JPS61117494A - Method of treating radioactive waste - Google Patents
Method of treating radioactive wasteInfo
- Publication number
- JPS61117494A JPS61117494A JP23766584A JP23766584A JPS61117494A JP S61117494 A JPS61117494 A JP S61117494A JP 23766584 A JP23766584 A JP 23766584A JP 23766584 A JP23766584 A JP 23766584A JP S61117494 A JPS61117494 A JP S61117494A
- Authority
- JP
- Japan
- Prior art keywords
- asphalt
- radioactive waste
- mixture
- solvent
- present
- 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
- Treatment Of Sludge (AREA)
- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、原子力発電所等からの放射性廃棄物を処理す
る方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for treating radioactive waste from nuclear power plants and the like.
原子力発電所からの放射性廃液の処理方法のひとつとし
て、該廃液を蒸発等によシ#縮した後にアスファルトに
よって固化し、ドラム缶内に封じ込める方法があり、現
在までにドラム缶の本数で数10万本に達しているが、
アスファルト劣化による放射性物質の漏えい及び保v#
I所が問題となっている。又、アスファルト固化の状態
では海洋投棄は不可能で、プラスチック固化などKよる
5次処理が必要である。One method for treating radioactive waste fluid from nuclear power plants is to condense the waste fluid through evaporation, solidify it with asphalt, and seal it in drums.Currently, several hundred thousand drums have been produced. Although it has reached
Leakage and preservation of radioactive materials due to asphalt deterioration#
I have a problem. In addition, it is impossible to dump the waste into the ocean when it is solidified as asphalt, and 5th treatment using K, such as plastic solidification, is required.
本発明の目的は、該アスファルト固化物よりアスファル
トの一部を選択的に回収し、アスファルト固化物を減容
化し、該減容化物の保管場所の縮小、さらKはプラスチ
ック固化などによる3次処理の前工程となる放射性廃棄
物の処理方法を提供するにある。即ち、本発明線、減容
化されたアスファルト固化物の周囲をプラスチックで固
化し、再びドラム缶詰めしてアスファルト劣化による放
射性物質の漏えいを防止し、さらにはグラスチックの性
能次第では海洋投棄も可能とする放射性廃棄物の処理方
法を提供することを目的とする。The purpose of the present invention is to selectively recover a part of asphalt from the asphalt solidified product, reduce the volume of the asphalt solidified product, reduce the storage area of the reduced volume product, and further perform tertiary treatment such as plastic solidification. The purpose of the present invention is to provide a method for treating radioactive waste, which is a pre-process. In other words, according to the present invention, the area around the reduced volume of solidified asphalt is solidified with plastic, and it is again canned in drums to prevent the leakage of radioactive materials due to asphalt deterioration.Furthermore, depending on the performance of the plastic, it is possible to dump it into the ocean. The purpose is to provide a method for disposing of radioactive waste.
そして、本発明は、上記目的を達成する手段として、放
射性廃棄物とアスファルトの加熱処理混合物に溶剤を混
合し、アスファルトと放射性廃莱物#縮残液とに分離す
る点にある。すなわち、本発明は、放射性廃棄物とアス
ファルトを混合加熱し、該加熱処理混合物に溶解溶剤を
混合して混合物を製造し、次いで、この混合物をアスフ
ァルトと放射性廃棄物が濃縮された残液とに分離するこ
とを特徴とする放射性廃棄物の処理方法である。The present invention, as a means for achieving the above object, consists in mixing a solvent into a heat-treated mixture of radioactive waste and asphalt, and separating the mixture into asphalt and radioactive waste/residual liquid. That is, the present invention mixes and heats radioactive waste and asphalt, mixes a dissolving solvent into the heated mixture to produce a mixture, and then converts this mixture into asphalt and a residual liquid in which radioactive waste is concentrated. This is a method for treating radioactive waste, which is characterized by separating it.
本発明者は、放射性廃棄物のアスファルト加熱処理混合
物に、アスファルトの一部のみを溶解させる溶解溶剤を
添加して、温度、圧力を制御し、重力沈降を行なうこと
によシ、アスファルト固化物中のM&*Ba0t又はN
aW8Q4 のほぼ全量と、アスファルトの一部が凝
集して違択的に沈殿物となることを見出した。そして、
かかる方法により、放射性廃棄物の減容化ができること
を見出し、本発明を完成したものである。この減容化率
は、アスファルトの溶剤への浴M量を?It制御すると
とKよって任意に制御できるものである。The present inventor added a dissolving solvent that dissolves only a portion of the asphalt to an asphalt heat-treated mixture of radioactive waste, controlled the temperature and pressure, and carried out gravity sedimentation. M&*Ba0t or N
It was found that almost the entire amount of aW8Q4 and a part of the asphalt coagulated and selectively formed a precipitate. and,
The present invention was completed based on the discovery that radioactive waste can be reduced in volume by such a method. This volume reduction rate is based on the amount of bath M added to the asphalt solvent? When it is controlled, it can be controlled arbitrarily by K.
以下第1図に基づいて本発明の詳細な説明する。第1図
は本発明を実施するためのフローシートを示す。The present invention will be explained in detail below based on FIG. FIG. 1 shows a flow sheet for implementing the invention.
放射性廃棄物は、加熱帯1でアスファルトと混合され、
水分をほぼ完全に除去された加熱処理混合物を製造する
。Radioactive waste is mixed with asphalt in heating zone 1,
A heat-treated mixture from which moisture has been almost completely removed is produced.
放射性廃棄物アスファルト加熱処理混合物の代表的な主
成分と組成は、
アスファルト 約6註〜40(約500pp
m)
である。The typical main components and composition of the radioactive waste asphalt heat treatment mixture are asphalt about 6 to 40 (about 500pp)
m).
NhgBOa又はlag B, Oyは原子炉の冷却水
中に存在し、放射線の吸収剤として多量に使用されてい
る。NhgBOa or lag B, Oy exists in the cooling water of nuclear reactors and is used in large amounts as a radiation absorber.
次に該加熱処理混合物と溶解溶剤を混合帯2にて混合し
、混合物を製造する。混合帯2は攪拌軸タイプのもの又
はスタテイクミキサー等の公知の装置で十分であシ、特
に工夫は喪しない。Next, the heat-treated mixture and the dissolving solvent are mixed in the mixing zone 2 to produce a mixture. The mixing zone 2 may be of a stirring shaft type or a known device such as a static mixer without any particular ingenuity.
又、該放射性廃棄物とアスファルトの加熱処理混合物1
!i量部に対して溶解溶剤を2〜8重1部添加するのが
好ましい。Moreover, the heat-treated mixture 1 of the radioactive waste and asphalt
! It is preferable to add 1 part by weight of 2 to 8 parts of the dissolving solvent per i part.
添加量が2重量部以下では粘度の増加により分離性能が
低下する。又、添加量が8i量部以上では分離性能はほ
ぼ一定であり、プロセスの熱効率の低下及び装置コスト
の増大をもたらす。If the amount added is less than 2 parts by weight, the separation performance will decrease due to an increase in viscosity. Moreover, when the amount added is 8i parts or more, the separation performance remains almost constant, resulting in a decrease in the thermal efficiency of the process and an increase in equipment cost.
温反圧力は、次工程の分離帯3とほぼ同一条件にて一間
御される。The temperature reaction pressure is controlled for one period under almost the same conditions as the separation zone 3 in the next step.
本発明において、溶解溶剤としては、その取扱い易さか
ら常温で液体であること、又アスファルトに対する溶解
性からパラフィン化合物、単環ナフテン化合物,単環芳
香族化合物又はそれらの混合物で、臨界温度が350℃
以下の物質が好ましい。この代表的な溶解溶剤を表1に
表1 代表的溶解溶剤
次に、該混合物は分離帯3に導入され、動力沈降により
Mac B、 07又はNa1SO4等が実質的に含ま
れないアスファルトをオーバーフローよシ回収し、溶解
溶剤は溶剤回収帯4で回収する。In the present invention, the dissolving solvent is a paraffin compound, a monocyclic naphthenic compound, a monocyclic aromatic compound, or a mixture thereof, which must be liquid at room temperature for ease of handling, and because of its solubility in asphalt, and has a critical temperature of 350. ℃
The following substances are preferred. Typical dissolving solvents are shown in Table 1.The mixture is then introduced into the separation zone 3, where the asphalt substantially free of Mac B, 07 or Na1SO4 etc. is overflowed by power settling. The dissolved solvent is recovered in the solvent recovery zone 4.
一方溶解溶剤に溶けないアスファルトの一部とNa1B
aOt又はNa1SO4からなる物質は凝集沈降しアン
ダーフローよシ回収し、溶解溶剤は溶剤回収帯5で回収
する。On the other hand, part of the asphalt that does not dissolve in the dissolving solvent and Na1B
The substance consisting of aOt or Na1SO4 coagulates and settles and is recovered in the underflow, and the dissolved solvent is recovered in the solvent recovery zone 5.
次に、該重力沈降の好ましい条件を以下に述べる。Next, preferred conditions for the gravity sedimentation will be described below.
操作温度としては、該混合物の粘度及び比重をできるだ
け小さくして分離効率を高めるために150℃以上にす
べきである。しかし、処理物は約550℃以上では重縮
合、熱分解反応によるコーキング反応が生じるので、こ
の温度以下にすべきである。The operating temperature should be 150° C. or higher in order to minimize the viscosity and specific gravity of the mixture and increase the separation efficiency. However, since coking reactions due to polycondensation and thermal decomposition reactions occur at temperatures above about 550° C., the temperature of the treated product should be below this temperature.
次に、圧力については、溶剤を均一相に安定に保持する
ために、溶解溶剤の蒸気圧以上にすべきである。実用上
は蒸気圧の1.0倍から5倍の加囲で十分である。Next, the pressure should be higher than the vapor pressure of the dissolving solvent in order to stably maintain the solvent in a homogeneous phase. Practically speaking, an enclosure of 1.0 to 5 times the vapor pressure is sufficient.
以下、本発明の実施例をあげて本発明の詳細な説明する
。Hereinafter, the present invention will be explained in detail by giving examples of the present invention.
実施例1
PWR方式の原子力発電所よシ発生した放射性廃棄物の
アスファルト加熱処理混合物1重量部に対して、溶解溶
剤としてn−ヘキサノを6重量部添加し、内容積6Lの
縦長オートクレーブに仕込み、攪拌しながら、温度20
0℃、圧力4011y/、ff1Gに10分保持後、同
一温度、圧力下で約30分静置し、サンプリングノズル
より上澄液と残液を回収し、各々蒸発によυn−ヘキサ
ンを除去した。Example 1 6 parts by weight of n-hexano was added as a dissolving solvent to 1 part by weight of an asphalt heat-treated mixture of radioactive waste generated from a PWR nuclear power plant, and the mixture was charged into a vertical autoclave with an internal volume of 6 L. While stirring, increase the temperature to 20
After holding at 0°C and pressure of 4011y/, ff1G for 10 minutes, it was allowed to stand for about 30 minutes at the same temperature and pressure, and the supernatant liquid and residual liquid were collected from the sampling nozzle, and υn-hexane was removed by evaporation. .
物質収支の結果を表2に示した。The material balance results are shown in Table 2.
この場合の減容化率は でちった。In this case, the volume reduction rate is It was made.
表2 (実施例1)
実施例2
実施例1において、溶解溶剤の添加量を変えて分離性能
を測定した。Table 2 (Example 1) Example 2 In Example 1, the separation performance was measured by changing the amount of dissolving solvent added.
その結果、該加熱処理混合物1重量部に対して溶解溶剤
を2部以下添加すると、上澄液中のNa*E40yの含
有量が4.0重量X以上となシ、その含有量が増加した
。As a result, when 2 parts or less of the dissolving solvent was added to 1 part by weight of the heat-treated mixture, the content of Na*E40y in the supernatant liquid increased to 4.0 parts by weight or more. .
実施例3
実施例1において、溶解溶剤としてシクロヘキサン、ペ
ンゼ/を用いた。その結果を表5.4に示した。減容化
率は各々40重′gCX、56重量%であった。Example 3 In Example 1, cyclohexane and Penze/ were used as the dissolving solvent. The results are shown in Table 5.4. The volume reduction rate was 40g CX and 56% by weight, respectively.
表3 (実施例3.シクロヘキサン)表4 (実
施例3.ベンゼン)
実施例4
実施例1において、BWR方式原子力発電所から発生し
た放射性廃棄物加熱処理混合物を処理した。その結果を
表5に示した。Table 3 (Example 3. Cyclohexane) Table 4 (Example 3. Benzene) Example 4 In Example 1, a radioactive waste heat treatment mixture generated from a BWR type nuclear power plant was treated. The results are shown in Table 5.
減容化率は30重量Xであった。The volume reduction rate was 30X by weight.
表5 (実施例4)
〔発明の効果〕
本発明は、以上詳記したように、放射性廃棄物のアスフ
ァルト加熱処理物を、溶解溶剤を使用して、アスファル
トと放射性廃菓物濃縮残液とに分離するものであるから
、アスファルト固化物の減容化効果が生ずるものであυ
、その結果、該アスファルト固化物の保管場所の縮小、
さらには、プラスチックによる再固化が容易に行うこと
ができ、アスファルトの劣化に伴う放射性物質の漏えい
を防止できる効果が生ずるものである。Table 5 (Example 4) [Effects of the Invention] As detailed above, the present invention uses a dissolving solvent to asphalt heat-treated radioactive waste into asphalt and radioactive waste concentrated residual liquid. Since the asphalt is separated into two parts, it has the effect of reducing the volume of the solidified asphalt.
, As a result, the storage space for the solidified asphalt is reduced;
Furthermore, the plastic can be easily re-solidified, which has the effect of preventing leakage of radioactive substances due to deterioration of asphalt.
表口面の簡単な説明
第1図は、本発明を実施するためのフローシートである
。BRIEF DESCRIPTION OF THE FACE FIG. 1 is a flow sheet for carrying out the present invention.
復代理人 内 1) 明 後代理人 荻 原 亮 −Sub-agent: 1) Akira Sub-agent Ryo Ogihara -
Claims (1)
混合物に溶解溶剤を混合して混合物を製造し、次いで、
該混合物をアスファルトと放射性廃棄物が濃縮された残
液とに分離することを特徴とする放射性廃棄物の処理法
。Radioactive waste and asphalt are mixed and heated, a dissolving solvent is mixed into the heated mixture to produce a mixture, and then,
A method for treating radioactive waste, comprising separating the mixture into asphalt and a residual liquid in which radioactive waste is concentrated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23766584A JPS61117494A (en) | 1984-11-13 | 1984-11-13 | Method of treating radioactive waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23766584A JPS61117494A (en) | 1984-11-13 | 1984-11-13 | Method of treating radioactive waste |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61117494A true JPS61117494A (en) | 1986-06-04 |
Family
ID=17018689
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23766584A Pending JPS61117494A (en) | 1984-11-13 | 1984-11-13 | Method of treating radioactive waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61117494A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0349444A (en) * | 1989-05-08 | 1991-03-04 | American Teleph & Telegr Co <Att> | Network comprising continuously interconnected plural stages and control method of the same |
-
1984
- 1984-11-13 JP JP23766584A patent/JPS61117494A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0349444A (en) * | 1989-05-08 | 1991-03-04 | American Teleph & Telegr Co <Att> | Network comprising continuously interconnected plural stages and control method of the same |
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