JP2000344348A - Powder collector - Google Patents
Powder collectorInfo
- Publication number
- JP2000344348A JP2000344348A JP11156062A JP15606299A JP2000344348A JP 2000344348 A JP2000344348 A JP 2000344348A JP 11156062 A JP11156062 A JP 11156062A JP 15606299 A JP15606299 A JP 15606299A JP 2000344348 A JP2000344348 A JP 2000344348A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- gas
- outlet
- granular material
- light
- 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
- 239000000843 powder Substances 0.000 title claims abstract description 38
- 239000008187 granular material Substances 0.000 claims abstract description 42
- 239000002245 particle Substances 0.000 claims abstract description 18
- 230000002093 peripheral effect Effects 0.000 claims description 6
- 239000000463 material Substances 0.000 description 5
- 239000011236 particulate material Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Landscapes
- Air Transport Of Granular Materials (AREA)
Abstract
(57)【要約】
【課題】 粉粒体捕集器に溜ったフレーク状の軽量の粉
粒体を確実に排出する。
【解決手段】 軽量の粉粒体が粉粒体入口4より上の所
定位置まで溜ると、気体吸引装置(図示略)を停止させ
た後、開閉蓋11を開き、その後、粉粒体押下具12を
押し下げて溜った軽量の粉粒体を下側に押すことによっ
て、テーパー筒8内の軽量の粉粒体を粉粒体出口3より
排出する。
(57) [Summary] [PROBLEMS] To reliably discharge flake-shaped light-weight granules collected in a granule collector. SOLUTION: When light and granular material accumulates to a predetermined position above a granular material inlet 4, after stopping a gas suction device (not shown), an opening / closing lid 11 is opened, and thereafter, a granular material pressing tool. By pushing down 12 and pushing down the accumulated light-weight powder and granules downward, the light-weight powder and granules in the tapered cylinder 8 are discharged from the powder-particle outlet 3.
Description
【0001】[0001]
【発明の属する技術分野】本発明は粉粒体捕集器に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a particulate collector.
【0002】[0002]
【従来の技術】従来、この種の粉粒体捕集器として以下
の如きものは知られている。粉粒体入口が形成された頂
壁を有すると共に、下部に粉粒体出口を有する下方すぼ
まりのテーパー下部を有し、更に側周壁に気体出口を有
する筒状本体と、この筒状本体内にそれとの間に所定間
隔をあけるようして気体出口を粉粒体入口及び粉粒体出
口と画するようにして設けられた、設定の大きさの粉粒
体の通過は許容せず気体の通過は許容するフィルター
と、筒状本体の粉粒体出口に設けられた開閉蓋とを有す
るものは知られている。2. Description of the Related Art Heretofore, the following types are known as this type of particulate collector. A cylindrical body having a top wall formed with a granular material inlet, having a tapered lower portion having a downward tapered portion having a granular material outlet at a lower portion, and further having a gas outlet on a side peripheral wall; The gas outlet is set so that the gas outlet is separated from the gas inlet and the powder outlet with a predetermined interval between them, and the passage of the powder of the set size is not allowed. Is known, which has a filter that allows the passage of air through the filter and an opening / closing lid provided at the outlet of the granular material of the cylindrical body.
【0003】[0003]
【従来の技術の作用】以下に従来の技術の作用を説明す
る。粉粒体入口に粉粒体が貯留された粉粒体貯留源(気
体入口を有するもの)を接続すると共に、気体出口に気
体吸引装置の吸引口を接続し、このような準備の後、開
閉蓋によって粉粒体出口を閉じた後、気体吸引装置を作
動すれば以下の作用が行なわれる。粉粒体捕集器内が負
圧となるので、粉粒体入口から気体と共に粉粒体が粉粒
体捕集器内に流入し、気体は気体出口から出て行き、粉
粒体は粉粒体捕集器内に溜められる。そして、気体吸引
装置を停止させた後、開閉弁を開くことによって粉粒体
捕集器内の粉粒体は粉粒体出口より排出される。The operation of the prior art will be described below. A powder material storage source (having a gas inlet) in which the powder is stored is connected to the powder inlet, and a suction port of a gas suction device is connected to the gas outlet. After closing the outlet of the granular material with the lid, the following operation is performed by operating the gas suction device. Since the inside of the particulate collector becomes negative pressure, the particulates flow into the particulate collector together with the gas from the particulate inlet, the gas exits from the gas outlet, and the particulate It is stored in the particle collector. After the gas suction device is stopped, the on-off valve is opened to discharge the powder in the powder collector from the powder outlet.
【0004】[0004]
【従来技術の欠点】前記従来の粉粒体捕集器には以下の
如き欠点があった。バージン原料である重量のあるペレ
ット等(一般的に見掛け密度が大きい)は前記従来の粉
粒体捕集器で捕集された後、開閉弁を開くことによって
自重落下による排出が出来るが、軽量の粉粒体(この明
細書で、軽量の粉粒体とは、下から上に向かう所定流速
の気体内においては、その気体の流れによって上方に舞
い上げられて、自重では落下しないか、又は落下しにく
い粉粒体をいう。)(一般的に見掛け密度が小さい)に
あっては、粉粒体入口から粉粒体捕集器内に供給された
軽量の粉粒体は、気体出口に向かう気体の流れに乗って
フィルターの表面に付着・蓄積されて行く。そして、軽
量の粉粒体が粉粒体捕集器に所定量溜った後、気体吸引
装置を停止させて軽量の粉粒体を排出するべく開閉弁を
開いても、軽量の粉粒体がフィルターの表面に付着・蓄
積していることや、筒状本体の下部が下方すぼまりのテ
ーパー下部であって壁面抵抗が大きいことのため、自重
では軽量の粉粒体の確実な排出が出来ないという欠点が
あった。なお、使用済の合成樹脂製品を再利用するため
に粉砕した再利用原料は軽量の粉粒体となることが多い
ので、地球環境保護の観点から使用済の合成樹脂製品の
再利用を促進するためには、前記欠点の解消は不可欠の
ものとなっている。Disadvantages of the prior art The above-mentioned conventional particulate collector has the following disadvantages. Virgin raw materials such as heavy pellets (generally having a large apparent density) can be discharged by their own weight drop by opening the on-off valve after being collected by the above-mentioned conventional particulate collector. (In this specification, a light-weighted powdery material means that in a gas having a predetermined flow velocity going from bottom to top, it is sowed upward by the flow of the gas and does not fall under its own weight, or (In general, the apparent density is low.) In the case of light-weight particles supplied from the particle inlet to the particle collector, the light-weight particles are supplied to the gas outlet. Attached and accumulated on the surface of the filter along with the flowing gas. Then, after a predetermined amount of the light and granular material has accumulated in the powder and particle collector, even if the gas suction device is stopped and the on-off valve is opened to discharge the light and fine material, the light and granular material remains Due to the fact that it adheres and accumulates on the surface of the filter, and that the lower part of the cylindrical body is a tapered lower part that tapers downward and has a large wall resistance, light weight particles can be reliably discharged under its own weight. There was a disadvantage that there was no. In addition, since the reused raw material crushed to reuse the used synthetic resin product is often a light powder, it promotes the reuse of the used synthetic resin product from the viewpoint of global environmental protection. Therefore, the elimination of the above drawbacks is indispensable.
【0005】[0005]
【前記欠点を解消するための手段】本発明は前記欠点を
解消するために以下の如き手段を採用した。請求項1の
発明は、上部に頂壁を有しており下部が粉粒体出口とな
されると共に、側周壁の下部に粉粒体入口が形成され、
側周壁の上部又は頂壁に気体出口が形成された筒状本体
と、この筒状本体内に気体出口を粉粒体入口及び粉粒体
出口と画するようにして設けられた、設定の大きさの粉
粒体の通過は許容せず気体の通過は許容するフィルター
からなる下方拡がりのテーパー筒と、筒状本体の粉粒体
出口に設けられた開閉蓋と、テーパー筒内において上下
動自在となされた粉粒体押下具とを有しており、気体の
流れによって粉粒体を粉粒体入口よりテーパー筒内に導
入し、気体を気体出口より排出するようにしたものであ
る。The present invention employs the following means to solve the above-mentioned drawbacks. The invention according to claim 1 has a top wall at an upper portion, a lower portion serving as a granule outlet, and a granule inlet formed at a lower portion of the side peripheral wall,
A cylindrical main body having a gas outlet formed on the upper or top wall of the side peripheral wall, and a setting size provided in the cylindrical main body such that the gas outlet is defined as a powder inlet and a powder outlet. A tapered cylinder with a filter that does not allow the passage of powder particles but allows the passage of gas, a downwardly expanding tapered cylinder, an opening / closing lid provided at the powder / particle outlet of the cylindrical body, and a vertically movable inside the tapered cylinder In this case, the granular material is introduced into the tapered cylinder from the granular material inlet by the flow of the gas, and the gas is discharged from the gas outlet.
【0006】[0006]
【発明の効果】本発明は前記した如き構成によって以下
の如き効果を奏する。軽量の粉粒体を下部の粉粒体入口
から粉粒体捕集器内に入れ、気体を上部の気体出口から
排出するようにして、軽量の粉粒体を気体の流れによっ
てテーパー筒の上方に移動させて、軽量の粉粒体をテー
パー筒の上部から順次下に向かって蓄積するようにし
て、軽量の粉粒体が上部ほど密で下部ほど疎になる傾向
としたこと、軽量の粉粒体の分離を行なうフィルターが
下方拡がりのテーパー筒であること、及び、開閉蓋をあ
けた後、粉粒体押下具によって軽量の粉粒体を押し下げ
ることの相乗効果によって、テーパー筒内に溜められた
軽量の粉粒体を粉粒体出口より確実に排出することが出
来る。According to the present invention, the following effects can be obtained by the above configuration. Put the lightweight powder into the powder collector through the lower powder inlet and discharge the gas through the upper gas outlet. To make the light and granular material accumulate from the upper part of the tapered cylinder to the lower part. The filter that separates the granules is a tapered cylinder that expands downward, and after the lid is opened, the synergistic effect of pushing down the lightweight granules with the granule pressing tool is retained in the tapered cylinder. It is possible to reliably discharge the obtained light-weight granules from the granules outlet.
【0007】[0007]
【発明の実施の形態】以下に本発明の実施の形態を説明
する。粉粒体捕集器1は、上部に頂壁2を有しており下
部が粉粒体出口3となされると共に、側周壁の下部に粉
粒体入口4が形成され、側周壁の上部(又は頂壁2)に
気体出口5が形成された筒状本体7と、この筒状本体7
内に気体出口5を粉粒体入口4及び粉粒体出口3と画す
るようにして設けられた、設定の大きさの粉粒体の通過
は許容せず気体の通過は許容するフィルターからなる下
方拡がりのテーパー筒8と、筒状本体7の粉粒体出口3
に設けられた開閉蓋11と、テーパー筒8内において上
下動自在に設けられた任意形状の粉粒体押下具12とを
有している。Embodiments of the present invention will be described below. The granular material collector 1 has a top wall 2 at an upper portion, a lower portion serving as a granular material outlet 3, a granular material inlet 4 formed at a lower portion of the side peripheral wall, and an upper portion ( Or, a cylindrical body 7 having a gas outlet 5 formed in the top wall 2), and the cylindrical body 7
The filter comprises a filter provided so as to define the gas outlet 5 as the powder-particle inlet 4 and the powder-particle outlet 3, and not allowing the passage of the powder having a predetermined size but permitting the passage of the gas. Downwardly expanding tapered cylinder 8, and granular material outlet 3 of cylindrical body 7
And an opening / closing lid 11 provided in the tapered cylinder 8 and an arbitrary-shaped powder / granular substance pressing tool 12 provided to be vertically movable within the tapered cylinder 8.
【0008】前記頂壁2には流体圧シリンダ15の本体
が軸心を上下方向に向けるようにして取り付けられ。こ
の流体圧シリンダ15のロッド16は頂壁2の開口を通
じてテーパー筒8内に臨んでおり、このロッド16の端
に粉粒体押下具12が取り付けられている。A main body of a fluid pressure cylinder 15 is mounted on the top wall 2 so that its axis is directed vertically. The rod 16 of the fluid pressure cylinder 15 faces the inside of the tapered cylinder 8 through the opening of the top wall 2, and the end of the rod 16 is attached with the powder pressing member 12.
【0009】前記筒状本体7の下部には粉粒体出口3よ
り大径の囲い筒19が設けられ、この囲い筒19に所要
個のブラケット20が設けられ、これらブラケット20
に回転軸21が回転自在に嵌められ、この回転軸21に
接続片22を介して開閉蓋11が固定されている。前記
回転軸21の一端は囲い筒19を貫通して外部に露出し
ており、この露出端部にアーム(図示略)が固定され、
このアームを公知の作動装置(図示略)によって揺動さ
せることにより、開閉蓋11は回転軸21を中心として
揺動開閉自在となされている。At the lower part of the cylindrical body 7, an enclosure 19 having a diameter larger than the granular material outlet 3 is provided, and the enclosure 19 is provided with a required number of brackets 20.
A rotating shaft 21 is rotatably fitted to the rotating shaft 21, and the opening / closing lid 11 is fixed to the rotating shaft 21 via a connecting piece 22. One end of the rotating shaft 21 is exposed to the outside through the surrounding tube 19, and an arm (not shown) is fixed to the exposed end.
By swinging the arm by a known actuator (not shown), the opening / closing lid 11 can swing open and close about the rotation shaft 21.
【0010】[0010]
【発明の実施の形態の作用】次に発明の実施の形態の作
用を説明する。粉粒体入口4に軽量の粉粒体が貯留され
た粉粒体貯留源(気体入口を有するもの)を接続すると
共に、気体出口5に気体吸引装置(図示略)の吸引口を
接続し、このような準備の後、開閉蓋11によって粉粒
体出口3を閉じた後、気体吸引装置(図示略)を作動す
れば以下の作用が行なわれる。粉粒体捕集器1内が負圧
となるので、粉粒体入口4から気体と共に軽量の粉粒体
が粉粒体捕集器1内に流入し、気体は気体出口5から出
て行く。そして、軽量の粉粒体は下から上に向かう気体
の流れによってテーパー筒8の上部に舞い上げられ、そ
こで相互に密着状態となって、テーパー筒8の上部から
順次下に向かって蓄積されていく。そして、軽量の粉粒
体が粉粒体入口4より上の所定位置まで溜ると、気体吸
引装置(図示略)を停止させた後、開閉蓋11を開き、
その後、粉粒体押下具12を押し下げて溜った軽量の粉
粒体を下側に押すことによって、テーパー筒8内の軽量
の粉粒体を粉粒体出口3より排出する。Next, the operation of the embodiment of the present invention will be described. A powder material storage source (having a gas inlet) in which light-weight particles are stored is connected to the powder material inlet 4, and a suction port of a gas suction device (not shown) is connected to the gas outlet 5; After such preparation, after closing the granular material outlet 3 with the opening / closing lid 11, if the gas suction device (not shown) is operated, the following operation is performed. Since the inside of the particulate material collector 1 has a negative pressure, a light-weight particulate material flows into the particulate material collector 1 together with the gas from the particulate material inlet 4, and the gas exits from the gas outlet 5. . Then, the light-weight powder particles are sowed to the upper portion of the tapered tube 8 by the gas flow from the bottom to the top, where they are in close contact with each other, and are sequentially accumulated downward from the upper portion of the tapered tube 8. Go. Then, when the light-weight powder particles accumulate to a predetermined position above the powder-particle inlet 4, the gas suction device (not shown) is stopped, and then the opening / closing lid 11 is opened.
Thereafter, the light and granular material in the tapered cylinder 8 is discharged from the granular material outlet 3 by pushing down the granular material pressing tool 12 and pushing the accumulated light and granular material downward.
【0011】[0011]
【変形例等】以下に変形例等について説明を加える。 (1)粉粒体には、粉体・粒体・微小薄片・短繊維片等
が含まれる。 (2)開閉蓋11は水平動するシャッターのようなもの
であってよい。 (3)フィルターは、要するに設定の大きさの粉粒体の
通過は許容せず気体の通過は許容するものであればよ
い。即ち、フィルターには多孔板や網も含まれるもので
ある。 (4)筒状本体7及びテーパー筒8の水平断面は一般的
には円形であるが、それに限定されず、例えば矩形であ
ってもよい。 (5)開閉蓋11及び粉粒体押下具12の作動装置は公
知の任意のものを使用することが出来る。[Modifications and the like] Modifications and the like will be described below. (1) The powders and granules include powders, granules, minute flakes, short fiber pieces and the like. (2) The opening / closing lid 11 may be like a shutter that moves horizontally. (3) The filter may be any filter as long as it does not allow the passage of the granular material having the set size and allows the passage of the gas. That is, the filter includes a perforated plate and a net. (4) The horizontal cross section of the cylindrical main body 7 and the tapered cylinder 8 is generally circular, but is not limited thereto, and may be, for example, rectangular. (5) Any known device for operating the opening / closing lid 11 and the granular material pressing tool 12 can be used.
【図1】本発明の実施の形態を示す要部断面図である。FIG. 1 is a cross-sectional view of a main part showing an embodiment of the present invention.
1 粉粒体捕集器 2 頂壁 3 粉粒体出口 4 粉粒体入口 5 気体出口 7 筒状本体 8 テーパー筒 11 開閉蓋 12 粉粒体押下具 DESCRIPTION OF SYMBOLS 1 Granular material collector 2 Top wall 3 Granular material outlet 4 Granular material inlet 5 Gas outlet 7 Cylindrical main body 8 Tapered cylinder 11 Opening / closing lid 12 Granular material pressing tool
Claims (1)
口となされると共に、側周壁の下部に粉粒体入口が形成
され、側周壁の上部又は頂壁に気体出口が形成された筒
状本体と、この筒状本体内に気体出口を粉粒体入口及び
粉粒体出口と画するようにして設けられた、設定の大き
さの粉粒体の通過は許容せず気体の通過は許容するフィ
ルターからなる下方拡がりのテーパー筒と、筒状本体の
粉粒体出口に設けられた開閉蓋と、テーパー筒内におい
て上下動自在となされた粉粒体押下具とを有しており、
気体の流れによって粉粒体を粉粒体入口よりテーパー筒
内に導入し、気体を気体出口より排出するようにした粉
粒体捕集器。1. An upper portion having a top wall, a lower portion serving as a powder outlet, a powder inlet being formed at a lower portion of a side peripheral wall, and a gas outlet being formed at an upper portion or a top wall of the side peripheral wall. A cylindrical body, and a gas outlet provided in the cylindrical body so as to define a gas outlet as a powder inlet and a powder outlet, and gas passing through a set size is not allowed. Has a downwardly expanding tapered cylinder made of a filter that allows passage, an opening / closing lid provided at the powder / particle outlet of the cylindrical main body, and a powder / granule pressing tool that is vertically movable within the tapered cylinder. And
A powder / particle collector in which powder is introduced into a tapered cylinder from a powder inlet by a gas flow, and gas is discharged from a gas outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15606299A JP4309513B2 (en) | 1999-06-03 | 1999-06-03 | Powder collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15606299A JP4309513B2 (en) | 1999-06-03 | 1999-06-03 | Powder collector |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000344348A true JP2000344348A (en) | 2000-12-12 |
| JP4309513B2 JP4309513B2 (en) | 2009-08-05 |
Family
ID=15619483
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15606299A Expired - Fee Related JP4309513B2 (en) | 1999-06-03 | 1999-06-03 | Powder collector |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4309513B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100840119B1 (en) | 2006-10-24 | 2008-06-19 | 주식회사 케이.알.티 | Suction nozzle for conveying powder slag |
| CN101844684A (en) * | 2010-03-10 | 2010-09-29 | 山东科技大学 | Mining pneumatic car unloader |
| CN106370484A (en) * | 2016-10-13 | 2017-02-01 | 苏州阿洛斯环境发生器有限公司 | Synthetic jet device, portable miniature particulate matter sampling apparatus and trapping method |
| CN108126898A (en) * | 2017-11-30 | 2018-06-08 | 湘潭大学 | A kind of filtering type powder classification device and stage division according to underbalance effect |
| JP2020015004A (en) * | 2018-07-26 | 2020-01-30 | 株式会社松井製作所 | Apparatus for collecting granular material and method for collecting granular material |
| JP2020132417A (en) * | 2019-02-26 | 2020-08-31 | 株式会社松井製作所 | Collection device of granule material |
-
1999
- 1999-06-03 JP JP15606299A patent/JP4309513B2/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100840119B1 (en) | 2006-10-24 | 2008-06-19 | 주식회사 케이.알.티 | Suction nozzle for conveying powder slag |
| CN101844684A (en) * | 2010-03-10 | 2010-09-29 | 山东科技大学 | Mining pneumatic car unloader |
| CN106370484A (en) * | 2016-10-13 | 2017-02-01 | 苏州阿洛斯环境发生器有限公司 | Synthetic jet device, portable miniature particulate matter sampling apparatus and trapping method |
| CN108126898A (en) * | 2017-11-30 | 2018-06-08 | 湘潭大学 | A kind of filtering type powder classification device and stage division according to underbalance effect |
| JP2020015004A (en) * | 2018-07-26 | 2020-01-30 | 株式会社松井製作所 | Apparatus for collecting granular material and method for collecting granular material |
| JP7112722B2 (en) | 2018-07-26 | 2022-08-04 | 株式会社松井製作所 | Granular material collecting device and granular material collecting method |
| JP2020132417A (en) * | 2019-02-26 | 2020-08-31 | 株式会社松井製作所 | Collection device of granule material |
| JP7197907B2 (en) | 2019-02-26 | 2022-12-28 | 株式会社松井製作所 | Collecting device for granular material |
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