JPH0450558B2 - - Google Patents
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- Publication number
- JPH0450558B2 JPH0450558B2 JP58146184A JP14618483A JPH0450558B2 JP H0450558 B2 JPH0450558 B2 JP H0450558B2 JP 58146184 A JP58146184 A JP 58146184A JP 14618483 A JP14618483 A JP 14618483A JP H0450558 B2 JPH0450558 B2 JP H0450558B2
- Authority
- JP
- Japan
- Prior art keywords
- flux
- ash
- container
- incineration ash
- radioactive waste
- 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 - Lifetime
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- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
本発明は放射性廃棄物の固化処理法に関するも
のであり、さらに詳しくは放射性廃棄物の焼却灰
を溶融固化する処理法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for solidifying radioactive waste, and more particularly to a method for melting and solidifying incinerated ash of radioactive waste.
従来原子力発電所等の放射性物質取扱施設から
発生する放射能によつて汚染された廃棄物のうち
可燃性のものは、一般的には焼却処理されこの焼
却灰はドラム罐等に充填されて施設内の適当な場
所に貯蔵されているのが普通である。しかしなが
らこれら焼却灰は粉粒状であるため、焼却灰を充
填したドラム罐を輸送または貯蔵するにあたつて
は焼却灰の安定化、減容処理を施すことが望まし
く、その処理法がいろいろ研究され例えば焼却灰
をセメントで固化する方法が提案されている。し
かしながらこの焼却灰をセメントで固化する方法
は、
(1) 灰とセメントを混合して安定した密度、強度
をもつ固化体を得るには、灰とセメントの重量
割合を灰1に対してセメント4以上とする必要
があり、このため固化体の容積が灰の容積より
も増大し、増容となつてしまう。 Conventionally, combustible waste contaminated with radioactivity generated from facilities handling radioactive materials such as nuclear power plants is generally incinerated, and the incinerated ash is filled into drum cans, etc., and transported to the facility. It is usually stored in an appropriate location inside the building. However, since these incinerated ash are in the form of powder, it is desirable to stabilize and reduce the volume of the incinerated ash before transporting or storing the drum can filled with incinerated ash, and various methods for this treatment have been studied. For example, a method of solidifying incineration ash with cement has been proposed. However, the method of solidifying this incineration ash with cement is as follows: (1) In order to mix ash and cement to obtain a solidified material with stable density and strength, the weight ratio of ash and cement must be 1 part ash to 4 parts cement. Therefore, the volume of the solidified material becomes larger than the volume of the ash, resulting in an increase in volume.
(2) 灰とセメントを混練するときに焼却灰中の金
属混入物とセメントのアルカリ水溶液が反応し
て水素ガスを発生するため、固化体中に空隙が
できて密度、強度等が低下することがあり、安
定性を欠く。(2) When mixing ash and cement, metal contaminants in the incinerated ash react with the alkaline aqueous solution of cement to generate hydrogen gas, which creates voids in the solidified material and reduces density, strength, etc. There is a lack of stability.
等の欠点があつた。There were other drawbacks.
本発明は上記従来の欠点を解消するもので、放
射性廃棄物焼却灰を安全に貯蔵、輸送できる無機
固化体に転換するとともに、得られる固化体の容
積をもとの焼却灰の容積より減少させ、貯蔵のた
めのスペースを少なくすることができる放射性廃
棄物焼却灰の溶融固化方法を提供しようとするも
のであつて、その要旨とするところは、誘導加熱
コイルをそなえた炉内に設けた金属製の筒状加熱
体内に、金属製の容器を設置し、放射性廃棄物焼
却灰と共融物を形成する融剤を上記容器内に供給
し、上記誘導加熱コイルにより上記容器内で液状
に融解させた上記融剤上に放射性廃棄物焼却灰を
供給するとともに、上記融剤の液面上に酸素含有
ガスを供給して上記焼却灰中の未燃分を燃焼さ
せ、上記焼却灰を上記融剤中に溶解させたのち冷
却して、上記焼却灰を上記融剤との共融物として
上記容器中に固定化させることを特徴とする放射
性廃棄物焼却灰の溶融固化方法にある。 The present invention solves the above conventional drawbacks by converting radioactive waste incineration ash into an inorganic solidified body that can be safely stored and transported, and at the same time reducing the volume of the obtained solidified body from the original volume of the incinerated ash. , which attempts to provide a method for melting and solidifying radioactive waste incineration ash that requires less storage space. A metal container is installed in a cylindrical heating body made of aluminum, and a flux that forms a eutectic with radioactive waste incineration ash is supplied into the container, and is melted into a liquid state in the container by the induction heating coil. At the same time, radioactive waste incineration ash is supplied onto the above-mentioned flux, and oxygen-containing gas is supplied above the liquid surface of the above-mentioned flux to burn unburned content in the above-mentioned incineration ash. A method for melting and solidifying radioactive waste incineration ash, characterized in that the incineration ash is dissolved in a solvent and then cooled, and the incineration ash is fixed in the container as a eutectic with the flux.
以下図面によつて本発明をさらに詳しく説明す
る。 The present invention will be explained in more detail below with reference to the drawings.
ドラム罐等の中に一時的に貯蔵されている放射
性廃棄物焼却灰1を密閉型のホツパー2内に貯留
するとともに、その焼却灰1の成分であるSiO2、
CaO、Fe2O3、MgO、AI2O3等と共融物を形成す
る例えばホウ酸、ホウ砂、炭酸ナトリウム等の融
剤3を別のホツパー4内に貯留する。一方誘導加
熱炉5の密閉容器状の炉体6内に設けた金属製の
筒状加熱体7内に、金属製の容器8を設置し、炉
体6の外周部の設けた誘導加熱コイル9により筒
状加熱体7を400〜1100℃程度に加熱する。ホツ
パ4内の融剤3を融剤供給機11によつて供給口
12を経て容器8内へ供給すれば、筒状加熱体7
からの熱輻射と熱伝達および誘導加熱コイル9に
よる容器8自体の加熱とにより、融剤は容器8内
で融解して液状となる。例えば融剤3としてホウ
酸を使用した場合には450℃程度で融解し、ホウ
砂またはホウ酸と炭酸ナトリウムの混合物を使用
した場合は800℃程度で融解して、それぞれ液状
となる。なおこの場合ホウ砂、ホウ酸、炭酸ナト
リウム等の専用の融剤を用いるかわりに、廃ガラ
ス、カレツト、使用ずみのHEPAフイルター濾
材などのガラス廃棄物を用い、これらのガラス中
のホウ素、ナトリウムなどを融剤として使用する
こともできる。 Radioactive waste incineration ash 1 temporarily stored in a drum can etc. is stored in a closed hopper 2, and the components of the incineration ash 1, SiO 2 ,
A fluxing agent 3 such as boric acid, borax, sodium carbonate, etc., which forms a eutectic with CaO, Fe 2 O 3 , MgO, AI 2 O 3 , etc., is stored in another hopper 4 . On the other hand, a metal container 8 is installed in a metal cylindrical heating body 7 provided in a closed container-shaped furnace body 6 of the induction heating furnace 5, and an induction heating coil 9 is provided on the outer periphery of the furnace body 6. The cylindrical heating body 7 is heated to about 400 to 1100°C. If the flux 3 in the hopper 4 is supplied into the container 8 through the supply port 12 by the flux supply machine 11, the cylindrical heating body 7
The flux melts in the container 8 and becomes liquid due to heat radiation and heat transfer from the container 8 and heating of the container 8 itself by the induction heating coil 9. For example, when boric acid is used as the fluxing agent 3, it melts at about 450°C, and when borax or a mixture of boric acid and sodium carbonate is used, it melts at about 800°C and becomes liquid. In this case, instead of using special fluxing agents such as borax, boric acid, and sodium carbonate, glass waste such as waste glass, cullet, and used HEPA filter media is used, and the boron, sodium, etc. in these glasses are used. can also be used as a flux.
次に、容器8内で融解した融剤上に焼却灰1を
焼却灰供給機13によつて少量ずつ供給するとと
もに、焼却灰1中に含まれる炭素等の未燃分を燃
焼するのに必要な燃焼用空気(好ましくは必要最
低量の酸素を含有するもの)14を導入管15に
より融剤液面上に供給し、この燃焼用空気により
燃却灰1中の未燃分を燃焼させ、灰分を構成する
SiO2その他の前記各成分を融剤との共融物とし
て溶解させる。なお焼却灰が融剤の中へ溶解する
のに要する時間を短縮することを目的として、焼
却灰1と同時に適量の融剤3を容器8内へ供給す
ることもできる。また容器8内へ供給される焼却
灰1中には、SiO2その他の前記各成分のほかに
金属類、レンガ、アスベスト、ガラス、コンクリ
ート、セラミツクフイルタエレメント等の不燃性
夾雑物が混入していることもあるが、これらは共
融物は形成しないが全て共融物中にとりこまれ
る。容器8内に共融物がほぼ一杯に充填されるま
で上記操作を続け、その後自然放冷等により炉体
6および容器8を冷却し、共融物を固化させ容器
8内に固定化させる。固化した共融物は容器8を
載置した底蓋17とともに降下させて容器8ごと
取出し、新たな容器8を底蓋17上に載置して以
下同様な工程を繰返すのである。 Next, the incinerated ash 1 is supplied little by little onto the melted flux in the container 8 by the incinerated ash feeder 13, and the incinerated ash 1 is supplied in small quantities to burn off the unburned matter such as carbon contained in the incinerated ash 1. Combustion air (preferably containing the minimum necessary amount of oxygen) 14 is supplied onto the flux surface through the introduction pipe 15, and the unburned content in the combustion ash 1 is combusted by this combustion air, make up ash
SiO 2 and other components are dissolved as a eutectic with a flux. In addition, for the purpose of shortening the time required for the incinerated ash to dissolve into the flux, an appropriate amount of the flux 3 can be supplied into the container 8 at the same time as the incinerated ash 1. In addition to SiO 2 and other components mentioned above, the incineration ash 1 supplied into the container 8 contains non-combustible impurities such as metals, bricks, asbestos, glass, concrete, and ceramic filter elements. Although these may not form a eutectic, they are all incorporated into the eutectic. The above operation is continued until the container 8 is almost completely filled with the eutectic, and then the furnace body 6 and the container 8 are cooled by natural cooling or the like, and the eutectic is solidified and fixed in the container 8. The solidified eutectic is lowered together with the bottom lid 17 on which the container 8 is placed, and the entire container 8 is taken out.A new container 8 is placed on the bottom lid 17, and the same process is repeated.
上記操作時には、放射性汚染を防止するため
に、焼却灰のホツパー2、焼却灰供給機13、誘
導加熱炉5内等は全てブロワ20によりダクト2
1を介して吸引排気され、フイルター22により
洗浄化処理される。 During the above operation, in order to prevent radioactive contamination, the inside of the incinerated ash hopper 2, incinerated ash feeder 13, induction heating furnace 5, etc. are all connected to the duct 2 by the blower 20.
The air is suctioned and exhausted through the filter 1, and is cleaned by the filter 22.
なお上記工程において焼却灰1を融解した融剤
3上に供給するときは、一度に多量の焼却灰を供
給すると焼却灰中の未燃物が完全燃焼せず液面に
浮遊して他の共融物の形成の妨害になるので、焼
却灰は未燃分が完全燃焼する程度に少量ずつ加え
ることがのぞましい。さらに焼却灰中の未燃分を
燃焼するに必要な酸素を炉体6内に大量に供給す
ると、筒状加熱体7あるいは金属製の容器8等が
高温酸化を受け劣化が著しくなるので、供給酸素
量は未燃分が燃焼するに必要な最低量の酸素供給
量とするとともに、炉体6内には不活性ガス18
等を供給することが好ましいものである。また、
この場合の未燃分の燃焼状態あるいは灰分の溶融
状態等はモニターテレビ、温度計等の検知器19
で検知することが必要である。 In addition, when feeding the incinerated ash 1 onto the melted flux 3 in the above process, if a large amount of incinerated ash is fed at once, the unburned substances in the incinerated ash will not be completely combusted and will float on the liquid surface and cause other co-occurrence. Since it interferes with the formation of melt, it is preferable to add incineration ash little by little to the extent that unburned matter is completely combusted. Furthermore, if a large amount of oxygen necessary to burn the unburned content in the incineration ash is supplied into the furnace body 6, the cylindrical heating element 7 or the metal container 8 will be subject to high-temperature oxidation, resulting in significant deterioration. The amount of oxygen supplied is the minimum amount necessary for the unburned matter to burn, and an inert gas 18 is provided in the furnace body 6.
It is preferable to supply the following. Also,
In this case, the state of combustion of unburned matter or the state of melting of ash can be detected using a detector 19 such as a monitor TV or thermometer.
It is necessary to detect the
次に本発明の実施例を挙げる。 Next, examples of the present invention will be given.
実施例
放射性廃棄物とほぼ同一組成の非放射性模擬焼
却灰(見かけ上の密度:0.4〜0.5g/cm3)を予め
調整し、出力100KWの高周波誘導加熱炉内で
1100℃に加熱された誘導加熱筒体内に設置した
350mmφ×500mmHのステンレス製容器内で融剤で
あるホウ砂を融解し、その融解液面上へ上記模擬
焼却灰を6〜12Kg/H程度の供給速度で供給し、
それと同時に焼却灰中の未燃分を燃焼させるため
に5〜30Nm3/Hの空気を供給して未燃分を燃焼
させ、灰分を全て融剤中に溶解した。そして、焼
却灰を融剤重量とほぼ同量まで供給した後冷却固
化し、融剤との共融物として容器内に固化させ
た。得られた固化体の密度は約2.4〜2.6g/cm3、
圧縮強度は約1000〜2000Kg/cm2であつた。また、
固化体からのCSの浸出率は約10-5〜10-7g/cm2・
dであつた。Example Non-radioactive simulated incineration ash (apparent density: 0.4 to 0.5 g/cm 3 ) having almost the same composition as radioactive waste was prepared in advance and heated in a high-frequency induction heating furnace with an output of 100 KW.
Installed inside an induction heating cylinder heated to 1100℃
Melt borax as a flux in a stainless steel container of 350 mmφ x 500 mmH, and feed the simulated incineration ash onto the melt surface at a feeding rate of about 6 to 12 kg/H,
At the same time, in order to burn the unburned content in the incineration ash, air of 5 to 30 Nm 3 /H was supplied to burn the unburned content, and all the ash was dissolved in the flux. After incineration ash was supplied in an amount almost equal to the weight of the flux, it was cooled and solidified, and solidified in the container as a eutectic product with the flux. The density of the obtained solidified material is approximately 2.4 to 2.6 g/cm 3 ,
The compressive strength was about 1000-2000 Kg/ cm2 . Also,
The leaching rate of C S from the solidified material is approximately 10 -5 to 10 -7 g/cm 2 .
It was d.
以上の説明と実施例に示すように、本発明の方
法によると次のような効果が得られる。 As shown in the above description and examples, the method of the present invention provides the following effects.
(1) 粉粒状の放射性廃棄物焼却灰を、安定な無機
固化体として容器内へ封じ込めることができ
る。(1) Powdered radioactive waste incineration ash can be contained in a container as a stable inorganic solid.
(2) 未燃分を多量に含む焼却灰であつても融剤液
面上に酸素含有ガスを供給して未燃分を燃焼さ
せるため、安定した固化体を得ることができ
る。(2) Even if the incineration ash contains a large amount of unburned matter, a stable solidified material can be obtained because the oxygen-containing gas is supplied above the flux surface to combust the unburned matter.
(3) 金属類、レンガ等の不燃夾雑物を含む焼却灰
であつても、これらの夾雑物を融剤と焼却灰の
共融物中へとりこんで固化することができる。(3) Even if the incineration ash contains non-combustible impurities such as metals and bricks, these impurities can be incorporated into the eutectic mixture of the flux and the incineration ash and solidified.
(4) 得られる固化体の容積は焼却灰の容積の1/3
〜1/5程度であり、大巾な減容化ができる。(4) The volume of the solidified material obtained is 1/3 of the volume of incinerated ash.
It is approximately 1/5th of the original size, allowing for a large volume reduction.
第1図は本発明方法に使用する装置の具体例を
示す縦断面図である。
1……放射性廃棄物焼却灰、3……融剤、5…
…誘導加熱炉、6……炉体、7……筒状加熱体、
8……容器、9……誘導加熱コイル、14……燃
焼用空気。
FIG. 1 is a longitudinal sectional view showing a specific example of the apparatus used in the method of the present invention. 1...Radioactive waste incineration ash, 3...Fluxing agent, 5...
... induction heating furnace, 6 ... furnace body, 7 ... cylindrical heating body,
8... Container, 9... Induction heating coil, 14... Combustion air.
Claims (1)
製の筒状加熱体内に、金属製の容器を設置し、放
射性廃棄物焼却灰と共融物を形成する融剤を上記
容器内に供給し、上記誘導加熱コイルにより上記
容器内で液状に融解させた上記融剤上に放射性廃
棄物焼却灰を供給するとともに、上記融剤の液面
上に酸素含有ガスを供給して上記焼却灰中の未燃
分を燃焼させ、上記焼却灰を上記融剤中に溶解さ
せたのち冷却して、上記焼却灰を上記融剤との共
融物として上記容器内に固定化させることを特徴
とする放射性廃棄物焼却灰の溶融固化方法。 2 融剤がホウ酸、ホウ砂、炭酸ナトリウムのう
ちの少なくとも1種以上から成る特許請求の範囲
第1項記載の放射性廃棄物焼却灰の溶融固化方
法。[Claims] 1. A metal container is installed in a metal cylindrical heating body provided in a furnace equipped with an induction heating coil, and a flux that forms a eutectic with radioactive waste incineration ash is placed in the metal container. Radioactive waste incineration ash is supplied onto the flux which is supplied into the vessel and melted into liquid form within the vessel by the induction heating coil, and an oxygen-containing gas is supplied onto the liquid surface of the flux. to burn the unburned content in the incinerated ash, dissolve the incinerated ash in the flux, cool it, and fix the incinerated ash in the container as a eutectic with the flux. A method for melting and solidifying radioactive waste incineration ash, characterized by: 2. The method for melting and solidifying radioactive waste incineration ash according to claim 1, wherein the fluxing agent is at least one of boric acid, borax, and sodium carbonate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14618483A JPS6038700A (en) | 1983-08-10 | 1983-08-10 | Method of melting and solidifying radioactive waste incinerated ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14618483A JPS6038700A (en) | 1983-08-10 | 1983-08-10 | Method of melting and solidifying radioactive waste incinerated ash |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6038700A JPS6038700A (en) | 1985-02-28 |
| JPH0450558B2 true JPH0450558B2 (en) | 1992-08-14 |
Family
ID=15402033
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14618483A Granted JPS6038700A (en) | 1983-08-10 | 1983-08-10 | Method of melting and solidifying radioactive waste incinerated ash |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6038700A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60186800A (en) * | 1984-03-06 | 1985-09-24 | 日本碍子株式会社 | Method and device for incinerating and solidifying radioactive waste |
| JPH0664192B2 (en) * | 1985-03-14 | 1994-08-22 | 日本碍子株式会社 | Equipment for melting and solidifying radioactive waste |
| USH1013H (en) * | 1989-08-11 | 1992-01-07 | W. R. Grace & Co.-Conn. | Process for the immobilization and volume reduction of low level radioactive wastes from thorium and uranium processing |
| JP5661066B2 (en) * | 2012-05-28 | 2015-01-28 | 株式会社 フュー・テクノロジー | Method for treating incinerated ash containing radioactive material and treated solids |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5752560B2 (en) * | 1973-02-21 | 1982-11-08 | ||
| JPS6046399B2 (en) * | 1980-05-29 | 1985-10-15 | 動力炉・核燃料開発事業団 | Incineration treatment method for radioactive waste ion exchange resin, etc. |
-
1983
- 1983-08-10 JP JP14618483A patent/JPS6038700A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6038700A (en) | 1985-02-28 |
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