[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JPH08133474A - Forced feed pressure tank, and method and equipment for counting and forcibly feeding powder - Google Patents

Forced feed pressure tank, and method and equipment for counting and forcibly feeding powder

Info

Publication number
JPH08133474A
JPH08133474A JP27236094A JP27236094A JPH08133474A JP H08133474 A JPH08133474 A JP H08133474A JP 27236094 A JP27236094 A JP 27236094A JP 27236094 A JP27236094 A JP 27236094A JP H08133474 A JPH08133474 A JP H08133474A
Authority
JP
Japan
Prior art keywords
powder
tank
pressure
feeding
weighing hopper
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
JP27236094A
Other languages
Japanese (ja)
Inventor
Sumitaka Ishimaru
純孝 石丸
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.)
ISHIMARU SEISAKUSHO KK
Original Assignee
ISHIMARU SEISAKUSHO KK
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 ISHIMARU SEISAKUSHO KK filed Critical ISHIMARU SEISAKUSHO KK
Priority to JP27236094A priority Critical patent/JPH08133474A/en
Publication of JPH08133474A publication Critical patent/JPH08133474A/en
Pending legal-status Critical Current

Links

Landscapes

  • Air Transport Of Granular Materials (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Abstract

PURPOSE: To provide a pressure tank for forcibly feeding powder, equipment and a method for counting and forcibly feeding the powder capable of counting and forcibly feeding the powder correctly and in a short time without increasing the forced feed pressure. CONSTITUTION: A forced feed pressure tank is provided with a tank 11, two outlet nozzle 12, a stirring machine 13, a hammering mechanism 14, an inner pressure relief valve 16 and a safety valve 17. After the compressed air is fed from each outlet nozzle 12 to fluidize the powder in the tank 11, the powder in the tank 11 is stirred by the stirring machine 13. The powder in the tank 11 is forcibly fed while the continuous vibration is given to the tank 11 by the hammering mechanism 14.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、粉体、顆粒体、ペレッ
トなどをサイロや各種処理容器などに定量圧送する圧送
加圧タンクと粉体定量圧送装置及び方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pressure-feeding pressure tank for quantitatively feeding powder, granules, pellets and the like to silos and various processing containers, and a powder-quantity feeding device and method.

【0002】[0002]

【従来の技術】粉体、顆粒体などを圧縮空気でサイロや
各種処理容器などに圧送する装置及び方法には、数多く
の従来例が報告され、実用化されている。例えば、建設
業界ではセメントをセメント積載車よりサイロへ大量に
連続圧送する装置及び方法、製粉業界では製品粉体原材
料をサイロや各種処理容器へ連続圧送する装置及び方法
がある。これらの従来例では、圧送加圧タンク内に粉体
を投入した後、そのタンク内に圧縮空気を吹き込むこと
により、タンクのホッパー排出口から指定したサイロな
どへ粉体を圧送させる方法を採用している。
2. Description of the Related Art Many conventional examples have been reported and put into practical use as an apparatus and method for pressure-feeding powder, granules, etc. to a silo or various processing vessels with compressed air. For example, in the construction industry, there are devices and methods for continuously pumping a large amount of cement from a cement loading vehicle to a silo, and in the flour milling industry there are devices and methods for continuously pumping product powder raw materials to silos and various processing containers. In these conventional examples, after the powder is put into a pressure-feeding pressure tank, compressed air is blown into the tank to force-feed the powder from a hopper discharge port of the tank to a designated silo or the like. ing.

【0003】[0003]

【発明が解決しようとする課題】ところで、前記した従
来例では、圧送加圧タンク内の粉体にブリッジが生じて
空気の吹き抜け部が形成したり、圧送加圧タンクの下部
に設けられたホッパー排出口が粉体によって閉塞した
り、圧送加圧タンクの内壁に相当量の粉体が付着したり
する現象が起き圧送量の変動を来たす。これらの現象
は、粉体をスムーズに圧送する上で妨げとなり、圧送加
圧タンク内に投入した粉体の全てを正確に指定されたサ
イロや各種処理容器などへ圧送することができないとい
う問題が生じている。
By the way, in the above-mentioned conventional example, a bridge is formed in the powder in the pressure-feeding pressure tank to form a blow-through portion for air, or a hopper provided under the pressure-feeding pressure tank. The discharge port is clogged with powder, and a considerable amount of powder adheres to the inner wall of the pressure-feeding pressure tank, resulting in fluctuations in the pressure-feeding amount. These phenomena hinder the smooth powder feeding, and there is a problem that it is impossible to accurately feed all the powder put into the pressure feeding pressure tank to the designated silo or various processing containers. Has occurred.

【0004】そこで、粉体を圧送するための圧送圧力を
高めたり、圧縮空気の圧力を周期的に変動させるなどの
技術が提案されている。しかし、粉体の圧送圧力を高め
ることは空気を大量に使用することになり、装置の稼働
コストが高くなるという問題がある。また、圧縮空気を
周期的に変動させる場合には、複雑な制御システムが必
要になるとともに、粉体の圧送時間が長くなるという問
題がある。さらに、従来の圧送装置では、タンクやサク
ションホース内に粉体が詰まったり、粉体に圧密現象が
起きたりして、粉体の圧送量が変動するという問題が生
じていた。よって、圧送加圧タンクに投入する粉体の投
入量と実際の圧送量とは等しくならず、これが作業の正
確性や信頼性を高める上でボトルネックとなっていた。
Therefore, there have been proposed techniques such as increasing the pressure for pressure-feeding the powder and periodically varying the pressure of the compressed air. However, increasing the powder feeding pressure requires a large amount of air, which raises the problem of increasing the operating cost of the device. Further, when the compressed air is changed periodically, there is a problem that a complicated control system is required and the powder feeding time becomes long. Further, in the conventional pressure feeding device, there is a problem that the powder is clogged in the tank or the suction hose, or the powder compaction phenomenon occurs, so that the powder feeding amount varies. Therefore, the amount of powder fed into the pressure-feeding pressure tank is not equal to the actual amount of pressure-feeding, which is a bottleneck in improving the accuracy and reliability of the work.

【0005】ここにおいて本発明の解決すべき主要な目
的は、次の通りである。本発明の第1の目的は、短時間
で粉体を定量圧送できる圧送加圧タンクと物体定量圧送
装置及び方法を提供せんとするものである。
The main objects to be solved by the present invention are as follows. It is a first object of the present invention to provide a pressure-feeding pressure tank capable of quantitatively pressure-feeding powder in a short time, and an apparatus and method for quantitatively feeding an object.

【0006】本発明の第2の目的は、使用する圧縮空気
の量が少ない圧送加圧タンクと粉体定量圧送装置及び方
法を提供せんとするものである。
A second object of the present invention is to provide a pressure-feeding pressure tank, a powder-quantitative pressure-feeding apparatus and a method which use a small amount of compressed air.

【0007】本発明の第3の目的は、使用する圧縮空気
が低圧である圧送加圧タンクと粉体定量圧送装置及び方
法を提供せんとするものである。
A third object of the present invention is to provide a pressure-feeding pressure tank in which compressed air to be used has a low pressure, and a powder quantitative feeding device and method.

【0008】本発明の第4の目的は、圧送中圧送加圧タ
ンク壁に強制振動を与えて粉体の内壁付着を阻止する圧
送加圧タンクと粉体定量圧送装置及び方法を提供せんと
するものである。
A fourth object of the present invention is to provide a pressure-feeding pressurizing tank and a powder-quantitative pressure-feeding apparatus and method for applying forced vibration to the wall of the pressure-feeding pressurizing tank during the pressure-feeding to prevent the powder from adhering to the inner wall. It is a thing.

【0009】本発明のその他の目的は、明細書,図面,
特に特許請求の範囲の記載から自ずと明かとなろう。
Other objects of the present invention include the specification, drawings,
In particular, it will be clear from the description of the claims.

【0010】[0010]

【課題を解決するための手段】前記した課題の解決は、
本発明が次に列挙する新規な特徴的構成手段及び手法を
採用することにより達成される。すなわち、本発明タン
クの第1の特徴は、バルブ付きの粉体投入口と粉体排出
口とを有するタンクと、前記タンク内に圧縮空気を吹き
込む吹出しノズルと、前記タンクに収容した粉体を撹拌
する撹拌機と、前記タンクに振動を与えるハンマーリン
グ機構とを備えてなる圧送加圧タンクである。
[Means for Solving the Problems] To solve the above-mentioned problems,
The present invention is achieved by adopting the novel characteristic construction means and techniques listed below. That is, the first feature of the tank of the present invention is to provide a tank having a powder inlet with a valve and a powder outlet, a blow-out nozzle for blowing compressed air into the tank, and a powder contained in the tank. A pressurizing and pressurizing tank comprising a stirrer for stirring and a hammer ring mechanism for applying vibration to the tank.

【0011】本発明タンクの第2の特徴は、前記本発明
タンクの第1の特徴におけるタンクが、下端に開閉上下
動自在なバルブを臨ませた粉体投入口を天部中央に開口
する一方、当該天部にそれぞれ内圧抜きバルブと安全弁
を設け、他方、テーパー形漏斗状下部に吹出しノズルを
貫着し、当該下部下端底に排出口開口して、密閉自在に
形成してなる圧送加圧タンクである。
A second feature of the tank of the present invention is that the tank according to the first feature of the tank of the present invention has a powder inlet opening at the center of the top, which has a valve openable and closable vertically at its lower end. , A pressure relief valve and a safety valve are provided on the top, respectively, while a blow-out nozzle is attached to the lower part of the tapered funnel, and a discharge port is opened at the bottom of the lower part to form a hermetically sealed pressurization pressurization. It is a tank.

【0012】本発明タンクの第3の特徴は、前記本発明
タンクの第1又は第2の特徴における撹拌機が、タンク
の上部両側壁に亙り回転自在に貫通支承した水平ロータ
軸の中央に貫通装着するギヤボックスに上端を噛合して
垂直駆動軸を垂下する一方、当該垂直駆動軸から枝別れ
延出するアーム先端に前記タンクの下部内壁面傾斜方向
に沿って臨ませた撹拌機固設してなる圧送加圧タンクで
ある。
A third feature of the tank of the present invention is that the agitator according to the first or second feature of the tank of the present invention penetrates through the center of a horizontal rotor shaft rotatably supported on both side walls of the upper part of the tank. A vertical drive shaft is suspended by meshing the upper end with a gear box to be mounted, and a stirrer is fixed to the tip of an arm that branches and extends from the vertical drive shaft along the inclination direction of the lower inner wall surface of the tank. It is a pressure-feeding pressure tank.

【0013】本発明タンクの第4の特徴は、前記本発明
タンクの第1,第2又は第3の特徴におけるハンマーリ
ング機構が、所要数、タンクの下部外側壁の所定箇所に
それぞれ装着してなる圧送加圧タンクである。
A fourth feature of the tank of the present invention is that the required number of hammer ring mechanisms of the first, second or third feature of the tank of the present invention are mounted at predetermined positions on the lower outer wall of the tank. It is a pressure feed pressure tank.

【0014】本発明タンクの第5の特徴は、前記本発明
タンクの第1,第2,第3又は第4の特徴における前記
タンクの吹出しノズルが、複数個有してなる圧送加圧タ
ンク。
A fifth feature of the tank of the present invention is a pressure-feed pressure tank comprising a plurality of blowing nozzles of the tank according to the first, second, third or fourth feature of the tank of the present invention.

【0015】本発明装置の第1の特徴は、粉体を貯蔵す
る貯蔵タンクと、予めセットされた重量に達するまで取
入口から粉体を取り入れ、一定量の粉体を排出口から排
出する計量ホッパーと、前記貯蔵タンクから前記計量ホ
ッパーへ粉体を搬送するコンベアと、バルブ付きの粉体
投入口及び粉体排出口を有するタンク内に圧縮空気を吹
き込む吹出しノズルを設けると共に、当該タンク内に収
容した粉体を撹拌する撹拌機及び当該タンクに振動を与
えるハンマーリング機構を設けた圧送加圧タンクとを備
え、前記計量ホッパーの排出口と前記圧送加圧タンクの
粉体投入口とを直結してなる粉体定量圧送装置である。
The first feature of the device of the present invention is that a storage tank for storing the powder and a metering device for taking in the powder from the inlet until a preset weight is reached and discharging a certain amount of the powder from the outlet. A hopper, a conveyor that conveys the powder from the storage tank to the weighing hopper, and a blowing nozzle that blows compressed air into a tank having a powder inlet and a powder outlet with a valve are provided in the tank. It is equipped with a stirrer for stirring the contained powder and a pressure-feeding pressure tank provided with a hammer ring mechanism for vibrating the tank, and the discharge port of the weighing hopper and the powder feeding port of the pressure-feeding pressure tank are directly connected. This is a powder quantitative feeding device.

【0016】本発明装置の第2の特徴は、前記本発明装
置の第1の特徴における計量ホッパーが、圧送加圧タン
クの粉体投入口と直結した排出口に開閉バルブを設ける
一方、エアー吹出しノズル先端を当該排出口上端に臨ま
せ、他方、所要数,外側壁の所定箇所にそれぞれハンマ
ーリング機構を装着してなる粉体定量圧送装置である。
A second feature of the device of the present invention is that the weighing hopper according to the first feature of the device of the present invention is provided with an opening / closing valve at the discharge port directly connected to the powder charging port of the pressure-feeding pressure tank, while the air blowing is performed. In the powder quantitative feeding device, the tip of the nozzle is made to face the upper end of the discharge port, and a required number of hammer ring mechanisms are mounted at predetermined positions on the outer wall.

【0017】本発明装置の第3の特徴は、前記本発明装
置の第1又は第2の特徴におけるコンベアが、貯蔵タン
クの排出口下端に臨む水平コンベアと、上端部に計量ホ
ッパーの取入口内に下端が臨む落下口を設けた上昇傾斜
コンベアとを、粉体を引継ぎ連続搬送自在に連結してな
る粉体定量圧送装置である。
A third feature of the device of the present invention is that the conveyor according to the first or second feature of the device of the present invention is a horizontal conveyor facing the lower end of the discharge port of the storage tank, and the intake port of the weighing hopper at the upper end. Is a powder quantitative pressure feeding device in which a descending slope conveyor having a lower end facing the same is connected to a powder for continuous and continuous transfer of powder.

【0018】本発明装置の第4の特徴は、前記本発明装
置の第1,第2又は第3の特徴におけるコンベアが、計
量ホッパーに投入された粉体量が予めセットされた重量
に達すると、その稼働を停止する自動停止手段を備えて
なる粉体定量圧送装置である。
The fourth feature of the device of the present invention is that when the amount of powder introduced into the weighing hopper of the conveyor in the first, second or third feature of the device of the present invention reaches a preset weight. The powder quantitative feeding device is provided with an automatic stopping means for stopping its operation.

【0019】本発明方法の第1の特徴は、計量した粉体
を密閉加圧自在な一定の雰囲気内に投入する第1工程
と、当該雰囲気を密閉状態にして、その内部に圧縮空気
を吹き込んで、投入済みの粉体を流動化させる第2工程
と、圧送加圧タンク内に設けた適宜機械手段により、一
定時間、その密閉加圧雰囲気内の粉体を撹拌する第3工
程と、適宜振動手段により、その密閉加圧雰囲気内周に
強制振動を与えると共に、当該密閉加圧雰囲気外の指定
された場所に粉体を圧送供給する第4工程とを含んでな
る粉体定量圧送方法である。
The first feature of the method of the present invention is that the first step is to introduce the measured powder into a constant atmosphere in which the powder can be sealed and pressurized, and the atmosphere is sealed, and compressed air is blown into the interior. Then, a second step of fluidizing the charged powder and a third step of agitating the powder in the hermetically pressurized atmosphere for a certain period of time by an appropriate mechanical means provided in the pressure feeding pressure tank, A powder quantitative feeding method comprising the step of applying forced vibration to the inner circumference of the closed pressurized atmosphere by the vibrating means and feeding the powder to a specified location outside the closed pressurized atmosphere. is there.

【0020】本発明方法の第2の特徴は、前記本発明方
法の第1の特徴における適宜振動手段が、機械的手段又
は電気的手段である粉体定量圧送方法である。
A second feature of the method of the present invention is a powder quantitative feeding method in which the appropriate vibrating means in the first feature of the method of the present invention is mechanical means or electrical means.

【0021】[0021]

【作用】本発明は、前記のような手段及び手法を講じて
いるので、次のような作用が生じる。圧送加圧タンクの
撹拌機によれば、タンク内の粉体を十分にかき落として
分散させることができ、さらにブリッジやラットホール
の発生を有効に防止させることができる。圧送加圧タン
クのハンマーリング機構によれば、粉体を圧送する際に
タンクに振動を与えることができ、粉体がタンク内壁に
付着する現象を最小限に抑えることができる。
Since the present invention takes the above-mentioned means and method, the following operation occurs. According to the agitator for the pressure-feeding pressure tank, the powder in the tank can be sufficiently scraped and dispersed, and the generation of bridges and ratholes can be effectively prevented. According to the hammer ring mechanism of the pressure-feeding pressure tank, the tank can be vibrated when the powder is pressure-fed, and the phenomenon that the powder adheres to the inner wall of the tank can be minimized.

【0022】圧送加圧タンクに吹出しノズルを複数個設
けた場合では、必要な量の圧縮空気を短時間のうちに、
そのタンク内に吹き込ませることができ、しかも粉体を
タンク内で流動化させ、粉体排出口の閉塞やラットホー
ル及びブリッジの発生を防止できる。さらに、前記した
作用の相乗効果により、粉体を圧送するのに必要な圧縮
空気の圧力を低く抑え、しかも粉体を正確に短時間に圧
送できる。
When a plurality of blowing nozzles are provided in the pressure-feeding pressure tank, a required amount of compressed air is supplied within a short time.
The powder can be blown into the tank, and the powder can be fluidized in the tank to prevent the powder discharge port from being blocked and the ratholes and bridges from being generated. Further, due to the synergistic effect of the above-mentioned actions, the pressure of the compressed air required for pressure-feeding the powder can be kept low, and the powder can be pressure-fed accurately in a short time.

【0023】粉体定量圧送装置によれば、貯蔵タンク、
計量ホッパー及びコンベアを備えているので、粉体を貯
蔵タンクから計量ホッパーへ自動搬送させ、さらに予め
セットされた重量の粉体を計量ホッパーから圧送加圧タ
ンクに投入させて、指定した場所に粉体を定量圧送させ
るシステムが容易に実現できる。
According to the powder quantitative feeding device, a storage tank,
Since it is equipped with a weighing hopper and a conveyor, powder is automatically conveyed from the storage tank to the weighing hopper, and a preset weight of powder is fed from the weighing hopper into the pressure-feeding pressure tank, and the powder is delivered to the designated location. A system for quantitatively pumping the body can be easily realized.

【0024】[0024]

【実施例】【Example】

(装置例)以下、添付図面を参照し、本発明をその装置
例に基づいて、より詳細に説明する。図1は本装置例の
圧送装置の構成を示し、図2は同装置の圧送加圧タンク
の構造を示している。本装置例の圧送装置1の構成は、
図1に示すように、貯蔵タンク2、第1水平コンベア
3、第2上昇傾斜コンベア4、計量ホッパー5、圧送加
圧タンク6、サクションホース7からなる。
(Example of Device) Hereinafter, the present invention will be described in more detail based on an example of the device with reference to the accompanying drawings. FIG. 1 shows the structure of a pressure-feeding device of this device example, and FIG. 2 shows the structure of a pressure-feeding pressure tank of the device. The configuration of the pressure feeding device 1 of this device example is as follows.
As shown in FIG. 1, it comprises a storage tank 2, a first horizontal conveyor 3, a second ascending slope conveyor 4, a weighing hopper 5, a pressure feeding pressure tank 6, and a suction hose 7.

【0025】ここで、タンク2内には圧送材料が貯蔵さ
れ、かかる圧送材料は貯蔵タンク2の下部の排出口が開
閉動作することにより、第1水平コンベア3に切り出さ
れる構造になっている。なお、本装置例の装置では、定
量圧送する材料として、コンクリート混和材のシリカフ
ェーム粉体を用いることとした。
Here, the pumping material is stored in the tank 2, and the pumping material is cut out to the first horizontal conveyor 3 by opening and closing the outlet of the storage tank 2. In the device of this device example, silica fume powder, which is a concrete admixture, was used as the material for quantitatively feeding.

【0026】第1水平コンベア3は、貯蔵タンク2から
切り出したシリカフェーム粉体を第2上昇傾斜コンベア
に搬送する働きをする。第2上昇傾斜コンベア4は、そ
の稼働速度を制御することができ、第1水平コンベア3
から順次送られるシリカフェーム粉体を落下口4aを介
して計量ホッパー5内に搬送する働きをする。かかる第
2上昇傾斜コンベア4には、計量ホッパー5に投入され
た粉体量が予めセットされた重量に達するとその稼働を
停止する機能が備えられている。
The first horizontal conveyor 3 serves to convey the silica fame powder cut out from the storage tank 2 to the second ascending slope conveyor. The second ascending slope conveyor 4 can control its operating speed, and the first horizontal conveyor 3
The silica fume powder, which is sequentially sent from the above, functions to be conveyed into the weighing hopper 5 through the dropping port 4a. The second ascending slope conveyor 4 has a function of stopping the operation when the amount of the powder put into the weighing hopper 5 reaches a preset weight.

【0027】計量ホッパー5は、その上部には落下口4
aから粉体を取り入れる取入口5aが設けられ、その下
部には開閉バルブ8を有する排出口5bが設けられてい
る。さらに、計量ホッパー5には、粉体を流動化させ排
出を容易にするエアー吹出しノズル9の先端9aが、排
出口5aに臨んで設けられ、さらに計量ホッパー5自体
を上下に振動させるハンマーリング機構10が設けられ
ている。図中、9bはエアー吹出しノズル開閉電磁弁で
ある。
The weighing hopper 5 has a drop port 4 at the top thereof.
An intake port 5a for taking in the powder from a is provided, and a discharge port 5b having an opening / closing valve 8 is provided below the intake port 5a. Further, the weighing hopper 5 is provided with a tip 9a of an air blowing nozzle 9 which fluidizes the powder and facilitates discharging, facing the discharge port 5a, and further, a hammer ring mechanism for vertically vibrating the measuring hopper 5 itself. 10 are provided. In the figure, 9b is an air blowing nozzle opening / closing solenoid valve.

【0028】これにより、計量ホッパー5の排出口5b
の開閉バルブ8が開閉器8aにより開くと、収容粉体は
ハンマーリング機構10による振動を受けるとともに、
エアー吹出しノズル9のエアーで流動化されて、下側の
圧送加圧タンク6に投入される。
As a result, the discharge port 5b of the weighing hopper 5 is
When the opening / closing valve 8 of is opened by the switch 8a, the contained powder is vibrated by the hammer ring mechanism 10 and
It is fluidized by the air from the air blowing nozzle 9 and put into the lower pressure-feeding pressure tank 6.

【0029】圧送装置1を構成し、本発明の実施例を示
す圧送加圧タンク6は、図2に示すように、天部11a
中央に粉体投入口6aを突出開口し、下部11bをテー
パー形漏斗状に形成したタンク11、下部10bの下寄
り両側に2個の吹出しノズル12、撹拌機13、ハンマ
ーリング機構14、天部10aの肩寄りにそれぞれ内圧
抜きバルブ16及び安全弁17を備えている。図中、1
2aはエアー吹出しノズル開閉電磁弁である。
As shown in FIG. 2, the pressure-feeding pressure tank 6 which constitutes the pressure-feeding device 1 and which is an embodiment of the present invention, has a top portion 11a.
A tank 11 in which a powder charging port 6a is projectingly opened in the center and a lower part 11b is formed in a tapered funnel shape, two blowout nozzles 12, an agitator 13, a hammer ring mechanism 14, and a top part on both sides of the lower part 10b. An internal pressure relief valve 16 and a safety valve 17 are provided near the shoulder of 10a, respectively. In the figure, 1
Reference numeral 2a is an air blowing nozzle opening / closing solenoid valve.

【0030】タンク11には、バルブ15が開閉上下動
自在に下端に臨んで取り付けられた粉体投入口6aと、
円錐ホッパー形に形成された下部11b下端底に開口す
る粉体排出口6bとが設けられている。粉体投入口6a
のバルブ15は、電磁弁にて開閉上下作動するコーン型
バルブによって構成され、閉鎖時圧縮空気を吹き込むこ
とにより内圧を高めることができるようにタンク11内
を密閉状態にさせる。
A valve 15 is attached to the tank 11 so that a valve 15 can be opened and closed and moved up and down so as to face the lower end.
A conical hopper-shaped lower part 11b is provided with a powder discharge port 6b opening at the bottom bottom. Powder charging port 6a
The valve 15 is a cone-type valve that is opened and closed vertically by an electromagnetic valve, and the inside of the tank 11 is hermetically closed so that the internal pressure can be increased by blowing compressed air when closed.

【0031】吹出しノズル12は、タンク11の内圧を
高めるために圧縮空気を外部からタンク11内に吹き込
む働きをする。なお、本実施例では、吹出しノズル12
をタンク11の下部11bの17箇所に貫着取付ける構
成にしたが、これに限定するものではなく、さらに多く
の吹出しノズル12を設けてもよい。
The blowing nozzle 12 functions to blow compressed air into the tank 11 from the outside in order to increase the internal pressure of the tank 11. In this embodiment, the blowout nozzle 12
Although it is configured to be attached by penetrating to the lower portion 11b of the tank 11 at 17 positions, the present invention is not limited to this, and more blowing nozzles 12 may be provided.

【0032】撹拌機13は、タンク11内に投入された
粉体をかき混ぜる働きをし、粉体によるブリッジやラッ
トホールの発生を有効に防ぐ働きをする。本実施例で
は、モータの水平ロータ軸13bをタンク11の上部1
1c両側に貫着設けた左右シール軸受13aに亙り両端
を回転自在に貫着支承し、さらにロータ軸11b中央に
貫通装着したギヤーボックス13cで水平ロータ軸13
bの回転を垂直駆動軸13dと一体の撹拌桟13eの回
転に変換させる構造のものを採用した。撹拌桟13eは
垂直駆動軸13dから枝別れ延出したアーム13fの先
端に下部11b内壁面の傾斜方向に沿って臨むよう固設
されている。
The stirrer 13 functions to stir the powder charged in the tank 11 and effectively prevent the generation of bridges and ratholes due to the powder. In this embodiment, the horizontal rotor shaft 13b of the motor is connected to the upper part 1 of the tank 11.
1c both ends are rotatably supported by the left and right seal bearings 13a provided on both sides, and the horizontal rotor shaft 13 is supported by a gear box 13c which is mounted through the center of the rotor shaft 11b.
A structure in which the rotation of b is converted into the rotation of the stirring bar 13e integrated with the vertical drive shaft 13d is adopted. The stirring bar 13e is fixed to the tip of an arm 13f branched and extended from the vertical drive shaft 13d so as to face along the inclination direction of the inner wall surface of the lower portion 11b.

【0033】ハンマーリング機構14は、タンク11の
下部10b外側に設けられ、粉体を圧送する際にタンク
11の下部11bを連続的に叩いてそれに振動を与える
働きをする。これにより、粉体を圧送する際に粉体自体
がタンク11の内壁に付着する現象を最小限に抑えるこ
とができる。
The hammer ring mechanism 14 is provided outside the lower portion 10b of the tank 11 and has a function of continuously striking the lower portion 11b of the tank 11 to vibrate it when the powder is fed under pressure. This can minimize the phenomenon that the powder itself adheres to the inner wall of the tank 11 when the powder is pressure-fed.

【0034】内圧抜きバルブ16は粉体圧送作業後にタ
ンク11に残存している圧縮空気を抜くために設けら
れ、安全弁17はタンク11をその高圧破壊から防止す
るために設けられている。そして、圧送加圧タンク6の
粉体排出口6bと図を省略したバッチャープラント上階
の生コンクリート製造用プラントミキサー混練室とは、
サクションホース7によって連通されている。
The internal pressure release valve 16 is provided to release the compressed air remaining in the tank 11 after the powder pressure feeding operation, and the safety valve 17 is provided to prevent the tank 11 from being destroyed by high pressure. And, the powder discharge port 6b of the pressure-feeding pressure tank 6 and the plant mixer kneading chamber for producing fresh concrete on the upper floor of the batcher plant (not shown)
It is connected by a suction hose 7.

【0035】(方法例)次に、上述した圧送装置1を用
いて、本発明のシリカフェーム粉体を定量圧送する方法
について説明する。まず、タンク2に貯蔵された粉体を
第1及び第2コンベア3、4によって計量ホッパー5に
送り出す。計量ホッパー5では、収容粉体が所定の重量
になると、その排出口の開閉バルブ8を開き、ハンマー
リング機構10を稼働させて、エアー吹出しノズル9か
らエアーを吹き込む。これにより、計量ホッパー5にお
いて、所定の重量に計量された粉体は内部に密閉加圧雰
囲気Aを形成自在な圧送加圧タンク6内に投入される
(第1工程)。
(Example of Method) Next, a method for quantitatively pressure-feeding the silica fame powder of the present invention using the above-described pressure-feeding device 1 will be described. First, the powder stored in the tank 2 is sent to the weighing hopper 5 by the first and second conveyors 3 and 4. In the weighing hopper 5, when the contained powder reaches a predetermined weight, the opening / closing valve 8 of the discharge port is opened, the hammer ring mechanism 10 is operated, and air is blown from the air blowing nozzle 9. As a result, the powder weighed to a predetermined weight in the weighing hopper 5 is put into the pressure-feeding pressure tank 6 in which the closed pressurized atmosphere A can be freely formed (first step).

【0036】続いて、計量ホッパー5内の粉体を圧送加
圧タンク6内に投入させた後、圧送加圧タンク6のバル
ブ15を閉動作させて、タンク11内を密閉状態にす
る。次に、各吹出しノズル12から圧縮空気をタンク1
1内に供給して、タンク11内を密閉加圧雰囲気Aと
し、投入済みの粉体を流動化させる(第2工程)。この
ようにタンク11内の粉体を流動化させた後、撹拌機1
3を稼働させて、タンク11内の密閉加圧雰囲気A中に
ある粉体をかき混ぜ、粉体によるブリッジやラットホー
ルの発生を抑える(第3工程)。
Then, after the powder in the weighing hopper 5 is put into the pressure-feeding pressure tank 6, the valve 15 of the pressure-feeding pressure tank 6 is closed to make the inside of the tank 11 airtight. Next, compressed air is supplied from each of the blowout nozzles 12 to the tank 1.
1, and the inside of the tank 11 is brought into a closed pressurized atmosphere A to fluidize the charged powder (second step). After fluidizing the powder in the tank 11 in this way, the stirrer 1
3 is operated to stir the powder in the closed pressurized atmosphere A in the tank 11 to suppress the generation of bridges and ratholes due to the powder (third step).

【0037】そして、ハンマーリング機構14を稼働さ
せて、タンク11を連続的に叩いて密閉加圧雰囲気A下
部内周に強制振動を与えつつ、タンク11内の粉体を圧
送加圧タンク6の粉体排出口6b及びサクションホース
8に通して密閉加圧雰囲気A外の後段の生コンクリート
製造用プラントミキサー混練室に連続圧送させる(第4
工程)。
Then, the hammer ring mechanism 14 is operated to continuously hit the tank 11 to apply a forced vibration to the lower inner circumference of the closed pressurized atmosphere A, and the powder in the tank 11 is pressure-fed. The powder is discharged through the powder discharge port 6b and the suction hose 8 and continuously fed under pressure outside the closed pressurized atmosphere A to the plant mixer kneading chamber for the production of fresh concrete in the subsequent stage (fourth step).
Process).

【0038】かかる粉体の連続圧送作業の終了は、圧送
加圧タンク6のバルブ15の開動作と同時に作動させて
所定時間経過後にハンマーリング機構14の作動を停止
させるタイマー装置を使用したり、また、圧送加圧タン
ク6の内圧力を検出するセンサを設けて、その内圧力が
所定値以下になった場合に、ハンマーリング機構14の
作動を停止させる制御系を使用したりする。なお、密閉
加圧雰囲気A下部内周に振動を与える手段として本方法
例では、専らハンマーリング機構14を用いたが、これ
に限定されず、叩打音のない超音波振動や圧送加圧タン
ク6の固有振動数で共振を電気的に励起しても良い。
For the end of the continuous powder pressure feeding operation, a timer device that is operated simultaneously with the opening operation of the valve 15 of the pressure feeding pressure tank 6 and stops the operation of the hammer ring mechanism 14 after a predetermined time has passed, or Also, a control system is provided which is provided with a sensor for detecting the internal pressure of the pressure-feed pressurizing tank 6 and stops the operation of the hammer ring mechanism 14 when the internal pressure falls below a predetermined value. In this example of the method, the hammer ring mechanism 14 was used exclusively as a means for vibrating the inner circumference of the lower portion of the closed pressurized atmosphere A. However, the present invention is not limited to this, and the ultrasonic vibration or the pressure feeding pressure tank 6 without tapping sound is used. The resonance may be electrically excited by the natural frequency of.

【0039】本装置例によれば、計量ホッパー5から圧
送加圧タンク6内に投入させた40kgのシリカフェー
ム粉体は、粉体排出口6bから例えば、毎秒1.6kg
の割合で、ほとんど変動もなく、連続的に排出させるこ
とができた(全粉体を排出するための所要時間は25
秒)。
According to this example of the apparatus, 40 kg of silica fame powder charged from the weighing hopper 5 into the pressure-feeding pressure tank 6 is, for example, 1.6 kg per second from the powder discharge port 6b.
It was possible to discharge continuously with almost no change at the rate of (the time required to discharge all powder is 25
Seconds).

【0040】(比較例)次に、一般的な従来の圧送方法
例と比較するために、本装置例の撹拌機13及びハンマ
ーリング機構14を停止させた状態で、各吹出しノズル
12から本方法例と同様の圧縮空気をタンク11内に供
給して、シリカフェーム粉体を従来の方法例で圧送させ
る試験を試みることとした。
(Comparative Example) Next, in order to compare with an example of a general conventional pressure feeding method, the agitator 13 and the hammer ring mechanism 14 of this apparatus example are stopped, and the method is carried out from each blowing nozzle 12. It was decided to try a test in which compressed air similar to the example was supplied into the tank 11 and the silica fame powder was pumped by the conventional method example.

【0041】その結果、従来の圧送方法例では粉体排出
口から排出される粉体量が極めて減少し、定量圧送がで
きなかった。よって、本発明の圧送加圧タンク6及びこ
れを用いた本方法例を採用すれば、圧送圧力を上げずに
正確に、しかも短時間に粉体を定量圧送できるという効
果を奏する。
As a result, in the conventional pressure feeding method example, the amount of powder discharged from the powder discharge port was extremely reduced, and constant pressure feeding was not possible. Therefore, if the pressure-feeding pressure tank 6 of the present invention and the example of the method using the same are adopted, the powder can be accurately and quantitatively pressure-fed without increasing the pressure-feeding pressure.

【0042】(試験例)以上の実施例では、圧送粉体と
してコンクリート混和材のシリカフェームを用いたが、
さらに本実施例の効果を確認すべく、同様の装置を用い
て、他の圧送粉体を混練ミキサー室に連続圧送する試験
を行うこととした。試験1、試験2、試験3では、それ
ぞれ圧送粉体として、コンクリート混和材のフライアッ
シュ、高炉スラグ微粉末、農作物粉砕粉末を用いること
とした。
(Test Example) In the above examples, silica fume, which is a concrete admixture, was used as the pressure-feeding powder.
Further, in order to confirm the effect of this example, it was decided to carry out a test of continuously feeding other pressure-fed powders to the kneading mixer chamber using the same apparatus. In Test 1, Test 2, and Test 3, fly ash of concrete admixture, blast furnace slag fine powder, and crushed powder of agricultural products were used as the pressure-feed powder.

【0043】(試験1)本試験1の結果、計量ホッパー
5から圧送加圧タンク6内に投入させた40kgのフラ
イアッシュ粉体は、粉体排出口6bから毎秒1.6kg
の割合で、ほとんど変動もなく、連続的に排出させるこ
とができた(全粉体を排出するための所要時間は25
秒)。
(Test 1) As a result of the main test 1, 40 kg of fly ash powder charged from the weighing hopper 5 into the pressure-feeding pressure tank 6 is 1.6 kg per second from the powder discharge port 6b.
It was possible to discharge continuously with almost no change at the rate of (the time required to discharge all powder is 25
Seconds).

【0044】(試験2)本試験2の結果、計量ホッパー
5から圧送加圧タンク6内に投入させた40kgの高炉
スラグ微粉末は、粉体排出口6bから毎秒1.6kgの
割合で、ほとんど変動もなく、連続的に排出させること
ができた(全粉体を排出するための所要時間は25
秒)。
(Test 2) As a result of the main test 2, the 40 kg of blast furnace slag fine powder charged from the weighing hopper 5 into the pressure-feeding pressure tank 6 was almost always discharged from the powder discharge port 6b at a rate of 1.6 kg per second. It was possible to discharge continuously without fluctuation (the time required to discharge all powder was 25
Seconds).

【0045】(試験3)本試験3の結果、計量ホッパー
5から圧送加圧タンク6内に投入させた50kgの農作
物粉砕粉末は、粉体排出口6bから毎秒2kgの割合
で、ほとんど変動もなく、連続的に排出させることがで
きた(全粉体を排出するための所要時間は25秒)。
(Test 3) As a result of this test 3, 50 kg of crushed powdered agricultural products put into the pressure-feeding pressure tank 6 from the weighing hopper 5 was 2 kg per second from the powder discharge port 6b, and there was almost no change. It was possible to discharge continuously (the time required to discharge all powder was 25 seconds).

【0046】以上の本試験例の結果から、本実施例の圧
送加圧タンク、粉体定量圧送装置及び粉体定量圧送方法
によれば、種々の粉体を正確に、短時間に定量圧送でき
るのを確認できる。よって、本実施例によれば、粉体の
圧送作業の信頼性を高めることができるので、圧送量の
変動を防止でき、生産作業の安定化をも図ることができ
る。
From the above results of this test example, various powders can be accurately and quantitatively fed in a short time according to the pressure feeding / pressurizing tank, the powder quantitative feeding device and the powder quantitative feeding method of this embodiment. Can be confirmed. Therefore, according to the present embodiment, it is possible to improve the reliability of the powder pressure feeding work, so that it is possible to prevent the fluctuation of the pressure feeding amount and to stabilize the production work.

【0047】[0047]

【発明の効果】以上説明したように本発明の装置及びこ
れを用いた方法発明によれば、圧送加圧タンクに撹拌
機、ハンマーリング機構及び吹出しノズルが設けられて
いるので、これらの作用により圧送加圧タンク内に粉体
が詰まり難くなり、圧送圧力を上げずに正確に、しかも
短時間に粉体を定量圧送できるという効果を奏する。
As described above, according to the apparatus of the present invention and the method invention using the same, the pressure-feeding pressure tank is provided with the agitator, the hammer ring mechanism and the blowing nozzle. The powder is less likely to be clogged in the pressure-feeding pressure tank, and the powder can be accurately and quantitatively pressure-fed without increasing the pressure-feeding pressure.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の装置例に係る圧送装置の構成を示す概
略図である。
FIG. 1 is a schematic diagram showing a configuration of a pressure feeding device according to an example of the present invention.

【図2】同圧送装置の圧送加圧タンクの構成を示す概略
図である。
FIG. 2 is a schematic view showing a configuration of a pressure-feeding pressure tank of the same pressure-feeding device.

【符号の説明】[Explanation of symbols]

A…密閉加圧雰囲気 1…圧送装置 2…タンク 3…水平コンベア 4…上昇傾斜コンベア 4a…落下口 5…計量ホッパー 5a…取入口 5b…排出口 6…圧送加圧タンク 6a…粉体投入口 6b…粉体排出口 7…サクションホース 8,12…吹出しノズル 9…エアー吹出しノズル 9a…先端 9b…エアー吹出しノズル開閉電磁弁 10…ハンマーリング機構 11…タンク 11a…天部 11b…下部 11c…上部 13…撹拌機 13a…シール軸受 13b…水平ロータ軸 13c…ギヤボックス 13d…垂直駆動軸 13e…撹拌桟 13f…アーム 14…ハンマーリング機構 15…バルブ 16…内圧抜きバルブ 17…安全弁 A ... Hermetically pressurized atmosphere 1 ... Pressure feeding device 2 ... Tank 3 ... Horizontal conveyor 4 ... Ascending slope conveyor 4a ... Falling port 5 ... Weighing hopper 5a ... Intake port 5b ... Discharge port 6 ... Pressure feeding pressure tank 6a ... Powder input port 6b ... powder discharge port 7 ... suction hose 8,12 ... blowing nozzle 9 ... air blowing nozzle 9a ... tip 9b ... air blowing nozzle opening / closing solenoid valve 10 ... hammer ring mechanism 11 ... tank 11a ... top 11b ... bottom 11c ... upper 13 ... Stirrer 13a ... Seal bearing 13b ... Horizontal rotor shaft 13c ... Gear box 13d ... Vertical drive shaft 13e ... Stirring bar 13f ... Arm 14 ... Hammer ring mechanism 15 ... Valve 16 ... Internal pressure relief valve 17 ... Safety valve

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】バルブ付きの粉体投入口と粉体排出口とを
有するタンクと、 前記タンク内に圧縮空気を吹き込む吹出しノズルと、 前記タンクに収容した粉体を撹拌する撹拌機と、 前記タンクに振動を与えるハンマーリング機構とを備え
たことを特徴とする圧送加圧タンク。
1. A tank having a powder inlet having a valve and a powder outlet, a blow-out nozzle for blowing compressed air into the tank, a stirrer for stirring the powder contained in the tank, A pressurizing and pressurizing tank comprising a hammer ring mechanism for giving vibration to the tank.
【請求項2】タンクは、 下端に開閉上下動自在なバルブを臨ませた粉体投入口を
天部中央に開口する一方、 当該天部にそれぞれ内圧抜きバルブと安全弁を設け、 他方、テーパー形漏斗状下部に吹出しノズルを貫着し、 当該下部下端底に排出口を開口して、 密閉自在に形成した、 ことを特徴とする請求項1記載の圧送加圧タンク。
2. A tank is provided with an internal pressure relief valve and a safety valve on the top, while a powder inlet having a valve openable and closable at the lower end is opened at the center of the top. The pressure-feed pressurization tank according to claim 1, wherein a blow-out nozzle is attached to the lower part of the funnel shape, and a discharge port is opened at the bottom end of the lower part so as to be hermetically sealed.
【請求項3】攪拌機は、 タンクの上部両側壁に亙り回転自在に貫通支承した水平
ロータ軸の中央に貫通装着するギヤボックスに上端を噛
合して垂直駆動軸を垂下する一方、 当該垂直駆動軸から枝別れ延出するアーム先端に前記タ
ンクの下部内壁面傾斜方向に沿って臨ませた撹拌機を固
設する、 ことを特徴とする請求項1又は2記載の圧送加圧タン
ク。
3. A stirrer, wherein a vertical drive shaft is suspended while a top end is meshed with a gear box which is mounted through the center of a horizontal rotor shaft rotatably supported on both side walls of an upper portion of the tank, while the vertical drive shaft is suspended. The pressure-feeding pressurized tank according to claim 1 or 2, wherein an agitator facing the lower inner wall surface of the tank is fixedly provided at the tip of an arm that branches and extends from the tank.
【請求項4】ハンマーリング機構は、 所要数、タンクの下部外側壁の所定箇所にそれぞれ装着
する、 ことを特徴とする請求項1,2又は3記載の圧送加圧タ
ンク。
4. The pressurization and pressurization tank according to claim 1, wherein the required number of hammer ring mechanisms are mounted at predetermined locations on the lower outer wall of the tank, respectively.
【請求項5】前記タンクの吹出しノズルは、 複数個有する、 ことを特徴とする請求項1,2,3又は4記載の圧送加
圧タンク。
5. The pressurizing / pressurizing tank according to claim 1, wherein the blowing nozzle of the tank has a plurality of nozzles.
【請求項6】粉体を貯蔵する貯蔵タンクと、予めセット
された重量に達するまで取入口から粉体を取り入れ、一
定量の粉体を排出口から排出する計量ホッパーと、前記
貯蔵タンクから前記計量ホッパーへ粉体を搬送するコン
ベアと、 バルブ付きの粉体投入口及び粉体排出口を有するタンク
内に圧縮空気を吹き込む吹出しノズルを設けると共に、
当該タンク内に収容した粉体を撹拌する撹拌機及び当該
タンクに振動を与えるハンマーリング機構を設けた圧送
加圧タンクとを備え、 前記計量ホッパーの排出口と前記圧送加圧タンクの粉体
投入口とを直結したことを特徴とする粉体定量圧送装
置。
6. A storage tank for storing the powder, a weighing hopper for taking in the powder from the intake port until a preset weight is reached, and discharging a certain amount of the powder from the discharge port, and the storage tank for storing the powder. A conveyor for transferring powder to the weighing hopper, and a blow-out nozzle for blowing compressed air into a tank having a powder inlet and a powder outlet with valves are provided.
An agitator for agitating the powder contained in the tank and a pressure feeding pressure tank provided with a hammer ring mechanism for vibrating the tank are provided, and the discharge port of the weighing hopper and the powder feeding of the pressure feeding pressure tank. A powder quantitative feeding device characterized by being directly connected to the mouth.
【請求項7】計量ホッパーは、 圧送加圧タンクの粉体投入口と直結した排出口に開閉バ
ルブを設ける一方、 エアー吹出しノズル先端を当該排出口上端に臨ませ、 他方、所要数,外側壁の所定箇所にそれぞれハンマーリ
ング機構を装着する、 ことを特徴とする請求項6記載の粉体定量圧送装置。
7. The weighing hopper is provided with an opening / closing valve at the discharge port directly connected to the powder feeding port of the pressurizing / pressurizing tank, while making the tip of the air blowing nozzle face the upper end of the discharging port. 7. The powder quantitative feeding device according to claim 6, wherein a hammer ring mechanism is attached to each of the predetermined positions of the.
【請求項8】コンベアは、 貯蔵タンクの排出口下端に臨む水平コンベアと、 上端部に計量ホッパーの取入口内に下端が臨む落下口を
設けた上昇傾斜コンベアとを、 粉体を引継ぎ連続搬送自在に連結する、 ことを特徴とする請求項6又は7記載の粉体定量圧送装
置。
8. The conveyor is a horizontal conveyor facing the lower end of the discharge port of the storage tank, and an ascending inclined conveyor having a drop port facing the lower end in the intake of the weighing hopper at the upper end. The powder quantitative feeding device according to claim 6 or 7, characterized in that the powder quantitative feeding device is freely connected.
【請求項9】コンベアは、 計量ホッパーに投入された粉体量が予めセットされた重
量に達すると、その稼働を停止する自動停止手段を備え
た、 ことを特徴とする請求項6,7又は8に記載の粉体定量
圧送装置。
9. The conveyor is provided with an automatic stop means for stopping the operation of the conveyor when the amount of the powder put into the weighing hopper reaches a preset weight. The powder quantitative feeding device according to item 8.
【請求項10】計量した粉体を密閉加圧自在な一定の雰
囲気内に投入する第1工程と、 当該雰囲気を密閉状態にして、その内部に圧縮空気を吹
き込んで、投入済みの粉体を流動化させる第2工程と、 圧送加圧タンク内に設けた適宜機械手段により、一定時
間、その密閉加圧雰囲気内の粉体を撹拌する第3工程
と、 適宜振動手段により、その密閉加圧雰囲気内周に強制振
動を与えると共に、当該密閉加圧雰囲気外の指定された
場所に粉体を圧送供給する第4工程とを含んだことを特
徴とする粉体定量圧送方法。
10. A first step of introducing the measured powder into a constant atmosphere which can be hermetically sealed and pressurized, and the atmosphere is hermetically sealed, and compressed air is blown into the interior of the atmosphere to remove the powder already introduced. The second step of fluidizing, the third step of agitating the powder in the hermetically pressurized atmosphere for a certain period of time by an appropriate mechanical means provided in the pressure-feeding pressure tank, and the hermetic pressurization by an appropriate vibrating means. And a fourth step of feeding the powder to a designated place outside the closed pressurized atmosphere while forcibly vibrating the inner circumference of the atmosphere.
【請求項11】適宜振動手段は、 機械的手段又は電気的手段である、 ことを特徴とする請求項10記載の粉体定量圧送方法。11. The powder quantitative feeding method according to claim 10, wherein the vibrating means is a mechanical means or an electrical means as appropriate.
JP27236094A 1994-11-07 1994-11-07 Forced feed pressure tank, and method and equipment for counting and forcibly feeding powder Pending JPH08133474A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27236094A JPH08133474A (en) 1994-11-07 1994-11-07 Forced feed pressure tank, and method and equipment for counting and forcibly feeding powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27236094A JPH08133474A (en) 1994-11-07 1994-11-07 Forced feed pressure tank, and method and equipment for counting and forcibly feeding powder

Publications (1)

Publication Number Publication Date
JPH08133474A true JPH08133474A (en) 1996-05-28

Family

ID=17512801

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27236094A Pending JPH08133474A (en) 1994-11-07 1994-11-07 Forced feed pressure tank, and method and equipment for counting and forcibly feeding powder

Country Status (1)

Country Link
JP (1) JPH08133474A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005343656A (en) * 2004-06-04 2005-12-15 Bab-Hitachi Industrial Co Powder and granular material supply device, combustion device, and its operation method
KR101143549B1 (en) * 2011-06-14 2012-06-15 (주)대우건설 Apparatus for taking blocking measures upon moving concrete pumping
JP2013117460A (en) * 2011-12-05 2013-06-13 Yamato Scale Co Ltd Washing unit and weighing device
CN104016022A (en) * 2014-06-18 2014-09-03 云南大红山管道有限公司 Anti-blocking stock bin feeding system and anti-blocking feeding method
JP2015044680A (en) * 2013-08-29 2015-03-12 三菱日立パワーシステムズ株式会社 Granule feeding system and combustion device with granule feeding system
CN106219245A (en) * 2016-08-26 2016-12-14 广州番中电气设备有限公司 Integral type granular material feed conveying system
CN108069198A (en) * 2017-12-22 2018-05-25 中国航天空气动力技术研究院 A kind of powder conveying device for during consecutive production
KR101971667B1 (en) * 2018-08-21 2019-05-16 정우중공업 주식회사 One cone type bulk trailer
KR102124621B1 (en) * 2019-01-11 2020-06-18 최종갑 pneumatic conveyor capable of load detection, and discharge control using the same
WO2022151329A1 (en) * 2021-01-15 2022-07-21 河南丰博自动化有限公司 Feeding machine capable of stabilizing flow

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS522773B2 (en) * 1971-09-23 1977-01-24
JPS5218984A (en) * 1975-07-31 1977-02-12 Enkin Kagaku Seni Kk Method of two tone ombre dyeing for textile
JPS571087A (en) * 1980-05-21 1982-01-06 Toyo Watch Case Mfg Method of preventing bridge phenomenon and rathole phenomenon of hopper
JPS574025U (en) * 1980-06-06 1982-01-09
JPS6251853A (en) * 1985-08-31 1987-03-06 Nec Corp Two-wire type time division direction control transmission system
JPS631631A (en) * 1986-06-20 1988-01-06 Hitachi Zosen Corp Pressure type powder quantitative feeder
JPS6434901A (en) * 1987-07-30 1989-02-06 Hodogaya Chemical Co Ltd Herbicidal composition

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS522773B2 (en) * 1971-09-23 1977-01-24
JPS5218984A (en) * 1975-07-31 1977-02-12 Enkin Kagaku Seni Kk Method of two tone ombre dyeing for textile
JPS571087A (en) * 1980-05-21 1982-01-06 Toyo Watch Case Mfg Method of preventing bridge phenomenon and rathole phenomenon of hopper
JPS574025U (en) * 1980-06-06 1982-01-09
JPS6251853A (en) * 1985-08-31 1987-03-06 Nec Corp Two-wire type time division direction control transmission system
JPS631631A (en) * 1986-06-20 1988-01-06 Hitachi Zosen Corp Pressure type powder quantitative feeder
JPS6434901A (en) * 1987-07-30 1989-02-06 Hodogaya Chemical Co Ltd Herbicidal composition

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005343656A (en) * 2004-06-04 2005-12-15 Bab-Hitachi Industrial Co Powder and granular material supply device, combustion device, and its operation method
KR101143549B1 (en) * 2011-06-14 2012-06-15 (주)대우건설 Apparatus for taking blocking measures upon moving concrete pumping
JP2013117460A (en) * 2011-12-05 2013-06-13 Yamato Scale Co Ltd Washing unit and weighing device
JP2015044680A (en) * 2013-08-29 2015-03-12 三菱日立パワーシステムズ株式会社 Granule feeding system and combustion device with granule feeding system
CN104016022A (en) * 2014-06-18 2014-09-03 云南大红山管道有限公司 Anti-blocking stock bin feeding system and anti-blocking feeding method
CN106219245A (en) * 2016-08-26 2016-12-14 广州番中电气设备有限公司 Integral type granular material feed conveying system
CN108069198A (en) * 2017-12-22 2018-05-25 中国航天空气动力技术研究院 A kind of powder conveying device for during consecutive production
CN108069198B (en) * 2017-12-22 2024-03-15 云航时代(重庆)科技有限公司 Powder conveying device used in continuous production process
KR101971667B1 (en) * 2018-08-21 2019-05-16 정우중공업 주식회사 One cone type bulk trailer
KR102124621B1 (en) * 2019-01-11 2020-06-18 최종갑 pneumatic conveyor capable of load detection, and discharge control using the same
WO2022151329A1 (en) * 2021-01-15 2022-07-21 河南丰博自动化有限公司 Feeding machine capable of stabilizing flow

Similar Documents

Publication Publication Date Title
US7413388B2 (en) Method and apparatus for pneumatically conveying bulk material which does not flow readily
US5433520A (en) Method and apparatus for continuously processing particulate cementitious material and fly ash solids and mixing them with a liquid to provide a liquid slurry of consistent proportions
US4917309A (en) Process for micronizing solid matter in jet mills
JP2703690B2 (en) Ultrafine powder quantitative batch feeder
JPH08133474A (en) Forced feed pressure tank, and method and equipment for counting and forcibly feeding powder
US20040007285A1 (en) Metering installation for powder pigments
CN201999524U (en) Vertical type rotary feeder and pneumatic blowing device
US5503198A (en) Method and apparatus for filling containers with dry ice pellets
CN105922449A (en) Multi-stirring-tank concrete production device
CN107029628B (en) Material proportioning system, equipment and method and mixture preparation equipment
JP2003305714A (en) Method and apparatus for manufacturing concrete
JPH051307A (en) Method for injecting powdery material
CN210943469U (en) Hazardous waste solidification equipment ton bag fly ash conveying and metering system
JPH03195619A (en) Oscillating feeder for supply of pulverized/granular substance
CN110919852B (en) Modular special mortar production equipment
JP2000033996A (en) Pressure regulating apparatus for auxiliary storage tank, soil improving apparatus with the pressure regulating apparatus, and method for stabilizing quality of improved soil
CN109292461A (en) For conveying the device and method for the material being at least mainly made of solid particle
SU900978A1 (en) Set for preparing multi-component powder mixtures
US2735625A (en) B freeman
CN215323367U (en) Powder packaging system
JP4610036B2 (en) Mixed powder production equipment
JP2002225031A (en) Apparatus and method for supplying powder and grain
CN219078341U (en) Quartz sand automatic weighing and feeding machine
JPH04365725A (en) Powder feeder
CN117225562A (en) Crushing equipment and method for glass raw materials easy to absorb moisture