JP3803040B2 - Pneumatic feeder for pneumatic transportation - Google Patents

Pneumatic feeder for pneumatic transportation Download PDF

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Publication number
JP3803040B2
JP3803040B2 JP2001165346A JP2001165346A JP3803040B2 JP 3803040 B2 JP3803040 B2 JP 3803040B2 JP 2001165346 A JP2001165346 A JP 2001165346A JP 2001165346 A JP2001165346 A JP 2001165346A JP 3803040 B2 JP3803040 B2 JP 3803040B2
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Prior art keywords
air
powder
pressure
storage chamber
nozzle
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JP2002356234A (en
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文治 金田
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大盛工業株式会社
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Description

【0001】
【発明の属する技術分野】
本発明は粉体を貯室、その上方のサイロから空気輸送管へ所定量吐出して粉体を遠方へ搬送するための空気輸送用給粉装置であって、空気輸送管の高圧の空気の影響で給粉精度が低下することを防ぐ技術に関する。
【0002】
【従来の技術】
従来、空気輸送路へ貯室から所定量の粉体を供給する空気輸送用給粉装置は、貯室底面の周辺に貯室内と貯室外とを股がるように回転供給盤を設け、同回転供給盤には貯室内の粉体を収容する小室を複数環状に設け、貯室内で粉体を小室に充填して回転して貯室外で空気輸送路内となる位置で小室の粉体を吐出して、空気とともに下流側へ粉体を流し込んで空気とともに遠方へ搬送する構造である。しかしながら、この従来の空気輸送用給粉装置で空気輸送の空気の圧力が高くなると、空気が回転供給盤を介して給粉装置の貯室内部に流入し、粉体の移動が乱れて給粉精度が悪くなるという問題点があった。この空気の影響は吐出部と貯室との空気圧差が1.0KPaを超えると大きいものとなっていた。
又、空気輸送部の途中にエジェクターを設け、同エジェクターで吐出部の空気圧を低くして負圧を発生させてその負圧で粉体を回転供給盤の吐出部から吸引するようにして空気輸送管へ粉体を送り込む給粉装置もある。しかしながら、この負圧利用による給粉装置では吸引力が弱いと粉体の排出が弱くなり閉塞し、又吸引力が強くなると粉体と空気のリークの方向が同じになるため粉体の供給量の変動が大きくなり、給粉精度が悪いという問題点がある。
【0003】
【発明が解決しようとする課題】
本発明が解決しようとする課題は、従来の問題点を解消し、空気圧が高くなってもその影響を小さくでき、給粉精度を高くできる空気輸送用給粉装置を提供することにある。本発明の他の課題は、低圧と高圧の空気圧を異にする空気輸送管を複数同時に使用できる空気輸送用給粉装置を提供することにある。
【0004】
【課題を解決するための手段】
かかる課題を解決した本発明の構成は、
1) 貯室内と貯室外とを股がるように設けられた回転供給盤に貯室内の粉体を所要量収容させ、回転供給盤の回転によって収容した粉体を貯室外へ移送し、貯室外の空気輸送路へ粉体を吐出する構造の空気輸送型給粉装置に於いて、回転供給盤が粉体を吐出する吐出部の少し上流位置の空気輸送路に空気流速加速用ノズルを設け、粉体の吐出部はノズルによる加速された空気流が直接回転供給盤に触れないように加速空気流から少し距離を離した位置に設け、吐出部での空気静圧を貯室内の空気圧より高い範囲で大きく低下させるようにして吐出部と貯室内との空気圧差を小さくして空気圧の影響を少なくさせることを特徴とする空気輸送用給粉装置
2) 空気流加速用ノズルの外周に回転供給盤の吐出部に向けて少量の空気を吹出す補助吹出部を設け、吐出部からの粉体の払い出しを確実にするようにした前記1)記載の空気輸送用給粉装置
3) 貯室内の空気圧と粉体の吐出部との圧力差を1.0KPa以下にするようにノズルによる空気流速を調整した前記1)又は2)記載の空気輸送用給粉装置
4) 前記1)〜3)記載の空気輸送用給粉装置において、更に貯室に前記回転供給盤・吐出部と同構造の第2回転供給盤と第2吐出部とを設け、第2吐出部と接触するように空気流を流すノズルなしの第2空気輸送路を設け、ノズルのある空気輸送路には高圧の圧縮空気を送って粉体を空気輸送し、ノズルのない第2空気輸送路には低圧の圧縮空気を送って粉体を空気輸送するようにした空気輸送用給粉装置
にある。
【0005】
【発明の実施の形態】
本発明の要部は、給粉装置の回転供給盤が粉体を吐出する吐出部の空気圧(静圧)を、ノズルによって空気輸送の空気の流速を大きくすることで大巾に低下させ、吐出部と貯室内の空気との差圧を吐出部の圧力が貯室内の圧力より高い範囲で低くすることにある。特にその差圧が1.0KPa以内にすれば空気圧による影響は大巾に抑えることができる。
粉体の吐出部は、ノズルによる加速された空気流が直接回転供給盤に触れないように加速空気流から少し距離を離した位置に設ける。
又、補助吹出部を設けることで、吐出部の位置において供給盤の粉体を収容した部分に向けて少量の空気を吹付け、吐出部における粉体の払い出しを確実にすることができる。
本発明において、一つの貯室に複数の回転供給盤・吐出部・空気輸送路を設け、各空気輸送路の空気圧に高低差があってもノズルによって差圧を略同じにすることができ、これによって互に影響されずに、複数の独立した粉体の空気輸送路を設けることができるようになる。
【0006】
【実施例】
以下、本発明の実施例を図面に基づいて説明する。
本実施例は、一つの貯室に高圧と低圧の2つの空気輸送路・給粉機構を設け、高圧の空気輸送路の方のみにノズルを設け、又高圧の給粉機構の回転供給盤の吐出部に向けて空気を吹付ける補助吹出部を設けた例である。
【0007】
図1は、実施例の説明図である。
図2は、実施例の要部の縦断面図である。
図3は、実施例の要部の平面図である。
図4は、実施例の空気流を示す説明図である。
【0008】
図中、1は貯室、1aは貯室底面、1bは貯室側面、1cは貯室底面1aの回転供給盤2a部分を開口した粉体充填口、1dは貯室1内に取付けた撹拌羽根、1eは同撹拌羽根を回動するモータ、2は貯室1の周辺側底部に設けた給粉機構、2aは同給粉機構の回転供給盤、2bは同回転供給盤の外周に放射状に一定ピッチで突設した羽根、2cは同羽根間に形成された粉体収容用小室、2dは回転供給盤2aを回動するモータ駆動部、2eは回転供給盤2aの貯室外部分を密封するケーシング、2fは同ケーシング内に設けた回転供給盤2aの吐出部、3はブロワ9の高圧空気を取り込んだ空気輸送路、4は同空気輸送路に設けた空気流速加速用ノズル、5は回転供給盤2aの吐出部2fに向けて少量の空気を吹出す補助吹出部、5aは補助吹出部の吹出管、5bは同吹出管に空気を空気輸送路3から導入する分岐管、5cは吐出部2f付近の空気圧(粉圧)の検出孔、6は粉体搬送用の空気輸送主管路、7は同空気輸送主管路へ空気輸送路3を接続する混合部、8は空気輸送管3への予備高圧空気源のコンプレッサ、9は空気輸送主管路6へ空気を送るブロワ、10は貯室1の上の粉体サイロ、11はバタフライ弁である。
又、図中、12は貯室1に設けた給粉機構2と略同構造の低圧空気輸送用給粉機構、12aは回転供給盤2aと同じ構造の低圧用回転供給盤、12eは同低圧用回転供給盤12aのケーシング、12fは低圧用回転供給盤12aの低圧用吐出部、13は同低圧用吐出部を通路途中に設けた低圧空気輸送路、14は低圧空気ブロワ、15は粉体吹出ノズルである。
【0009】
この実施例では、粉体サイロ10の粉体は貯室1へ移動し、撹拌羽根1dの回転で撹拌されながら貯室1内の粉体は回転供給盤2aの外周の羽根2b間に形成される小室2c間に充填される。
回転供給盤2aはモータ駆動部2dによって回転されていて、小室2cに充填された粉体は回転供給盤2aの回転とともに回送され、ケーシング2eの天井壁で摺り切られて定量になって吐出部2fで排出される。
【0010】
空気輸送路の高圧空気3は、ブロワ9で発生される高圧空気が空気輸送主管路6から分岐して取り込まれる。その空気圧は30KPa以上(ゲージ圧)であり、ノズル4によって流速が200m/s以上に加速され、静圧は3.0KPa程となる。
【0011】
このとき、ノズル4の外周の補助吹出部5の吹出管5aからも少量の空気が吹出され、回転供給盤2aの吐出部2を吹き付け、吐出部2での粉体の吐出を確実にしている。
【0012】
これによって吐出部2eは1.0KPa程だけ貯室内の空気圧に比べ正の差圧となり、その差圧はノズルがない場合の10KPa程から1.0KPa程へ大巾に低減され、小さな正圧の差圧にした。この1.0KPa程の正の差圧が吐出部2fに作用し、粉圧とバランスさせてフラッシング現象なく、又空気圧・粉圧の影響をほとんど受けずに円滑に所定量の粉体を空気輸送路3へ送り込み、空気流とともに下方へ搬送する。
空気輸送路3の粉体を運ぶノズル4下流側の空気流は、その通路の面積が大きくなることで流速が低下して10KPa程の圧力に戻り、混合部7を介して粉体と空気は空気輸送主管路6へ送られ、他の供給装置からの粉体・空気とともに遠方の粉体吹出ノズル15へ送られる。
高圧の空気輸送路の空気源としてコンプレッサ8を使用した場合でも吐出部2fの静圧を20KPa以上低下させることができる。
【0013】
又、実施例の貯室1には別の低圧用空気輸送路13への給粉機構12が設けられ、同供給機構12の低圧用回転供給盤12aは前記高圧側の回転供給盤2aと同様に貯室1内の粉体を充填して回送し、低圧用吐出部12fで吐出する。同低圧吐出部12fには低圧空気輸送路13中に配置され、直接空気輸送路13中の空気で吹き払うようにして粉体は払い出されて空気輸送される。低圧用吐出部12fと貯室1内の空気圧との間の差圧と、高圧側の吐出部2fと貯室1との間の空気圧の差圧とは、高圧側のノズル4によって大略同じ程度とすることができ、空気輸送路の空気圧が違っても高い精度で複数の空気輸送を可能としている。
【0014】
【発明の効果】
以上の様に、本発明によれば粉体の吐出部の少し上流の空気輸送路に流速加速用ノズルを設けることによって、吐出部の空気静圧を大きく低下させて貯室内の空気圧より少し高い圧力値とすること(小さな差圧とすること)で、輸送空気の圧力で給粉が乱れて給粉精度を低下させないようにした。又、低圧と高圧の空気輸送路を同時に使用でき易くした。
ノズルの空気噴出流の外周に少量の空気を補助吹出部から吐出部に向けて吹出すことによって、吐出部での粉体の払い出しを確実にできるようになる。
【図面の簡単な説明】
【図1】実施例の説明図である。
【図2】実施例の要部の縦断面図である。
【図3】実施例の要部の平面図である。
【図4】実施例の空気流を示す説明図である。
【符号の説明】
1 貯室
1a 貯室底面
1b 貯室側面
1c 粉体充填口
1d 撹拌羽根
1e モータ
2 給粉機構
2a 回転供給盤
2b 羽根
2c 小室
2d モータ駆動部
2e ケーシング
2f 吐出部
3 空気輸送路
4 ノズル
5 補助吹出部
5a 吹出管
5b 分岐管
5c 検出孔
6 空気輸送主管路
7 混合部
8 コンプレッサ
9 ブロワ
10 粉体サイロ
12 低圧空気輸送用給粉機構
12a 低圧用回転供給盤
12e ケーシング
12f 低圧用吐出部
13 低圧空気輸送路
14 低圧空気ブロワ
15 粉体吹出ノズル
[0001]
BACKGROUND OF THE INVENTION
The present invention is an air transporting powder feeder for transporting powder to a distance by discharging a predetermined amount of powder from a storage chamber and a silo above the storage chamber, and the high pressure air in the air transport pipe The present invention relates to a technique for preventing a decrease in powder feeding accuracy due to influence.
[0002]
[Prior art]
Conventionally, pneumatic transporting powder feeders that supply a predetermined amount of powder from a storage chamber to an air transport path have been provided with a rotating supply board around the bottom of the storage chamber so that the storage chamber and the outside of the storage chamber can be crotched. The rotating supply board is provided with a plurality of small chambers for storing the powder in the storage chamber, and the powder in the storage chamber is filled with the powder in the storage chamber and rotated to place the powder in the chamber outside the storage chamber in the air transport path. It is a structure in which the powder is discharged, flows into the downstream side together with air, and is conveyed away with air. However, when the pressure of air for pneumatic transportation increases in this conventional pneumatic transport powder feeder, air flows into the storage chamber of the powder feeder via the rotary feeder, and the powder movement is disturbed. There was a problem that accuracy deteriorated. The influence of this air was significant when the air pressure difference between the discharge part and the storage chamber exceeded 1.0 KPa.
In addition, an ejector is installed in the middle of the pneumatic transport section, and the ejector lowers the air pressure of the discharge section to generate a negative pressure, so that the negative pressure causes the powder to be sucked from the discharge section of the rotary feeding board. There is also a powder feeder that feeds powder into the tube. However, in this powder feeding device using negative pressure, if the suction force is weak, the discharge of the powder becomes weak and clogs, and if the suction force is strong, the powder and air leak directions are the same. There is a problem that the fluctuation of the powder becomes large and the powder feeding accuracy is poor.
[0003]
[Problems to be solved by the invention]
The problem to be solved by the present invention is to provide an air transporting powder feeder capable of solving the conventional problems, reducing the influence even when the air pressure is increased, and improving the powder feeding accuracy. Another object of the present invention is to provide an air transporting powder feeder capable of simultaneously using a plurality of air transport pipes having different low pressure and high pressure air pressure.
[0004]
[Means for Solving the Problems]
The configuration of the present invention that solves this problem is as follows.
1) A required amount of powder in the storage chamber is accommodated in a rotating supply board provided so that the storage chamber and the outside of the storage room are crotched, and the stored powder is transferred to the outside of the storage room by rotation of the rotary supply board. In an air transport type powder feeder that discharges powder to an outdoor air transport path, a nozzle for accelerating the air flow rate is installed in the air transport path slightly upstream of the discharge part where the rotary supply board discharges the powder. The powder discharge section is located at a distance from the acceleration air flow so that the air flow accelerated by the nozzle does not directly touch the rotating supply board, and the static air pressure at the discharge section is determined by the air pressure in the storage chamber. Pneumatic transporting powdering device characterized in that the effect of air pressure is reduced by reducing the air pressure difference between the discharge part and the storage chamber so as to be greatly reduced in a high range. 2) Rotating to the outer periphery of the air flow acceleration nozzle Auxiliary blowout that blows a small amount of air toward the discharge part of the supply panel 1) The pneumatic transporting powder feeding device 3) described above, wherein the discharge of the powder is ensured, and the pressure difference between the air pressure in the storage chamber and the powder discharging part is 1.0 KPa. The air transporting powder feeder 4) according to 1) or 2), wherein the air flow rate by the nozzle is adjusted as described below. In the air transporting powder feeder according to 1) to 3), the rotation is further performed in the storage chamber. A second rotary supply disk and a second discharge part having the same structure as the supply board / discharge part are provided, and a second air transport path without a nozzle for flowing an air flow is provided so as to be in contact with the second discharge part. Powder supply for pneumatic transportation, in which high-pressure compressed air is sent to the pneumatic transportation path to pneumatically transport powder, and low-pressure compressed air is sent to the second pneumatic transportation path without nozzles to pneumatically transport powder. In the device.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
The main part of the present invention is that the air pressure (static pressure) of the discharge part where the rotary supply board of the powder feeder discharges the powder is greatly reduced by increasing the air flow velocity of air transportation by the nozzle, and the discharge The pressure difference between the air outlet and the air in the storage chamber is made lower in the range where the pressure in the discharge section is higher than the pressure in the storage chamber. In particular, if the differential pressure is within 1.0 KPa, the effect of air pressure can be greatly reduced.
The powder discharge unit is provided at a position slightly away from the accelerated air flow so that the air flow accelerated by the nozzle does not directly touch the rotating supply board.
Further, by providing the auxiliary blowing part, it is possible to spray a small amount of air toward the part of the supply board where the powder is accommodated at the position of the discharge part, and to ensure the discharge of the powder in the discharge part.
In the present invention, a single storage chamber is provided with a plurality of rotary supply panels, discharge sections, and air transportation paths, and even if there is a difference in the air pressure of each air transportation path, the differential pressure can be made substantially the same by the nozzle, This makes it possible to provide a plurality of independent powder air transport paths without being affected by each other.
[0006]
【Example】
Embodiments of the present invention will be described below with reference to the drawings.
In this embodiment, a high-pressure and low-pressure pneumatic transport path / powder supply mechanism is provided in one storage chamber, a nozzle is provided only in the high-pressure pneumatic transport path, and a rotary feeder disk of the high-pressure powder supply mechanism is provided. It is the example which provided the auxiliary blowing part which blows air toward a discharge part.
[0007]
FIG. 1 is an explanatory diagram of the embodiment.
FIG. 2 is a vertical cross-sectional view of a main part of the embodiment.
FIG. 3 is a plan view of a main part of the embodiment.
FIG. 4 is an explanatory diagram showing an air flow in the embodiment.
[0008]
In the figure, 1 is a storage chamber, 1a is a storage chamber bottom surface, 1b is a storage chamber side surface, 1c is a powder filling port that opens the rotary supply disk 2a portion of the storage chamber bottom surface 1a, and 1d is an agitation mounted in the storage chamber 1 The blade 1e is a motor for rotating the stirring blade, 2 is a powder supply mechanism provided at the bottom of the peripheral side of the storage chamber 1, 2a is a rotary supply plate of the powder supply mechanism, 2b is radially on the outer periphery of the rotary supply plate 2c is a small powder storage chamber formed between the blades, 2d is a motor drive unit for rotating the rotary supply board 2a, and 2e is for sealing a portion outside the storage chamber of the rotary supply board 2a. The casing 2f is a discharge part of the rotary supply board 2a provided in the casing 3 is an air transport path that takes in the high-pressure air of the blower 9, 4 is an air velocity acceleration nozzle 5 provided in the air transport path, Auxiliary blow-out section 5a for blowing out a small amount of air toward the discharge section 2f of the rotary supply board 2a The outlet pipe 5b is a branch pipe for introducing air into the outlet pipe from the air transport path 3, 5c is a detection hole for air pressure (powder pressure) near the discharge section 2f, and 6 is an air transport main pipe for powder transport. , 7 is a mixing unit for connecting the air transportation path 3 to the same air transportation main line, 8 is a compressor of a pre-high pressure air source to the air transportation pipe 3, 9 is a blower for sending air to the air transportation main line 6, and 10 is A powder silo above the storage chamber 1, 11 is a butterfly valve.
In the drawing, 12 is a low-pressure pneumatic transporting powder feed mechanism having the same structure as the powder feed mechanism 2 provided in the storage chamber 1, 12a is a low-pressure rotary feed board having the same structure as the rotary feed board 2a, and 12e is the same low pressure. Casing 12a, 12f is a low-pressure discharge part of low-pressure rotary supply board 12a, 13 is a low-pressure air transport passage in which the low-pressure discharge part is provided in the middle of the passage, 14 is a low-pressure air blower, and 15 is powder. It is a blowout nozzle.
[0009]
In this embodiment, the powder in the powder silo 10 moves to the storage chamber 1, and the powder in the storage chamber 1 is formed between the blades 2b on the outer periphery of the rotary supply board 2a while being stirred by the rotation of the stirring blade 1d. Between the small chambers 2c.
The rotary supply board 2a is rotated by a motor drive unit 2d, and the powder filled in the small chamber 2c is sent along with the rotation of the rotary supply board 2a, and is slid by the ceiling wall of the casing 2e to become a fixed amount. It is discharged at 2f.
[0010]
The high-pressure air 3 in the air transportation path is taken in by branching the high-pressure air generated by the blower 9 from the air transportation main pipeline 6. The air pressure is 30 KPa or more (gauge pressure), the nozzle 4 accelerates the flow velocity to 200 m / s or more, and the static pressure is about 3.0 KPa.
[0011]
At this time, a small amount of air is also blown from the blow pipe 5a of the auxiliary blow section 5 on the outer periphery of the nozzle 4, and the discharge section 2 of the rotary supply board 2a is blown to ensure discharge of the powder at the discharge section 2. .
[0012]
As a result, the discharge portion 2e has a positive differential pressure of about 1.0 KPa compared to the air pressure in the storage chamber, and the differential pressure is greatly reduced from about 10 KPa to 1.0 KPa when there is no nozzle, and a small positive pressure. Differential pressure was used. This positive differential pressure of about 1.0 KPa acts on the discharge part 2f and balances it with the powder pressure so that there is no flushing phenomenon, and a predetermined amount of powder is smoothly transported by air without being affected by air pressure or powder pressure. It feeds into the path 3 and is conveyed downward together with the air flow.
The air flow on the downstream side of the nozzle 4 that carries the powder in the air transport path 3 is reduced in flow rate to a pressure of about 10 KPa due to the increase in the area of the passage, and the powder and air are mixed through the mixing unit 7. It is sent to the air transport main pipeline 6 and sent to a distant powder blowing nozzle 15 together with powder and air from other supply devices.
Even when the compressor 8 is used as the air source of the high-pressure air transportation path, the static pressure of the discharge part 2f can be reduced by 20 KPa or more.
[0013]
In addition, the storage chamber 1 of the embodiment is provided with a powder feeding mechanism 12 for another low-pressure air transport path 13, and the low-pressure rotary supply board 12 a of the supply mechanism 12 is the same as the high-pressure side rotary supply board 2 a. The powder in the storage chamber 1 is filled and fed into the storage chamber 1 and discharged by the low pressure discharge section 12f. The low-pressure discharge part 12f is disposed in the low-pressure air transport path 13, and the powder is discharged and pneumatically transported by blowing off the air in the air transport path 13 directly. The differential pressure between the low pressure discharge section 12f and the air pressure in the storage chamber 1 and the differential pressure between the high pressure side discharge section 2f and the storage chamber 1 are approximately the same by the high pressure side nozzle 4. Even if the air pressure in the air transport path is different, a plurality of air transports are possible with high accuracy.
[0014]
【The invention's effect】
As described above, according to the present invention, by providing the nozzle for accelerating the flow velocity in the air transport path slightly upstream of the powder discharge section, the static air pressure of the discharge section is greatly reduced to be slightly higher than the air pressure in the storage chamber. By setting the pressure value (small differential pressure), the powder supply is not disturbed by the pressure of the transport air, and the powder supply accuracy is not lowered. In addition, the low-pressure and high-pressure air transportation paths can be used simultaneously.
By discharging a small amount of air from the auxiliary blowing portion toward the discharge portion on the outer periphery of the air jet flow of the nozzle, it becomes possible to reliably discharge the powder at the discharge portion.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram of an embodiment.
FIG. 2 is a longitudinal sectional view of a main part of the embodiment.
FIG. 3 is a plan view of a main part of the embodiment.
FIG. 4 is an explanatory view showing an air flow of the embodiment.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Storage chamber 1a Storage chamber bottom surface 1b Storage chamber side surface 1c Powder filling port 1d Stirring blade 1e Motor 2 Powder supply mechanism 2a Rotation supply board 2b Blade 2c Small chamber 2d Motor drive part 2e Casing 2f Discharge part 3 Air transport path 4 Nozzle 5 Auxiliary Blowing section 5a Blowing pipe 5b Branch pipe 5c Detection hole 6 Pneumatic transport main line 7 Mixing section 8 Compressor 9 Blower 10 Powder silo 12 Powder supply mechanism 12a for low-pressure air transport Low-pressure rotary supply panel 12e Casing 12f Low-pressure discharge section 13 Low pressure Air transport path 14 Low pressure air blower 15 Powder blowing nozzle

Claims (4)

貯室内と貯室外とを股がるように設けられた回転供給盤に貯室内の粉体を所要量収容させ、回転供給盤の回転によって収容した粉体を貯室外へ移送し、貯室外の空気輸送路へ粉体を吐出する構造の空気輸送型給粉装置に於いて、回転供給盤が粉体を吐出する吐出部の少し上流位置の空気輸送路に空気流速加速用ノズルを設け、粉体の吐出部はノズルによる加速された空気流が直接回転供給盤に触れないように加速空気流から少し距離を離した位置に設け、吐出部での空気静圧を貯室内の空気圧より高い範囲で大きく低下させるようにして吐出部と貯室内との空気圧差を小さくして空気圧の影響を少なくさせることを特徴とする空気輸送用給粉装置。A rotating supply disc provided so that the storage chamber and the outside of the storage chamber can be crawled to store a required amount of powder in the storage chamber, and the powder stored by the rotation of the rotary supply disc is transferred to the outside of the storage chamber. In an air transport type powder feeder having a structure for discharging powder to an air transport path, a nozzle for accelerating air flow velocity is provided in the air transport path slightly upstream of the discharge section where the rotary supply board discharges powder. The body discharge unit is located at a distance from the acceleration air flow so that the air flow accelerated by the nozzle does not directly touch the rotating supply board, and the static air pressure at the discharge unit is higher than the air pressure in the storage chamber. A pneumatic feeder for reducing the influence of the air pressure by reducing the air pressure difference between the discharge part and the storage chamber so as to greatly reduce the air pressure. 空気流加速用ノズルの外周に回転供給盤の吐出部に向けて少量の空気を吹出す補助吹出部を設け、吐出部からの粉体の払い出しを確実にするようにした請求項1記載の空気輸送用給粉装置。 The air according to claim 1, wherein an auxiliary blow-out portion for blowing a small amount of air toward the discharge portion of the rotary supply board is provided on the outer periphery of the air flow acceleration nozzle so as to ensure discharge of the powder from the discharge portion. Transport powder feeder. 貯室内の空気圧と粉体の吐出部との圧力差を1.0KPa以下にするようにノズルによる空気流速を調整した請求項1又は2記載の空気輸送用給粉装置。  3. The air transporting powder feeding device according to claim 1, wherein the air flow rate by the nozzle is adjusted so that the pressure difference between the air pressure in the storage chamber and the discharge part of the powder is 1.0 KPa or less. 請求項1〜3記載の空気輸送用給粉装置において、更に貯室に前記回転供給盤・吐出部と同構造の第2回転供給盤と第2吐出部とを設け、第2吐出部と接触するように空気流を流すノズルなしの第2空気輸送路を設け、ノズルのある空気輸送路には高圧の圧縮空気を送って粉体を空気輸送し、ノズルのない第2空気輸送路には低圧の圧縮空気を送って粉体を空気輸送するようにした空気輸送用給粉装置。  4. The pneumatic transporting powder feeding device according to claim 1, wherein the storage chamber is further provided with a second rotating supply disk and a second discharging part having the same structure as the rotating supply disk / discharge part, and in contact with the second discharging part. A second air transport path without a nozzle for flowing an air flow is provided, and high pressure compressed air is sent to the air transport path with the nozzle to pneumatically transport the powder, and the second air transport path without the nozzle is Pneumatic feeding powder feeder that sends low-pressure compressed air to pneumatically transport powder.
JP2001165346A 2001-05-31 2001-05-31 Pneumatic feeder for pneumatic transportation Expired - Lifetime JP3803040B2 (en)

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