JPS6265829A - Powder supply device - Google Patents

Powder supply device

Info

Publication number
JPS6265829A
JPS6265829A JP20407485A JP20407485A JPS6265829A JP S6265829 A JPS6265829 A JP S6265829A JP 20407485 A JP20407485 A JP 20407485A JP 20407485 A JP20407485 A JP 20407485A JP S6265829 A JPS6265829 A JP S6265829A
Authority
JP
Japan
Prior art keywords
powder
pipe
hopper
supply
circulation
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
JP20407485A
Other languages
Japanese (ja)
Inventor
Kazuhisa Ogasawara
和久 小笠原
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.)
Kurabo Industries Ltd
Kurashiki Spinning Co Ltd
Original Assignee
Kurabo Industries Ltd
Kurashiki Spinning Co Ltd
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 Kurabo Industries Ltd, Kurashiki Spinning Co Ltd filed Critical Kurabo Industries Ltd
Priority to JP20407485A priority Critical patent/JPS6265829A/en
Publication of JPS6265829A publication Critical patent/JPS6265829A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To prevent the fluidity of powder from lowering due to blocking and adhering of powder in a hopper or a pipe line, by providing such an arrangement that powder in a feed pipe connected to a hopper, upstream of a large capacity supply valve, is sucked into a circulation pipe by means of an ejector so that the sucked powder is circulated to the inlet of the hopper. CONSTITUTION:In a supply and weighting device 1 for powder-like drug materials, a feed pipe 3 is connected to the outlet port 2b of a hopper 2 having large and small agitating blades 7, 8 adapted to be rotated by a motor 9 when it is operated, and the material is fed by a large amount into a cup 14 disposed on a weighing unit 13 in the hopper 2 under the control of a large volume supply valve 12 disposed in the feed pipe 2. In this arrangement, a circulation pipe 17 is disposed between the feed pipe 2 upstream of the large capacity supply valve 12 and the inlet port 2a of the hopper 2, a circulation ejector 18 being disposed in the circulation pipe 17, and the upper side end part 17a of the circulation pie 17 is connected to a cyclone 19. Further, a slight volume supply pipe 21 is connected between two parts of the feed pipe 3 upstream and downstream of the large capacity supply valve 12, and a slight capacity supply ejector 22 is disposed in the pipe 21, a cyclone 23 being disposed in the pipe 21 downstream of the ejector 22.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、粉体の供給装置の改良に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to an improvement in a powder supply device.

(従来技術) 従来、粉体の供給装置としては、ホッパ内でブリッジを
形成した船体が排出されにくくなるのを防止するため、
電磁振動フィーダの振動を大きくしてブリッジを破壊す
るようにしたちのが提案されている(48開昭60−1
28106号公報参照)。
(Prior Art) Conventionally, as a powder supply device, in order to prevent the hull forming a bridge from being difficult to discharge in the hopper,
It has been proposed to destroy the bridge by increasing the vibration of the electromagnetic vibration feeder (1986-1948).
(See Publication No. 28106).

また、ホッパ内の粉体を、気体を利用して搬送する供給
装置も提案されている(特公昭58−23301号公報
、特開昭60−77023号公報参照)。
Furthermore, a supply device has been proposed that uses gas to convey the powder in the hopper (see Japanese Patent Publication No. 58-23301 and Japanese Patent Application Laid-Open No. 60-77023).

ところで、粉体が塩化ナトリウム(NaC1)や硫酸マ
グネシウム(MgS04 ・7H20)などのような化
学薬品である場合、吸湿性や固結度がきわめて強く、固
結および付着により流動性が着しく低下するという特性
があり、上述のような電磁振動フィーダでは充分に破壊
できないので、安定に供給できないという問題、があっ
た。
By the way, when the powder is a chemical such as sodium chloride (NaC1) or magnesium sulfate (MgS04/7H20), its hygroscopicity and degree of caking are extremely strong, and fluidity is severely reduced due to caking and adhesion. Because of this characteristic, the electromagnetic vibrating feeder described above cannot sufficiently destroy the material, resulting in a problem that it cannot be stably supplied.

(発明の目的) 本発明は、上記従来の問題点に鑑みてなされたもので、
とくに固結および付着による流動性の低下が著しい化学
薬品等の粉体を、安定に、かつ高精度で供給することを
可能とした粉体の供給装置を提供することを基本的な目
的とするものである。
(Object of the invention) The present invention has been made in view of the above-mentioned conventional problems.
Our basic objective is to provide a powder supply device that can stably and accurately supply powders, such as chemicals, whose fluidity is particularly markedly reduced due to caking and adhesion. It is something.

(発明の構成) このため本発明は、ホッパの出口に連設された供給管に
多量供給弁が介設されていて、該供給管の多量供給弁の
上流側と上記ホッパの入口との間に循環管が設けられ、
該循環管に、供給管内の粉体をホッパの入口に吸引循環
させる循環エゼクタ−が介設される一方、上記供給管の
多量供給弁の上流側と下流側との間に微量供給管が設け
られ、該a1供給管に、供給管内の粉体を供給管の吐出
口に吸引供給させる微量供給エゼクタ−が介設されてい
ることを特徴とするものである。
(Structure of the Invention) For this reason, the present invention includes a large quantity supply valve interposed in a supply pipe connected to the outlet of the hopper, and a gap between the upstream side of the large quantity supply valve of the supply pipe and the inlet of the hopper. A circulation pipe is installed in the
A circulation ejector is interposed in the circulation pipe to suck and circulate the powder in the supply pipe to the inlet of the hopper, and a small quantity supply pipe is provided between the upstream side and the downstream side of the large quantity supply valve of the supply pipe. The a1 supply pipe is characterized in that a small amount supply ejector is interposed in the a1 supply pipe to suck and supply the powder in the supply pipe to the discharge port of the supply pipe.

(発明の効果) 本発明によれば、ホッパに連結された供給管の多量供給
弁よりも上流側の粉体は、循環エゼクタ−により循環管
に吸引されてホッパの入口に循環される上うになるから
、この循環系によりホッパ内及び供給管内における粉体
の固結および付着による流動性の低下が効果的に防止さ
れて、粉体の供給が安定に行なえるようになる。
(Effects of the Invention) According to the present invention, the powder on the upstream side of the bulk supply valve of the supply pipe connected to the hopper is sucked into the circulation pipe by the circulation ejector and circulated to the inlet of the hopper. Therefore, this circulation system effectively prevents a decrease in fluidity due to solidification and adhesion of the powder in the hopper and the supply pipe, thereby making it possible to stably supply the powder.

また、供給管の多量供給弁の上流側の粉体は、微量供給
エゼクタ−により微量供給管に吸引されて供給管の吐出
口に供給されるようになるか呟多量供給弁による多量供
給系と、エゼクタ−による微量供給系とにより、粉体の
供給が高・精度で行なえるようになる。
In addition, the powder on the upstream side of the large quantity supply valve of the supply pipe is sucked into the small quantity supply pipe by the small quantity supply ejector and supplied to the discharge port of the supply pipe. , and a small amount supply system using an ejector, the powder can be supplied with high precision.

(実施例) 以下、本発明の実施例を添付図面について詳細に説明す
る。
(Embodiments) Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.

第1図に示すように、粉体薬品の供給・計量装置1には
、上部に入口2a、下部に出口2bを有するホッパ2が
備えられ、該ホッパ2の出口2bには供給管3が連設さ
れている。
As shown in FIG. 1, the powder chemical supply/measuring device 1 is equipped with a hopper 2 having an inlet 2a at the top and an outlet 2b at the bottom, and a supply pipe 3 is connected to the outlet 2b of the hopper 2. It is set up.

上記ホッパ2内には、下部軸受4と下部軸受5とで軸承
された攪拌軸6が挿入され、該攪拌軸6には、大径の攪
拌羽根7と小径の攪拌羽根8とが上下位置に取付けられ
ていて、攪拌モータ9で攪拌軸6および攪拌軸6を介し
て各羽根7,8を回転させることにより、粉体を攪拌し
てホッパ2内及び多量供給弁12の上流の供給管3内に
おける粉体の架橋・閉塞を防止するようになっている。
A stirring shaft 6 supported by a lower bearing 4 and a lower bearing 5 is inserted into the hopper 2, and a large-diameter stirring blade 7 and a small-diameter stirring blade 8 are arranged in vertical positions on the stirring shaft 6. By rotating the stirring shaft 6 and the blades 7 and 8 via the stirring shaft 6 with the stirring motor 9, the powder is stirred and fed into the supply pipe 3 in the hopper 2 and upstream of the bulk supply valve 12. It is designed to prevent cross-linking and clogging of powder inside.

上記供給管3には多量供給弁12が介設されていて、該
多量供給弁12により、ホッパ2内の粉体を、供給管3
の吐出口3aから計量器13上のカップ14へ多量供給
するようになる。
A large quantity supply valve 12 is interposed in the supply pipe 3, and the large quantity supply valve 12 transfers the powder in the hopper 2 to the supply pipe 3.
A large amount of liquid is supplied to the cup 14 on the measuring device 13 from the discharge port 3a.

上記供給管3の吐出口3aからカップ14へ粉体が落下
供給される際、周囲に粉塵が飛散する恐れがあるが、吐
出口3aの先部を絞っていること、及び吐出口3aの回
りに粉塵吸引管15.15を配置していることにより、
粉塵の飛散を防止するようになっている。
When the powder is dropped and supplied from the outlet 3a of the supply pipe 3 to the cup 14, there is a risk that dust may be scattered around. By arranging the dust suction pipe 15.15,
It is designed to prevent dust from scattering.

一方、上記供給管3の多量供給弁12の上流側と上記ホ
ッパ2の入口2aとの間には循環管17が設けられ、該
循環管17には循環エゼクタ−18が介設されるととも
に、該循環管17のホッパ側端部17aは、ホッパ2の
入口2aに対して設けられたサイクロン19に連結され
ている。
On the other hand, a circulation pipe 17 is provided between the upstream side of the bulk supply valve 12 of the supply pipe 3 and the inlet 2a of the hopper 2, and a circulation ejector 18 is interposed in the circulation pipe 17. A hopper side end 17a of the circulation pipe 17 is connected to a cyclone 19 provided to the inlet 2a of the hopper 2.

上記供給管3の多量供給弁12の上流側と下流側との間
には微量供給管21が設けられ、該微量供給管21の上
流側には微量供給エゼクタ−22カf会貢昏3れ入ンと
ムに、肢工シクダー22の下情側にはサイクロン23が
介設されている。
A small amount supply pipe 21 is provided between the upstream side and the downstream side of the large amount supply valve 12 of the supply pipe 3, and a small amount supply ejector 22 is provided on the upstream side of the small amount supply pipe 21. At the same time, a cyclone 23 is installed on the lower side of the limb worker Shikuda 22.

該微量供給管21のサイクロン23の下流側には、下流
側に向って気体を噴出する掃除配管24が設けられてい
る。
On the downstream side of the cyclone 23 of the minute supply pipe 21, a cleaning pipe 24 is provided that blows out gas toward the downstream side.

上記循環エゼクタ−18、微量供給エゼクタ−22及び
掃除配管24は、それぞれ第1〜第3気体制御弁26a
、26b、26cが介設された第1〜第3気体配管27
a、 27b、 27cを介して、圧縮気体源28から
供給される気体の圧力・流量を制御する制御部29に連
結されている。
The circulation ejector 18, the small amount supply ejector 22, and the cleaning pipe 24 each have first to third gas control valves 26a.
, 26b, 26c are interposed between the first to third gas pipes 27
A, 27b, and 27c are connected to a control section 29 that controls the pressure and flow rate of gas supplied from a compressed gas source 28.

上記攪拌モータ9、多量供給弁12、気体制御弁26a
〜26c及び気体圧力・流量制御部29は、計量器13
等からの情報に基づいてマイクロコンピュータ30によ
り制御される。
The above-mentioned stirring motor 9, large quantity supply valve 12, gas control valve 26a
~26c and the gas pressure/flow rate control section 29 are the meter 13
It is controlled by the microcomputer 30 based on information from etc.

上記のような構成であれば、供給・計量装置1の運転前
もしくは適当な時間間隔毎に、マイクロコンピュータ3
0により第3制御弁26cを開制御すると、圧縮気体源
28からの圧縮気体が循環エゼクタ−18に供給され、
該圧縮気体に上る負圧により、供給管3内の粉体が気体
とともに循環管17内に吸引されて、ホッパ上部のサイ
クロン19に入り、気体は気体出口19aから排出され
ると同時に、粉体は粉体出口19bからホッパ2内に循
環供給されるようになる。
With the above configuration, the microcomputer 3
When the third control valve 26c is controlled to open by 0, compressed gas from the compressed gas source 28 is supplied to the circulation ejector 18,
Due to the negative pressure rising on the compressed gas, the powder in the supply pipe 3 is sucked into the circulation pipe 17 together with the gas, enters the cyclone 19 at the top of the hopper, and the gas is discharged from the gas outlet 19a, and at the same time the powder is is circulated and supplied into the hopper 2 from the powder outlet 19b.

これにより、ホッパ2内及び供給管3内の粉体の固結お
上び付着による流動性の低下が防止されると同時に粉体
のかさ密度の増大化による供給量の変化が減少して、粉
体の安定供給が保障される。
This prevents a decrease in fluidity due to solidification and adhesion of the powder in the hopper 2 and the supply pipe 3, and at the same time reduces changes in the supply amount due to an increase in the bulk density of the powder. Stable supply of powder is guaranteed.

上記圧縮気体として、除湿済みの乾燥気体を使用すると
、吸湿により著しく固結する現象をもつ粉体に乾燥効果
が生じ、粉体の安定供給がより保障される。
When a dehumidified dry gas is used as the compressed gas, a drying effect is produced on the powder, which tends to solidify significantly due to moisture absorption, and a stable supply of the powder is further ensured.

次に、ホッパ2内及び多量供給弁12の上流の供給管3
内の粉体の流動化が完了した状態で、粉体を多量供給す
る場合には、マイクロフンピユータ30により多量供給
弁12を開制御すると、ホッパ2内の粉体は供給管3を
通って吐出口3aからカップ14に供給されてゆき、計
量器13により所定量の粉体が供給されたことを検出す
ると、マイクロコンピュータ30により多量供給弁12
が閉制御される。
Next, the supply pipe 3 inside the hopper 2 and upstream of the bulk supply valve 12
When a large amount of powder is to be supplied after fluidization of the powder in the hopper has been completed, the micro pump 30 controls the opening of the large quantity supply valve 12, and the powder in the hopper 2 passes through the supply pipe 3. The powder is supplied from the discharge port 3a to the cup 14, and when the meter 13 detects that a predetermined amount of powder has been supplied, the microcomputer 30 closes the large quantity supply valve 12.
is controlled to close.

また、粉体を高精度で@量供給する場合には、マイクロ
コンピュータ30により第2気体制御弁26bを開制御
すると、圧縮気体源28がらの圧縮気体が微量供給エゼ
クタ−22に供給され、該圧縮気体による負圧により、
供給管3内の粉体が気体とともに@1供給管21に吸引
されてサイクロン23に入り、気体は気体出口23aが
ら排出されると同時に、粉体は粉体出口23bから微量
供給管21を通って供給管3の吐出口3aがらカップ1
4に供給されてゆき、計量器13により所定量の粉体が
供給されたことを検出すると、マイクロコンピュータ3
0により第2気体制御弁26bが閉制御される。
When powder is to be supplied in a highly accurate amount, when the second gas control valve 26b is controlled to be opened by the microcomputer 30, the compressed gas from the compressed gas source 28 is supplied to the small amount supply ejector 22, and the Due to negative pressure caused by compressed gas,
The powder in the supply pipe 3 is sucked together with the gas into the @1 supply pipe 21 and enters the cyclone 23, and at the same time the gas is discharged from the gas outlet 23a, the powder passes through the small amount supply pipe 21 from the powder outlet 23b. The cup 1 is opened from the outlet 3a of the supply pipe 3.
When the meter 13 detects that a predetermined amount of powder has been supplied, the microcomputer 3
0, the second gas control valve 26b is controlled to close.

このように、多量供給弁12による多量供給系の池に、
エゼクタ−22による微量供給系が哉けられているので
、粉体の供給が高精度で行なえる。
In this way, in the pond of the large quantity supply system by the large quantity supply valve 12,
Since the small amount supply system using the ejector 22 is operated, powder can be supplied with high precision.

なお、第2気体制御弁26bが閉制御されたとき、付着
性の強い粉体では、きわめて微量ではあるがサイクロン
23に滞留することがあるので、マイクロコンピュータ
30に上り第1気体制御弁26aを開制御して、掃除配
管24がら圧縮気体を噴出させ、滞留粉体を供給管3の
吐出口3aから排出させる。
Note that when the second gas control valve 26b is controlled to close, highly adhesive powder may stay in the cyclone 23, albeit in a very small amount, so it goes up to the microcomputer 30 and closes the first gas control valve 26a. The opening control is performed to blow out compressed gas from the cleaning pipe 24 and discharge the accumulated powder from the discharge port 3a of the supply pipe 3.

第2図は、複数種(4種)の粉体(化学薬品)を所定量
づつ供給・計量して調合するための装置で、第1図の供
給・計1装置1を4台設け、それぞれをケーシング35
.・・・、351こ組込んでユニット化する一方、第1
ユニツト36と第3ユニツト38とをハ字状に設置する
とともに、第1ユニツト36に第2ユニツト37をヒン
ジ紬40でヒンジ結合し、第3ユニツト38に第4ユニ
ツト39をヒンジ紬41でヒンジ結合する。
Figure 2 shows a device for supplying, measuring and mixing multiple types (4 types) of powder (chemicals) in predetermined amounts. The casing 35
.. ..., while incorporating 351 units into a unit, the first
The unit 36 and the third unit 38 are installed in a V-shape, and the second unit 37 is hinged to the first unit 36 with a hinge pongee 40, and the fourth unit 39 is hinged to the third unit 38 with a hinge pongee 41. Join.

そして、第1ユニツト36と第3ユニツト38tこ対称
となるように第2ユニツ)37と第4ユニツト39を内
方へ逆ハ字状に設置し、メンテナンス時には第2ユニツ
ト37と第4ユニツト39を二点鎖線で示すように外方
へ旋回させるようにする。
Then, the second unit 37 and the fourth unit 39 are installed inward in an inverted V shape so that the first unit 36 and the third unit 38t are symmetrical. Rotate outward as shown by the two-dot chain line.

上記第3.第4ユニツ)38.39の側方には御ユニッ
ト42が設置され、第2.第4ユニツト37.39の前
方にはカップ供給装置43(第3図参照)が設置され、
上記各ユニット36〜39の中央にはカップ14を積載
して粉体の重量を計量する上記計量器13が設置され、
該計量器13の後方にはカップ供給装置43で供給され
るカップ14を計量器13上に移動させるカップ移動装
置44(第4図参照)が設置されている。
3 above. A control unit 42 is installed on the side of the 4th unit) 38.39, and a control unit 42 is installed on the side of the 2nd unit. A cup supply device 43 (see FIG. 3) is installed in front of the fourth unit 37, 39,
The measuring device 13 is installed in the center of each of the units 36 to 39 to measure the weight of the powder by loading the cup 14,
A cup moving device 44 (see FIG. 4) is installed behind the measuring device 13 to move the cup 14 supplied by the cup feeding device 43 onto the measuring device 13.

上記カップ供給装置43は、第3図にも示すように、連
続搬送されてきた空のカップ14.・・・。
As shown in FIG. 3, the cup supplying device 43 stores the empty cups 14 that have been continuously conveyed. ....

14を、チャックシリンダ45のチャックアーム46で
カップ受皿14aとともにチャックして、送りシリンダ
48によりベルトコンベア47の始端部47aに1個づ
つ供給する一方、後述するカップ移動装置44でベルト
コンベア47の始端部47alこ戻された粉体調合済の
カップ14をベルトコンベア47で間欠的に搬出するよ
うになっている。
14 are chucked together with the cup tray 14a by the chuck arm 46 of the chuck cylinder 45, and supplied one by one to the starting end 47a of the belt conveyor 47 by the feeding cylinder 48, while the cup moving device 44, which will be described later, A belt conveyor 47 intermittently carries out the cup 14 which has been returned and has been mixed with powder.

なお、チャックシリンダ45、チャックアーム大連する
カップ移動装置44の構成とほぼ同じである。
Note that the configuration is almost the same as that of the chuck cylinder 45 and the cup moving device 44 connected to the chuck arm.

上記カップ移動装置44は、第4図に示すように、基台
50上に設けられた移動板51の後部に前後方向に伸長
するラック52.52が取付けられ、該ラック52.5
2に、基台50に取付けられたビニオン53.53が噛
合して、送りシリンダ54の駆動により移動板51がラ
ック52とビニオン53でガイドされて平行に前後移動
するようになる。
As shown in FIG. 4, the cup moving device 44 has a rack 52.52 extending in the front-rear direction attached to the rear of a moving plate 51 provided on a base 50.
2, the pinions 53 and 53 attached to the base 50 mesh with each other, and as the feed cylinder 54 is driven, the moving plate 51 is guided by the rack 52 and the pinion 53 and moves back and forth in parallel.

上記移動板51には、チャックシリンダ55の駆動でリ
ンク56.56を介してカップ14をカップ受皿14a
とともにチャックするチャックアーム57.57が設け
られている。
The movable plate 51 has a cup 14 attached to the cup tray 14a via links 56 and 56 by driving the chuck cylinder 55.
A chuck arm 57.57 is provided for chucking together.

従って、ベルトコンベア47の始端部47aに空のカッ
プ14が供給されると、送りシリンダ54により移動板
51が前動して、チャックシリンダ55によりチャック
アーム57がカップ14をチャックし、その後、送りシ
リンダ54により移動板51が後動して、チャックシリ
ンダ55によりチャックアーム57をアンチャックして
カップ14を計量器13上に積載するようになる。
Therefore, when an empty cup 14 is supplied to the starting end 47a of the belt conveyor 47, the moving plate 51 is moved forward by the feed cylinder 54, the chuck arm 57 chucks the cup 14 by the chuck cylinder 55, and then the feed cylinder 54 causes the chuck arm 57 to chuck the cup 14. The moving plate 51 is moved backward by the cylinder 54, the chuck arm 57 is unchucked by the chuck cylinder 55, and the cup 14 is loaded onto the measuring device 13.

計量器13上のカップ14に対しては、各ユニット36
〜39の4本の供給管3.・−13が求心的に臨み、4
種の粉体がカップ14に所定量づつ供給・計量されて調
合されてゆく。
For each cup 14 on the scale 13, each unit 36
~39 four supply pipes 3.・-13 approaches centripetally, 4
A predetermined amount of seed powder is supplied and measured into the cup 14 and mixed.

そして、再びチャックアーム57が計量器13上のカッ
プ14をチャックして送りシリンダ54により移動板5
1が前動し、チャックシリンダ55によりチャックアー
ム57をアンチャックして粉[4合済のカップ14をベ
ルトフンベア47の始端部47gに戻すようになる。
Then, the chuck arm 57 chucks the cup 14 on the measuring instrument 13 again, and the moving plate 5 is moved by the feed cylinder 54.
1 moves forward, the chuck arm 57 is unchucked by the chuck cylinder 55, and the powdered cup 14 is returned to the starting end 47g of the belt holder 47.

なお、流動性の異なる種々の粉体を供給する場合、多量
供給と微量供給の供給流量をあらかじめマイクロコンピ
ュータ30に個別に入力しておけば、上記攪拌モータ9
、多量供給弁12、気体制御弁26a〜26c及び気体
圧力・流量制御部29は計量器13等からの情報に基づ
いてマイクロコンピュータ30により制御され、複数種
の粉体が調合される。
In addition, when supplying various powders with different fluidities, if the supply flow rates for large quantity supply and small quantity supply are individually input into the microcomputer 30 in advance, the stirring motor 9
, the large quantity supply valve 12, the gas control valves 26a to 26c, and the gas pressure/flow control section 29 are controlled by the microcomputer 30 based on information from the meter 13, etc., and a plurality of types of powder are mixed.

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

第1図は本発明に係る粉体の供給・計量装置の構成図、
第2図は4ユニツトタイプの供給・計量装置の斜視図、
第3図はカップ供給装置の側面図、第4図はカップ移動
装置の平面図である。 1・・・供給・計量装置、  2・・・ホッパ、2a・
・・入口、      2b・・・出口、3・・・供給
管、      12・・・多量供給弁、17・・・循
環管、     18・・・循環エゼクタ−121・・
・微量供給管、 22・・・微量供給エゼクタ−1 28・・・圧縮気体源。
FIG. 1 is a configuration diagram of a powder supply/measuring device according to the present invention;
Figure 2 is a perspective view of a 4-unit type supply/metering device.
FIG. 3 is a side view of the cup feeding device, and FIG. 4 is a plan view of the cup moving device. 1... Supply/metering device, 2... Hopper, 2a.
...Inlet, 2b...Outlet, 3...Supply pipe, 12...Mass supply valve, 17...Circulation pipe, 18...Circulation ejector-121...
- Trace supply pipe, 22... Trace supply ejector-1 28... Compressed gas source.

Claims (1)

【特許請求の範囲】[Claims] (1)ホッパの出口に連設された供給管に多量供給弁が
介設されていて、該供給管の多量供給弁の上流側と上記
ホッパの入口との間に循環管が設けられ、該循環管に、
供給管内の粉体をホッパの入口に吸引循環させる循環エ
ゼクターが介設される一方、上記供給管の多量供給弁の
上流側と下流側との間に微量供給管が設けられ、該微量
供給管に、供給管内の粉体を供給管の吐出口に吸引供給
させる微量供給エゼクターが介設されていることを特徴
とする粉体の供給装置。
(1) A large quantity supply valve is interposed in a supply pipe connected to the outlet of the hopper, and a circulation pipe is provided between the upstream side of the large quantity supply valve of the supply pipe and the inlet of the hopper, In the circulation pipe,
A circulation ejector is interposed to suck and circulate the powder in the supply pipe to the inlet of the hopper, and a small quantity supply pipe is provided between the upstream side and the downstream side of the large quantity supply valve of the supply pipe, and the small quantity supply pipe A powder supply device characterized in that a small amount supply ejector is interposed to suck and supply the powder in the supply pipe to the discharge port of the supply pipe.
JP20407485A 1985-09-13 1985-09-13 Powder supply device Pending JPS6265829A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20407485A JPS6265829A (en) 1985-09-13 1985-09-13 Powder supply device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20407485A JPS6265829A (en) 1985-09-13 1985-09-13 Powder supply device

Publications (1)

Publication Number Publication Date
JPS6265829A true JPS6265829A (en) 1987-03-25

Family

ID=16484337

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20407485A Pending JPS6265829A (en) 1985-09-13 1985-09-13 Powder supply device

Country Status (1)

Country Link
JP (1) JPS6265829A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01261816A (en) * 1988-04-12 1989-10-18 Showa Alum Corp Cooling apparatus for vacuum in vacuum chamber
JP2010083652A (en) * 2008-10-01 2010-04-15 Daishowa Seiki Co Ltd Discharging device
CN103708228A (en) * 2013-12-18 2014-04-09 镇江立达纤维工业有限责任公司 Novel powder pumping machine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01261816A (en) * 1988-04-12 1989-10-18 Showa Alum Corp Cooling apparatus for vacuum in vacuum chamber
JP2010083652A (en) * 2008-10-01 2010-04-15 Daishowa Seiki Co Ltd Discharging device
CN103708228A (en) * 2013-12-18 2014-04-09 镇江立达纤维工业有限责任公司 Novel powder pumping machine

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