JPS6035037B2 - Waste liquid treatment method - Google Patents
Waste liquid treatment methodInfo
- Publication number
- JPS6035037B2 JPS6035037B2 JP12770578A JP12770578A JPS6035037B2 JP S6035037 B2 JPS6035037 B2 JP S6035037B2 JP 12770578 A JP12770578 A JP 12770578A JP 12770578 A JP12770578 A JP 12770578A JP S6035037 B2 JPS6035037 B2 JP S6035037B2
- Authority
- JP
- Japan
- Prior art keywords
- waste liquid
- syrup
- distillation
- residual
- radioactive
- 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
Links
- 239000007788 liquid Substances 0.000 title claims description 18
- 239000002699 waste material Substances 0.000 title claims description 13
- 238000000034 method Methods 0.000 title claims description 9
- 238000004821 distillation Methods 0.000 claims description 17
- 239000006188 syrup Substances 0.000 claims description 14
- 235000020357 syrup Nutrition 0.000 claims description 14
- 239000000941 radioactive substance Substances 0.000 claims description 12
- 125000005397 methacrylic acid ester group Chemical group 0.000 claims description 7
- 229920000642 polymer Polymers 0.000 claims description 4
- 239000002901 radioactive waste Substances 0.000 claims description 2
- 239000003960 organic solvent Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000006116 polymerization reaction Methods 0.000 description 6
- 239000012857 radioactive material Substances 0.000 description 6
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 150000002978 peroxides Chemical class 0.000 description 4
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 4
- 239000004926 polymethyl methacrylate Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000002685 polymerization catalyst Substances 0.000 description 3
- JHPBZFOKBAGZBL-UHFFFAOYSA-N (3-hydroxy-2,2,4-trimethylpentyl) 2-methylprop-2-enoate Chemical compound CC(C)C(O)C(C)(C)COC(=O)C(C)=C JHPBZFOKBAGZBL-UHFFFAOYSA-N 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- YZCKVEUIGOORGS-NJFSPNSNSA-N Tritium Chemical compound [3H] YZCKVEUIGOORGS-NJFSPNSNSA-N 0.000 description 1
- 125000005396 acrylic acid ester group Chemical group 0.000 description 1
- -1 acrylic ester Chemical class 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000010894 electron beam technology Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- 229910052722 tritium Inorganic materials 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
本発明は、放射性物質を含有する廃液を完全に処理する
方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for the complete treatment of waste liquids containing radioactive substances.
従来、放射性物質を含有する廃液、例えば有機シンチレ
ーター廃液の処理方法としては、該廃液を直ちに燃焼処
理することが試みられたが、水分を多量に含んだ廃液が
多く、直接燃焼させるには、大規模の燃焼設備と専任の
技術者を必要とする。Conventionally, attempts have been made to immediately incinerate waste liquids containing radioactive materials, such as organic scintillator waste liquids, but since most waste liquids contain large amounts of water, direct combustion is difficult. Requires large-scale combustion equipment and dedicated engineers.
そのため、大多数の事業所毎の処理は下可能であり、一
方、集中処理する場合でもラジオアイソトープを含む有
機溶媒や廃液の安全な輸送は、実施が困難である。この
ような、処理の困難さから、廃液の保管は未処理のまま
集積されているのが現状である。この状態は、放射性物
質に起因する災害の防止ならびに火災の予防の見地から
、非常に危険であり、これを避けるために、液体シンチ
レーション計測装直の使用を禁止する場合も発生してい
る。本発明者らは、かかる現状を改善するために該有機
シンチレータ−廃液を通気蒸溜によってラジオアイソト
ープを殆ど含まない有機溶剤と水とからなる蒸溜々分と
、ラジオアイソトープの殆どを含む蒸留残澄とに分け、
そのそれぞれを別個に処理する方法を考案し、更に鋭意
検討した結果、本発明に到達した。Therefore, it is possible to carry out treatment at each facility in most cases, but even in the case of centralized treatment, it is difficult to safely transport organic solvents and waste liquids containing radioisotopes. Due to the difficulty of treatment, waste liquid is currently stored in piles without being treated. This condition is extremely dangerous from the standpoint of preventing disasters caused by radioactive materials and fire prevention, and to avoid this, there are cases where direct use of liquid scintillation measurement equipment is prohibited. In order to improve the current situation, the present inventors conducted aeration distillation of the organic scintillator waste liquid to obtain a distillate fraction consisting of an organic solvent and water that contains almost no radioisotopes, and a distillation residue that contains most of the radioisotopes. Divide into
As a result of devising a method for treating each of these separately and conducting further intensive studies, we have arrived at the present invention.
本発明は放射性物質を含有する廃液を通気蒸溜によって
溜出部と残留部とに分離し、溜出部を適宜の手段で処理
する一方、残留部にメタクリル酸ェステル系シラップを
加えて重合固化せしめることにより、残留部をメタクリ
ル酸ヱステル系シラップ内に封じこめた後、燃焼するこ
とにより、残留部を上記重合物と共に焼却処理すること
を特徴とする、放射性廃液の完全な処理方法である。In the present invention, waste liquid containing radioactive substances is separated into a distillation part and a residual part by aerated distillation, and while the distillation part is treated by an appropriate means, a methacrylic acid ester syrup is added to the residual part and polymerized and solidified. This is a complete treatment method for radioactive waste liquid, which is characterized in that the residual portion is sealed in methacrylic acid ester syrup and then incinerated together with the above-mentioned polymer.
本発明の処理方法によって、その処理に多大の配慮を要
する放射性物質含有廃液は、先ず放射性物質を殆ど含ま
ない溜出部と放射性物質の大部分を含む残留部とに分け
られ、溜出成分である有機溶剤や水は通常の方法、例え
ば焼却や排水として処理することが可能であるので、原
液の量からみればきわめて少量の残留部の処理が問題と
して残される。放射性物質の大部分を含む残留部につい
ては、これを集中的に焼却処理することを前提に保管、
取扱い、輪送、焼却に際して、放射性物質の飛散、漏洩
を防ぐために固型化を検討した。According to the treatment method of the present invention, radioactive substance-containing waste liquid, which requires great consideration in its treatment, is first divided into a distillation part that contains almost no radioactive substances and a residual part that contains most of the radioactive substances. Since certain organic solvents and water can be disposed of in the usual manner, such as by incineration or as wastewater, the problem remains how to dispose of the residual portion, which is extremely small compared to the amount of the raw solution. The remaining parts containing most of the radioactive materials will be stored on the premise that they will be intensively incinerated.
We considered solidifying the material to prevent the scattering and leakage of radioactive materials during handling, transportation, and incineration.
その結果、メタクリル酸ェステル系シラップを残留部に
添加混合したのちに重合固化させて残留物を封じこめる
ことにより、残留部の固型化が容易で、黒煙を出さずか
つ残澄を残さないで、上記固型化物を焼却処理すること
ができることを見し、出した。本発明に用いられるメタ
クリル酸ェステル系シラップは、ポリメタクリル酸メチ
ルメタクリル酸メチルを混合して成る液状物を主成分と
するものである。本発明においては、該シラップの重合
性及び重合物の燃焼性を損わない範囲でポリメタクリル
酸メチルの代りに、メタクリル酸メチルに少量の他のメ
タクリル酸ェステル及び/又はアクリル酸ェステルを添
加して重合して得られるコポリマーを用いてもよい。As a result, by adding and mixing methacrylic acid ester syrup to the residual part and then polymerizing and solidifying it to seal in the residual part, the residual part can be easily solidified without emitting black smoke or leaving a residue. Then, they found that the solidified material could be incinerated, so they released it. The methacrylic acid ester syrup used in the present invention is mainly composed of a liquid mixture of polymethyl methacrylate and methyl methacrylate. In the present invention, a small amount of other methacrylic acid ester and/or acrylic acid ester is added to methyl methacrylate instead of polymethyl methacrylate within a range that does not impair the polymerizability of the syrup and the combustibility of the polymer. A copolymer obtained by polymerization may also be used.
又、同様にメタクリル酸ェステル系シラップに、少量の
他のメタクリル酸ェステル及び/又はアクリル酸ェステ
ルを添加してもよい。Similarly, a small amount of other methacrylic ester and/or acrylic ester may be added to the methacrylic ester syrup.
上記〆タクリル酸ェステル系シラップの製造方法として
は、例えばポリメタクリル酸メチルをメタクリル酸メチ
ルに溶解する方法、又はメタクリル酸メチルを一部重合
させた状態で重合停止させて、部分重合シラップを製造
する方法が挙げられる。As a method for producing the above-mentioned taacrylate syrup, for example, a method of dissolving polymethyl methacrylate in methyl methacrylate, or a partially polymerized syrup is produced by stopping the polymerization in a state where methyl methacrylate is partially polymerized. There are several methods.
固型化処理の方法は、放射性物質の殆どを含む蒸留残簿
と該メタクリル酸ェステル系シラップを混合し、これに
重合触媒を加え、該混合物を固型化させる。The solidification treatment involves mixing the distillation residue containing most of the radioactive substances with the methacrylate syrup, adding a polymerization catalyst thereto, and solidifying the mixture.
このとき、該蒸溜残澄中に通気蒸溜で分別しされなかっ
た有機溶剤が少量残存することは差支えないが、多量に
残存することは園型化物を軟化させたり、後になって、
有機溶剤が揮散するので好ましくない。また、該蒸溜残
澄中に少量の水が存在することは差支えないが、重合反
応を阻害する程或いは固型化物の燃焼を妨げる程、多量
に存在することは好ましくない。重合触媒としては、油
溶性の過酸化物、例えば過酸化ペンゾィルなどが最適で
あるが、アゾビス系の重合触媒の使用や活性化エネルギ
ー源としての熱、紫外線、電子線の使用も可能である。At this time, it is okay for a small amount of organic solvent that has not been fractionated by aerated distillation to remain in the distillation residue, but if a large amount remains, it may cause softening of the molded product or
This is not preferable because the organic solvent will volatilize. Further, although it is acceptable for a small amount of water to be present in the distillation residue, it is not preferable for the water to be present in such a large amount that it inhibits the polymerization reaction or the combustion of the solidified product. As the polymerization catalyst, an oil-soluble peroxide such as penzoyl peroxide is most suitable, but it is also possible to use an azobis-based polymerization catalyst or to use heat, ultraviolet rays, or electron beams as an activation energy source.
また過酸化物による重合反応を促進させるため、例えば
第3級ァミンなどの促進剤を併用することが可能である
。更に重合反応に対する空気中の酸素の影響を少なくす
るため、パラフィンの併用や空気遮断フィルムなども併
用できる。実施例
放射性物質のトリチウムを含有する放射性有機シンチレ
ーター廃液1000肌を通気蒸溜によって、放射性物質
を殆ど含まない易揮発生の有機溶剤310の‘、水49
0の‘及び大部分の放射性物質を含む蒸溜残燈200私
に分別した。Further, in order to promote the polymerization reaction by peroxide, it is possible to use a promoter such as a tertiary amine in combination. Furthermore, in order to reduce the influence of oxygen in the air on the polymerization reaction, paraffin or an air-blocking film can be used in combination. Example 1,000 pieces of radioactive organic scintillator waste liquid containing tritium, a radioactive substance, were subjected to aeration distillation, and 310 pieces of an easily volatile organic solvent containing almost no radioactive substances and 49 pieces of water were extracted.
Distilled residual light containing 0' and most radioactive materials was separated into 200 I.
分別された有機溶剤、水及び蒸溜残澄中の放射性物質量
は、それぞれ4.1×10‐3マイクロキュリー(山C
i)、2.7×10‐2仏Ci、9.4仏Ciであって
、分別された有機溶剤及び水の中に存在する放射性物質
の量は、これらを通常の方法例えば焼却や排水として処
理するのに何ら、差支えない範囲であり、該廃液中に存
在していた放射性物質の殆どが、蒸溜残澄中に含まれて
いた。The amount of radioactive substances in the separated organic solvent, water, and distillation residue was 4.1 × 10-3 microcuries (mountain C
i), 2.7 x 10-2 French Ci, 9.4 French Ci, and the amount of radioactive substances present in the separated organic solvent and water is that if these are removed by normal methods such as incineration or drainage, Most of the radioactive substances present in the waste liquid were contained in the distillation residue, which was within a range that would pose no problem for treatment.
したがってこの通気蒸溜による分別によって、放射性物
質に必要な特別処理を必要とする量は初めの廃液の20
%まで減量された。分別された放射性物質を含む蒸溜残
簿50の重量部に、ポリメタクリル酸メチル150重量
部とメタクリル酸メチルモノマー35の重量部とN,N
′ージメチルパラトルィジン1重量部から成るシラップ
を混合し、更に過酸化ペンゾィル5重量部を混合したと
ころ、室温で約30分後に重合反応が終了し、蒸溜残澄
とシラップの混合物は間型化物になった。Therefore, by this aerated distillation separation, the amount of radioactive materials that require special treatment can be reduced to 20% of the initial waste liquid.
It was reduced to %. 150 parts by weight of polymethyl methacrylate, 35 parts by weight of methyl methacrylate monomer, and N,N
When a syrup consisting of 1 part by weight of -dimethyl-paratoluidine was mixed with 5 parts by weight of penzoyl peroxide, the polymerization reaction was completed after about 30 minutes at room temperature, and the mixture of distillation residue and syrup was mixed with a mixture of distillation residue and syrup. I became a monster.
Claims (1)
部と残留部とに分離し、溜出部を適宜の手段で処理する
一方、残留部にメタクリル酸エステル系シラツプを加え
て重合固化せしめることにより、残留部をメタクリル酸
エステル系シラツプの重合物内に封じこめた後、燃焼す
ることにより、残留部を上記重合物と共に焼却処理する
ことを特徴とする、放射性廃液の完全な処理方法。1 Separate the waste liquid containing radioactive substances into a distillate part and a residual part by aerated distillation, treat the distillate part by appropriate means, and add methacrylic acid ester syrup to the residual part to polymerize and solidify it. A method for completely disposing of radioactive waste liquid, which comprises: trapping the residual portion in a polymer of methacrylic acid ester syrup, and then incinerating the residual portion together with the polymer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12770578A JPS6035037B2 (en) | 1978-10-17 | 1978-10-17 | Waste liquid treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12770578A JPS6035037B2 (en) | 1978-10-17 | 1978-10-17 | Waste liquid treatment method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5554498A JPS5554498A (en) | 1980-04-21 |
| JPS6035037B2 true JPS6035037B2 (en) | 1985-08-12 |
Family
ID=14966659
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12770578A Expired JPS6035037B2 (en) | 1978-10-17 | 1978-10-17 | Waste liquid treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6035037B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58151318A (en) * | 1982-02-26 | 1983-09-08 | Shin Etsu Chem Co Ltd | Synthetic silica and resin composition containing it for sealing electronic parts |
-
1978
- 1978-10-17 JP JP12770578A patent/JPS6035037B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5554498A (en) | 1980-04-21 |
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