JPS62200299A - Radioactive waste transporter - Google Patents
Radioactive waste transporterInfo
- Publication number
- JPS62200299A JPS62200299A JP4272386A JP4272386A JPS62200299A JP S62200299 A JPS62200299 A JP S62200299A JP 4272386 A JP4272386 A JP 4272386A JP 4272386 A JP4272386 A JP 4272386A JP S62200299 A JPS62200299 A JP S62200299A
- Authority
- JP
- Japan
- Prior art keywords
- incinerated ash
- radioactive waste
- gas
- incinerator
- ash
- 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.)
- Granted
Links
- 239000002901 radioactive waste Substances 0.000 title claims description 17
- 238000000926 separation method Methods 0.000 claims description 12
- 239000002956 ash Substances 0.000 description 37
- 101100002917 Caenorhabditis elegans ash-2 gene Proteins 0.000 description 12
- 239000000126 substance Substances 0.000 description 4
- 238000011109 contamination Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002910 solid waste Substances 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 230000002285 radioactive effect Effects 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 239000012790 adhesive layer Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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、放射性廃棄物を移送する放射性廃棄物移送装
置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a radioactive waste transfer device for transferring radioactive waste.
一般に、原子力発電所等から発生する放射性廃棄物は、
気体、液体、固体の3種類に大別され、放射能の強さは
高しヘル、中レベル、低レベルに分類される。In general, radioactive waste generated from nuclear power plants, etc.
It is roughly divided into three types: gas, liquid, and solid, and the strength of radioactivity is classified as high, medium, and low.
従来、低レベル固体廃棄物のうち、可燃物は、焼却され
た後、その灰をドラム缶に入れて保管されている。Conventionally, among low-level solid wastes, combustible materials are incinerated and the ashes thereof are stored in drums.
しかしながら、上記固体廃棄物の増加に連れて、焼却処
理後の灰が多量に発生し、保管量も年々多くなっている
ため、上述のような処理では、自ずと限界がある。However, as the amount of solid waste increases, a large amount of ash is generated after incineration, and the amount of ash stored increases year by year, so the above-mentioned treatment naturally has its limits.
そこで、上記固体廃棄物(焼却灰)を、マイクロ波を利
用して処理することが、例えば、特開昭55−1433
80号公報で開示されている。Therefore, it has been proposed to treat the solid waste (incineration ash) using microwaves, for example, in Japanese Patent Application Laid-Open No. 55-1433.
It is disclosed in Publication No. 80.
これらのマイクロ波溶融装置によって処理される放射性
廃棄物は、原子力発電所等から排出された放射性廃棄物
に一旦焼却処理を施したいわゆる焼却灰である。The radioactive waste processed by these microwave melting devices is so-called incinerated ash, which is obtained by incinerating radioactive waste discharged from nuclear power plants and the like.
この焼却灰は、ドラム缶に収納されて、処理場に運ばれ
てくる。処理場では、焼却灰をドラム缶から空気輸送し
、サイクロン、フィルタ(布9紙製)等を用いて空気と
焼却灰とを分離し、焼却灰をホッパに蓄え、必要に応じ
てフィーダに供給している。This incinerated ash is stored in drums and transported to a processing plant. At the treatment plant, the incinerated ash is air-transported from a drum can, the air and incinerated ash are separated using a cyclone, a filter (made of cloth and paper), etc., the incinerated ash is stored in a hopper, and is fed to a feeder as needed. ing.
しかしながら、上述したような方法では、焼却炉で焼却
された焼却灰をドラム缶を介して移送しているため、ド
ラム缶への焼却灰の詰め込み時、あるいは取り出し時に
、焼却灰が外部へ飛散し、放射能汚染を引き起こす虞が
ある。However, in the method described above, the incinerated ash in the incinerator is transferred through the drum, so when the incinerated ash is packed into the drum or taken out, the incinerated ash scatters outside and causes radiation. There is a risk of contamination.
本発明は、上記のような問題を解決したもので、焼却炉
内の焼却灰を飛散することなく次の工程に移送すること
のできる放射性廃棄物移送装置を提供することを目的と
する。The present invention solves the above-mentioned problems, and aims to provide a radioactive waste transfer device that can transfer incinerated ash in an incinerator to the next process without scattering it.
本発明にかかわる放射性廃棄物移送装置は、焼却炉の下
部に形成され、この焼却炉で焼却さた焼却灰を一時貯蔵
する貯蔵部に一端を開口し、前記焼却灰を気体により移
送する焼却灰移送管と、この焼却灰移送管の他端を接続
され、前記焼却灰移送管からの前記焼却灰を前記気体と
分離する気体分離装置とを備えたものである。The radioactive waste transfer device according to the present invention is formed at the lower part of an incinerator, has one end opened to a storage section for temporarily storing the incinerated ash incinerated in the incinerator, and has an incinerated ash transfer device for transferring the incinerated ash by gas. The apparatus includes a transfer pipe and a gas separation device connected to the other end of the incinerated ash transfer pipe to separate the incinerated ash from the incinerated ash transfer pipe from the gas.
本発明においては、焼却炉の貯蔵部内の焼却灰は、移送
流体である気体とともに焼却灰移送管を通り、気体分離
装置内に供給され、この気体分離gHにより、焼却灰と
気体とが分離される。In the present invention, the incinerated ash in the storage section of the incinerator passes through the incinerated ash transfer pipe together with the gas that is the transfer fluid, and is supplied into the gas separation device, and the incinerated ash and the gas are separated by this gas separation gH. Ru.
以下、本発明の詳細を図面に示す一実施例について説明
する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, details of the present invention will be described with reference to an embodiment shown in the drawings.
第り図は、本発明の放射性廃棄物移送装置の一実施例を
示すもので、図において符号1は、放射性廃棄物を焼却
する焼却炉を示している。この焼却炉lの下部には、焼
却炉1で焼却さた焼却灰2を一時貯蔵する貯蔵部3が形
成されている。貯蔵部3の上下には、モータ等により開
閉されるダンパー4,5が形成されている。貯蔵部3に
は、焼却灰2を例えば空気のような気体により移送する
焼却灰移送管6の一端が開口しており、その先端部には
、フィルタ7が配置されている。図において、符号8は
、焼却灰移送管6からの焼却灰2を気体と分離する気体
分離装置を示すもので、この気体分離装置8の容器本体
13には、焼却灰移送管6の他端が接続されている。ご
の焼却灰移送管6には、バルブ16が配置されている。Figure 2 shows an embodiment of the radioactive waste transfer apparatus of the present invention, and in the figure, reference numeral 1 indicates an incinerator for incinerating radioactive waste. A storage section 3 for temporarily storing incinerated ash 2 incinerated in the incinerator 1 is formed in the lower part of the incinerator 1. Dampers 4 and 5 are formed above and below the storage section 3 and are opened and closed by a motor or the like. One end of an incinerated ash transfer pipe 6 for transferring incinerated ash 2 using a gas such as air is open in the storage section 3, and a filter 7 is disposed at the tip end of the incinerated ash transfer pipe 6. In the figure, reference numeral 8 indicates a gas separation device that separates the incinerated ash 2 from the gas from the incinerated ash transfer pipe 6. is connected. A valve 16 is arranged in the incineration ash transfer pipe 6.
容器本体13内には、筒状の多孔体からなる回転式フィ
ルタ19が配置されている。この回転式フィルタ19は
、セラミックス、パールコン(ダイセル化学工業の登録
商標)等により形成されている。この回転式フィルタ1
9の上部には、この回転式フィルタ19を回転するため
のスプロケット21と、このスプロケット21にチェー
ン23を介して連結するギアドモータ25とが配置され
ている。さらに、この回転式フィルタ19の上部には、
この回転式フィルタ19内の空気を吸引する配管27の
一端が接続され、他端は、例えば、ブロワ−のような吸
引手段28に接続されている。回転式フィルタ19の外
周には、回転式フィルタ19の外周に付着した焼却灰2
を掻き取る分離板29が、回転式フィルタ19と一定間
隔、例えば1tlの間隔を置いて配置されている。容器
本体13の下部は、ホッパ31に開口している。なお、
このホッパ31は、例えば、図示しないマイクロ波溶融
装置、アーク溶融装置等に焼却灰2を供給するものであ
る。A rotary filter 19 made of a cylindrical porous body is arranged inside the container body 13. This rotary filter 19 is made of ceramics, Pearlcon (registered trademark of Daicel Chemical Industries), or the like. This rotary filter 1
A sprocket 21 for rotating the rotary filter 19 and a geared motor 25 connected to the sprocket 21 via a chain 23 are disposed above the rotary filter 9 . Furthermore, on the top of this rotary filter 19,
One end of a pipe 27 for suctioning the air in the rotary filter 19 is connected, and the other end is connected to a suction means 28 such as a blower. Incineration ash 2 attached to the outer periphery of the rotary filter 19 is disposed on the outer periphery of the rotary filter 19.
A separation plate 29 for scraping the water is disposed at a constant distance from the rotary filter 19, for example, at a distance of 1 tl. The lower part of the container body 13 opens into the hopper 31 . In addition,
This hopper 31 supplies the incinerated ash 2 to, for example, a microwave melting device, an arc melting device, etc. (not shown).
以上のように構成された放射性廃棄物移送装置では、焼
却炉1の下部に形成される貯蔵部3内の焼却灰2は、移
送流体である空気とともにフィルタ7、焼却灰移送管6
を通り容器本体13内に供給された後、容器本体13内
に配置される筒状の多孔体からなる回転式フィルタ19
の外周に、第2図に示すように付着し、順次積層し付着
層33を形成し、その厚みが、例えば1)1を越えると
、回転式フィルタ19の外周に一定間隔を置いて配置さ
れる分離板29により掻き取られる。掻き取られた放射
性廃棄物は、容器本体13の下部からホッパ31に落下
される。In the radioactive waste transfer device configured as described above, the incinerated ash 2 in the storage section 3 formed at the lower part of the incinerator 1 is transported through the filter 7 and the incinerated ash transfer pipe 6 together with the air that is the transfer fluid.
A rotary filter 19 made of a cylindrical porous body is placed inside the container body 13 after being supplied into the container body 13 through
As shown in FIG. 2, they adhere to the outer periphery of the rotary filter 19 and are sequentially laminated to form an adhesion layer 33, and when the thickness thereof exceeds, for example, 1), the adhesive layer 33 is placed around the outer periphery of the rotary filter 19 at regular intervals. It is scraped off by the separating plate 29. The scraped radioactive waste is dropped into the hopper 31 from the lower part of the container body 13.
一方、第2図に矢符で示すように、多孔体からなる回転
式フィルタ19を通過した気体は、吸引手段28により
吸引され外部に排出される。On the other hand, as shown by arrows in FIG. 2, the gas that has passed through the rotary filter 19 made of a porous body is sucked by the suction means 28 and discharged to the outside.
すなわち、以上のように構成された放射性廃棄物移送装
置では、貯蔵部3内の焼却灰21才、移送流体である気
体とともに焼却灰移送管6を通り、気体分離装置8内に
供給され、この気体分離装置8により、焼却灰2と気体
とが分離される。従って、従来のように、焼却炉1で焼
却された焼却灰2をドラム缶を介して移送する必要がな
くなり、ドラム缶への焼却灰2の詰め込み時、あるいは
取り出し時に、焼却灰2が外部へ飛散することがなくな
り、放射能汚染を引き起こす虞を確実に解消することが
できる。That is, in the radioactive waste transfer device configured as described above, the incinerated ash in the storage section 3 passes through the incinerated ash transfer pipe 6 together with the gas as the transfer fluid, and is supplied into the gas separation device 8. The gas separation device 8 separates the incinerated ash 2 from the gas. Therefore, unlike in the past, there is no need to transfer the incinerated ash 2 in the incinerator 1 via a drum, and the incinerated ash 2 is scattered outside when it is packed into the drum or taken out. This eliminates the risk of radioactive contamination.
また、以上のように構成された放射性廃棄物移送装置で
は、焼却灰移送管6の先端にフィルタ7を配置したので
、金属、砂利等の異物をフィルタ7により分離し、例え
ば直径10韮以内の焼却灰2のみを気体分離袋M8に移
送することが可能となり、後工程におけるフィーダー、
バルブ等の選定を容易にすることができる。なお、この
場合には、適当な時期にホッパ5が開とされ、金属、砂
利等の異物のみが容器33内に収容される。In addition, in the radioactive waste transfer device configured as described above, since the filter 7 is placed at the tip of the incinerated ash transfer pipe 6, foreign substances such as metals and gravel are separated by the filter 7, and foreign substances of, for example, within 10 square meters in diameter are separated by the filter 7. It is now possible to transfer only the incinerated ash 2 to the gas separation bag M8, and the feeder in the post-process,
Selection of valves etc. can be made easier. In this case, the hopper 5 is opened at an appropriate time, and only foreign substances such as metal and gravel are accommodated in the container 33.
なお、焼却炉1の下部には、従来から貯蔵部3が形成さ
れているため、本発明は、この貯蔵部3に焼却灰移送管
6を開口することで容易に実施可能である。また、焼却
灰移送管6を耐熱部材により形成することにより、焼却
灰2の温度が高い時tこも焼却灰2の移送が容易に可1
)ヒとなる。In addition, since the storage part 3 is conventionally formed in the lower part of the incinerator 1, this invention can be implemented easily by opening the incineration ash transfer pipe 6 into this storage part 3. Furthermore, by forming the incinerated ash transfer pipe 6 from a heat-resistant material, the incinerated ash 2 can be easily transferred even when the temperature of the incinerated ash 2 is high.
)
なお、以上述べた実施例では、気体分離装置8として、
セラミックフィルタを用いた例について説明したが、本
発明はかかる実施例に限定されるものではなく、例えば
、サイクロン型のフィルタ等を用いても良いことは勿論
である。In addition, in the embodiment described above, as the gas separation device 8,
Although an example using a ceramic filter has been described, the present invention is not limited to this example, and it goes without saying that, for example, a cyclone type filter or the like may be used.
以上のように本発明によれば、焼却炉内の焼却灰を焼却
灰移送管により、直接気体分離装置に移送するようにし
たので、焼却灰が外部に飛散することがなくなり、放射
能汚染を引き起こす虞を確実に解消することができると
いう利点がある。As described above, according to the present invention, the incinerated ash in the incinerator is directly transferred to the gas separation device through the incinerated ash transfer pipe, so the incinerated ash is not scattered outside, and radioactive contamination is prevented. This has the advantage of being able to reliably eliminate the possibility of this occurring.
第1図は本発明の放射性廃棄物移送装置の一実施例を示
す一部縦断面図、第2図は第1図の回転式フィルタ近傍
を示す縦断面図である。
1・・・焼却炉、2・・・焼却灰、3・・・貯蔵部、6
・・・焼却灰移送管、8・・・気体分離装置。FIG. 1 is a partial vertical cross-sectional view showing an embodiment of the radioactive waste transfer device of the present invention, and FIG. 2 is a vertical cross-sectional view showing the vicinity of the rotary filter of FIG. 1... Incinerator, 2... Incineration ash, 3... Storage section, 6
... Incineration ash transfer pipe, 8... Gas separation device.
Claims (2)
焼却灰を一時貯蔵する貯蔵部に一端を開口し、前記焼却
灰を気体により移送する焼却灰移送管と、この焼却灰移
送管の他端を接続され、前記焼却灰移送管からの前記焼
却灰を前記気体と分離する気体分離装置とを備えたこと
を特徴とする放射性廃棄物移送装置。(1) An incinerated ash transfer pipe formed at the lower part of the incinerator, one end of which is opened to a storage section that temporarily stores incinerated ash in the incinerator, and which transfers the incinerated ash using gas; A radioactive waste transfer device characterized by comprising a gas separation device connected to the other end of the pipe to separate the incinerated ash from the incinerated ash transfer pipe from the gas.
放射性廃棄物移送装置。(2) The radioactive waste transfer device according to claim 1, wherein the gas is air.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61042723A JPH0797158B2 (en) | 1986-02-27 | 1986-02-27 | Radioactive waste transfer device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61042723A JPH0797158B2 (en) | 1986-02-27 | 1986-02-27 | Radioactive waste transfer device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62200299A true JPS62200299A (en) | 1987-09-03 |
JPH0797158B2 JPH0797158B2 (en) | 1995-10-18 |
Family
ID=12643985
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61042723A Expired - Fee Related JPH0797158B2 (en) | 1986-02-27 | 1986-02-27 | Radioactive waste transfer device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0797158B2 (en) |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5445979A (en) * | 1977-09-20 | 1979-04-11 | Babcock Hitachi Kk | Apparatus for cooling and conveying hot ash |
JPS55137021A (en) * | 1979-04-14 | 1980-10-25 | Ngk Insulators Ltd | High temperature-use ceramic filter |
JPS5764652U (en) * | 1980-09-29 | 1982-04-17 | ||
JPS5833600A (en) * | 1981-08-21 | 1983-02-26 | 日本電気株式会社 | Controller for nutation of artificial satellite |
JPS5833600U (en) * | 1981-08-31 | 1983-03-04 | 東洋物産株式会社 | tunnel waterproofing device |
JPS58216715A (en) * | 1982-06-09 | 1983-12-16 | Seiken:Kk | Separating device of solid from gas |
JPS59192339A (en) * | 1983-04-18 | 1984-10-31 | 三菱電機株式会社 | Electric cleaner |
JPS602371U (en) * | 1983-06-15 | 1985-01-09 | 三菱電機株式会社 | Air filter device for cooling rotating electric machines |
JPS60100016U (en) * | 1983-12-10 | 1985-07-08 | 新日本製鐵株式会社 | ceramic filter |
JPS60172321A (en) * | 1984-02-16 | 1985-09-05 | Mitsubishi Heavy Ind Ltd | Filtration apparatus |
JPS61425A (en) * | 1984-06-13 | 1986-01-06 | Toshiba Corp | Air purification system |
-
1986
- 1986-02-27 JP JP61042723A patent/JPH0797158B2/en not_active Expired - Fee Related
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5445979A (en) * | 1977-09-20 | 1979-04-11 | Babcock Hitachi Kk | Apparatus for cooling and conveying hot ash |
JPS55137021A (en) * | 1979-04-14 | 1980-10-25 | Ngk Insulators Ltd | High temperature-use ceramic filter |
JPS5764652U (en) * | 1980-09-29 | 1982-04-17 | ||
JPS5833600A (en) * | 1981-08-21 | 1983-02-26 | 日本電気株式会社 | Controller for nutation of artificial satellite |
JPS5833600U (en) * | 1981-08-31 | 1983-03-04 | 東洋物産株式会社 | tunnel waterproofing device |
JPS58216715A (en) * | 1982-06-09 | 1983-12-16 | Seiken:Kk | Separating device of solid from gas |
JPS59192339A (en) * | 1983-04-18 | 1984-10-31 | 三菱電機株式会社 | Electric cleaner |
JPS602371U (en) * | 1983-06-15 | 1985-01-09 | 三菱電機株式会社 | Air filter device for cooling rotating electric machines |
JPS60100016U (en) * | 1983-12-10 | 1985-07-08 | 新日本製鐵株式会社 | ceramic filter |
JPS60172321A (en) * | 1984-02-16 | 1985-09-05 | Mitsubishi Heavy Ind Ltd | Filtration apparatus |
JPS61425A (en) * | 1984-06-13 | 1986-01-06 | Toshiba Corp | Air purification system |
Also Published As
Publication number | Publication date |
---|---|
JPH0797158B2 (en) | 1995-10-18 |
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