JPH0127934B2 - - Google Patents
Info
- Publication number
- JPH0127934B2 JPH0127934B2 JP56199747A JP19974781A JPH0127934B2 JP H0127934 B2 JPH0127934 B2 JP H0127934B2 JP 56199747 A JP56199747 A JP 56199747A JP 19974781 A JP19974781 A JP 19974781A JP H0127934 B2 JPH0127934 B2 JP H0127934B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- ventilation member
- housing
- port
- dampers
- 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
Links
Landscapes
- Air Transport Of Granular Materials (AREA)
- Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Description
【発明の詳細な説明】
本発明は粉粒体の減容装置に関するものであ
り、粉粒体(以下単に原料という)中に存在して
いる空気のみを脱気し、これによつて当該原料の
容積を減少させることを目的とするものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a volume reduction device for powder and granular materials, which deaerates only the air present in the powder and granular materials (hereinafter simply referred to as raw materials), thereby reducing the volume of the raw materials. The purpose is to reduce the volume of
以下、本発明を実施例において説明する。第1
図において、1はハウジングで上部には原料の供
給口7が、下部には製品の排出口8が設けられて
いる。そして、供給口7上部には短管10が具備
され、該短管10を介し図示省略のホツパの他、
サイクロン、バツグフイルター等の下部に設けら
れた粉粒体の貯留部が連結されるが、該短管10
に換え必要によりスクリユーフイーダ、その他供
給機が接続されてもよい。他方、排出口8には包
袋17が付設されるが必要により包袋17に換え
てスクリユーフイーダやロータリーバルブ等を介
し次工程の装置との連結が可能である。また、ハ
ウジング1内には前記供給口7と排出口8とを連
通させて筒状の通気部材4が配設されており、該
通気部材4を以つてハウジング1内を減容室3と
脱気室2とに区画している。つまり、通気部材4
の内部は減容室3としてその上部及び底部にはコ
ンプレツサ及び真空ポンプ等の圧力空気源12に
連結され時限装置11によつて制御操作されるダ
ンパー5,6がそれぞれに配設されており、他方
通気部材4の外周部空間は脱気室2としてハウジ
ング1側に排気口9を配設させ、該排気口9を前
記圧力空気源12の吸入側に連結させている。な
お、吸気用にはブロアーを使用してもよく、また
ダンパー5,6の作動部材としてエアシリンダ1
3,14が組込まれ前記空気源12に接続される
が、特にこれに限定されるものではなく、エアシ
リンダに替えて油シリンダや電動シリンダを使用
する構成であつてもよい。15,16は電磁弁で
あり、電磁弁15は排気口9と圧力空気源12の
吸入側とを接続する管20に付設され、電磁弁1
6は管20と管18とを接続する管26に配設さ
れている。これら電磁弁15,16は前記時限装
置11と接続され、該時限装置11の操作によつ
て管20内の空気流を間欠的に停止、あるいは逆
流させ、これによつて前記通気部材4の洗浄を行
わせる構成となつている。なお、第1図で示す通
気部材4で包囲された減容室3は下方排出口9に
向つて大径とし、すなわち通気部材4による内壁
面25が下方に向つて拡がる勾配をもたせること
によつて原料減容塊の排出時の離型を容易にする
ことが出来る。このように本実施例は上部供給口
7と下部排出口8とを有するハウジング1内にこ
れら供給口7と排出口8とを連通させて配設した
筒状の通気部材4を以つて該通気部材4に包囲さ
れた内部を減容室3とし、外周部を脱気室2とし
て区画させ、減容室3上部及び底部にダンパー
5,6を、脱気室2側に排気口9を具備させ、そ
れぞれを圧力空気源12の排出側及び吸入側に連
通させ、これらを時限装置11によつて操作制御
させるものであり、原料の供給から脱気、排出及
び排出後の通気部材4の目詰り除去のための逆圧
洗浄に至る一貫した工程によつて原料の容積を減
少させる装置である。第2図は、これらの工程を
示す説明図であり、aは供給、bは脱気、cは排
出、dは洗浄を表わすもので、aは減容室3上下
部の両ダンパー5,6が閉じた状態から上部ダン
パー5のみが開き、減容室3内に原料Pが送り込
まれる状態であり、次にbにおいては上部ダンパ
ー5が再び閉じられ、それと同時に開始される吸
気によつて減容室3内の空気は吸引脱気される
が、この時原料P中に存在する空気も共に排出さ
れるため該原料Pの減容が計られるわけである。
なお、この吸気の時期についてはa図の状態、つ
まり供給と共に行なわれていてもよい。次にcは
所定の脱気がなされた後に下部ダンパー6のみが
開き原料Pを落下排出させている状態であり、こ
の時には吸気は停止されている。そして、dは前
記吸気に換えて逆に圧力空気を送り原料減容塊の
離型を容易にし、また通気部材4の目詰り解消の
ための洗浄を行わせる。また、この時は上部ダン
パー5は閉じられ下部ダンパー6は開いており、
原料減容塊の排出後、下部ダンパー6は閉じられ
上部ダンパー5が開かれaの供給の状態へと還り
前述の工程が順次繰り返されるわけである。ま
た、他の実施例としてはハウジング1を複数個並
列に配置させ、あるいは第3図及び第4図に示す
ようにハウジング1a,1b,1c,1dを集合
させ、前記ダンパー5,6に換えて共通する二つ
の回転仕切盤21,22を配設させて構成するこ
とも可能で、それぞれのハウジング1a,1b,
1c,1dの位置(1a,1b,1c,1dの各
位置はそれぞれ供給、脱気、排出洗浄、完了の状
態を示す。)に該仕切盤21,22を順次回転移
動させていくことによつて原料を連続的に減容処
理することができる。なお、仕切盤21,22と
ハウジング1a,1b,1c,1dとは、仕切盤
21,22側を固定しハウジング1a,1b,1
c,1dを回転する形成のものであつてもよく、
さらに、仕切盤21,22に対しては、その表面
に通気性材料23を張り、かつ、該仕切盤21,
22の内部に前記圧力空気源12と連通する気体
の通路24を形成させ、該仕切盤21,22から
も脱気させることも可能である。 The present invention will be explained below with reference to Examples. 1st
In the figure, reference numeral 1 denotes a housing, with a raw material supply port 7 provided at the top and a product discharge port 8 provided at the bottom. A short pipe 10 is provided above the supply port 7, and a hopper (not shown) is passed through the short pipe 10.
A storage section for powder and granular material provided at the bottom of a cyclone, bag filter, etc. is connected to the short pipe 10.
Alternatively, a screw feeder or other feeder may be connected as necessary. On the other hand, a packaging bag 17 is attached to the discharge port 8, but if necessary, it can be connected to a device for the next process via a screw feeder, rotary valve, etc. in place of the packaging bag 17. Further, a cylindrical ventilation member 4 is disposed in the housing 1 so that the supply port 7 and the discharge port 8 communicate with each other. It is divided into two air chambers. In other words, the ventilation member 4
The inside of the chamber is a volume reduction chamber 3, and dampers 5 and 6 connected to a pressure air source 12 such as a compressor and a vacuum pump and controlled by a timer 11 are arranged at the top and bottom of the chamber, respectively. On the other hand, the outer circumferential space of the ventilation member 4 serves as a deaeration chamber 2, and an exhaust port 9 is disposed on the housing 1 side, and the exhaust port 9 is connected to the suction side of the pressurized air source 12. Note that a blower may be used for intake, and the air cylinder 1 may be used as an operating member for the dampers 5 and 6.
3 and 14 are incorporated and connected to the air source 12, but the invention is not particularly limited to this, and an oil cylinder or an electric cylinder may be used instead of the air cylinder. 15 and 16 are solenoid valves; the solenoid valve 15 is attached to a pipe 20 connecting the exhaust port 9 and the suction side of the pressure air source 12;
6 is disposed in a pipe 26 that connects the pipe 20 and the pipe 18. These electromagnetic valves 15 and 16 are connected to the timer 11, and when the timer 11 is operated, the air flow in the pipe 20 is intermittently stopped or reversed, thereby cleaning the ventilation member 4. The structure is such that this is done. The volume reduction chamber 3 surrounded by the ventilation member 4 shown in FIG. This makes it easier to release the volume-reduced lump of raw material from the mold. In this way, this embodiment uses the cylindrical ventilation member 4 disposed in the housing 1 having the upper supply port 7 and the lower discharge port 8 so that the supply port 7 and the discharge port 8 communicate with each other. The interior surrounded by the member 4 is defined as a volume reduction chamber 3, the outer peripheral part is divided as a deaeration chamber 2, dampers 5 and 6 are provided at the top and bottom of the volume reduction chamber 3, and an exhaust port 9 is provided on the deaeration chamber 2 side. These are connected to the discharge side and the suction side of the pressurized air source 12, and these are operated and controlled by the timer 11, which controls the supply of raw materials, deaeration, discharge, and the ventilation member 4 after discharge. This is a device that reduces the volume of raw materials through a consistent process that includes back pressure washing to remove blockages. FIG. 2 is an explanatory diagram showing these steps, where a represents supply, b degassing, c discharge, and d cleaning, where a represents both dampers 5 and 6 at the upper and lower parts of the volume reduction chamber 3. From the closed state, only the upper damper 5 opens and the raw material P is fed into the volume reduction chamber 3. Next, in b, the upper damper 5 is closed again and the volume is reduced by the intake air that starts at the same time. The air in the container chamber 3 is suctioned and degassed, but at this time, the air present in the raw material P is also exhausted, so that the volume of the raw material P is reduced.
Note that the timing of this intake may be in the state shown in Figure a, that is, it may be performed at the same time as the supply. Next, c is a state in which only the lower damper 6 is opened and the raw material P is dropped and discharged after a predetermined amount of degassing has been performed, and at this time the intake of air is stopped. Then, in d, compressed air is sent instead of the above-mentioned suction to facilitate release of the volume-reduced mass of the raw material and to clean the ventilation member 4 to eliminate clogging. Also, at this time, the upper damper 5 is closed and the lower damper 6 is open.
After the volume-reduced mass of raw material is discharged, the lower damper 6 is closed and the upper damper 5 is opened to return to the supply state of a, and the above-mentioned steps are sequentially repeated. Further, as another embodiment, a plurality of housings 1 may be arranged in parallel, or housings 1a, 1b, 1c, and 1d may be assembled as shown in FIGS. 3 and 4, and the dampers 5 and 6 may be replaced with It is also possible to arrange two common rotary partition boards 21 and 22, and the respective housings 1a, 1b,
By sequentially rotating and moving the partition plates 21 and 22 to positions 1c and 1d (positions 1a, 1b, 1c, and 1d indicate the states of supply, deaeration, discharge cleaning, and completion, respectively). The raw material can be subjected to continuous volume reduction treatment. Note that the partition boards 21, 22 and the housings 1a, 1b, 1c, 1d are fixed on the partition boards 21, 22 side, and the housings 1a, 1b, 1
It may be formed by rotating c and 1d,
Furthermore, the surfaces of the partition boards 21 and 22 are covered with a breathable material 23, and the partition boards 21 and 22 are covered with breathable material 23.
It is also possible to form a gas passage 24 communicating with the pressurized air source 12 inside the pressure air source 22, and to also degas from the partition panels 21 and 22.
このように本発明は、供給、脱気、排出、洗浄
の各工程を循環、かつ連続的に行わせることによ
り、きわめて効率よい粉粒体の減容が行え、また
減容度合いの調節も排気圧力の加減調節のほか時
限装置11によるダンパー5,6及び電磁弁1
5,16の開度調節によつて容易に行なえ粉粒体
の性状に合わせた減容が可能である。しかも、簡
潔な構造であるため当該装置自体の保守面におい
て有利であるほか、他の装置との接続も容易であ
るなど本発明の効果は顕著である。 In this way, the present invention allows extremely efficient volume reduction of powder and granular material by circulating and continuously performing each process of supply, deaeration, discharge, and washing, and the degree of volume reduction can also be adjusted by exhaust gas. In addition to adjusting the pressure, dampers 5 and 6 and a solenoid valve 1 by a timer 11
By adjusting the opening of 5 and 16, it is possible to easily reduce the volume according to the properties of the powder or granular material. Moreover, since the structure is simple, it is advantageous in terms of maintenance of the device itself, and it is also easy to connect to other devices, so the effects of the present invention are remarkable.
第1図は本発明の実施例を示す要部断面図、第
2図は本実施例の作用説明図、第3図は他の実施
例、第4図は第3図A−A′断面視図、第5図は
仕切盤21,22の別の実施例である。
図において、1……ハウジング、2……脱気
室、3……減容室、4……通気部材、5……ダン
パー、6……ダンパー、7……供給口、8……排
出口、9……排気口、11……時限装置、12…
…圧力空気源である。
Fig. 1 is a sectional view of essential parts showing an embodiment of the present invention, Fig. 2 is an explanatory diagram of the operation of this embodiment, Fig. 3 is another embodiment, and Fig. 4 is a sectional view taken along the line A-A' in Fig. 3. FIG. 5 shows another embodiment of the partition panels 21, 22. In the figure, 1...housing, 2...deaeration chamber, 3...volume reduction chamber, 4...ventilation member, 5...damper, 6...damper, 7...supply port, 8...discharge port, 9...Exhaust port, 11...Timer, 12...
...is a source of pressurized air.
Claims (1)
ジング1内に、これら供給口7と排出口8とを共
有する筒状の通気部材4を設け、供給口7及び排
出口8にダンパ5,6を設けてハウジング1内及
び通気部材4内を密閉構造とし、ハウジング1外
周部に設けた排気口9を圧力空気源12の吸入側
と管20で接続すると共に、圧力空気源12の排
出管18と前記管20とを接続する管26を設
け、これら管20,26に具備させた弁15,1
6及びダンパ5,6を時限装置11に接続させて
構成したことを特徴とする粉粒体の減容装置。 2 前記通気部材4は、その内壁面25が下方に
向かつて拡大する形状を有する請求項1記載の粉
粒体の減容装置。[Scope of Claims] 1. A cylindrical ventilation member 4 that shares the supply port 7 and the discharge port 8 is provided in the housing 1 having an upper supply port 7 and a lower discharge port 8. Dampers 5 and 6 are provided at the outlet 8 to create a sealed structure inside the housing 1 and the ventilation member 4, and an exhaust port 9 provided on the outer periphery of the housing 1 is connected to the suction side of the pressure air source 12 through a pipe 20, and the pressure A pipe 26 is provided to connect the discharge pipe 18 of the air source 12 and the pipe 20, and valves 15, 1 are provided on these pipes 20, 26.
6 and dampers 5 and 6 are connected to a timer 11. 2. The granular material volume reduction device according to claim 1, wherein the ventilation member 4 has an inner wall surface 25 that expands downward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19974781A JPS58101724A (en) | 1981-12-10 | 1981-12-10 | Volume reducing device for powder and granule |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19974781A JPS58101724A (en) | 1981-12-10 | 1981-12-10 | Volume reducing device for powder and granule |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58101724A JPS58101724A (en) | 1983-06-17 |
| JPH0127934B2 true JPH0127934B2 (en) | 1989-05-31 |
Family
ID=16412953
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19974781A Granted JPS58101724A (en) | 1981-12-10 | 1981-12-10 | Volume reducing device for powder and granule |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58101724A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07102891B2 (en) * | 1986-09-15 | 1995-11-08 | 株式会社松井製作所 | Suction-type pneumatic transportation method and device |
| JP4528416B2 (en) * | 2000-05-09 | 2010-08-18 | 本田技研工業株式会社 | Powder paint supply device |
| JP4190215B2 (en) * | 2002-06-13 | 2008-12-03 | ツカサ工業株式会社 | Deaerator |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS50136775A (en) * | 1974-04-17 | 1975-10-30 | ||
| DE2625734A1 (en) * | 1976-06-09 | 1977-12-22 | Motan Gmbh | SEPARATOR FOR SUCTION CONVEYORS, IN PARTICULAR FOR POWDER-LIKE TRANSPORTED GOODS |
-
1981
- 1981-12-10 JP JP19974781A patent/JPS58101724A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58101724A (en) | 1983-06-17 |
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