JPH0658436B2 - Pneumatic transportation method for radioactive waste - Google Patents
Pneumatic transportation method for radioactive wasteInfo
- Publication number
- JPH0658436B2 JPH0658436B2 JP60245985A JP24598585A JPH0658436B2 JP H0658436 B2 JPH0658436 B2 JP H0658436B2 JP 60245985 A JP60245985 A JP 60245985A JP 24598585 A JP24598585 A JP 24598585A JP H0658436 B2 JPH0658436 B2 JP H0658436B2
- Authority
- JP
- Japan
- Prior art keywords
- air
- pipeline
- transportation
- blower
- powder
- 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
Links
- 238000000034 method Methods 0.000 title claims description 9
- 239000002901 radioactive waste Substances 0.000 title claims description 6
- 239000008187 granular material Substances 0.000 claims description 14
- 239000000843 powder Substances 0.000 claims description 10
- 238000001914 filtration Methods 0.000 claims description 6
- 239000000941 radioactive substance Substances 0.000 claims description 6
- 230000032258 transport Effects 0.000 description 13
- 239000002245 particle Substances 0.000 description 5
- 239000012857 radioactive material Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
Landscapes
- Air Transport Of Granular Materials (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、放射性廃棄物等の放射性物質を含む粉粒体の
空気輸送法に関するものである。TECHNICAL FIELD The present invention relates to a method for pneumatically transporting a powder or granular material containing a radioactive substance such as radioactive waste.
従来の技術 一般産業に採用されている吸引式空気輸送方法において
は、第2図に示すように、貯留ホツパ(1)に供給された
粉粒体がロータリーバルブ(2)により切り出され、吸込
口(3)から吸引された空気により管路内を輸送され、サ
イクロン(4)とバグフイルタ(5)とにより粉粒体と空気と
に分離される。分離された粉粒体はロータリーバルブ
(6),(7)により切り出されて収集ホツパ(8)内に送給さ
れ、一方、粉粒体を除去された空気はブロア(9)から大
気中に放出されている。空気流量は、バルブ(10)により
手動又は自動的に調節される。このような方法で放射性
廃棄物(例えば放射性焼却灰)を輸送すると、バグフイ
ルタ(5)を出た空気中には依然として微量の放射性物質
が混入しており、これが大気中に放出される弊害がある
が、これは、バグフイルタ(5)の下流にHEPAフイルタ
(微粒子除去フイルタ)(図示省略)を設けることによ
り解消可能である。2. Description of the Related Art In the suction type pneumatic transportation method adopted in the general industry, as shown in FIG. 2, the granular material supplied to the storage hopper (1) is cut out by the rotary valve (2) and the suction port is The air sucked from (3) transports the inside of the pipeline, and the cyclone (4) and the bag filter (5) separate the powder and granules from the air. Rotary valve for separated powder
The air cut out by (6) and (7) is fed into the collection hopper (8), while the air from which the particulates have been removed is released from the blower (9) into the atmosphere. The air flow rate is adjusted manually or automatically by the valve (10). When radioactive waste (such as radioactive incineration ash) is transported by such a method, trace amounts of radioactive substances are still mixed in the air that exits the bag filter (5), which may be harmful to the atmosphere. However, this can be solved by providing a HEPA filter (fine particle removal filter) (not shown) downstream of the bag filter (5).
発明が解決しようとする問題点 ところで、放射性物質の空気輸送に使用された空気は、
HEPAフイルタを通過させた後でも、放射線測定装置によ
り放射性物質の量が規定値以下であることを確認してか
ら、スタツクを経由して大気中に放出されなければなら
ないので、放出される空気量はなるべく少ない方が望ま
しい。しかし、上記従来の方法によれば、輸送能力との
兼合いから空気量の低減には制約を受けるという問題が
ある。また、ブロア(9)の運転中は管路内を負圧状態に
保てるが、低支持には管路内が大気圧となり、管路内に
残留した放射性物質が管路外に洩れ出るという問題があ
る。Problems to be Solved by the Invention By the way, the air used for pneumatic transportation of radioactive materials is
Even after passing through the HEPA filter, it must be released to the atmosphere via the stack after confirming that the amount of radioactive material is below the specified value with a radiation measurement device. It is desirable that the number is as small as possible. However, according to the above-mentioned conventional method, there is a problem in that the reduction of the air amount is restricted in consideration of the transportation capacity. Also, while the blower (9) is in operation, it is possible to maintain a negative pressure inside the pipeline, but due to the low support, atmospheric pressure inside the pipeline causes the radioactive material remaining in the pipeline to leak out of the pipeline. There is.
本発明は、上記問題点を解決することを目的としてお
り、管路を閉管路として空気を循環使用するとともに、
管路内を常時負圧状態に保つものである。An object of the present invention is to solve the above problems and to circulate and use air with a pipe line as a closed pipe line,
The inside of the pipeline is always kept in a negative pressure state.
問題点を解決するための手段 上記問題点を解決するため、本発明の放射性廃棄物等の
空気輸送方法は、放射性物質を含有する粉粒体を空気輸
送する輸送管路に、該輸送管路内を常時負圧状態に保つ
排気管路が接続され、前記輸送管路においては、貯留ホ
ツパ内に供給された前記粉粒体が空気により分離手段に
送給され、該分離手段は前記粉粒体を前記空気から分離
して収集ホツパ内に送給し、前記粉粒体を除去された空
気は輸送用ブロアにより前記貯留ホツパにもどされて循
環し、前記排気管路においては、排気用ブロアが前記粉
粒体を除去された空気の一部をろ過手段を介して大気中
に常時放出することにより、前記輸送管路内を常時負圧
状態に保つていることを特徴とするものである。Means for Solving the Problems In order to solve the above problems, a method for pneumatically transporting radioactive waste or the like according to the present invention provides a transportation pipeline for pneumatically transporting a granular material containing a radioactive substance. An exhaust pipe line for keeping a negative pressure inside is always connected, and in the transport pipe line, the granular material supplied into the storage hopper is fed to the separating means by air, and the separating means forms the powder particles. The body is separated from the air and sent into the collection hopper, and the air from which the particulates have been removed is returned to the storage hopper by the transport blower and circulates, and the exhaust blower is circulated in the exhaust pipe line. Constantly discharge a part of the air from which the powder and granules have been removed into the atmosphere through a filtering means, so that the inside of the transportation pipeline is always kept in a negative pressure state. .
作用 上記本発明の構成において、輸送管路では空気が循環し
て使用されるので、輸送管路から大気中に放出される空
気は皆無であり、僅かに清浄空気の一部が排気管路から
大気中に放出されるに過ぎない。また、輸送管路内は常
時負圧状態に保たれているので、輸送管路内の放射性物
質が管路外に洩れ出ることはない。Action In the above configuration of the present invention, since air is circulated and used in the transportation pipeline, there is no air released from the transportation pipeline to the atmosphere, and a portion of the clean air is slightly discharged from the exhaust pipeline. It is only released into the atmosphere. Further, since the inside of the transportation pipeline is always kept in a negative pressure state, radioactive substances in the transportation pipeline do not leak out of the pipeline.
実施例 以下、本発明の一実施例を第1図に基づいて説明する。
第1図は、本実施例の空気輸送方法が適用される空気輸
送装置(11)の系統図である。Embodiment One embodiment of the present invention will be described below with reference to FIG.
FIG. 1 is a system diagram of an air transportation device (11) to which the air transportation method of this embodiment is applied.
空気輸送装置(11)は、輸送管路(12)に排気管路(13)が接
続されてなる。輸送管路(12)においては、貯留ホツパ(1
4)、分離手段(15)、バルブ(16)及び輸送用ブロア(17)が
閉管路を形成するように接続されている。貯留ホツパ(1
4)にはロータリーバルブ(18)が装着されている。分離手
段(15)は、サイクロン(19)とバグフイルタ(20)とが直列
に接続されてなる。サイクロン(19)とバグフイルタ(20)
とは、それぞれに装着されたロータリーバルブ(21),(2
2)を介して収集ホツパ(23)に接続されている。バグフイ
ルタ(20)の下流から分岐して圧力調節計(24)が接続さ
れ、バルブ(16)の開度を制御する。排気管路(13)におい
ては、輸送用ブロア(17)の下流から分岐して、ろ過手段
(25)、バルブ(26)及び排気用ブロア(27)が互いに直列に
接続されるとともに、圧力調節計(28)が接続されてい
る。ろ過手段(25)は、HEPAフイルタ等が適している。圧
力調設計(28)は、バルブ(26)の開度を制御する。The air transportation device (11) is formed by connecting the exhaust pipeline (13) to the transportation pipeline (12). In the transportation pipeline (12), the storage hopper (1
4), the separating means (15), the valve (16) and the transport blower (17) are connected so as to form a closed pipe. Storage hopper (1
The rotary valve (18) is installed in 4). The separating means (15) is composed of a cyclone (19) and a bag filter (20) connected in series. Cyclone (19) and Bagfilter (20)
And are the rotary valves (21), (2
It is connected to the collection hopper (23) via 2). A pressure controller (24) is connected to the bag filter (20) branched from the downstream side of the bag filter (20) to control the opening of the valve (16). In the exhaust pipe line (13), branch from the downstream of the transport blower (17) to obtain a filtering means.
The valve (25), the valve (26) and the exhaust blower (27) are connected to each other in series, and the pressure regulator (28) is connected. A HEPA filter or the like is suitable for the filtration means (25). The pressure regulation design (28) controls the opening of the valve (26).
次に、上記構成の空気輸送装置(11)について本実施例の
空気輸送方法を説明する。Next, the air transportation method of this embodiment for the air transportation device (11) having the above-mentioned configuration will be described.
放射性物質を含有した粉粒体は、貯留ホツパ(14)内に供
給されている。まず、排気用ブロア(27)が運転され、輸
送管路(2)内の空気の一部が大気中に放出される。圧力
調節計(28)は、輸送管路(2)内の圧力を検出し、バルブ
(26)の開度を制御して、輸送管路(2)内を適度の負圧に
保つ。放出すべき空気中に放射性物質が含有されている
ときは、ろ過手段(25)により除去される。The granular material containing the radioactive substance is supplied into the storage hopper (14). First, the exhaust blower (27) is operated, and a part of the air in the transportation pipeline (2) is released into the atmosphere. The pressure regulator (28) detects the pressure in the transport line (2) and
By controlling the opening of (26), the inside of the transportation pipeline (2) is maintained at an appropriate negative pressure. When radioactive material is contained in the air to be discharged, it is removed by the filtration means (25).
次に、輸送用ブロア(17)が運転される。このとき、排気
用ブロア(27)は運転され続けている。輸送用ブロア(17)
の下流側(吐出側)の圧力が上昇し、圧力調節計(28)は
バルブ(26)の開度を大きくし、排気用ブロア(27)からの
放出量が増加する。一定時間経過後、輸送用ブロア(17)
の下流側の圧力も負圧となり、輸送管路(2)内に負圧の
圧力平衡状態が形成される。このとき、圧力調節計(24)
は、バルブ(16)の開度を制御して、輸送管路(2)内の空
気流量を一定に保つ。輸送管路(2)内の圧力平衡状態及
び空気流量が一定になつた後、ロータリーバルブ(18)に
より貯留ホツパ(14)内の粉粒体が切り出される。輸送用
ブロア(17)により輸送管路(2)内を循環させられている
空気は、粉粒体を分離手段(15)に送給する。分離手段(1
5)においては、サイクロン(19)が遠心力により粉粒体を
空気から分離し、空気のみをバグフイルタ(20)に送給す
る。バグフイルタ(20)は、バグにより更に微細な粉粒体
を空気から分離する。このようにして分離され粉粒体
は、各ロータリーバルブ(21),(22)により切り出され
て、収集ホツパ(23)内に送給される。一方、粉粒体が除
去された清浄空気は、輸送用ブロア(17)により吸引され
て、貯留ホツパ(14)にもどされ循環するのである。Next, the transport blower (17) is operated. At this time, the exhaust blower (27) continues to operate. Transport blowers (17)
The pressure on the downstream side (discharging side) rises, the pressure regulator (28) increases the opening of the valve (26), and the discharge amount from the exhaust blower (27) increases. After a certain time, a blower for transportation (17)
The pressure on the downstream side also becomes a negative pressure, and a negative pressure pressure equilibrium state is formed in the transportation pipeline (2). At this time, pressure regulator (24)
Controls the opening of the valve (16) to keep the air flow rate in the transportation pipeline (2) constant. After the pressure equilibrium state and the air flow rate in the transportation pipeline (2) have become constant, the rotary valve (18) cuts out the granular material in the storage hopper (14). The air circulated in the transportation pipeline (2) by the transportation blower (17) sends the powdery particles to the separating means (15). Separation means (1
In 5), the cyclone (19) separates the granular material from the air by centrifugal force and sends only the air to the bag filter (20). The bag filter (20) separates finer particles from the air due to the bag. The powder particles thus separated are cut out by the rotary valves (21) and (22) and fed into the collection hopper (23). On the other hand, the clean air from which the particles have been removed is sucked by the transport blower (17), returned to the storage hopper (14) and circulated.
なお、輸送用ブロア(17)の停止時には、該ブロア(17)や
各ロータリーバルブ(18),(21),(22)の軸封部から空気
が輸送管路(2)内に流入し、また、運転時には、バグフ
イルタ(20)の逆洗用空気が加わる。しかし、これらの空
気増加分は、常時運転されている排気用ブロア(27)によ
り大気中に排出される。When the transportation blower (17) is stopped, air flows into the transportation pipeline (2) from the blower (17) and the shaft seals of the rotary valves (18), (21) and (22), In addition, air for backwashing the bag filter (20) is added during operation. However, these increased air amounts are discharged into the atmosphere by the exhaust blower (27) that is constantly operating.
発明の効果 本発明は、上記のように構成されたものであるが、輸送
用ブロアの停止時、運転時にかかわりなく、常に輸送管
路内が負圧状態に保たれているので、放射性物質が管路
外に漏洩するおそれがなく、また、輸送管路が閉管路に
形成されているので、輸送用空気は循環して使用され、
管路外に放出される空気は従来の開放形管路の場合の1/
100以下と大幅に減少するなど、優れた効果を奏する。EFFECTS OF THE INVENTION The present invention is configured as described above, but since the inside of the transportation pipeline is always kept in a negative pressure state regardless of whether the transportation blower is stopped or operating, the radioactive material is There is no risk of leakage to the outside of the pipeline, and since the transport pipeline is formed as a closed pipeline, the transport air is circulated and used,
The air released to the outside of the pipeline is 1/1 of that of the conventional open pipeline.
It has an excellent effect such as a significant decrease of 100 or less.
第1図は本発明の放射性廃棄物等の空気輸送方法が適用
される空気輸送装置の系統図、第2図は従来の一般産業
に使用されている空気輸送装置の一例を示す系統図であ
る。 (11)……空気輸送装置、(12)……輸送管路、(13)……排
気管路、(14)……貯留ホツパ、(15)……分離手段、(17)
……輸送用ブロア、(23)……収集ホツパ、(25)……ろ過
手段、(27)……排気用ブロア。FIG. 1 is a system diagram of an air transportation device to which the method of pneumatic transportation of radioactive waste of the present invention is applied, and FIG. 2 is a system diagram showing an example of a conventional air transportation device used in general industry. . (11) …… Pneumatic transport device, (12) …… Transport pipeline, (13) …… Exhaust pipeline, (14) …… Storage hopper, (15) …… Separation means, (17)
...... Transportation blower, (23) …… Collection hopper, (25) …… Filtration means, (27) …… Exhaust blower.
Claims (1)
る輸送管路に、該輸送管路内を常時負圧状態に保つ排気
管路が接続され、前記輸送管路においては、貯留ホツパ
内に供給された前記粉粒体が空気により分離手段に送給
され、該分離手段は前記粉粒体を前記空気から分離して
収集ホツパ内に送給し、前記粉粒体を除去された空気は
輸送用ブロアにより前記貯留ホツパにもどされて循環
し、前記排気管路においては、排気用ブロアが前記粉粒
体を除去された空気の一部をろ過手段を介して大気中に
常時放出することにより、前記輸送管路内を常時負圧状
態に保つていることを特徴とする放射性廃棄物等の空気
輸送方法。1. An exhaust pipeline for keeping a negative pressure inside the transport pipeline is connected to a transport pipeline for pneumatically transporting a granular material containing a radioactive substance, and the storage pipeline is provided in the transport pipeline. The powder and granules supplied inside are fed to the separating means by air, and the separating means separates the powder and granules from the air and feeds them into the collecting hopper, and the powder and granules are removed. The air is returned to the storage hopper by the transportation blower and circulates, and in the exhaust pipe line, the exhaust blower constantly discharges a part of the air from which the powder and granules have been removed into the atmosphere through the filtering means. By doing so, the method for pneumatic transportation of radioactive waste, characterized in that the inside of the transportation pipeline is always kept in a negative pressure state.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60245985A JPH0658436B2 (en) | 1985-10-31 | 1985-10-31 | Pneumatic transportation method for radioactive waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60245985A JPH0658436B2 (en) | 1985-10-31 | 1985-10-31 | Pneumatic transportation method for radioactive waste |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62105094A JPS62105094A (en) | 1987-05-15 |
JPH0658436B2 true JPH0658436B2 (en) | 1994-08-03 |
Family
ID=17141756
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60245985A Expired - Lifetime JPH0658436B2 (en) | 1985-10-31 | 1985-10-31 | Pneumatic transportation method for radioactive waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0658436B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2222584A4 (en) * | 2007-12-21 | 2018-01-03 | Maricap OY | Method in pneumatic material conveying system and a pneumatic material conveying system |
EP2222585B1 (en) * | 2007-12-21 | 2024-06-26 | Maricap OY | Method in pneumatic material conveying system and a pneumatic material conveying system |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2591638B2 (en) * | 1988-01-07 | 1997-03-19 | 千葉製粉株式会社 | Pneumatic transportation of powder |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5811421A (en) * | 1981-07-07 | 1983-01-22 | Nippon Alum Mfg Co Ltd:The | Circulation system for powdery or granular material carrying gas |
JPS624129A (en) * | 1985-06-27 | 1987-01-10 | Mitsubishi Heavy Ind Ltd | Pneumatic conveyor |
-
1985
- 1985-10-31 JP JP60245985A patent/JPH0658436B2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2222584A4 (en) * | 2007-12-21 | 2018-01-03 | Maricap OY | Method in pneumatic material conveying system and a pneumatic material conveying system |
EP2222585B1 (en) * | 2007-12-21 | 2024-06-26 | Maricap OY | Method in pneumatic material conveying system and a pneumatic material conveying system |
Also Published As
Publication number | Publication date |
---|---|
JPS62105094A (en) | 1987-05-15 |
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