JPS58104839A - Fixed quantity supply mechanism for equipment for continuously supplying fixed quantity of powder - Google Patents
Fixed quantity supply mechanism for equipment for continuously supplying fixed quantity of powderInfo
- Publication number
- JPS58104839A JPS58104839A JP20302281A JP20302281A JPS58104839A JP S58104839 A JPS58104839 A JP S58104839A JP 20302281 A JP20302281 A JP 20302281A JP 20302281 A JP20302281 A JP 20302281A JP S58104839 A JPS58104839 A JP S58104839A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- hopper
- amount
- signal
- pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G47/00—Article or material-handling devices associated with conveyors; Methods employing such devices
- B65G47/02—Devices for feeding articles or materials to conveyors
- B65G47/16—Devices for feeding articles or materials to conveyors for feeding materials in bulk
- B65G47/18—Arrangements or applications of hoppers or chutes
- B65G47/19—Arrangements or applications of hoppers or chutes having means for controlling material flow, e.g. to prevent overloading
Abstract
Description
【発明の詳細な説明】
ヒの発明は粉体の連続定量供給装置の定量供給機構に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a quantitative feeding mechanism of a continuous quantitative feeding device for powder.
従来、粉体連続定量供給装置の粉体の供給方法としては
、サージビンに貯られた粉体をロータリフィーダ、スク
リュフィーダ、スラットバルブなどによって定量的にベ
ルトコンベアやエゼクタに送シ込むのが一般的であった
。しかし、これらの方法では、サージビン内の粉体のフ
ラッシュ現象や金−などの粉体中に混在する粗粒子を噛
み込む現象が発生しやすく、またこれらの現象が発生し
た場合に粉体の計量やその制御を全く行うことができな
いなどの欠点があった。また、特にフィーダにスクリュ
フィーダを用いるものでは、サージビン内の粉体の層厚
によって、スクリュフィーダの吐出量が変動し、定量供
給が困難となる欠点奄あった。Conventionally, the conventional method for supplying powder with continuous quantitative powder supply equipment is to quantitatively feed the powder stored in a surge bin to a belt conveyor or ejector using a rotary feeder, screw feeder, slat valve, etc. Met. However, these methods tend to cause a flash phenomenon of the powder in the surge bin and a phenomenon in which coarse particles mixed in the powder such as gold are caught, and when these phenomena occur, it is difficult to weigh the powder. There were drawbacks such as the inability to control the process at all. In addition, particularly in the case where a screw feeder is used as the feeder, the discharge amount of the screw feeder varies depending on the layer thickness of the powder in the surge bin, which makes it difficult to supply the powder in a constant quantity.
この発明は上記事情に鑑みてなされたもので、フラツシ
エ現象や粗粒子噛込み現象を防止でき、粉体を精度よく
、確実に定量供給できる粉体連続定量供給装置の定量供
給機構を提供することを目的とし、サージビンとフィー
ダとの間にホッパを設け、このホッパにサージビンから
流入する粉体を制御するパルプと、ホッパ内に貯えられ
る粉体量を検出する検出機構とを設け、さらにこの検出
機構で検出された粉体量信号によって上記パルプの開度
を制御するパルプ制御機構を設けたことを特徴とするも
のである。The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a metering mechanism for a continuous metering powder feeder that can prevent the flashier phenomenon and the coarse particle clogging phenomenon, and can accurately and reliably supply a metered amount of powder. For the purpose of The present invention is characterized in that a pulp control mechanism is provided that controls the opening degree of the pulp based on a powder amount signal detected by the mechanism.
以下、図面を参照してこの発明の詳細な説明する。Hereinafter, the present invention will be described in detail with reference to the drawings.
第１図はこの発明の定量供給機構を備えた粉体連続定量
供給装置の一例を示すもので、図中符号１はセメントな
どの粉体を貯えるサージビンである。このサージビンｌ
は、その上方には粉体投入口２が設けられ、下方底部は
テーパ状に絞られ排出口３とされている・そして、内部
の粉体を常に流動状態に保つために底部が二重壁となっ
ておシ、内側の壁は多孔質板４で形成され、この多孔質
板４ｔｌ−通して粉体に空気が吹きつけられている。サ
ージビン１の下方には、排出口３に連続してホッパ５が
設けられている。このホッパ５は、ホッパ本体６と、仁
のホッパ本体６とサージビン１の排出口３とを繋〈流入
パイプ７とからなっているゎホッパ本体６は、その底部
が粉体を移送するベルトコンペア８上に開口し、また一
方の側部が切り出し口９として開口している。また、ホ
ッパ本体６内部には、サージビン１よシ流入する粉体の
脱気を促進するバッフル６αが設けられ、ホッパ本体６
上方には排気弁６ｋが設けられている。流入パイグーの
途中には、サージビン１がらホッパ本体６に流れ込む粉
体の流れを制御するバタフライバルブＩＯが設けられて
いる。そして、このバタフライバルブ１０には、このパ
ルプ１ｏｔ−開閉するエアシリンダー１と、パルプ１ｏ
の開度を規定パζ。FIG. 1 shows an example of a powder continuous quantitative feeding device equipped with a quantitative feeding mechanism according to the present invention, and reference numeral 1 in the figure is a surge bin for storing powder such as cement. This surge bottle
is provided with a powder inlet 2 above, and a tapered bottom at the bottom to serve as an outlet 3.The bottom is double-walled to keep the powder inside always in a fluid state. The inner wall is formed of a porous plate 4, and air is blown onto the powder through this porous plate 4tl. A hopper 5 is provided below the surge bin 1 and is continuous with the discharge port 3. This hopper 5 consists of a hopper body 6, an inlet pipe 7 that connects the powder hopper body 6 and the discharge port 3 of the surge bin 1; 8 , and one side thereof is opened as a cutout 9 . Furthermore, a baffle 6α is provided inside the hopper body 6 to promote deaeration of powder flowing from the surge bin 1.
An exhaust valve 6k is provided above. A butterfly valve IO is provided in the middle of the inflow pipe to control the flow of powder flowing from the surge bin 1 into the hopper body 6. The butterfly valve 10 is equipped with an air cylinder 1 that opens and closes the pulp 1ot, and an air cylinder 1 that opens and closes the pulp 1ot.
Specify the opening degree of Paζ.
するポジショナ早２とが付設されている。A positioner 2 is attached.
また、ホッパ本体６には、その上部から底部に
□向けて延び、先端が開口した検出管１３が設けられて
いる。この検出管１３の他方の端は図示しない空気供給
装置に接続され、ホッパ本体６内の開口端よシ所定の流
量の清浄な空気が所定の圧力で噴出されるようになって
いる。そして、この検出管１３の途中には一分岐管１４
が設けられ、検出管１３内の空気圧の変化を検出する圧
力検出機構１５に接続されている。圧力検出機構１５で
検出された検出管１３の圧力変化は、電気信号もしくは
空気圧信号に変換されて調節計１６に送られる。In addition, the hopper body 6 has a
A detection tube 13 is provided that extends toward □ and has an open end. The other end of the detection tube 13 is connected to an air supply device (not shown), so that a predetermined flow rate of clean air is blown out at a predetermined pressure from the open end in the hopper body 6. A branch pipe 14 is located in the middle of this detection tube 13.
is connected to a pressure detection mechanism 15 that detects changes in air pressure within the detection tube 13. The pressure change in the detection tube 13 detected by the pressure detection mechanism 15 is converted into an electrical signal or a pneumatic signal and sent to the controller 16.
調節計１６からは圧力変化に対応するパルプ制御信号が
エアシリンダ１１に送られ、検出管１３の圧力変化に対
応してエアシリンダ１１が駆動され、バタフライバルブ
ｌＯが開閉される。A pulp control signal corresponding to the pressure change is sent from the controller 16 to the air cylinder 11, and the air cylinder 11 is driven in response to the pressure change in the detection tube 13, thereby opening and closing the butterfly valve IO.
また１ベルトコンベア８には、ベル）１７上の粉体の荷
重ｔＩＩＩｌ定するロードセル１８とベルト１７の走行
速度を測定する速度計１９が設けられている。オた、は
−ドセル１８および速度計１９で検出された信号が入力
される輸送量積算計２０゜輸送量積算計２０からの信号
を変換するＦＡ変換１１！２１およびＦＡ変換器２１か
らの信号が入力される調節計２２が設けられている。さ
らに、ベルト１７の駆動モータ（図示せず）の回転を制
御する速度制御機構２３が設けられている。The belt conveyor 8 is also provided with a load cell 18 for determining the load tIII of powder on the bell 17 and a speed meter 19 for measuring the running speed of the belt 17. Also, the transport volume totalizer 20° into which the signals detected by the drive cell 18 and the speedometer 19 are input; the FA converter 11 which converts the signal from the transport volume totalizer 20; the signal from the FA converter 21 and the FA converter 21; A controller 22 is provided to which the information is input. Furthermore, a speed control mechanism 23 for controlling the rotation of a drive motor (not shown) for the belt 17 is provided.
次に、このように構成された定量供給機構の作用を第１
図について説明する。サージビン１内の粉体は、流入パ
イプ７、バタフライバルブｌＯを通ッテ、ホッパ本体６
内のベルトコンベア８のベル）１７上に堆積する。粉体
が、ホッパ本体６に設けられ九検出管１３の開口端に接
触するまで堆積すると、検出管１３の開口端から吹き出
されている空気は、粉体によってその流れが妨げられ、
そのため検出管１３内の空気の背圧が高くなる。Next, the operation of the fixed quantity supply mechanism configured in this way will be explained as follows.
The diagram will be explained. The powder in the surge bin 1 passes through the inflow pipe 7, the butterfly valve lO, and the hopper body 6.
It is deposited on the bell) 17 of the belt conveyor 8 inside. When the powder accumulates until it contacts the open end of the detection tube 13 provided in the hopper body 6, the flow of air blown out from the open end of the detection tube 13 is blocked by the powder.
Therefore, the back pressure of the air inside the detection tube 13 increases.
この圧力増加は、圧力検出機構１５によって検出され調
節計１６に送られる。調節計１６は、この圧力増加信号
によってエアシリンダ１１にバタフライバルブ１０ｔ−
閉じるようこの圧力増加信号に対応したパルプ閉信号を
送る。エアシリンダ１１は、この信号によって動作し、
バタフライバルブ１０′を閉じる。この一連の動作によ
ってホッパ５内の粉体量は一定に保もたれる。ついで、
ベルトコンベア８が動きはじめ、粉体の一定量がホッパ
本体６の切シ出し口９よシ移送されはじめると、ホッパ
５内の粉体量は減少し、検出管１３の開口端は粉体よ〕
露出し、検出管１３内の空気圧は低下する・この圧力低
下は同様に圧力検出機構１５によって検出され、圧力低
下信号として調節計１６に送られる。調節計１６はこの
信号に基づいてパルプ開信号をエアシリンダ１１に送る
。エアシリンダ１１はパルプ開信号によってバタフライ
バルブ１０を圧力低下信号に対応し丸味度まで開ける。This pressure increase is detected by the pressure detection mechanism 15 and sent to the controller 16. The controller 16 uses this pressure increase signal to apply a butterfly valve 10t- to the air cylinder 11.
A pulp closing signal corresponding to this pressure increase signal is sent to close the pulp. The air cylinder 11 operates according to this signal,
Close the butterfly valve 10'. Through this series of operations, the amount of powder in the hopper 5 is kept constant. Then,
When the belt conveyor 8 begins to move and a certain amount of powder begins to be transferred through the cutting outlet 9 of the hopper body 6, the amount of powder in the hopper 5 decreases, and the open end of the detection tube 13 becomes larger than the powder. ]
The air pressure inside the detection tube 13 decreases. This pressure decrease is similarly detected by the pressure detection mechanism 15 and sent to the controller 16 as a pressure decrease signal. The controller 16 sends a pulp open signal to the air cylinder 11 based on this signal. The air cylinder 11 opens the butterfly valve 10 to the roundness level in response to the pressure drop signal according to the pulp open signal.
バタフライバルブ１０の開放によってサージビン１内の
粉体はホッパ５内に流入する。ここで、粉体が検出管１
３の開口端に接触するまで堆積すると先に説明し九よう
に粉体の流入が抑制される。このようにして、ホッパ５
内の粉体量はその一部がベルトコンベア８によって常に
移送されるにもかかわらず常に一定に保もたれる。した
がって、サージビンｌ内で粉体の７ツクシ：Ｌ現象が生
じ、多量の粉体が一度に流動しだすことがあっても、常
にホッパ５内の粉体量は、検出管１３の開口端のレベル
によって定まる一定量に保４九れ、フラッシュ現象がベ
ルトコンベア８にまで波及することが防止されるｃｔた
、サージビン１内の粉体に金物などの粗粒子が混入して
いる場合でも、バタフライバルブ１０′ｔ−用いている
ので粗粒子を噛み込むことがない。When the butterfly valve 10 is opened, the powder in the surge bin 1 flows into the hopper 5. Here, the powder is in the detection tube 1.
If the powder is deposited until it contacts the open end of No. 3, the inflow of the powder will be suppressed as described above. In this way, hopper 5
Although part of the powder is constantly transferred by the belt conveyor 8, the amount of powder inside is always kept constant. Therefore, even if the phenomenon of 7:L of powder occurs in the surge bin 1 and a large amount of powder starts to flow at once, the amount of powder in the hopper 5 will always be at the level of the open end of the detection tube 13. The butterfly valve prevents the flash phenomenon from spreading to the belt conveyor 8 by maintaining a constant amount determined by the butterfly valve. Since 10't is used, coarse particles will not be caught.
かくして、粉体がベルトコンベア８上に移送されだすと
、輸送量積算計２０によって求められた輸送量を表わす
パルス信号がＦＡ変換器２１に人力される。ＦＡ変換器
２１では上記パルス信号がアナｐグ信号に変換され、調
節計２２に入力される。調節計２２モは、実測輸送量と
供給能力設定値との差に応じた信号が得られ、この信号
は速度制御機構２３に入力され、実測輸送量と供給能力
設定値との差がゼロとなるようにベルトコンベア８０走
行速度が調節される。これらの一連の動作によって、ベ
ルトコンベア８上で移送される粉体７１）
は常に一定に保もた五る・
なお、この例で示した粉体連続定量供給装置の供給能力
設定値が刻々変動するような場合には、供給能力設定値
をバタフライバルブ１０の開度基準信号として利用して
もよく、この場合はホツノく５内の粉体の定量化がより
一層向上する。In this way, when the powder begins to be transferred onto the belt conveyor 8, a pulse signal representing the transportation amount determined by the transportation amount totalizer 20 is inputted to the FA converter 21. The FA converter 21 converts the pulse signal into an analog/pg signal, which is input to the controller 22 . The controller 22 mo obtains a signal corresponding to the difference between the measured transport amount and the supply capacity set value, and this signal is input to the speed control mechanism 23, and the signal is inputted to the speed control mechanism 23 to indicate that the difference between the measured transport amount and the supply capacity set value is zero. The traveling speed of the belt conveyor 80 is adjusted so that. Through these series of operations, the powder 71) transferred on the belt conveyor 8 is always kept constant. Note that the supply capacity setting value of the powder continuous quantitative supply device shown in this example fluctuates from moment to moment. In such a case, the supply capacity setting value may be used as the opening degree reference signal of the butterfly valve 10, and in this case, the quantification of the powder in the hole 5 is further improved.
第２図はこの発明の定量供給機構を用いた粉体連続定量
供給装置の第２の例會示すもので、第１図に示したもの
と同一構成部分には同−符号上付してその説明を省略す
る。この例の粉体連続定量供給装置は、フィーダにスク
リュフィーダ３１を用い、スクリュフィーダ３１から吐
出された粉体はエゼクタ３２によって空気輸送されるよ
うになっている。また、エゼクタ３２に送られる空気輸
送用の高圧空気の圧力が、検出管１３の圧力変化に変動
を与えることを防止するため、スクリュフィーダ３１の
スクリュピッチを漸次狭くして粉体をスクリュフィーダ
３１内で圧縮し、この圧縮された粉体で上記圧力ｔ−遮
断している。FIG. 2 shows a second example of a continuous quantitative supply of powder using the quantitative supply mechanism of the present invention, and the same components as those shown in FIG. omitted. The powder continuous quantitative supply device of this example uses a screw feeder 31 as a feeder, and the powder discharged from the screw feeder 31 is pneumatically transported by an ejector 32. In addition, in order to prevent the pressure of the high-pressure air for pneumatic transport sent to the ejector 32 from causing fluctuations in the pressure change of the detection tube 13, the screw pitch of the screw feeder 31 is gradually narrowed to transfer the powder to the screw feeder 31. The compressed powder is used to block the pressure t-.
この粉体連続定量供給装置では、従来のδフリエフィー
ダ３１をサージビン１に直結したものとは異夛、サージ
ビン１内の粉体層厚によってスクリュフィーダ３１の粉
体の吐出量が変動することが防止される。This continuous quantitative powder supply device differs from the conventional one in which the δ Freef feeder 31 is directly connected to the surge bin 1, in that the amount of powder discharged from the screw feeder 31 varies depending on the thickness of the powder layer in the surge bin 1. Prevented.
第３図は、この発明の定量供給機構を具備した粉体連続
定量供給装置の第３の実施例を示すもので、第２図に示
したものと同一構成部分には同一符号を付してその説明
を省略する。この例では、エゼクタ３２の高圧空気の圧
力を、サージビン１０投入口２に設けられた２段式のロ
ックホッパ３３によって遮断し、検出管１３の圧力変化
に変動を与えないようになっている。FIG. 3 shows a third embodiment of a powder continuous quantitative feeding device equipped with a quantitative feeding mechanism according to the present invention, and the same components as those shown in FIG. 2 are given the same reference numerals. The explanation will be omitted. In this example, the pressure of high-pressure air in the ejector 32 is shut off by a two-stage lock hopper 33 provided at the input port 2 of the surge bin 10, so as to prevent pressure changes in the detection tube 13 from changing.
以上説明したように、この発明の定量供給機構はサージ
ビンとフィーダとの間にホッパを設け、このホッパにサ
ージビンから流入する粉体を制御するパルプと、ホッパ
内に貯えられる粉体量を検出する検出機構とを設け、さ
らにこの検出機構で検出され九粉体量信号によって上記
バルブの開度を制御するパルプ制御機構を設けたもので
あるので、ホッパ内に貯えられる粉体量はその一部がフ
ィーダに常に送られるに本かかわらず、常に一定とな９
、粉体連続定量供給装置の粉体供給量の計量精度が向上
する。また、サージビン内の粉体にフラッシュ現象が生
じても、これがフィーダまで波及することがなく、粉体
のフィーダへの供給は平常通〕おこなわれる。さらに１
粉体中に金物などの粗粒子が混入していても、パルプに
バタフライバルブを用いれば粗粒子の噛み込゛みが防止
される−さらにまた、フィーダとしてスクリュフィーダ
を用いたものでは、従来のスクリュフィーダの吐出量が
サージビン内の粉体層厚によって変化するという欠点も
解決される。As explained above, the quantitative feeding mechanism of the present invention includes a hopper between the surge bin and the feeder, and detects the pulp that controls the powder flowing into the hopper from the surge bin and the amount of powder stored in the hopper. A detection mechanism is provided, and a pulp control mechanism is further provided that controls the opening degree of the valve based on the nine powder amount signals detected by this detection mechanism, so that the amount of powder stored in the hopper is only a part of the amount of powder stored in the hopper. 9 is always constant regardless of whether it is always sent to the feeder.
, the accuracy of measuring the powder supply amount of the powder continuous quantitative supply device is improved. Furthermore, even if a flash phenomenon occurs in the powder in the surge bin, this does not spread to the feeder, and the powder is supplied to the feeder as usual. 1 more
Even if coarse particles such as metal objects are mixed into the powder, using a butterfly valve for pulp will prevent the coarse particles from getting caught in the pulp. The disadvantage that the discharge amount of the screw feeder varies depending on the thickness of the powder layer in the surge bin is also solved.
第１図ないし第３図はいずれもこの発明の定量供給機構
を備えた粉体連続定量供給装置の例會示す概略構成図で
ある。
１・・・・・・サージビン、５・・・・・・ホッパ、６
・・・・・・ホッパ本体、７・・・・・・流入パイプ、
１０・川・・バタフライバルブ、１１・・・・・・エア
シリンダ、１２・・・・・・ポジシ舊す、１３・・・・
・・検出管、力４ ”則分岐管、１５・・・・・・圧力
検出機構、１６・・・・・・調節針。
第１図1 to 3 are schematic configuration diagrams showing an example of a powder continuous quantitative feeding apparatus equipped with a quantitative feeding mechanism of the present invention. 1... Surge bin, 5... Hopper, 6
...Hopper body, 7...Inflow pipe,
10.Butterfly valve, 11..Air cylinder, 12..Position, 13..
...detection tube, force 4" law branch pipe, 15...pressure detection mechanism, 16...adjustment needle. Figure 1
Claims (1)
ジビンとこのサージピンからの粉体を移送するフィーダ
との間にホッパを設け、このホッパに上記サージビンか
らホッパに流入する粉体な制御するパルプと、ホッパ内
に貯えられる粉体量を検知する検出機構とを設け、さら
にこの検出機構から得られた粉体量信号によって、上記
パルプの開度を制御するバルブ制御機構を設けたことを
特徴とする粉体連続定量供給装置の定量供給機構。 ３ 上記検出機構が、ホッパ内に設けられ九検出管の開
口端からホッパ内の粉体に気体を吹きりけ、検出管内の
気体の背圧弯化によってホッパ内の粉体量を検出するも
のである特許請求の範囲第１項記載の粉体連続定量供給
装置の定量供給機構。 Ｓ 上記パルプがバタフライバルブである特許請求の範
囲第１項または第２項記載の粉体連続定量供給装置の定
量供給機構。[Scope of Claims] 1. In a powder continuous quantitative supply device, a hopper is provided between a surge bin for storing powder and a feeder for transferring powder from the surge pin, and the powder flowing from the surge bin into the hopper is provided in the hopper. A detection mechanism is provided to detect the amount of powder stored in the hopper, and a valve control mechanism is provided to control the opening degree of the pulp based on the powder amount signal obtained from the detection mechanism. A quantitative feeding mechanism of a powder continuous quantitative feeding device, characterized in that: 3 The above detection mechanism is installed in the hopper and blows gas from the open end of the detection tube onto the powder in the hopper, and detects the amount of powder in the hopper by increasing the back pressure of the gas in the detection tube. A quantitative feeding mechanism of a powder continuous quantitative feeding device according to claim 1. S. The quantitative feeding mechanism of the powder continuous quantitative feeding device according to claim 1 or 2, wherein the pulp is a butterfly valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20302281A JPS58104839A (en) | 1981-12-16 | 1981-12-16 | Fixed quantity supply mechanism for equipment for continuously supplying fixed quantity of powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20302281A JPS58104839A (en) | 1981-12-16 | 1981-12-16 | Fixed quantity supply mechanism for equipment for continuously supplying fixed quantity of powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58104839A true JPS58104839A (en) | 1983-06-22 |
| JPH0151407B2 JPH0151407B2 (en) | 1989-11-02 |
Family
ID=16467046
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20302281A Granted JPS58104839A (en) | 1981-12-16 | 1981-12-16 | Fixed quantity supply mechanism for equipment for continuously supplying fixed quantity of powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58104839A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6193915A (en) * | 1984-10-15 | 1986-05-12 | House Food Ind Co Ltd | Hopper type fixed quantity supplying device |
| JP2009256090A (en) * | 2008-04-21 | 2009-11-05 | Babcock Hitachi Kk | Pressurized powder supplying device and operating method therefor |
| CN102756920A (en) * | 2012-07-30 | 2012-10-31 | 巨石集团有限公司 | Continuous dense-phase positive-pressure pneumatic conveying apparatus and conveying method |
| JP2012230064A (en) * | 2011-04-27 | 2012-11-22 | Yamato Scale Co Ltd | Measuring object feeding device |
| CN103523419A (en) * | 2013-09-28 | 2014-01-22 | 无锡市麦杰机械工程有限公司 | Material cutting valve device of conveying mechanism |
| JP2020041205A (en) * | 2018-09-13 | 2020-03-19 | アイシン精機株式会社 | Method for manufacturing metal composite material and apparatus for manufacturing metal composite material |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5042582A (en) * | 1973-08-23 | 1975-04-17 | ||
| JPS53122491A (en) * | 1977-03-31 | 1978-10-25 | Sumitomo Metal Ind | Controlling method for production of powder |
-
1981
- 1981-12-16 JP JP20302281A patent/JPS58104839A/en active Granted
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5042582A (en) * | 1973-08-23 | 1975-04-17 | ||
| JPS53122491A (en) * | 1977-03-31 | 1978-10-25 | Sumitomo Metal Ind | Controlling method for production of powder |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6193915A (en) * | 1984-10-15 | 1986-05-12 | House Food Ind Co Ltd | Hopper type fixed quantity supplying device |
| JPH0238491B2 (en) * | 1984-10-15 | 1990-08-30 | House Food Industrial Co | |
| JP2009256090A (en) * | 2008-04-21 | 2009-11-05 | Babcock Hitachi Kk | Pressurized powder supplying device and operating method therefor |
| JP2012230064A (en) * | 2011-04-27 | 2012-11-22 | Yamato Scale Co Ltd | Measuring object feeding device |
| CN102756920A (en) * | 2012-07-30 | 2012-10-31 | 巨石集团有限公司 | Continuous dense-phase positive-pressure pneumatic conveying apparatus and conveying method |
| CN103523419A (en) * | 2013-09-28 | 2014-01-22 | 无锡市麦杰机械工程有限公司 | Material cutting valve device of conveying mechanism |
| CN103523419B (en) * | 2013-09-28 | 2015-11-25 | 无锡市麦杰机械工程有限公司 | The blank valve gear of conveying mechanism |
| JP2020041205A (en) * | 2018-09-13 | 2020-03-19 | アイシン精機株式会社 | Method for manufacturing metal composite material and apparatus for manufacturing metal composite material |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0151407B2 (en) | 1989-11-02 |
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