JPH0365699A - Recovering and reusing device for abrasive grain in dry grain blasting abrasive device - Google Patents

Recovering and reusing device for abrasive grain in dry grain blasting abrasive device

Info

Publication number
JPH0365699A
JPH0365699A JP20034689A JP20034689A JPH0365699A JP H0365699 A JPH0365699 A JP H0365699A JP 20034689 A JP20034689 A JP 20034689A JP 20034689 A JP20034689 A JP 20034689A JP H0365699 A JPH0365699 A JP H0365699A
Authority
JP
Japan
Prior art keywords
abrasive
grain
abrasive grains
grains
suction hose
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.)
Pending
Application number
JP20034689A
Other languages
Japanese (ja)
Inventor
Koji Togo
東郷 浩二
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GENSHIRYOKU DAIKO KK
Original Assignee
GENSHIRYOKU DAIKO KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by GENSHIRYOKU DAIKO KK filed Critical GENSHIRYOKU DAIKO KK
Priority to JP20034689A priority Critical patent/JPH0365699A/en
Publication of JPH0365699A publication Critical patent/JPH0365699A/en
Pending legal-status Critical Current

Links

Landscapes

  • Combined Means For Separation Of Solids (AREA)

Abstract

PURPOSE:To intend to realize a sound particle size classification by vacuuming abrasive grains, by making an air flow of vacuuming rise up from a lower end of a straight stand pipe which is provided at an upper part of an abrasive grain collecting tank, and by dropping and collecting the abrasive grains having sizes larger than those can be borne by the air flow velocity. CONSTITUTION:Abrasive grains 3 which are transferred by a suction hose 4 are discharged upwardly from a spouting end 7 of the suction hose 4 at a lower part of a straight stand pipe 6 erected on an upper part of an abrasive grain collector 5. An inner diameter of the straight stand pipe 6, is designed to give a final falling velocity corresponding to a required size of an abrasive grain diameter to be collected. Coarse grains from which fine grains are already removed by a wind power grain classification in the straight stand pipe 6, are dropped down into a rotary tank 5 and then are spouted again and used as abrasive grains for a contamination removal work. An air flow exhausted from a fine grain discharge pipe 8 which is connected to an upper end of the straight stand pipe 6, is sucked and exhausted by a volume typed blower 12 after a dust collection by a cyclon 9 and bag filter 10.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は原子炉設備で使用され、放射性物質で汚染され
た部材を砥粒噴射研磨装置で除染する際に利用する砥粒
回収再使用装置に関するものである。
Detailed Description of the Invention (Industrial Field of Application) The present invention is used in nuclear reactor equipment to recover and reuse abrasive particles used when decontaminating members contaminated with radioactive materials using an abrasive jet polishing device. It is related to the device.

(従来の技術) 砥粒噴射研磨装置で噴射した砥粒は、回収して再使用し
ながら作業を続けてゆく、砥粒は使用中に破砕されるの
で、補給と粉砕砥粒の除去が必要となる。
(Prior technology) The abrasive particles injected by an abrasive jet polishing device are collected and reused to continue work. Since the abrasive particles are crushed during use, it is necessary to replenish and remove the crushed abrasive particles. becomes.

原子炉設備の除染では、密閉したハウス内の作業となる
から、視界確保のためと粉砕砥粒側に集まる放射性物質
の防除のため、回収砥粒から確実に粉体を除去する手段
が期待されている。
Decontamination of nuclear reactor equipment involves work inside a sealed house, so a method is expected to reliably remove powder from recovered abrasive grains in order to ensure visibility and prevent radioactive materials that collect on the grinding abrasive grain side. has been done.

従来は、(1)篩を使う、(2)吸引回収ライン中にサ
イクロン等を設ける。(3)吸引回収ラインの気流中に
簡単な屈折部を設けて粗粒を分離する・・・等の手段を
講じていた。
Conventionally, (1) a sieve is used, and (2) a cyclone or the like is installed in the suction and recovery line. (3) Measures such as providing a simple bend in the airflow of the suction and recovery line to separate coarse particles have been taken.

上記(1)の篩は確実ではあるが、装置が巨大化し、ま
た篩の網の損耗も大きい、(2)のライン中のサイクロ
ンについては、本来、微粉捕集のための装−諺であるか
ら、砥粒の分別(数100μm)では微粉域まで回収さ
れ、しかも装置の摩耗も大きいという問題がある。さら
に(3)の屈折部を設ける方法は、砥粒の分別サイズ数
100μ臘を狙いやすいが、風量変動や管内の堆積物に
よる通風路の形状変化の影響を敏感にうけ、砥粒の沈降
箇所に変化を生じて精度の悪さを来すなどの難点がある
Although the sieve in (1) above is reliable, the equipment is large and the sieve mesh is subject to a lot of wear and tear.The cyclone in the line in (2) is originally a device for collecting fine particles. Therefore, when the abrasive grains are separated (several 100 μm), fine particles are recovered, and there is a problem in that the wear of the equipment is also large. Furthermore, the method (3) of providing a bending part makes it easy to aim for separation of abrasive grains with a size of several 100 microns, but it is sensitive to changes in the shape of the ventilation passage due to changes in air volume and deposits in the pipe, and the location where the abrasive grains settle is However, there are some drawbacks such as changes in the data, resulting in poor accuracy.

(発明により解決しようとする課題) 本発明は、上記従来技術の問題点である大型化、損耗化
、分級精度の悪さ、などを解決可能な砥粒の回収分級装
置を提供することを目的とする。
(Problems to be Solved by the Invention) An object of the present invention is to provide an abrasive grain recovery and classification device that can solve the problems of the prior art described above, such as large size, wear and tear, and poor classification accuracy. do.

(課題を解決するための手段) 作業ハウス内で研磨作業中、床に堆積した使用ずみの砥
粒を回収再使用するため、まず砥粒3を真空吸引し、そ
の気流を砥粒回収槽5の上部に設けた直立筒6の下端か
ら上昇させる。上昇気流中の砥粒は、その風速に見合っ
た粒径サイズ以上のものは落下して回収され、*粉は気
流に乗って次の工程の集塵!I9,10で捕集される。
(Means for solving the problem) In order to collect and reuse the used abrasive grains deposited on the floor during polishing work in the work house, the abrasive grains 3 are first vacuum-suctioned, and the airflow is transferred to the abrasive grain collection tank 5. It is raised from the lower end of an upright tube 6 provided at the top of the tube. Abrasive grains in the rising air, those with a particle size larger than the wind speed, fall and are collected, *The powder rides on the air current and is collected for the next process! Collected at I9 and 10.

直立筒6での分級サイズを規制する風速(すなわち風量
)を、通気ラインの抵抗変化にか)おらず、略一定に保
ちやすい容積型排風機12で動作させ、かつ風量調節弁
11も備える。さらに、堆積砥粒を吸引する吸引ホース
4の一端側に真空破壊弁14を設け、堆積砥粒3の吸引
時に、吸引口が突発的に閉塞されても、吸引ホース4内
で真空破壊弁が開き、外気を吸引して通気ラインの通風
量が確保されるようにした。これらの対策によって直立
筒6を通過する風量は略一定に保たれ、直立筒6内での
砥粒の分級を精度よく行うことができる。なお、直立筒
6″の下部は外気から密閉されて砥粒回収槽5と連通さ
せた。
The air velocity (that is, the air volume) that regulates the classification size in the upright tube 6 is operated by a positive displacement fan 12 that can be easily kept substantially constant without depending on the resistance change of the ventilation line, and is also provided with an air volume control valve 11. Furthermore, a vacuum breaker valve 14 is provided at one end of the suction hose 4 that sucks the deposited abrasive grains, so that even if the suction port is suddenly blocked during suction of the deposited abrasive grains 3, the vacuum breaker valve 14 is installed in the suction hose 4. It was opened to draw in outside air and ensure the amount of ventilation in the ventilation line. By these measures, the amount of air passing through the upright cylinder 6 is kept substantially constant, and the abrasive grains can be classified within the upright cylinder 6 with high accuracy. Note that the lower part of the upright cylinder 6'' was sealed from the outside air and communicated with the abrasive grain recovery tank 5.

(実施例) 本発明の実施例を図によって説明する。原子炉汚染部材
1を除染する為、乾式の砥粒2を噴射する作業では、床
上に飛散した堆積砥粒3を回収して再使用する。吸引ホ
ース4で運ばれた堆積砥粒3は、砥粒回収槽5の上部に
立設した直立筒6の下部で吸引ホース4の噴出端7から
直立筒内に向けて上向きに放出される。直立筒6の内径
は、回収砥粒径の必要サイズに対応した落下終端速度(
Teminal Velacity)を与えるように、
沈降のニュートン式等で設計しておく。
(Example) An example of the present invention will be described with reference to the drawings. In the work of spraying dry abrasive grains 2 to decontaminate reactor contaminated parts 1, the deposited abrasive grains 3 scattered on the floor are collected and reused. The deposited abrasive grains 3 carried by the suction hose 4 are ejected upward from the spouting end 7 of the suction hose 4 into the upright cylinder at the lower part of the upright cylinder 6 erected above the abrasive grain recovery tank 5. The inner diameter of the upright cylinder 6 is determined by the final falling velocity (
terminal velocity).
Design using the Newtonian method of sedimentation.

直立筒6内での風力分級によって微粉を除かれた粗粒は
、砥粒回収槽5へ落下させ、再度汚染除去作業用の砥粒
として噴射使用する。直立筒6の上端に連結された微粉
排出管8から排出される微粒を含んだ気流は、後続する
サイクロン9.バグフィルタlOで集塵した後、風量調
節弁11、容積型排風機12で吸引排気される。
The coarse grains from which fine powder has been removed by air classification in the upright cylinder 6 are dropped into the abrasive grain recovery tank 5 and are used again by injection as abrasive grains for decontamination work. The airflow containing fine particles discharged from the fine powder discharge pipe 8 connected to the upper end of the upright cylinder 6 is transferred to the following cyclone 9. After the dust is collected by the bag filter IO, it is sucked and exhausted by the air volume control valve 11 and the positive displacement exhaust fan 12.

一方、吸引ホース4での堆積砥粒3の吸引作業は、偶発
的に吸引ホース4の吸引端で閉塞を超こしても、この近
傍に設けた真空破壊弁14により、吸引ホース4の端1
3側のホース内負圧が増大して真空破壊弁14が開口し
、外気を吸引して吸引ホース4内の風量が一定に維持さ
れる。これは外部の通気抵抗の増減があっても、比較的
一定風量の得やすい容積型排風機(例えばルーツブロワ
)12と相まって、直立筒6での分級風速を一定にする
作用がある。
On the other hand, even if the suction end of the suction hose 4 accidentally becomes blocked, the suction operation of the deposited abrasive grains 3 with the suction hose 4 is carried out by the vacuum breaker valve 14 provided near the suction end of the suction hose 4.
The negative pressure inside the hose on the 3 side increases, the vacuum breaker valve 14 opens, and outside air is sucked in to keep the air volume inside the suction hose 4 constant. This has the effect of keeping the classification air speed in the upright tube 6 constant, in combination with the displacement type exhaust fan (for example, a Roots blower) 12, which makes it easy to obtain a relatively constant air volume even if the external ventilation resistance increases or decreases.

第2図は真空破壊弁14の一例を示す断面図である。吸
引ホース4の側部に開口14aを設け、該開口14aを
蓋14bで閉塞している。蓋14bはその中心に調整ね
じ14cが螺合されており、該ねじ14cによって、設
定圧を調整できるようになっている。
FIG. 2 is a sectional view showing an example of the vacuum breaker valve 14. An opening 14a is provided on the side of the suction hose 4, and the opening 14a is closed with a lid 14b. An adjustment screw 14c is screwed into the center of the lid 14b, and the set pressure can be adjusted by the screw 14c.

即ち調整ねじ14cの下端にそれ自体に通気部を有する
ばね保持具14dに保持されているばね14fがあり、
該ばね14fは調整ねじ14cによって上下動される押
圧板14eによってばね力が調整される。
That is, at the lower end of the adjustment screw 14c there is a spring 14f held by a spring holder 14d which itself has a ventilation section.
The spring force of the spring 14f is adjusted by a pressing plate 14e that is moved up and down by an adjusting screw 14c.

そして吸引ホース4内の真空圧が過大になると蓋14b
が引かれて(大気圧に押されて)開き、外気が矢印の如
く開口14aから流入し、真空圧を減殺するようになっ
ている。
When the vacuum pressure inside the suction hose 4 becomes excessive, the lid 14b
is pulled open (pushed by atmospheric pressure), and outside air flows in from the opening 14a as shown by the arrow, reducing the vacuum pressure.

なお15は砥粒2の噴射作業や砥粒吸引ホースでの吸引
作業を区画密閉する作業ハウス、16は作業ハウス15
内の発しん空気を別の濾過器に導くためのハウス内吸引
浄化配管である617は砥粒回収槽5内の金網、18は
貯砂切替弁、19は砥粒貯槽、20は砥粒供給弁である
。21は噴射用の圧縮空気、22はサイクロン用密封捕
集塵コンテナ、23はバグフィルタ用密封捕集塵コンテ
ナである。
In addition, 15 is a work house where the spraying work of abrasive grains 2 and suction work with an abrasive grain suction hose are divided and sealed, and 16 is a work house 15.
617 is a wire mesh inside the abrasive grain collection tank 5, 18 is a sand storage switching valve, 19 is an abrasive grain storage tank, and 20 is an abrasive grain supply valve. be. 21 is compressed air for injection, 22 is a sealed collection dust container for the cyclone, and 23 is a sealed collection dust container for the bag filter.

(効果) l)直立筒6で砥粒の重力落下と気流上昇とによる風力
分級を行うため、比較的に粗い砥粒径(数100μm)
での分級が確実に行われる。
(Effects) l) Since wind classification is performed by gravity falling of the abrasive grains and rising air current in the upright tube 6, the abrasive grain diameter is relatively coarse (several 100 μm).
Classification is carried out reliably.

2)砥粒の気流輸送の途中で分級するので、粗粒と微粒
が空間で分離し、粗粒と微粒との付着がなく、分級効率
が優れている。
2) Since the abrasive grains are classified during air flow transport, coarse grains and fine grains are separated in space, and there is no adhesion between coarse grains and fine grains, resulting in excellent classification efficiency.

3)風量調節弁11によって風量を変えると、分級粒径
を自由に変えることができる。
3) By changing the air volume using the air volume control valve 11, the classified particle size can be changed freely.

4)容積型排風機12と真空破壊弁14の組合せ使用に
よって、風力分級に必要な風速(すなわち風量)を一定
に保ちやすい。
4) By using the positive displacement exhaust fan 12 and the vacuum breaker valve 14 in combination, it is easy to maintain a constant wind speed (ie, air volume) necessary for wind classification.

5)作業上の効果として、真空破壊弁14の使用によっ
て、吸引気流輸送の代表的トラブルである吸引ホース4
の立上り部の管内閉塞(吸引口の突発的な閉塞時に粉体
量/空気量の比が増大して起こる〉が防止される。
5) As an operational effect, by using the vacuum break valve 14, the suction hose 4, which is a typical trouble in suction air flow transportation, can be removed.
This prevents the tube from being blocked at the rising end (which occurs when the ratio of powder amount/air amount increases when the suction port is suddenly blocked).

6)直立筒6での分級流速は数m/秒以下で行なわれる
もので、装置の摩耗は少なく、かつ装置も簡単小型です
む。
6) The classification flow rate in the upright tube 6 is several meters per second or less, so there is little wear on the equipment, and the equipment is simple and compact.

7)回収使用中の砥粒の流れの中で、連続的に微粉(破
砕砥粒と削り取られた放射性物質微粉)を除去している
ので、作業ハウス15内の視界、作業環境が極めて良好
に保たれる。
7) Since fine powder (crushed abrasive grains and radioactive material fine powder scraped off) is continuously removed from the flow of abrasive grains during collection and use, the visibility and work environment inside the work house 15 are extremely good. It is maintained.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の砥材回収再使用装置、およびこれが使
用されている関連機器の構成、配置を示す。 第2図は真空破壊弁の原理図。 図において; 1 汚染部材     2 砥粒 3 堆積砥粒    4 吸引ホース 5 回収槽      6 直立筒 7 (吸引ホースの)噴出端 8 微粉排出管    9 サイクロンlOバグフィル
タ  11  風量調節弁12  容積型排風機 13  (吸引ホース)吸引端 真空破壊弁   15  作業ハウス ハウス内吸引浄化配管 金網      18  貯砂切替弁 砥粒貯槽    20  砥粒供給弁 圧縮空気 サイクロン用密封捕集塵コンテナ バグフィルタ用密封捕集塵コンテナ 以上
FIG. 1 shows the structure and arrangement of the abrasive material recovery and reuse device of the present invention and related equipment in which this device is used. Figure 2 is a diagram of the principle of the vacuum breaker valve. In the figure: 1 Contaminated member 2 Abrasive grains 3 Deposited abrasive grains 4 Suction hose 5 Collection tank 6 Upright tube 7 Spout end (of suction hose) 8 Fine powder discharge pipe 9 Cyclone lO bag filter 11 Air volume control valve 12 Positive displacement exhaust fan 13 ( Suction hose) Suction end vacuum break valve 15 Work house Suction purification piping wire mesh inside the house 18 Sand storage switching valve Abrasive grain storage tank 20 Abrasive grain supply valve Sealed collection dust container for compressed air cyclone Sealed collection dust container for bag filter and above

Claims (1)

【特許請求の範囲】[Claims] 原子炉設備の除染用の乾式砥粒噴射研磨装置において、
作業ハウス(15)内での噴射研磨中の堆積砥粒を吸引
ホース(4)で回収する吸引ホースの吸引端(13)側
に真空破壊弁(14)を設け、吸引ホースの他端は砥粒
の落下分級回収サイズに必要な上昇風速を与える筒径を
有する直立筒(6)の下部に上方に向けて開口させ、直
立筒(6)の上端は微粒排出管(8)を介し集塵器(9
、10)および風量調節弁(11)を備えた容積型排風
機(12)に連結し、他方直立筒(6)の下端は砥粒回
収槽(5)の上部に外気閉鎖状態で結合させたことを特
徴とする乾式砥粒噴射研磨装置における砥粒回収再使用
装置。
In dry abrasive jet polishing equipment for decontaminating nuclear reactor equipment,
A vacuum breaker valve (14) is provided on the suction end (13) side of the suction hose (4) that collects accumulated abrasive grains during spray polishing in the work house (15), and the other end of the suction hose is connected to the abrasive The lower part of the upright cylinder (6), which has a cylinder diameter that provides the upward wind speed necessary for the particle falling classification and collection size, is opened upward, and the upper end of the upright cylinder (6) is used for dust collection through the fine particle discharge pipe (8). Vessel (9
, 10) and a positive displacement exhaust fan (12) equipped with an air volume control valve (11), while the lower end of the upright cylinder (6) was connected to the upper part of the abrasive grain collection tank (5) in a closed state to outside air. An abrasive grain recovery and reuse device in a dry abrasive jet polishing device characterized by the following.
JP20034689A 1989-08-03 1989-08-03 Recovering and reusing device for abrasive grain in dry grain blasting abrasive device Pending JPH0365699A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20034689A JPH0365699A (en) 1989-08-03 1989-08-03 Recovering and reusing device for abrasive grain in dry grain blasting abrasive device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20034689A JPH0365699A (en) 1989-08-03 1989-08-03 Recovering and reusing device for abrasive grain in dry grain blasting abrasive device

Publications (1)

Publication Number Publication Date
JPH0365699A true JPH0365699A (en) 1991-03-20

Family

ID=16422765

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20034689A Pending JPH0365699A (en) 1989-08-03 1989-08-03 Recovering and reusing device for abrasive grain in dry grain blasting abrasive device

Country Status (1)

Country Link
JP (1) JPH0365699A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100571564B1 (en) * 2002-12-09 2006-04-17 주식회사 데콘엔지니어링 Decontamination and dust collector of surface radioactive material using high pressure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100571564B1 (en) * 2002-12-09 2006-04-17 주식회사 데콘엔지니어링 Decontamination and dust collector of surface radioactive material using high pressure

Similar Documents

Publication Publication Date Title
US5092527A (en) Fluorescent tube crusher with particulate separation and recovery
JP5317953B2 (en) Wet dust collector
SE1100739A1 (en) Dust separator with constant suction power
CN105126529A (en) Method and device for inorganized emission flying dust pollution government
CN102686295A (en) Device for recovering nanopowders and ultrafine powders contained in a gas
US5775979A (en) Enclosed abrasive blasting apparatus
JP4635180B2 (en) Cyclone device for powder collection
JP5745058B2 (en) Filtration apparatus and filtration method
CN207641981U (en) A kind of workshop powder lot negative pressure absorption hierarchy system
CN220125738U (en) Ore dressing dust processor
JPH0365699A (en) Recovering and reusing device for abrasive grain in dry grain blasting abrasive device
CN200991624Y (en) Dust-removal fan
CN1024907C (en) Recovery separator for powder spray
CN206483279U (en) High-pressure vortex sack cleaner
JPH09323263A (en) Blasting machine
CN212881524U (en) Dust removal pipeline filter equipment
JPH07289998A (en) Method for separating foreign matter mixed with finely-pulverized abrasive material, method for separating foreign matter and dust mixed with finely-pulverized abrasive material, and separating apparatus for them
JPH1066818A (en) Dust collecting apparatus
CN211462418U (en) Retrieve dust collector of powdered sugar
CN207429972U (en) Dust-extraction unit and sand production line processed
CN207667308U (en) A kind of exhaust gas particle object filter device
CN109499792B (en) Abrasive recovery device used in abrasive cloth production process
CN217807437U (en) Fluidization trolley with double-pipe pinch valves and large-bag powder collecting, air locking and ash discharging device thereof
CN209564794U (en) Inertia and media filtration integral type high vacuum deduster
JPS6012599B2 (en) Solids collection device