Graph showing the water content of sludge after dehydration using the hollow fiber membrane filter in Figure 2
【図4】 電気浸透装置を設置した処理容器の断面図
[Figure 4] Cross-sectional view of a processing container equipped with an electroosmosis device
【図5】 図4の電気浸透装置による脱水処理後のス
ラッジの含水率を示すグラフである。5 is a graph showing the water content of sludge after dehydration treatment by the electroosmosis device of FIG. 4. FIG.
1 …スラッジ貯蔵槽 2 …スラッジ 3 …処理容器 4 …固形化剤 5 …モジュール 6 …ヒータ 7 …プレス 11 …中空糸膜フィルタ 12 …模擬スラッジ 21 …陽極 22 …陰極 23 …電極液 24 …陽イオン交換膜 25 …多孔膜 26 …模擬スラッジ 27 …脱水液 1...Sludge storage tank 2…Sludge 3...Processing container 4...Solidifying agent 5...Module 6...Heater 7...Press 11...Hollow fiber membrane filter 12…Simulated sludge 21...Anode 22...Cathode 23...Electrode liquid 24...Cation exchange membrane 25... Porous membrane 26…Simulated sludge 27…Dehydrated liquid
Claims (1)
射性スラッジを固化処理するにあたり、該放射性スラッ
ジを貯蔵槽から直接最終保存容器内に移送して前処理し
、しかる後安定化処理して固化体にすることを特徴とす
る放射性廃スラッジの処理方法。Claim 1: When solidifying radioactive sludge generated from a radioactive substance handling facility, the radioactive sludge is directly transferred from a storage tank to a final storage container, pretreated, and then stabilized to form a solidified body. A method for treating radioactive waste sludge, characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP40590390A JPH04221799A (en) | 1990-12-25 | 1990-12-25 | Treating method for radioactive sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP40590390A JPH04221799A (en) | 1990-12-25 | 1990-12-25 | Treating method for radioactive sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04221799A true JPH04221799A (en) | 1992-08-12 |
Family
ID=18515515
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP40590390A Withdrawn JPH04221799A (en) | 1990-12-25 | 1990-12-25 | Treating method for radioactive sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04221799A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2728719A1 (en) * | 1994-12-22 | 1996-06-28 | Rtc Realisations Tech Et Comme | METHOD AND INSTALLATION FOR THE TREATMENT OF RADIOACTIVE RESIDUES IN THE FORM OF SLUDGE |
JP2019196956A (en) * | 2018-05-09 | 2019-11-14 | 太平電業株式会社 | Storage method of radioactive granular waste resin to shielding container |
-
1990
- 1990-12-25 JP JP40590390A patent/JPH04221799A/en not_active Withdrawn
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2728719A1 (en) * | 1994-12-22 | 1996-06-28 | Rtc Realisations Tech Et Comme | METHOD AND INSTALLATION FOR THE TREATMENT OF RADIOACTIVE RESIDUES IN THE FORM OF SLUDGE |
EP0724271A1 (en) * | 1994-12-22 | 1996-07-31 | R.T.C. Realisations Techniques Et Commerciales | Process and device for treating radioactive waste by hydraulic binding agent |
JP2019196956A (en) * | 2018-05-09 | 2019-11-14 | 太平電業株式会社 | Storage method of radioactive granular waste resin to shielding container |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Application deemed to be withdrawn because no request for examination was validly filed |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 19980312 |