JPS6112237B2 - - Google Patents
Info
- Publication number
- JPS6112237B2 JPS6112237B2 JP11556581A JP11556581A JPS6112237B2 JP S6112237 B2 JPS6112237 B2 JP S6112237B2 JP 11556581 A JP11556581 A JP 11556581A JP 11556581 A JP11556581 A JP 11556581A JP S6112237 B2 JPS6112237 B2 JP S6112237B2
- Authority
- JP
- Japan
- Prior art keywords
- metal
- particles
- vitrified
- glass
- coating
- 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
- 239000002184 metal Substances 0.000 claims description 39
- 229910052751 metal Inorganic materials 0.000 claims description 39
- 239000002245 particle Substances 0.000 claims description 39
- 238000000576 coating method Methods 0.000 claims description 25
- 239000002901 radioactive waste Substances 0.000 claims description 22
- 239000011248 coating agent Substances 0.000 claims description 19
- 239000011521 glass Substances 0.000 claims description 19
- 238000000034 method Methods 0.000 claims description 17
- 238000005245 sintering Methods 0.000 claims description 13
- 238000002844 melting Methods 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 6
- 238000003860 storage Methods 0.000 description 18
- 239000000463 material Substances 0.000 description 14
- 238000007906 compression Methods 0.000 description 8
- 230000006835 compression Effects 0.000 description 8
- 239000010949 copper Substances 0.000 description 8
- 238000011049 filling Methods 0.000 description 8
- 239000000126 substance Substances 0.000 description 7
- 150000002739 metals Chemical class 0.000 description 6
- 239000002699 waste material Substances 0.000 description 6
- 238000009792 diffusion process Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 238000002386 leaching Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 239000000956 alloy Substances 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000002131 composite material Substances 0.000 description 4
- 230000007774 longterm Effects 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000004017 vitrification Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000005388 borosilicate glass Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 238000007747 plating Methods 0.000 description 3
- 230000005258 radioactive decay Effects 0.000 description 3
- 239000012857 radioactive material Substances 0.000 description 3
- 229910052718 tin Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000007772 electroless plating Methods 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 229910052745 lead Inorganic materials 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- BQJTUDIVKSVBDU-UHFFFAOYSA-L copper;sulfuric acid;sulfate Chemical compound [Cu+2].OS(O)(=O)=O.[O-]S([O-])(=O)=O BQJTUDIVKSVBDU-UHFFFAOYSA-L 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 239000002925 low-level radioactive waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000005365 phosphate glass Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
- 239000000941 radioactive substance Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000010944 silver (metal) Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000002915 spent fuel radioactive waste Substances 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Description
本発明は、放射性廃棄物の固化処理方法に関
し、更に詳しくは、放射性廃棄物を含有するガラ
ス固化体粒子を形成したのち、これら粒子の表面
に金属を被覆してから圧縮・焼結を行うことによ
り、化学的・機械的に安定であり、半永久的貯蔵
に適する放射性廃棄物貯蔵体を得る方法に関す
る。
原子発電の普及にともない使用済核燃料の再処
理工場から発生する高濃度の放射性廃液は、
年々、増大する傾向にある。これらの放射性廃液
を液状のままでタンク貯蔵することには安全上の
問題があるため、より安全に保管できる固形貯蔵
体への変換技術の確立が切望されている。
一般に放射性廃棄物の処分に際しては、放射性
物質の周囲への拡散が最小限となる形態に廃棄物
を固形化し、得られた固形貯蔵体が、化学的・機
械的に安定していて、長期の貯蔵によつても環境
汚染の原因にならないことが必要である。このよ
うな観点で従来より行われている固形化方法は、
ガラス固化技術(たとえば特公昭46−3240号、同
50−4840号各公報に記載のもの等)が主流を占
め、高濃度の法射性廃棄物をリン酸もしくはホウ
ケイ酸ガラス等ガラス材料とともに溶融し、一定
形状のガラスインゴツトに凝固させ、固化する方
法が用いられ、固化体はその後貯蔵容器に封入さ
れ、たとえば地下貯蔵により保管される。
上記方法によれば、廃棄物含有量、ガラスの組
成などを検討することにより、機械的強度も比較
的大きいガラス固化体を得ることができるが、次
のような問題点を有する。
(イ) 貯蔵容器が破損した場合、固化体は、外部雰
囲気、たとえば地下貯蔵の場合は地下水など、
に直接接することになるため、長期にわたる安
定な貯蔵のためには、水による放射性物質の浸
出率を可能な限り小さくすることが要請され
る。この点、ガラス固化体は、基本材料である
ガラスが組成による制約をうけるため、固化体
の機械的強度ないしは一体性と浸出率の低下と
をガラス材料により両立させることは必ずしも
容易でない。
(ロ) ガラスの熱伝導度は、金属に比較すると本質
的に小さいため含有する法射性物質の放射線崩
壊による発熱によつてガラス固化体内部の温度
は上昇し、中心部では500〜700℃に及ぶことも
あり得る。かかる温度上昇はガラス固化体の構
造を脆弱にし、機械的および化学的安定性をそ
こない、長期にわたる放射性廃棄の安全な貯蔵
を困難にする。
以上のようなガラス固化処理の欠点を除くた
め、たとえばガラス固化体の小粒を作り、その集
合体にたとえばSn,Pbなどの低融点金属の溶融
物を注入し固化することにより金属マトリクス中
にガラス固化体を埋め込んだ形態のより安定性の
向上した廃棄物貯蔵体を得る方法も開発されてい
る。
しかし、この方法も、熱伝導度、化学的安定性
の畿分向上した貯蔵体は与えるものの、一般に低
融点金属は機械的強度が低く、また熱伝導度およ
び化学的安定性もCu,Niなどより高融点の金属
のそれと比較すると著しく劣るため、得られる貯
蔵体の安定性も未だ満足なものとは云い難い。ま
た溶融金属を注入する工程によるため、金属マト
リクス中でのガラス固化体粒の分散の均一性に欠
け、ガラス固化体粒間の接触部分が残存し、熱の
放散に対し、障害となる。更に、ガラス固化体粒
同志の接触を避けるためには、ガラス固化体粒の
金属マトリクスに対する配合比率を下げる必要が
あり、その結果、一定量の放射性廃棄物を貯蔵す
るために必要な複合固化体の体積および重量が著
しく増大する欠点がある。
本発明の目的は、上述した従来のガラス固化に
よる放射性廃棄物の処理法の欠点を除き、放射性
廃棄物を高い充填度で均一に分散含有し、なお且
つ化学的安定性、機械的強度および熱伝導度に優
れ、長期に安全に貯蔵し得るような、複合固化貯
蔵体の製造法を提供することにある。
本発明者らの研究によれば、上述の目的の達成
のためには、ガラス固体粒子の表面を、好ましく
は、化学的安定性、機械的強度および熱伝導度に
優れた金属で被覆し、これら粒子を前記金属の加
熱・圧縮下での接合力を利用して一体化すること
が極めて有効であることが見出された。すなわ
ち、本発明の放射性廃棄物の固化処理方法は、放
射性廃棄物を含有する固化体粒子の外表面に金属
を被覆する工程と、得られた金属を被覆したガラ
ス固化体粒子の集体をガラスの軟化点以上で且金
属の融点以下の温度で圧縮し焼結する工程とから
なることを特徴とするものである。
以下、本発明を更に詳細に説明する。以下の記
載において「部」および「%」は特に断らない限
り、重量基準とする。
本発明の処理対象となる放射性廃棄物として
は、例えば使用済核燃料を処理した後、U,Pu
を回収した残りの放射性廃棄物の他、混床式脱塩
器の再生廃液の濃縮液、建屋から発生する床ドレ
インあるいは機器ドレインの濃縮廃液などの放射
性物質を含む各種の廃液、更には、原子濾水浄化
系、燃料プール系、復水系、ドレイン系の各系統
から生ずる使用済イオン交換樹脂、フイルタース
ラツジ、廃液の凝集沈澱処理によつて生ずる沈澱
スラツジなどの各種の固体廃棄物など、高レベル
および中低レベルの放射性廃棄物が含まれる。
これら放射性廃棄物の溶液あるいは粉末は、従
来法と同様にその乾燥酸化物としての重量30部に
対して例えば70部のホウケイ酸系ガラス、リン酸
系ガラスなどの溶融物中に分散ないしは共溶融さ
れ、次いで粉砕、滴下などガラス工業における常
法により小径化され、ガラス固化体粒子とされ
る。
ガラス固化体粒子の寸法に関しては、特に制限
はないが、あまりさい場合は、金属被覆工程での
被覆膜厚制御や被覆にメツキ法を採用した際の粒
子凝集の問題が生じ、また大きすぎる場合は、中
心部での放射性崩壊による温度上昇が大となるた
め、径2mm〜50mmの範囲が適当である。またガラ
ス固化体粒子の形状は、球状、およびそれに近い
長円球、円柱状、多角柱状、凸面体状などの各種
形状が用いられるが、金属被覆工程に続く、圧
縮、焼結工程での圧縮ならびに充填の均一性の観
点からは、球状で直径のそろつた粒子が望まし
い。
本発明にしたがい、このような放射性廃棄物を
含有するガラス固化体粒子の外表面を金属で被覆
する。被覆用金属としては、引き続く圧縮・焼結
工程において、ガラスの軟化点以上の温度で内部
にガラスを保持するだけの強度を有し、且つ空間
を埋めるように変形するだけの変形能を有し、更
に相互拡散により接合する必要があり、Cu,
Ni,Fe,Agおよびこれらの合金が好ましく用い
られる。
また被覆方法としては、ガラス固化体粒子が一
般に絶縁体であるため、無電解メツキ法、スパツ
タリング法、蒸着法、ペースト焼付法等により表
面に導電性被膜を形成した後、電解メツキ法を含
む各種の被覆方法により上記のような金属の被覆
を形成する。また金属被覆を行つた後、さらにそ
の表面に薄く、金属被膜相互での拡散を促進する
ために、たとえばSn,Pb,Znあるいはこれらの
合金等の低融点金属の被膜を形成することもでき
る。金属被膜の厚さは、ガラス固体化粒子の粒径
によつても異なるが、薄すぎると后の圧縮焼結工
程での被膜が破れと、それによるガラスのしみ出
しを生じ、また厚すぎると、複合固化体中のガラ
スの充填率が下がるため0.02〜10mmの範囲が好ま
しく用いられる。
次いで、このようにして得られた金属覆1を施
したガラス固化体粒子2を、第1図に示すよう
に、カーボン等の耐熱性且つ金属と非反応性の材
料からなる型3中に充填し、加熱下に、同様な材
料からなるフタ4を介して荷重5をかけることに
より、第2図に示すように、ガラス固化体粒子な
らびに金属被覆を変形(変形後の状態を、それぞ
れ2a,1aで表わす)し、また金属被覆相互間
での界面6を通して、被覆金属相互の加熱拡散、
すなわち焼結、を起させる。加熱温度は、所望の
充填効果が得られるように、ガラスの軟化点温度
以上、金属の融点以下の温度とし、被覆金属の相
互拡散を妨げないよう、被覆したガラス固化体粒
子を非酸化性雰囲気(不活性ないしは還元性雰囲
気)中におくのがよい。
以上の工程により得られた金属―ガラス複合固
化体は、そのまま、貯蔵に供してもよいが、必要
に応じてより安全な貯蔵のために、たとえば
SUS304等の耐蝕合金製容器中に装入し、密閉し
てから貯蔵してもよい。
また第1図、第2図で説明した圧縮・焼結工程
において、型3として耐蝕合金製容器を用い、圧
縮焼結後、そのままフタをして密閉貯蔵を行うこ
ともできる。
上記した本発明の方法によつて得られる放射性
廃棄物の固化体においては、放射性廃棄物を含む
ガラス固化体の粒子は、各粒子毎に独立して均質
な金属の被覆により包まれ、しかも金属被覆をし
た粒子は変形し、被覆金属相互の拡散により接合
し、空間を完全に充填しているために、化学的安
定性、機械的強度が優れているとともに放射性崩
壊によるガラス固化体からの熱の放散も充分に行
なわれる。またガラス固化体粒子間の接触は被覆
金属により完全に遮断されているため、ガラス固
化体の充填率を上げ、その全体に占める体積比を
50%以上まで上昇させることも可能である。
以下、実施例、比較例により、本発明を更に具
体的に説明する。
実施例 1
下表に示す組成の模擬放射性廃棄物30%を含有
する球状のホウケイ酸ガラス粒子(直径5mm)を
用意した。
The present invention relates to a method for solidifying radioactive waste, and more specifically, it involves forming vitrified particles containing radioactive waste, coating the surfaces of these particles with metal, and then compressing and sintering the particles. This invention relates to a method for obtaining a radioactive waste storage body that is chemically and mechanically stable and suitable for semi-permanent storage. With the spread of nuclear power generation, highly concentrated radioactive waste fluid generated from spent nuclear fuel reprocessing plants is
It tends to increase year by year. Since there are safety issues in storing these radioactive waste liquids in their liquid state in tanks, there is a strong desire to establish a technology to convert them into solid storage bodies that can be stored more safely. Generally, when disposing of radioactive waste, the waste is solidified in a form that minimizes the diffusion of radioactive materials into the surrounding area, and the resulting solid storage medium is chemically and mechanically stable and has a long-term lifespan. It is necessary that storage does not cause environmental pollution. From this point of view, the conventional solidification methods are:
Vitrification technology (for example, Special Publication No. 46-3240,
50-4840, etc.) are the mainstream, in which highly concentrated radioactive waste is melted together with glass materials such as phosphoric acid or borosilicate glass, and solidified into glass ingots of a certain shape. The solidified product is then sealed in a storage container and stored, for example, in underground storage. According to the above method, by considering the waste content, the composition of the glass, etc., it is possible to obtain a vitrified material with relatively high mechanical strength, but it has the following problems. (b) If the storage container is damaged, the solidified material will be released into the external atmosphere, such as groundwater in the case of underground storage.
Therefore, for long-term stable storage, it is necessary to minimize the rate of leaching of radioactive materials by water. In this respect, since the glass, which is the basic material of the vitrified body, is subject to restrictions due to the composition, it is not necessarily easy to achieve both the mechanical strength or integrity of the solidified body and a reduction in the leaching rate using a glass material. (b) Since the thermal conductivity of glass is inherently lower than that of metals, the temperature inside the vitrified body rises due to the heat generated by the radioactive decay of the radioactive substances it contains, reaching 500 to 700°C in the center. It may even extend to. Such temperature increases weaken the structure of the vitrified body, impair its mechanical and chemical stability, and make safe long-term storage of radioactive waste difficult. In order to eliminate the above-mentioned disadvantages of vitrification treatment, for example, small particles of vitrification are made, and a molten substance of a low melting point metal such as Sn or Pb is injected into the aggregate and solidified to form glass in the metal matrix. Methods have also been developed to obtain more stable waste storage bodies in the form of embedded solidified bodies. However, although this method provides a storage medium with significantly improved thermal conductivity and chemical stability, low-melting point metals generally have low mechanical strength, and thermal conductivity and chemical stability are low, such as Cu and Ni. The stability of the resulting storage medium is still far from satisfactory, as it is significantly inferior to that of metals with higher melting points. Furthermore, since the process involves injecting molten metal, the vitrified particles are not uniformly dispersed in the metal matrix, and contact areas between the vitrified particles remain, which becomes an obstacle to heat dissipation. Furthermore, in order to avoid contact between the vitrified particles, it is necessary to lower the mixing ratio of the vitrified particles to the metal matrix, and as a result, the composite solidified material required to store a certain amount of radioactive waste The disadvantage is that the volume and weight of the product increase significantly. The object of the present invention is to eliminate the drawbacks of the conventional radioactive waste treatment method by vitrification as described above, to contain radioactive waste uniformly dispersed with a high degree of filling, and to achieve chemical stability, mechanical strength, and thermal stability. The object of the present invention is to provide a method for producing a composite solidified storage body that has excellent conductivity and can be safely stored for a long period of time. According to the research of the present inventors, in order to achieve the above object, the surface of the glass solid particles is preferably coated with a metal having excellent chemical stability, mechanical strength and thermal conductivity, It has been found that it is extremely effective to integrate these particles by utilizing the bonding force of the metal under heating and compression. That is, the method for solidifying radioactive waste of the present invention includes the steps of coating the outer surface of solidified particles containing radioactive waste with metal, and converting the resulting aggregate of metal-coated vitrified particles into glass. It is characterized by comprising a step of compressing and sintering at a temperature above the softening point and below the melting point of the metal. The present invention will be explained in more detail below. In the following description, "parts" and "%" are based on weight unless otherwise specified. Radioactive waste to be treated by the present invention includes, for example, U, Pu,
In addition to the remaining radioactive waste collected, various waste liquids containing radioactive materials, such as concentrated liquid waste recycled from mixed-bed desalination equipment, concentrated waste liquid from floor drains or equipment drains generated from buildings, and even atomic Various types of solid waste such as used ion exchange resins and filter sludge generated from the filtrate purification system, fuel pool system, condensate system, and drain system, and precipitated sludge generated from coagulation and sedimentation treatment of waste liquid, etc. This includes low- and medium- and low-level radioactive waste. Similar to the conventional method, these radioactive waste solutions or powders are dispersed or co-melted in a melt of borosilicate glass, phosphate glass, etc. at a ratio of 70 parts to 30 parts by weight of the dry oxide. The particles are then reduced in diameter by conventional methods in the glass industry, such as crushing and dropping, to form vitrified particles. There are no particular restrictions on the size of the vitrified particles, but if they are too small, problems will arise when controlling the coating film thickness in the metal coating process and particle aggregation when the plating method is used for coating, and if they are too large. In this case, since the temperature rise due to radioactive decay in the center becomes large, a diameter in the range of 2 mm to 50 mm is appropriate. The shape of the vitrified particles can be spherical, ellipsoidal, cylindrical, polygonal, convex, etc.; Also, from the viewpoint of uniformity of filling, particles that are spherical and have a uniform diameter are desirable. According to the invention, the outer surface of the vitrified particles containing such radioactive waste is coated with metal. The covering metal has enough strength to hold the glass inside at a temperature above the glass's softening point during the subsequent compression and sintering process, and has enough deformability to deform to fill the space. , it is necessary to further bond by mutual diffusion, and Cu,
Ni, Fe, Ag and alloys thereof are preferably used. In addition, as coating methods, since vitrified particles are generally insulators, a conductive film is formed on the surface by electroless plating, sputtering, vapor deposition, paste baking, etc., and then various methods including electrolytic plating are used. A metal coating as described above is formed by the coating method. Further, after the metal coating is applied, a thin coating of a low melting point metal such as Sn, Pb, Zn, or an alloy thereof may be formed on the surface to promote diffusion between the metal coatings. The thickness of the metal coating varies depending on the particle size of the glass solidification particles, but if it is too thin, the coating will break during the subsequent compression sintering process and the glass will seep out. Since the filling rate of glass in the composite solidified body decreases, a range of 0.02 to 10 mm is preferably used. Next, the vitrified particles 2 coated with the metal covering 1 thus obtained are filled into a mold 3 made of a heat-resistant material such as carbon and non-reactive with metals, as shown in FIG. Then, by applying a load 5 through a lid 4 made of the same material while heating, the vitrified particles and the metal coating are deformed as shown in FIG. 1a), and through the interface 6 between the metal coatings, heating diffusion between the coating metals,
In other words, sintering occurs. The heating temperature is set to be above the softening point of the glass and below the melting point of the metal so as to obtain the desired filling effect, and the coated vitrified particles are placed in a non-oxidizing atmosphere so as not to interfere with the interdiffusion of the coated metal. (inert or reducing atmosphere). The metal-glass composite solidified body obtained through the above steps may be stored as is, but if necessary, for safer storage, e.g.
It may be placed in a container made of a corrosion-resistant alloy such as SUS304, sealed, and then stored. Furthermore, in the compression and sintering process described in FIGS. 1 and 2, a container made of a corrosion-resistant alloy may be used as the mold 3, and after compression and sintering, the container may be closed and stored with a lid. In the radioactive waste solidified material obtained by the method of the present invention described above, each particle of the vitrified material containing radioactive waste is individually wrapped in a homogeneous metal coating, and The coated particles are deformed and bonded by mutual diffusion of the coated metals, completely filling the space, so they have excellent chemical stability and mechanical strength, and they also resist heat from the vitrified material due to radioactive decay. is also sufficiently dissipated. In addition, since the contact between the vitrified particles is completely blocked by the coating metal, the filling rate of the vitrified material can be increased and the volume ratio of the entire vitrified material can be increased.
It is also possible to increase it to more than 50%. Hereinafter, the present invention will be explained in more detail with reference to Examples and Comparative Examples. Example 1 Spherical borosilicate glass particles (diameter 5 mm) containing 30% of simulated radioactive waste having the composition shown in the table below were prepared.
【表】【table】
【表】
上記粒子にCu無電解メツキを行つた後、硫酸
銅―硫酸浴中、室温にてCu電解メツキを行な
い、厚さ0.63mmのCu被覆を形成した。次いで得
られたCu被覆粒子を、第1図に示すように内径
50mm、高さ150mmのカーボン容器に充填し、上部
に容器の内径よりわずかに外径の小さいカーボン
製の円盤状のフタをかぶせ10Kg/cm2の荷重を加
え、水素気流中で750℃、3時間の熱処理を行つ
た。得られた固化体は、充填率96%(容積基準)
のほぼ密な固化体であり、被覆を通じてのガラス
のしみ出しは全くなかつた。
また、別途、被覆粒子20個を相互に接触せずに
カーボン容器中で水素気流中、750℃、3時間の
熱処理を施した後、100℃の純水100ml中に1時間
浸漬し、溶液中のMoイオンを測定し、浸出率を
算出したところ、検出限界の1×10-6g/cm2day
未満であつた。
実施例 2
実施例1と同様に厚さ0.63mmのCu被覆を形成
したガラス固化体粒子上にさらに厚さ約5μの錫
メツキを施してから、内径50mm、高さ150mmの内
面にCuメツキを施したSUS304製容器中に充填
し、上部より容器の内径よりわずかに外径の小さ
い下面にCuメツキを施したSUS304製円盤でフタ
をした。次いで、このフタを通して50Kg/cm2の荷
重をかけ、700℃で3時間、水素気流中にて焼結
を行い、焼結後、SUS304製円盤をその位置で容
器に溶接し、密封した。
得られた固化体の充填率は約95%(容積基準)
であつた。
比較例
実施例1において、金属被覆を施す前のガラス
固化体粒子10個を100℃の純水100ml中に1時間浸
漬し、溶液中のMoイオンを測定し、浸出率を求
めた所、2.5×10-5g/cm2、dayの値が得られた。
以上の実施例、比較例から明らかなように、本
発明による貯蔵体は、最外側の容器が破損して内
部の固体が外界に露出した場合でも、さらにガラ
ス固化体粒子が被覆金属マトリクス中に均一に分
散し、被覆されているため、放射性元素の浸出が
防止され、また熱放散性および機械的性質に優れ
ており、ガラス固化体の含有率を高くとることが
できるとともに安全性、長期貯蔵性に優れてい
る。[Table] After performing Cu electroless plating on the above particles, Cu electroplating was performed at room temperature in a copper sulfate-sulfuric acid bath to form a Cu coating with a thickness of 0.63 mm. Next, the obtained Cu-coated particles were
Fill a carbon container with a diameter of 50 mm and a height of 150 mm, cover the top with a carbon disc-shaped lid with an outer diameter slightly smaller than the inner diameter of the container, apply a load of 10 kg/ cm2 , and heat at 750°C in a hydrogen stream for 30 minutes. Heat treatment was performed for several hours. The obtained solidified body has a filling rate of 96% (volume basis)
It was a nearly dense solidified body with no glass seeping through the coating. Separately, 20 coated particles were heat-treated for 3 hours at 750°C in a hydrogen stream in a carbon container without contacting each other, and then immersed in 100ml of 100°C pure water for 1 hour. When we measured Mo ions and calculated the leaching rate, we found that the detection limit was 1×10 -6 g/cm 2 day
It was less than Example 2 As in Example 1, tin plating with a thickness of approximately 5 μm was applied to the vitrified particles on which a Cu coating with a thickness of 0.63 mm was formed, and then Cu plating was applied to the inner surface with an inner diameter of 50 mm and a height of 150 mm. The mixture was filled into a SUS304 container, and the top was covered with a SUS304 disk whose bottom surface was Cu-plated and had an outer diameter slightly smaller than the inner diameter of the container. Next, a load of 50 kg/cm 2 was applied through this lid, and sintering was performed at 700° C. for 3 hours in a hydrogen stream. After sintering, a SUS304 disk was welded to the container at that position and sealed. The filling rate of the obtained solidified material is approximately 95% (based on volume)
It was hot. Comparative Example In Example 1, 10 vitrified particles before metal coating were immersed in 100 ml of pure water at 100°C for 1 hour, Mo ions in the solution were measured, and the leaching rate was determined to be 2.5. A value of ×10 −5 g/cm 2 , day was obtained. As is clear from the above Examples and Comparative Examples, in the storage body according to the present invention, even if the outermost container is damaged and the solid inside is exposed to the outside world, the vitrified particles are still contained in the coated metal matrix. Because it is uniformly dispersed and coated, leaching of radioactive elements is prevented, and it also has excellent heat dissipation and mechanical properties, allowing a high content of vitrified material, as well as safety and long-term storage. Excellent in sex.
第1図は、本発明方法の一態様によるガラス固
化体粒子を充填した型の圧縮・焼結前における縦
断面図、第2図は同じく圧縮・焼結後の縦断面図
である。
1…金属被覆、2…ガラス固化体粒子、3…
型、4…上ブタ、5…荷重、6…金属被覆間の界
面、添字aは、圧縮・焼結後の状態であることを
示す。
FIG. 1 is a longitudinal sectional view of a mold filled with vitrified particles according to one embodiment of the method of the present invention before compression and sintering, and FIG. 2 is a longitudinal sectional view of the same after compression and sintering. 1... Metal coating, 2... Vitrified particles, 3...
Mold, 4... Upper lid, 5... Load, 6... Interface between metal coatings, and the subscript a indicates the state after compression and sintering.
Claims (1)
表面に金属を被覆する工程と、得られた金属を被
覆したガラス固化体粒子の集体をガラスの軟化点
以上且つ金属の融点以下の温度で圧縮し焼結する
工程とからなることを特徴とする放射性廃棄物の
固化処理方法。1. The step of coating the outer surface of vitrified particles containing radioactive waste with metal, and compressing the resulting aggregate of metal-coated vitrified particles at a temperature above the softening point of glass and below the melting point of metal. A method for solidifying radioactive waste, comprising a step of sintering.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11556581A JPS5817398A (en) | 1981-07-23 | 1981-07-23 | Method of solidifying radioactive waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11556581A JPS5817398A (en) | 1981-07-23 | 1981-07-23 | Method of solidifying radioactive waste |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5817398A JPS5817398A (en) | 1983-02-01 |
| JPS6112237B2 true JPS6112237B2 (en) | 1986-04-07 |
Family
ID=14665691
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11556581A Granted JPS5817398A (en) | 1981-07-23 | 1981-07-23 | Method of solidifying radioactive waste |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5817398A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6036999A (en) * | 1983-08-09 | 1985-02-26 | 株式会社荏原製作所 | Volume-reduction solidified body of radioactive sodium borate waste liquor, volume-reduction solidifying method anddevice thereof |
-
1981
- 1981-07-23 JP JP11556581A patent/JPS5817398A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5817398A (en) | 1983-02-01 |
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