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JP4564153B2 - Powder feeder - Google Patents
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JP4564153B2 - Powder feeder - Google Patents

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JP4564153B2
JP4564153B2 JP2000298774A JP2000298774A JP4564153B2 JP 4564153 B2 JP4564153 B2 JP 4564153B2 JP 2000298774 A JP2000298774 A JP 2000298774A JP 2000298774 A JP2000298774 A JP 2000298774A JP 4564153 B2 JP4564153 B2 JP 4564153B2
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powder
discharge port
air
storage tank
nozzle
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JP2002104655A (en
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忠男 餌取
久美子 大澤
恒美 林
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赤武エンジニアリング株式会社
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Description

【0001】
【発明の属する技術分野】
本発明は、粉体供給装置、さらに詳しくは、複数個の計量室を備える回転テーブルを利用して、粉体貯槽内の粉体を、連続的にかつ定量的に空気輸送管路に供給する粉体供給装置に関する。
【0002】
【従来の技術】
複数個の計量室を備える回転テーブルにより、粉体貯槽内の粉体を、連続的にかつ定量的に空気輸送管路に供給する粉体供給装置の一つの典型例は、空気輸送管路に開口する排出口が形成された粉体貯槽と、粉体貯槽内に回転自在に配設され外周部の周方向に粉体を導入し排出口に排出するための複数個の計量室が形成された回転テーブルとを備えている。電動モータにより回転テーブルが回転駆動されると、計量室の各々は、粉体が導入される導入部、粉体が排出口に排出される排出部、並びに排出口の回転方向前後に形成され計量室が閉塞される前側閉塞部及び後側閉塞部を通して移動される。
【0003】
導入部において計量室に導入された粉体は、導入部に続く前側閉塞部において計量室が閉塞され計量室の容積に規定され計量される。続く排出部に計量室が移動すると、計量室の閉塞は解除され、粉体は排出口を通して空気輸送管路に排出される。排出された粉体は、空気輸送管路を流れる圧力空気により所定の場所に送られる。
【0004】
排出部において粉体の排出された空の計量室は、続く後側閉塞部に通され閉塞される。この閉塞された計量室の中には、排出部において連通する空気輸送管路の圧力空気が流入している(以後、この計量室に流入した圧力空気を置換空気、あるいは置換圧力空気と呼ぶことがある)。後側閉塞部を通過した計量室は、再び粉体貯槽内の導入部に移動し、空の計量室には粉体貯槽内の粉体が再び導入される。
【0005】
かくして、回転テーブルの計量室の容積、回転数、などを規定することにより、粉体は連続的にかつ定量的に空気輸送管路に供給される。
【0006】
上述のように構成された粉体供給装置において、粉体の排出口の前後に形成された閉塞部は、計量室を閉塞し粉体を計量する目的の他に、重要な役目を有している。すなわち、前側閉塞部及び後側閉塞部の閉塞された計量室によって、排出口の開口した空気輸送管路を流れる圧力空気が、粉体貯槽の中に流れ込むのが阻止されている。空気輸送管路の圧力空気が粉体貯槽の中に多量に漏れてしまうと、粉体の適切な空気輸送が不可能になる。したがって、計量室を閉塞するための手段である計量室の開口部に摺接される、例えばすり切り板、底壁などと、計量室とのすき間は極力小さくし、圧力空気の漏れをできるだけ回避することが重要である。
【0007】
【発明が解決しようとする課題】
しかしながら、上述したとおりの形態の従来の粉体供給装置には、次のとおりの解決すべき問題がある。
【0008】
すなわち、計量室とこれに摺接するすり切り板、底壁などとのすき間を極限までに小さくしても、粉体の排出された計量室の中に入った置換圧力空気は、計量室が後側閉塞部から粉体の導入部に移動し、計量室の閉塞が解除されると、粉体貯槽の粉体の中に放出され、吹き上がる。このように、粉体貯槽内への圧力空気の流出は、計量室とそれに摺接するすり切り板、底壁などとのすき間からだけでなく、回転テーブルが回転し計量室が後側閉塞部から粉体の導入部に移動すると必ず発生し、回避することができない。さらに、粉体の輸送先が遠方や高所になると、また粉体の質量が大きくなると、輸送管路を流れる圧力空気の圧力は必然的に大きくなり、粉体貯槽の中へ放出される空気の量、そして吹き上げも、より大きなものになる。
【0009】
そして、粉体貯槽の中に放出される圧力空気が、粉体の中を通り、外部に放出されることにより、
(1)粉体を吹き上げ粉塵を発生させる、
(2)粉体に空気が混入し粉体のかさ密度(単位容積当たりの粉体の重量)が小さくなり、計量室に導入される粉体の量が少なくなって定量性が保持できなくなる、などの問題が発生する。
【0010】
本発明は上記事実に鑑みてなされたもので、その主たる技術的課題は、複数個の計量室を備える回転テーブルを利用して、粉体を連続的にかつ定量的に空気輸送管路に供給する粉体供給装置において、粉体を排出し空になった計量室を介し粉体貯槽の中に粉体輸送管路の圧力空気が流れ込むのを防止することができるようにした、粉体供給装置を提供することである。
【0011】
【課題を解決するための手段】
本発明においては、上記技術的課題を解決する粉体供給装置として、空気輸送管路に開口する排出口が形成された粉体貯槽と、該粉体貯槽内に回転自在に配設され外周部の周方向に粉体を導入し該排出口に排出するための複数個の計量室が形成された回転テーブルと、該回転テーブルの回転方向における該排出口の前後に形成され計量室を閉塞し粉体貯槽と排出口との間を閉塞させる前側閉塞部及び後側閉塞部と、該排出口の開口する部分に形成され該空気輸送管路の圧力空気が流されることにより排出された粉体が吸引されるエゼクタとを備え、該エゼクタは、該粉体貯槽の該排出口の開口する部分に形成された該空気輸送管路の一部を構成する円筒状のエゼクタ設置部に設けられ、該圧力空気を高速度で噴射させるノズルと、その下流に設けられ漸次に流路を拡大させるディフューザとを備え、該排出口は該ノズルとディフューザとの間に連通し、該計量室は、該排出口において該円筒状のエゼクタ設置部の中に位置している、ことを特徴とする粉体供給装置が提供される。
【0012】
本発明による粉体供給装置においては、粉体が排出される排出口の部分に吸引作用を有するエゼクタを備えている。そして、排出口の部分の圧力がエゼクタの吸引作用により低くなるので、空になった計量室に流入する置換空気の圧力は低くなり、粉体貯槽の中に圧力空気の流れ込むのが防止される。したがって、従来の、粉体が吹き上げられ粉塵が発生する、粉体のかさ密度が小さくなり粉体の定量性が保持できなくなる、などの問題が解消される。
【0014】
そして、空気輸送管路の圧力空気は、ノズルから噴射された部分で静圧が下げられ排出された粉体を吸引するとともに計量室の置換空気の圧力を低くし、ディフューザを通されることによって静圧は再度上昇される。
【0015】
他の実施形態においては、該排出口に位置する計量室に向け圧力空気を噴射する排出ノズルを備えている。また、該排出ノズルには、該空気輸送管路の該エゼクタより上流側を分岐して取り出された圧力空気が流される。
【0016】
そして、排出ノズルの噴射圧力空気により、計量室の粉体を、容易に、完全に排出させる。また、空気輸送管路の圧力空気を分岐して排出ノズルに流し、圧力空気回路を別途設けることなく排出ノズルを設置できるようにする。
【0017】
【発明の実施の形態】
以下、本発明に従って構成された粉体供給装置の好適実施形態を図示している添付図面を参照して、さらに詳細に説明する。
【0018】
図1及び図2を参照して説明すると、図示の粉体供給装置は、空気輸送管路2に開口する排出口4が形成された粉体貯槽6と、粉体貯槽6内に回転自在に配設され外周部の周方向に粉体を導入し排出口4に排出するための上開口8a及び下開口8bを有する複数個の計量室8が形成された回転テーブル10とを備えている。排出口4が開口する空気輸送管路2の部分には、空気輸送管路2を流れる圧力空気が通されることにより吸引作用を有するエゼクタ12が備えられている。
【0019】
計量室8の各々は、回転テーブル10が矢印R(図2)で示す方向に回転されると、符号Xで示す粉体が導入される導入部及び符号Yで示す排出口4に排出される排出部を通って移動される。導入部X及び排出部Yにおいては、上開口8a及び下開口8bは開口されている。回転方向Rにおける排出部Yの前後には、少なくとも一個以上の計量室8の上開口8a及び下開口8bが閉塞される符号Z1で示す前側閉塞部及び符号Z2で示す後側閉塞部が形成されている。
【0020】
粉体貯槽6は、円板状の底壁14及び底壁14の周縁部から上方に延びる円筒状の周壁16を備えている。周壁16の一部には、空気輸送管路2の一部を構成し上下方向に延びる円筒状のエクタ設置部18が設けられている。粉体の排出口4はこのエクタ設置部18に開口している。底壁14は、円筒状の支持フレーム20上に取付けられている。支持フレーム20には、上下方向に延びる回転軸22が回転自在に支持され、その一端部(上端部)は、底壁14を貫通し粉体貯槽6の中に突出するように位置付けられている。回転軸22と底壁14との間には、それ自体周知のもので構成することができる軸受・シール手段24が介在されている。回転テーブル10は、回転軸24の上端部に固定されている。回転軸22の他端部(下端部)は、支持フレーム20の下端に取付けられた電動モータ26に連結されている。
【0021】
回転テーブル10は、円板状の本体部28と、本体部28の外周部に周方向に所定の間隔で放射状に立設された複数個の仕切板30とを備えている。この隣り合った一対の仕切板30、30が、粉体貯槽6の周壁16の内面と協働して、上開口8a及び下開口8bを有する計量室8を規定している。本体部28の中央には、回転軸22に固定されるボス32が形成されている。ボス32にはまた、粉体貯槽6内の粉体を攪拌させるための攪拌翼34が周方向に等間隔を置いて四個固定されている。
【0022】
計量室8の上開口8a及び下開口8bは、前側閉塞部Z1及び後側閉塞部Z2において、上開口8aは周壁16の内面に設けられたすり切り板36に摺接し、下開口8bは底壁14の一部に摺接しそれぞれ閉塞されている。すり切り板36は、円周方向に配設された計量室8を閉塞する幅に板部材を弧状に切断して形成されている。
【0023】
エゼクタ12は、圧力空気を高速度で噴射させる漸次に流路が縮小されたノズル38と、その下流に設けられ漸次に流路が拡大されたディフューザ40とを備えている。ノズル38は、エクタ設置部18の上端を閉じる蓋39に貫通して固定され、ディフューザ40は、エクタ設置部18の下端を閉じる蓋41に貫通して固定されている。ノズル38とディフューザ40の間のディフューザ40の入口側には、エクタ設置部18の内面とを結ぶテーパ部42が設けられている。エゼクタ12は、そのエゼクタ効果により、ノズル38から高速度で噴射された圧力空気の周囲の静圧が下げられる吸引作用を有し、噴射された空気は、ディフューザ40を通されるとその特性によって静圧が再度上昇される。
【0024】
空気輸送管路2は、圧力空気源としての、例えばルーツブロワ46に接続されている。ルーツブロワ46から吐出された圧力空気は、先ずエゼクタ12のノズル38側に流入し、ノズル38から噴出された圧力空気は、それに続くテーパ部42において粉体貯槽6の排出口4から排出され粉体と一緒になり、ディフューザ41を通り、粉体とともに粉体の供給先(図示していない)に流される。
【0025】
図3を参照して粉体供給装置の他の実施形態について説明する。この形態における粉体供給装置は、排出口4に位置する計量室8に向けて圧力空気を噴射する排出ノズル50を、エクタ設置部18の中に備えている。この排出ノズル50は、計量室8に向け圧力空気を噴射するものであるので、空気輸送管路2に設けられたエゼクタ12のノズル38に比較して格段に小径のものでよく、真直の細管によって形成されている。排出ノズル50には、空気輸送管路2のエゼクタ12の設置部分より上流側を分岐した管路52により取り出された圧力空気が流される。この管路52には、圧力空気の流れを必要により断続することができる開閉弁54が設けられている。排出ノズル50により圧力空気を、必要により、排出口4の計量室8に吹き付けることにより、計量室8内の粉体は完全に排出される。
【0026】
図1〜図3とともに図4を参照して、上述したとおりの粉体供給装置の作用を説明する。
【0027】
(1)粉体の空気輸送管路への供給:
粉体貯槽6の中に収容された粉体は、回転テーブル10が電動モータ26により矢印R方向に回転駆動されると、導入部Xにおいて計量室8の各々に、図示の形態においては主として上開口8aから導入され、回転テーブル10の回転とともに移動され、続く前側閉塞部Z1において上開口8a及び下開口8bが閉塞される計量室8によりその量が計量室8の容積に規定され計量される。計量室8が排出部Yに移動すると、上開口8a及び下開口8bの閉塞は解除され、粉体は排出口4からエゼクタ12が設けられたエゼクタ設置部18の中に排出される。排出された粉体は、エゼクタ12の作用により吸引され、ディフューザ40に流れ、圧力空気とともに粉体供給先(図示していない)に送られる。空になった計量室8には、エゼクタ12の作用により静圧の下がった低圧の空気が置換空気として流入する。置換空気の入った計量室8は、順次に後側閉塞部Z2に移動する。
後側閉塞部Z2を通過した計量室8は、導入部Xに移動し、再び粉体が導入される。
【0028】
(2)粉体貯槽内への置換圧力空気の放出防止:
粉体が排出され空になった計量室8には、上述のようにエゼクタ12の吸引作用により静圧の下がった低圧の空気が流入するので、中の空気は空気輸送管路2の圧力空気よりも格段に低圧のものになり、粉体貯槽6の粉体の中に置換空気は実質上放出されない。したがって、粉体の中への計量室8の置換空気の図4に矢印Hで示すような吹き上げは防止され、粉塵の発生、粉体に空気が混じることによる粉体のかさ密度が小さくなる、などの問題は解消される。
【0029】
(3)排出ノズル:
粉体貯槽6内に収容される粉体が付着性の強いものである場合には、排出口4において粉体が計量室8から重力により完全に自然落下するのが困難な場合がある。この場合には、図3に示す排出ノズル50につながる管路52の開閉弁54を開け、排出ノズル50によって圧力空気を計量室8に吹き付けることにより、粉体を計量室8から完全に排出させることができる。
【0030】
(4)排出ノズル:
排出ノズル50は、空気輸送管路2を分岐して圧力空気を流すようにしたので、設置が容易である。また、排出ノズル50に流れる圧力空気の量は、エゼクタ12を流れる空気の量に比べて格段に少ないので、エゼクタ12の吸引作用には影響しない。
【0031】
以上、本発明を実施の形態に基づいて詳細に説明したが、本発明は上記の実施の形態に限定されるものではなく、例えば下記のように、本発明の範囲内においてさまざまな変形あるいは修正ができるものである。
【0032】
(1)圧力空気の流れ方向:
本発明の実施の形態においては、空気輸送管路2の圧力空気の流れの方向は、排出口4の開口するエゼクタ設置部18において、上方から下方(図1参照)に流れるようにしたが、ノズル38とディフューザ40の組合せの設置形態を上下逆にして、圧力空気を下方から上方に向けて流すようにすることもできる。
【0033】
(2)排出ノズル:
本発明の実施の形態においては、排出ノズル50には空気輸送管路2を分岐した圧力空気を流したが、適宜の空気圧源の利用が好都合であれば、排出ノズル50への圧力空気源は別にしてもよい。
【0034】
【発明の効果】
本発明に従って構成された粉体供給装置によれば、複数個の計量室を備える回転テーブルを利用して、粉体を連続的にかつ定量的に空気輸送管路に供給する粉体供給装置において、粉体を排出し空になった計量室を介し粉体貯槽の中に粉体輸送管路の圧力空気が流れ込むのを防止することができるようにした、粉体供給装置が提供される。
【図面の簡単な説明】
【図1】本発明に従って構成された粉体供給装置の一実施形態を示す側面図。
【図2】図1のA−A矢印方向に見た断面図。
【図3】図2のB矢印方向に見て示した作用説明図。
【図4】図1に示す粉体供給装置に排出ノズルを備えた形態を示した側面図。
【符号の説明】
2:空気輸送管路
4:排出口
6:粉体貯槽
8:計量室
10:回転テーブル
12:エゼクタ
38:ノズル
40:ディフューザ
R:回転方向
X:導入部
Y:排出部
Z1:前側閉塞部
Z2:後側閉塞部
[0001]
BACKGROUND OF THE INVENTION
The present invention uses a powder supply device, more specifically, a rotary table having a plurality of measuring chambers, and continuously and quantitatively supplies the powder in the powder storage tank to the pneumatic transport line. The present invention relates to a powder supply apparatus.
[0002]
[Prior art]
One typical example of a powder supply device that continuously and quantitatively supplies powder in a powder storage tank to a pneumatic transport line by a rotary table having a plurality of measuring chambers is provided in the pneumatic transport line. A powder storage tank in which an opening for opening is formed, and a plurality of measuring chambers are formed that are rotatably disposed in the powder storage tank and introduce powder into the circumferential direction of the outer periphery and discharge it to the discharge outlet. And a rotating table. When the rotary table is rotationally driven by the electric motor, each of the weighing chambers is formed before and after the introduction portion for introducing the powder, the discharge portion for discharging the powder to the discharge port, and the rotation direction of the discharge port. The chamber is moved through the front closure and the rear closure where the chamber is blocked.
[0003]
The powder introduced into the measurement chamber in the introduction part is measured by being regulated in the volume of the measurement chamber by closing the measurement chamber in the front closing part following the introduction part. When the metering chamber moves to the subsequent discharge section, the blockage of the metering chamber is released, and the powder is discharged to the pneumatic transport pipe through the discharge port. The discharged powder is sent to a predetermined place by the pressure air flowing through the air transportation pipeline.
[0004]
The empty measuring chamber in which the powder is discharged in the discharge portion is passed through the subsequent rear closing portion and closed. In this closed measurement chamber, the pressure air from the air transport line communicating with the discharge portion flows (hereinafter, the pressure air flowing into the measurement chamber is referred to as replacement air or replacement pressure air). There is). The measurement chamber that has passed through the rear blocking portion moves again to the introduction portion in the powder storage tank, and the powder in the powder storage tank is again introduced into the empty measurement chamber.
[0005]
Thus, the powder is continuously and quantitatively supplied to the pneumatic transport line by defining the volume of the measuring chamber of the rotary table, the number of rotations, and the like.
[0006]
In the powder supply apparatus configured as described above, the closed portion formed before and after the powder discharge port has an important role in addition to the purpose of closing the measuring chamber and measuring the powder. Yes. That is, the measurement chamber closed by the front blocking portion and the rear blocking portion prevents the pressure air flowing through the air transport pipe having the discharge port from flowing into the powder storage tank. If a large amount of compressed air in the pneumatic transportation line leaks into the powder storage tank, proper pneumatic transportation of the powder becomes impossible. Therefore, the gap between the measuring chamber, for example, the scraping plate and the bottom wall, which is in sliding contact with the opening of the measuring chamber, which is a means for closing the measuring chamber, is made as small as possible to avoid leakage of pressure air as much as possible. This is very important.
[0007]
[Problems to be solved by the invention]
However, the conventional powder supply apparatus having the configuration as described above has the following problems to be solved.
[0008]
In other words, even if the gap between the measuring chamber and the scraper plate, bottom wall, etc. that are in sliding contact with the measuring chamber is minimized, the replacement pressure air that has entered the measuring chamber from which the powder has been discharged is When moving from the closed part to the powder introduction part and releasing the blockage of the measuring chamber, the powder is discharged into the powder in the powder storage tank and blown up. In this way, the flow of pressurized air into the powder storage tank is not only from the gap between the weighing chamber and the ground plate, bottom wall, etc. that slides in contact with it, but also the rotating table rotates and the weighing chamber is discharged from the rear blocking part. It always occurs when moving to the body introduction and cannot be avoided. In addition, when the powder is transported to a distant location or at a high location, or when the mass of the powder increases, the pressure of the pressure air flowing through the transport pipe inevitably increases, and the air released into the powder storage tank The amount, and the blow-up will be bigger.
[0009]
And, the compressed air released into the powder storage tank passes through the powder and is released to the outside.
(1) Blow up the powder to generate dust,
(2) Air is mixed into the powder, the bulk density of the powder (the weight of the powder per unit volume) is reduced, the amount of powder introduced into the measuring chamber is reduced, and quantitative properties cannot be maintained. Problems occur.
[0010]
The present invention has been made in view of the above-mentioned facts, and the main technical problem thereof is to supply powder continuously and quantitatively to the air transport pipe using a rotary table having a plurality of measuring chambers. In the powder supply device, it is possible to prevent the pressure air in the powder transport line from flowing into the powder storage tank through the measurement chamber that is emptied by discharging the powder. Is to provide a device.
[0011]
[Means for Solving the Problems]
In the present invention, as a powder supply device that solves the above technical problem, a powder storage tank in which a discharge port that opens to an air transportation pipeline is formed, and an outer peripheral portion that is rotatably disposed in the powder storage tank A rotary table formed with a plurality of weighing chambers for introducing powder into the circumferential direction and discharging it to the discharge port, and closing the measurement chamber formed before and after the discharge port in the rotation direction of the rotary table. Powder that is formed by flowing the pressure air of the air transport pipe formed in the front opening part and the rear side closing part for closing the space between the powder storage tank and the discharge port and the opening of the discharge port The ejector is provided in a cylindrical ejector installation portion that constitutes a part of the air transport pipe formed in the opening portion of the discharge port of the powder storage tank, A nozzle that injects the compressed air at a high speed, and downstream of the nozzle Vignetting and a diffuser for expanding the flow channel gradually, the discharge port communicates between the nozzle and the diffuser, the metering chamber is located within the ejector installation portion of the cylindrical shape in the discharge port A powder supply device is provided.
[0012]
In the powder supply apparatus according to the present invention, an ejector having a suction action is provided at a portion of the discharge port from which the powder is discharged. Since the pressure at the discharge port is lowered by the suction action of the ejector, the pressure of the replacement air flowing into the emptied measuring chamber is reduced, and the pressure air is prevented from flowing into the powder storage tank. . Therefore, the conventional problems such as the generation of dust when powder is blown up, the bulk density of the powder becomes small, and the quantitative property of the powder cannot be maintained are solved.
[0014]
And the pressure air of the air transportation pipeline is lowered by reducing the pressure of the replacement air in the measuring chamber while lowering the static pressure at the portion ejected from the nozzle and sucking the discharged powder, and passing through the diffuser. The static pressure is increased again.
[0015]
In another embodiment, a discharge nozzle for injecting pressurized air toward the measurement chamber located at the discharge port is provided. Further, the discharge nozzle is supplied with the pressure air taken out from the air transport pipe that is branched upstream of the ejector.
[0016]
Then, the powder in the measurement chamber is easily and completely discharged by the jet pressure air of the discharge nozzle. Further, the pressure air in the air transport pipe is branched and allowed to flow to the discharge nozzle, so that the discharge nozzle can be installed without providing a separate pressure air circuit.
[0017]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, a preferred embodiment of a powder supply apparatus constructed according to the present invention will be described in more detail with reference to the accompanying drawings.
[0018]
Referring to FIGS. 1 and 2, the illustrated powder supply apparatus includes a powder storage tank 6 in which a discharge port 4 that opens to the air transport pipe 2 is formed, and a powder storage tank 6 that is freely rotatable. And a turntable 10 having a plurality of weighing chambers 8 having an upper opening 8a and a lower opening 8b for introducing and discharging powder in the circumferential direction of the outer peripheral portion. An ejector 12 having a suction action is provided in a portion of the air transport pipe 2 where the discharge port 4 is opened, by allowing pressurized air flowing through the air transport pipe 2 to pass therethrough.
[0019]
Each of the weighing chambers 8 is discharged to the introduction part to which the powder indicated by X is introduced and the discharge port 4 indicated to Y when the rotary table 10 is rotated in the direction indicated by the arrow R (FIG. 2). Moved through the discharge section. In the introduction part X and the discharge part Y, the upper opening 8a and the lower opening 8b are opened. Before and after the discharge part Y in the rotational direction R, a front side closed part indicated by reference numeral Z1 and a rear side closed part indicated by reference numeral Z2 are formed in which the upper opening 8a and the lower opening 8b of at least one weighing chamber 8 are closed. ing.
[0020]
The powder storage tank 6 includes a disk-shaped bottom wall 14 and a cylindrical peripheral wall 16 extending upward from the peripheral edge of the bottom wall 14. The part of the peripheral wall 16 includes a cylindrical et peptidase Kuta installing portion 18 extending in the vertical direction to constitute a part of the air transport pipe 2 is provided. Outlet 4 of the powder are opened to the error zero Kuta installing portion 18. The bottom wall 14 is mounted on a cylindrical support frame 20. A rotary shaft 22 extending in the vertical direction is rotatably supported by the support frame 20, and one end (upper end) thereof is positioned so as to penetrate the bottom wall 14 and protrude into the powder storage tank 6. . Between the rotary shaft 22 and the bottom wall 14, a bearing / seal means 24, which can be constituted by a well-known one, is interposed. The rotary table 10 is fixed to the upper end portion of the rotary shaft 24. The other end (lower end) of the rotating shaft 22 is connected to an electric motor 26 attached to the lower end of the support frame 20.
[0021]
The turntable 10 includes a disk-shaped main body 28 and a plurality of partition plates 30 erected radially at predetermined intervals in the circumferential direction on the outer periphery of the main body 28. The pair of adjacent partition plates 30 and 30 cooperate with the inner surface of the peripheral wall 16 of the powder storage tank 6 to define the measuring chamber 8 having the upper opening 8a and the lower opening 8b. A boss 32 fixed to the rotary shaft 22 is formed at the center of the main body portion 28. Also, four agitating blades 34 for agitating the powder in the powder storage tank 6 are fixed to the boss 32 at equal intervals in the circumferential direction.
[0022]
The upper opening 8a and the lower opening 8b of the measuring chamber 8 are slidably contacted with a scraping plate 36 provided on the inner surface of the peripheral wall 16, and the lower opening 8b is a bottom wall in the front blocking part Z1 and the rear blocking part Z2. 14 are in sliding contact with each other and are respectively closed. The slitting plate 36 is formed by cutting a plate member into an arc shape with a width that closes the measuring chamber 8 disposed in the circumferential direction.
[0023]
The ejector 12 includes a nozzle 38 having a gradually reduced flow path for injecting pressurized air at a high speed, and a diffuser 40 provided downstream thereof and having a gradually expanded flow path. Nozzle 38 is fixed by penetrating the lid 39 closing the upper end of the d peptidase Kuta installing portion 18, the diffuser 40 closes the lower end of the d peptidase Kuta installing portion 18 is fixed through the lid 41. The inlet side of the diffuser 40 between the nozzle 38 and the diffuser 40, a tapered portion 42 connecting the inner surface of d peptidase Kuta installing portion 18 is provided. The ejector 12 has a suction action in which the static pressure around the pressurized air ejected from the nozzle 38 at a high speed is lowered by the ejector effect. When the ejected air is passed through the diffuser 40, the ejector 12 The static pressure is increased again.
[0024]
The pneumatic transport line 2 is connected to, for example, a roots blower 46 as a pressure air source. The pressure air discharged from the Roots blower 46 first flows into the nozzle 38 side of the ejector 12, and the pressure air discharged from the nozzle 38 is discharged from the discharge port 4 of the powder storage tank 6 at the subsequent tapered portion 42 and powder. Together with the powder, and flows together with the powder to a powder supply destination (not shown).
[0025]
Another embodiment of the powder supply apparatus will be described with reference to FIG. The powder supplying device in form, the discharge nozzle 50 for injecting compressed air toward the metering chamber 8 located at the outlet 4 comprises in the picture peptidase Kuta installing portion 18. Since the discharge nozzle 50 injects pressurized air toward the measuring chamber 8, the discharge nozzle 50 may be much smaller in diameter than the nozzle 38 of the ejector 12 provided in the air transport pipe 2, and is a straight thin tube. Is formed by. The discharge nozzle 50 is supplied with pressurized air taken out by a pipe 52 that branches upstream from the installation portion of the ejector 12 in the air transport pipe 2. The conduit 52 is provided with an on-off valve 54 that can interrupt the flow of pressurized air as necessary. The powder in the measurement chamber 8 is completely discharged by blowing the pressure air from the discharge nozzle 50 to the measurement chamber 8 of the discharge port 4 if necessary.
[0026]
The operation of the powder supply apparatus as described above will be described with reference to FIGS.
[0027]
(1) Supply of powder to pneumatic transportation pipeline:
When the rotary table 10 is rotationally driven in the direction of arrow R by the electric motor 26, the powder stored in the powder storage tank 6 is placed in each of the weighing chambers 8 in the introduction portion X, mainly in the illustrated form. It is introduced from the opening 8a, moved along with the rotation of the turntable 10, and the amount is regulated and measured by the measuring chamber 8 in which the upper opening 8a and the lower opening 8b are closed in the subsequent front side closing portion Z1. . When the weighing chamber 8 moves to the discharge portion Y, the upper opening 8a and the lower opening 8b are unblocked, and the powder is discharged from the discharge port 4 into the ejector installation portion 18 provided with the ejector 12. The discharged powder is sucked by the action of the ejector 12, flows into the diffuser 40, and is sent to the powder supply destination (not shown) together with the pressure air. Low-pressure air that has been reduced in static pressure by the action of the ejector 12 flows into the measuring chamber 8 that has become empty as replacement air. The measuring chamber 8 containing the replacement air sequentially moves to the rear closed portion Z2.
The measuring chamber 8 that has passed through the rear blocking portion Z2 moves to the introduction portion X, and the powder is again introduced.
[0028]
(2) Preventing the release of substitution pressure air into the powder storage tank:
Since the low-pressure air, which has been reduced in static pressure by the suction action of the ejector 12 as described above, flows into the measurement chamber 8 where the powder has been discharged and emptied, the air therein is the pressure air in the air transport pipe 2. Since the pressure is much lower than that in the powder storage tank 6, the replacement air is not substantially discharged into the powder. Therefore, blowing up of the replacement air in the measuring chamber 8 into the powder as shown by the arrow H in FIG. 4 is prevented, and the generation of dust and the bulk density of the powder due to the mixing of air with the powder are reduced. Such problems are solved.
[0029]
(3) Discharge nozzle:
When the powder stored in the powder storage tank 6 is highly adherent, it may be difficult for the powder to spontaneously fall from the weighing chamber 8 by gravity at the discharge port 4. In this case, the open / close valve 54 of the pipe line 52 connected to the discharge nozzle 50 shown in FIG. 3 is opened, and the discharge nozzle 50 blows the pressure air to the measurement chamber 8 to completely discharge the powder from the measurement chamber 8. be able to.
[0030]
(4) Discharge nozzle:
The discharge nozzle 50 is easy to install because the compressed air is made to flow by branching the air transport pipe 2. Further, the amount of pressurized air flowing through the discharge nozzle 50 is much smaller than the amount of air flowing through the ejector 12, so that the suction action of the ejector 12 is not affected.
[0031]
As described above, the present invention has been described in detail based on the embodiments. However, the present invention is not limited to the above-described embodiments, and various modifications or corrections may be made within the scope of the present invention, for example, as described below. It is something that can be done.
[0032]
(1) Pressure air flow direction:
In the embodiment of the present invention, the direction of the flow of pressurized air in the air transport pipe 2 is made to flow from the upper side to the lower side (see FIG. 1) in the ejector installation portion 18 where the discharge port 4 opens. The installation form of the combination of the nozzle 38 and the diffuser 40 can be turned upside down so that the pressurized air flows upward from below.
[0033]
(2) Discharge nozzle:
In the embodiment of the present invention, the pressure air branched from the air transport pipe 2 is flowed to the discharge nozzle 50. However, if it is convenient to use an appropriate air pressure source, the pressure air source to the discharge nozzle 50 is You may make another.
[0034]
【The invention's effect】
According to the powder supply apparatus configured in accordance with the present invention, in the powder supply apparatus that supplies powder to the air transport pipe continuously and quantitatively using a rotary table having a plurality of measuring chambers. There is provided a powder supply apparatus capable of preventing the flow of pressurized air in the powder transport pipe into the powder storage tank through the measurement chamber which has been emptied by discharging the powder.
[Brief description of the drawings]
FIG. 1 is a side view showing an embodiment of a powder supply apparatus constructed according to the present invention.
FIG. 2 is a cross-sectional view taken in the direction of arrows AA in FIG.
FIG. 3 is an explanatory diagram of the action shown in the direction of arrow B in FIG. 2;
4 is a side view showing a form in which the powder supply apparatus shown in FIG. 1 is provided with a discharge nozzle. FIG.
[Explanation of symbols]
2: Pneumatic transport line 4: Discharge port 6: Powder storage tank 8: Measuring chamber 10: Rotary table 12: Ejector 38: Nozzle 40: Diffuser R: Rotating direction X: Introduction part Y: Discharge part Z1: Front side blocking part Z2 : Rear occlusion

Claims (3)

空気輸送管路に開口する排出口が形成された粉体貯槽と、該粉体貯槽内に回転自在に配設され外周部の周方向に粉体を導入し該排出口に排出するための複数個の計量室が形成された回転テーブルと、該回転テーブルの回転方向における該排出口の前後に形成され計量室を閉塞し粉体貯槽と排出口との間を閉塞させる前側閉塞部及び後側閉塞部と、該排出口の開口する部分に形成され該空気輸送管路の圧力空気が流されることにより排出された粉体が吸引されるエゼクタとを備え
該エゼクタは、該粉体貯槽の該排出口の開口する部分に形成された該空気輸送管路の一部を構成する円筒状のエゼクタ設置部に設けられ、該圧力空気を高速度で噴射させるノズルと、その下流に設けられ漸次に流路を拡大させるディフューザとを備え、該排出口は該ノズルとディフューザとの間に連通し、
該計量室は、該排出口において該円筒状のエゼクタ設置部の中に位置している、ことを特徴とする粉体供給装置。
A powder storage tank having a discharge port opened to the air transport pipe, and a plurality of powder storage tanks rotatably disposed in the powder storage tank for introducing powder into the circumferential direction of the outer peripheral portion and discharging it to the discharge port A rotary table in which a single weighing chamber is formed, and a front blocking portion and a rear side that are formed before and after the discharge port in the rotation direction of the rotary table and close the measurement chamber and block between the powder storage tank and the discharge port A closing portion, and an ejector that is formed in a portion where the discharge port is opened and that sucks out the powder discharged by flowing the pressure air of the air transport pipe ,
The ejector is provided in a cylindrical ejector installation portion constituting a part of the air transport pipe formed in a portion where the discharge port of the powder storage tank is opened, and jets the pressurized air at a high speed. A nozzle and a diffuser provided downstream of the nozzle and gradually expanding the flow path, and the discharge port communicates between the nozzle and the diffuser;
The powder supply apparatus , wherein the weighing chamber is located in the cylindrical ejector installation portion at the discharge port .
該排出口に位置する計量室に向け圧力空気を噴射する排出ノズルを備えている、請求項1記載の粉体供給装置。And a discharge nozzle for injecting pressurized air toward the measuring chamber located in the exhaust port, claim 1 Symbol placement of the powder feeder. 該排出ノズルには、該空気輸送管路の該エゼクタより上流側を分岐して取り出された圧力空気が流される、請求項記載の粉体供給装置。The powder supply apparatus according to claim 2 , wherein the discharge nozzle is supplied with compressed air taken out from the upstream side of the ejector of the air transport pipe.
JP2000298774A 2000-09-29 2000-09-29 Powder feeder Expired - Fee Related JP4564153B2 (en)

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