JPH07213887A - Discharge method of powder and granular material and its apparatus - Google Patents

Discharge method of powder and granular material and its apparatus

Info

Publication number
JPH07213887A
JPH07213887A JP1018794A JP1018794A JPH07213887A JP H07213887 A JPH07213887 A JP H07213887A JP 1018794 A JP1018794 A JP 1018794A JP 1018794 A JP1018794 A JP 1018794A JP H07213887 A JPH07213887 A JP H07213887A
Authority
JP
Japan
Prior art keywords
container
granular material
powder
compressed gas
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
Application number
JP1018794A
Other languages
Japanese (ja)
Other versions
JP2816527B2 (en
Inventor
Yasushi Watanabe
靖 渡邊
Kiyoshi Morimoto
清 森本
Yoshika Sanada
芳香 真田
Sadakazu Miwa
禎弌 三輪
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.)
KH Neochem Co Ltd
Original Assignee
Kyowa Hakko Kogyo 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 Kyowa Hakko Kogyo Co Ltd filed Critical Kyowa Hakko Kogyo Co Ltd
Priority to JP6010187A priority Critical patent/JP2816527B2/en
Publication of JPH07213887A publication Critical patent/JPH07213887A/en
Application granted granted Critical
Publication of JP2816527B2 publication Critical patent/JP2816527B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Supply Of Fluid Materials To The Packaging Location (AREA)
  • Basic Packing Technique (AREA)
  • Air Transport Of Granular Materials (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

(57)【要約】 【目的】 粉粒体を作業員の人手によることなく高精度
で且つ定量的に、しかも連続的に微量吐出させる方法及
び装置を提供し、もって微量添加物の添加作業等の作業
能率を高める。 【構成】 先端にノズル2を備えた容器3内に圧縮ガス
を供給し、この容器内圧力を一定の圧力範囲内に維持さ
せることにより、容器3内の粉粒体mを前記ノズル2か
ら連続的に且つ定量的に吐出させる。
(57) [Summary] [Purpose] To provide a method and a device for discharging minute amounts of powder and granules with high accuracy, quantitatively, and continuously without the need for manual labor of workers. Improve work efficiency. [Composition] A compressed gas is supplied into a container 3 having a nozzle 2 at its tip, and the internal pressure of the container is maintained within a certain pressure range so that powder m in the container 3 continues from the nozzle 2. Discharge quantitatively and quantitatively.

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、食品、医薬品、塗料、
粉末冶金、及びその他様々な種類の粉粒体を他の主成分
に対して微量配合し、或いは微量添加するのに好適な粉
粒体の吐出方法とその装置に関する。
The present invention relates to foods, pharmaceuticals, paints,
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a powder metallurgical method and an apparatus for discharging the powdery particles suitable for variously mixing various kinds of powdery particles with other main components or adding them in a trace amount.

【0002】[0002]

【従来の技術】例えば、医薬品としての錠剤の製造に際
しては、計量−混合−造粒−混合−製錠−検査の6工程
を経るのが一般的であるが、医薬品の能書きに微量と表
示される微量添加物の添加作業は、計量時において精密
天秤によって精秤されてから混合又は製錠工程で主薬成
分に添加されている。而して、精密天秤を用いて添加物
の精秤を行う作業にあっては、その添加物が微量で、秤
量が微小であることにより、その秤量作業を自動化する
ことが困難である。そこで、従来では、微量添加物の秤
量を作業員が手作業で行っており、このため従来ではこ
の秤量された微量添加物を主薬成分に添加する作業につ
いてもやはり作業員が手作業で行っていたのが一般的で
あった。
2. Description of the Related Art For example, in the manufacture of tablets as pharmaceuticals, it is common to go through the six steps of weighing-mixing-granulating-mixing-tabletting-inspection. In the addition work of a small amount of additive, it is added to the main ingredient in the mixing or tableting process after being precisely weighed by a precision balance at the time of measurement. Thus, in the work of precisely weighing the additive by using the precision balance, it is difficult to automate the weighing work because the amount of the additive is very small and the amount of the additive is minute. Therefore, conventionally, a worker manually weighs a trace amount of additive, and therefore, conventionally, the worker also manually adds the weighed trace amount of additive to the active ingredient. It was common.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記従
来のように人手作業によって添加物を添加していたので
は、作業員の労力負担が大きく、作業性も劣るという難
点があった。特に、医薬品の製造については、通常バッ
チ生産であるから、生産数量分の秤量作業が必要となっ
て、作業員の労力負担は一層顕著となっており、このよ
うな難点が改善されるように強く要望されていた。
However, if the additive is manually added as in the above-mentioned conventional method, there is a problem that the labor burden on the worker is large and the workability is poor. In particular, since the production of pharmaceuticals is usually batch production, it is necessary to weigh out the production quantity, and the labor burden on the workers becomes more significant, so that such difficulties will be improved. It was strongly requested.

【0004】尚、上記難点を解消する策としては、例え
ば顆粒剤の分包機に用いられる升による擦り切り方式
や、スクリューの押出しによる供給方式等に代表される
容積式の定量供給方法を採用し、添加物となる粉粒体の
秤量を行うことなく、添加物を主薬成分に対して定量供
給させることも考えられる。ところが、このような方法
では、医薬錠剤1錠あたりで微量とされる0.1〜1
〔mg〕オーダーの粉粒体の定量且つ微量の連続供給
が、粉粒体の付着性や機械の総合精度の点から困難とな
っていた。従って、錠剤の製造のように微量添加物の添
加量に非常に高い精度が要求される場合には、結局は、
その秤量を人手によって行ってから、この添加物を人手
によって主成分に添加せざるを得ない状況となってい
た。
As a measure for solving the above-mentioned difficulties, for example, a volumetric quantitative supply method represented by a scraping method using a box used in a granule packing machine, a supply method by screw extrusion, etc. is adopted, It is also conceivable that the additive is quantitatively supplied to the main drug component without weighing the powder or granules as the additive. However, in such a method, a trace amount is 0.1 to 1 per pharmaceutical tablet.
It has been difficult to quantitatively supply a minute amount of the powder or granules in the order of [mg] and continuously supply the powder or granules from the viewpoint of the adhesion of the powder or granules or the overall accuracy of the machine. Therefore, when extremely high accuracy is required for the amount of addition of a trace amount of additives, such as the production of tablets, after all,
After the weighing was performed manually, the additive had to be added to the main component manually.

【0005】本発明は上記の点に鑑みて提案されたもの
で、粉粒体を作業員の人手によることなく高精度で且つ
定量的に、しかも連続的に微量吐出させる方法及び装置
を提供し、もって微量添加物の添加作業の作業能率を高
めることを、その目的としている。
The present invention has been proposed in view of the above points, and provides a method and a device for discharging a minute amount of a granular material with high accuracy, quantitatively, and continuously without the manual operation of an operator. Therefore, the purpose is to increase the work efficiency of the work of adding a trace amount of additive.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に提案された請求項1に記載の本発明は、先端にノズル
を備えた容器内に圧縮ガスを供給し、この容器内圧力を
一定の圧力範囲内に維持させることにより、容器内の粉
粒体を前記ノズルから連続的に且つ定量的に吐出させ
る、粉粒体の吐出方法である。
The present invention as set forth in claim 1, which is proposed to achieve the above object, supplies a compressed gas into a container having a nozzle at its tip, and the pressure in the container is kept constant. By maintaining the pressure within the pressure range, the powder or granular material in the container is continuously and quantitatively discharged from the nozzle, and the powder or granular material is discharged.

【0007】請求項2に記載の本発明では、かかる請求
項1の構成において、前記容器内への圧縮ガスの供給
を、粉粒体の物性に応じて連続的又は断続的に行わせる
ようにしている。
According to a second aspect of the present invention, in the structure of the first aspect, the compressed gas is supplied into the container continuously or intermittently in accordance with the physical properties of the granular material. ing.

【0008】請求項3乃至5に記載の本発明は、上記請
求項1又は2に記載の粉粒体の吐出方法を実施するため
の装置である。即ち、請求項3に記載の本発明は、内部
に粉粒体を収容するための空間部を形成し且つ先端側に
ノズルを備えた容器と、この容器内へ圧縮ガスを供給す
るための圧縮ガス源と、この圧縮ガス源から容器内へ供
給される圧縮ガスの圧力を所定の圧力範囲内に維持させ
るための圧力設定手段とを備えた、粉粒体の吐出装置で
ある。
The present invention according to claims 3 to 5 is an apparatus for carrying out the method for discharging a powder or granular material according to claim 1 or 2. That is, the present invention according to claim 3 provides a container having a space portion for accommodating the powder and granule therein and having a nozzle on the tip side, and a compression for supplying compressed gas into the container. A powdery or granular material discharge device comprising a gas source and a pressure setting means for maintaining the pressure of the compressed gas supplied from the compressed gas source into the container within a predetermined pressure range.

【0009】請求項4に記載の本発明は、上記請求項3
の構成において、前記圧力設定手段が、容器内の圧力値
の検出を行うための圧力センサと、この圧力センサで検
出された圧力値を所定の圧力範囲内に維持させるべく圧
縮ガス源から容器内への圧縮ガスの供給の制御を行う自
動開閉バルブとから構成されている。
The present invention according to claim 4 is the above claim 3.
In the above configuration, the pressure setting means includes a pressure sensor for detecting a pressure value in the container, and a pressure sensor for maintaining the pressure value detected by the pressure sensor within a predetermined pressure range. It is composed of an automatic opening / closing valve for controlling the supply of compressed gas to.

【0010】請求項5に記載の本発明は、上記請求項3
又は4の構成において、前記容器内の粉粒体の充填量を
所定の一定量に維持させるべく容器に連結された粉粒体
貯蔵ホッパーから容器内への粉粒体の供給制御を行う粉
粒体の供給制御手段を備えている。
The present invention according to claim 5 provides the above-mentioned claim 3.
Or in the configuration of 4, the powder particles for controlling the supply of the powder particles into the container from the powder particle storage hopper connected to the container in order to maintain the filling amount of the powder particles in the container at a predetermined fixed amount. The body supply control means is provided.

【0011】請求項6乃至8は、上記請求項1、2とは
異なった構成の粉粒体の吐出方法である。即ち、請求項
6に記載の本発明は、多数の小孔を形成した多孔部を備
えた容器中に粉粒体を充填させた状態で、この容器の少
なくとも多孔部をガス流中で振動させることにより、こ
の容器内の粉粒体を前記多孔部の小孔から連続的に且つ
定量的にガス流中に吐出させる、粉粒体の吐出方法であ
る。
[0011] Claims 6 to 8 are a method of discharging a powder or granular material, which is different from the above-mentioned claims 1 and 2. That is, according to the present invention of claim 6, at least at least the porous portion of the container is vibrated in a gas flow in a state where the powdery or granular material is filled in the container having the porous portion having a large number of small holes. Thus, the method of discharging a powder or granule in which the powder or granule in the container is continuously and quantitatively discharged into the gas flow from the small holes of the porous portion.

【0012】請求項7に記載の本発明は、上記請求項6
の構成において、前記容器の少なくとも多孔部を振動さ
せる手段が、ハンマリング又はバイブレータ等による機
械的手段によって容器に振動を付与する手段である。
The present invention according to claim 7 provides the above-mentioned claim 6.
In the above configuration, the means for vibrating at least the porous portion of the container is means for imparting vibration to the container by mechanical means such as hammering or a vibrator.

【0013】請求項8に記載の本発明は、上記請求項7
とは異なり、上記請求項6の構成において、前記容器の
少なくとも多孔部を振動させる手段が、前記ガス流を脈
動流又は圧縮ガスのパルス的な噴流とする手段である。
The present invention according to claim 8 is the above claim 7.
Unlike the above, in the configuration of the above-mentioned claim 6, the means for vibrating at least the porous portion of the container is means for making the gas flow into a pulsating flow or a pulsed jet of compressed gas.

【0014】請求項9に記載の本発明は、上記請求項6
に記載の本発明に係る粉粒体の吐出方法を実施するため
の装置であり、内部に粉粒体を収容するための空間部を
形成し且つ少なくとも先端側に多数の小孔を形成した多
孔部を備えた容器と、この容器の多孔部が配置される位
置へガス流を供給させるためのガス流供給手段とを備
え、前記容器の多孔部がガス流内で振動することにより
この容器内の粉粒体が多孔部の小孔から連続的に且つ定
量的にガス流中へ吐出されるように構成された、粉粒体
の吐出装置である。
The present invention according to claim 9 is the above-mentioned claim 6.
A device for carrying out the method for discharging a powder or granule according to the present invention according to claim 1, wherein a space for accommodating the powder or granule is formed inside, and a large number of small holes are formed at least on the tip side. And a gas flow supply means for supplying a gas flow to the position where the porous part of the container is arranged, and the porous part of the container vibrates in the gas flow to thereby Is a device for discharging a granular material, which is configured to be continuously and quantitatively discharged into the gas flow from the small holes of the porous portion.

【0015】[0015]

【作用】上記構成を特徴とする請求項1に記載の本発明
に係る粉粒体の吐出方法においては、粉粒体を収容した
容器内に圧縮ガスを供給すれば、この容器内とノズル外
部との圧力差に基づいて圧縮ガスがノズルから流出し、
これに伴って容器内の粉粒体もノズルから外部へ吐出さ
れる。而して、かかる粉粒体の吐出量は、ノズルの口
径、ノズルの長さ、圧縮ガスの供給圧力等によって任意
に設定することができ、容器内の圧力を所定の圧力範囲
内で一定化させるべく制御することにより、粉粒体を微
量ずつ定量的に且つ連続的に外部へ吐出させることが可
能となる。
In the method for discharging a powder or granule according to the present invention as set forth in claim 1, the compressed gas is supplied into the container containing the powder or granule, and the inside of the container and the outside of the nozzle. Compressed gas flows out of the nozzle based on the pressure difference between
Along with this, the powder particles in the container are also discharged from the nozzle to the outside. Thus, the discharge amount of the powder or granular material can be arbitrarily set by the nozzle diameter, the nozzle length, the supply pressure of the compressed gas, etc., and the pressure in the container is made constant within a predetermined pressure range. By controlling so that it becomes possible, it is possible to discharge the powder or granular material to the outside quantitatively and continuously in minute amounts.

【0016】請求項2に記載の本発明に係る粉粒体の吐
出方法においては、容器内への圧縮ガスの供給を連続的
又は断続的に行わせるが、このうち断続的に圧縮ガスの
供給を行わせる方法は、ノズルが粉粒体によって閉塞し
易い場合に有効である。即ち、粉粒体が収容されている
容器内の圧力は、時間と共に低下するので、断続的に圧
縮ガスを供給することにより、容器内の圧力を一定の圧
力範囲内に維持させることができる。而して、このよう
な断続的な圧縮ガスの供給がなされると、パルス的な圧
力波が容器内に生じ、これが粉粒体に衝撃力又は強制的
な振動を付与するので、粉粒体がノズルに詰まりを生じ
るといった現象が解消されることとなる。尚、圧縮ガス
の断続的な供給の場合には、粉粒体の吐出量の定量性が
低下することが懸念されるものの、容器の容積に比較し
てノズルが小径であれば、容器内は圧縮ガスの供給圧と
略同等に維持され、また容器内圧力の時間的圧力降下は
微小であることより、容器内に圧縮ガスが断続的に供給
された場合であっても、ノズルからの粉粒体の吐出量は
さほど大きな変化を生じることはない。従って、充分な
定量性を確保することが可能である。
In the discharge method of the granular material according to the second aspect of the present invention, the compressed gas is supplied into the container continuously or intermittently, of which the compressed gas is intermittently supplied. This method is effective when the nozzle is likely to be blocked by the powder or granules. That is, since the pressure in the container in which the powder or granular material is stored decreases with time, the pressure in the container can be maintained within a certain pressure range by intermittently supplying the compressed gas. Thus, when such an intermittent supply of compressed gas is made, a pulsed pressure wave is generated in the container, which imparts an impact force or a forced vibration to the powder or granular material. Will eliminate the phenomenon that the nozzle is clogged. Incidentally, in the case of intermittent supply of compressed gas, although there is a concern that the quantitativeness of the discharge amount of the powder or granules may decrease, if the nozzle has a small diameter compared to the volume of the container, the inside of the container Even if the compressed gas is intermittently supplied to the container, the powder from the nozzle is maintained even if the compressed gas is supplied intermittently because the pressure of the compressed gas is maintained almost equal and the temporal pressure drop of the pressure in the container is minute. The discharge amount of the particles does not change so much. Therefore, it is possible to secure sufficient quantitativeness.

【0017】請求項3に記載の本発明に係る粉粒体の吐
出装置においては、容器内に粉粒体を収容させた状態
で、圧縮ガス源からこの容器内に圧縮ガスを供給し、し
かもこの圧縮ガス圧を圧力設定手段によって所定の圧力
範囲内に一定化させることができるので、上記請求項1
に記載の本発明に係る粉粒体の吐出方法を適切に実施で
きる。
According to the third aspect of the present invention, there is provided a powdery or granular material discharging apparatus, wherein compressed gas is supplied from a compressed gas source into the container while the powdery or granular material is contained in the container. The compressed gas pressure can be made constant within a predetermined pressure range by the pressure setting means.
The method of discharging a powder or granular material according to the present invention described in 1) can be appropriately implemented.

【0018】請求項4に記載の本発明に係る粉粒体の吐
出装置においては、圧力設定手段が圧力センサと自動開
閉バルブとで構成されているので、この自動開閉バルブ
の開閉制御によって容器内の圧力を所定の範囲内で一定
化させて粉粒体の定量吐出を行わせることができること
は勿論のこと、この自動開閉バルブの開閉によって容器
内への圧縮ガスの断続的な供給をも行うこともでき、請
求項2に記載の本発明に係る粉粒体の吐出方法をも適切
に実施できる。
In the powdery- or granular-material discharging device according to the fourth aspect of the present invention, since the pressure setting means is composed of the pressure sensor and the automatic opening / closing valve, the inside of the container is controlled by opening / closing the automatic opening / closing valve. It is of course possible to make the pressure of the container constant within a predetermined range to discharge the powdered material in a fixed amount, and also to intermittently supply the compressed gas into the container by opening and closing the automatic opening / closing valve. It is also possible to appropriately carry out the method for discharging a powder or granular material according to the present invention as set forth in claim 2.

【0019】請求項5に記載の本発明に係る粉粒体の吐
出装置においては、容器内の粉粒体がノズルから吐出さ
れることにより容器内の粉粒体の充填量が減少すると、
所定の粉粒体の供給制御手段が作動し、粉粒体貯蔵ホッ
パーから容器内へ新たな粉粒体を供給させて補充する。
従って、容器内の粉粒体の全量が短時間で消費されてし
まうことを回避でき、粉粒体の微量吐出は長時間にわた
って連続して行えることとなる。
In the discharging apparatus for powder or granular material according to the present invention as set forth in claim 5, when the powder or granular material in the container is discharged from the nozzle to reduce the filling amount of the powder or granular material in the container,
The supply control means of a predetermined powder or granular material operates to supply new powder or granular material from the powder or granular material storage hopper into the container to replenish it.
Therefore, it is possible to avoid that the entire amount of the powder or granules in the container is consumed in a short time, and a small amount of the powder or granules can be continuously discharged for a long time.

【0020】請求項6に記載の本発明に係る粉粒体の吐
出方法においては、容器の多孔部をガス流中で振動させ
ると、容器内の粉粒体がその振動作用によって多孔部の
小孔を通過してガス流中に連続的に且つ定量的に吐出さ
れる。而して、かかる粉粒体の吐出量は、多孔部の小孔
の開口径、数、多孔部の振動の周期、振幅、及びガス流
の状況等の条件により左右され、これらの各条件を所望
の条件に一定化させることにより、やはり粉粒体を微量
ずつ定量的に且つ連続して吐出させることができる。
In the discharging method of the powdery or granular material according to the sixth aspect of the present invention, when the porous portion of the container is vibrated in the gas flow, the powdery or granular material in the container is caused to vibrate by the vibrating action. It is continuously and quantitatively discharged into the gas flow through the holes. Thus, the discharge amount of the powdery particles depends on conditions such as the opening diameter and number of the small holes in the porous portion, the vibration period of the porous portion, the amplitude, and the gas flow condition. By making the desired condition constant, it is possible to quantitatively and continuously discharge a small amount of powder or granular material.

【0021】請求項8に記載の本発明に係る粉粒体の吐
出方法では、脈動流又は圧縮ガスのパルス的な噴流とさ
れたガス流によって容器の多孔部を振動させることがで
きるので、容器の多孔部を振動させるための機械的な手
段を別途設けるような必要はなく、装置構成の簡素化が
図れることとなる。
In the discharge method of powdery or granular material according to the present invention, the porous portion of the container can be vibrated by the gas flow which is a pulsating flow or a pulsed jet of compressed gas. Since it is not necessary to separately provide a mechanical means for vibrating the porous portion of the device, the device configuration can be simplified.

【0022】請求項9に記載の本発明に係る粉粒体の吐
出装置においては、多孔部を備えた容器内に粉粒体を収
容させた状態で、ガス流供給手段からその容器の多孔部
にガス流を供給させて、この容器の多孔部を振動させる
ことができるので、上記請求項6に記載の本発明に係る
粉粒体の吐出方法を適切に実施することができる。
According to a ninth aspect of the present invention, there is provided a powdery or granular material discharging device according to the present invention, wherein the powdery or granular material is contained in a container having a porous portion, and the porous portion of the container is supplied from the gas flow supply means. Since a gas flow can be supplied to the container to vibrate the porous portion of the container, the method for discharging a powder or granular material according to the present invention described in claim 6 can be appropriately implemented.

【0023】[0023]

【実施例】以下、本発明の実施例について図面を参照し
て説明する。 〔第1実施例(請求項1乃至5に対応)〕図1は、本発
明の第1実施例に係る粉粒体の吐出装置Aを示す一部切
欠断面正面図である。この吐出装置Aは、注射筒の如き
形状に形成された容器3、この容器3の上部に自動開閉
バルブ8bを介して連設された粉粒体貯蔵ホッパー4、
この粉粒体貯蔵ホッパー4や前記容器3内へ圧縮ガス
(例えば圧縮空気)を供給するための圧縮ガス源として
のガス圧縮機1(エアコンプレッサ)、及びその他後述
の各機器を具備している。
Embodiments of the present invention will be described below with reference to the drawings. [First Embodiment (corresponding to claims 1 to 5)] FIG. 1 is a partially cutaway sectional front view showing a powdery or granular material discharge device A according to a first embodiment of the present invention. The discharging device A includes a container 3 formed in a shape like an injection cylinder, a powder and granular material storage hopper 4 connected to an upper portion of the container 3 via an automatic opening / closing valve 8b,
A gas compressor 1 (air compressor) as a compressed gas source for supplying a compressed gas (for example, compressed air) to the powder and granular material storage hopper 4 and the container 3, and other devices described later are provided. .

【0024】上記のうち、容器3は、内部に粉粒体mを
収容するための空間部30を形成したもので、その下端
先端側には、細長状のパイプ部2aを有するノズル2が
装着されている。容器3の底部側は、例えばその形状が
円錐状に形成される等して、容器3内の粉粒体mがノズ
ル2内へスムースに流入するように配慮されている。ま
た、粉粒体mがノズル2の上方位置で不当に凝固して詰
まりを生じる現象(ブリッジ現象)を生じさせないよう
に、容器3内の底部に例えば陣笠状、或いはリング状の
部材(不図示)が必要に応じて設けられている。
Of the above, the container 3 has a space portion 30 for accommodating the powder or granular material m therein, and the nozzle 2 having the elongated pipe portion 2a is attached to the lower end tip side thereof. Has been done. The bottom side of the container 3 is formed in a conical shape, for example, so that the powder m or m in the container 3 smoothly flows into the nozzle 2. Further, in order to prevent a phenomenon (bridge phenomenon) in which the granular material m is improperly solidified above the nozzle 2 to cause clogging (bridge phenomenon), for example, a cap-shaped or ring-shaped member (not shown) is provided at the bottom of the container 3. ) Is provided as needed.

【0025】容器3内への粉粒体mの充填は、自動開閉
バルブ8bが開状態とされ、粉粒体貯蔵ホッパー4内に
充填されている粉粒体mが容器3内へ落下することによ
りなされる。容器3の側方には、粉粒体mの充填レベル
を検出するためのホトセンサ等で構成された粉粒体mの
上限検知センサ9と下限検知センサ10aとが設けられ
ており、容器3内の粉粒体mの充填レベルが下限検知セ
ンサ10aよりも低くなると、自動開閉バルブ8bが開
放して容器3内への粉粒体mの補給がなされる。次い
で、その後粉粒体mの充填レベルが上限検知センサ9の
レベルに達すると、自動開閉バルブ8bが閉状態となっ
て、粉粒体mの補給が停止される構成とされている。こ
の自動開閉バルブ8bの開閉動作は、別途設けられたコ
ントローラ(制御盤)12aによって制御されるように
構成されている。
The filling of the granular material m into the container 3 is carried out by opening the automatic opening / closing valve 8b and dropping the granular material m filled in the granular material storage hopper 4 into the container 3. Made by. On the side of the container 3, an upper limit detection sensor 9 and a lower limit detection sensor 10a for the granular material m, which are configured by a photosensor or the like for detecting the filling level of the granular material m, are provided. When the filling level of the granular material m becomes lower than that of the lower limit detection sensor 10a, the automatic opening / closing valve 8b is opened and the granular material m is replenished into the container 3. Then, after that, when the filling level of the powder or granular material m reaches the level of the upper limit detection sensor 9, the automatic opening / closing valve 8b is closed and the supply of the powder or granular material m is stopped. The opening / closing operation of the automatic opening / closing valve 8b is configured to be controlled by a separately provided controller (control panel) 12a.

【0026】粉粒体貯蔵ホッパー4内には配管部20か
ら逐次新たな粉粒体mを供給できるように構成されてい
る。粉粒体貯蔵ホッパー4内への粉粒体mの供給は、例
えば粉粒体貯蔵ホッパー4の底部に設けた下限検知セン
サ10bよりも粉粒体mのレベルが低下すると、その時
点で配管部20に設けられた自動開閉バルブ8cを開放
状態とさせて、新たな粉粒体mが粉粒体貯蔵ホッパー4
内へ投入されるように構成することができる。但し、こ
のような構成に代えて、例えば下限検知センサ10bよ
りも粉粒体mのレベルが低下すると、その時点で自動開
閉バルブ8aを閉、自動開閉バルブ8cを開として、容
器3内及び粉粒体貯蔵ホッパー4内を大気圧状態に復帰
させ、警報を発生させるようにしてもよい。このような
制御もコントローラ12aによって実行させることがで
きる。
Inside the powder and granular material storage hopper 4, a new powder and granular material m can be successively supplied from the pipe section 20. The supply of the granular material m into the granular material storage hopper 4 is performed, for example, when the level of the granular material m becomes lower than that of the lower limit detection sensor 10b provided at the bottom of the granular material storage hopper 4 at that time. The automatic opening / closing valve 8c provided in 20 is opened so that the new granular material m is stored in the granular material storage hopper 4.
It can be configured to be thrown in. However, instead of such a configuration, for example, when the level of the granular material m becomes lower than that of the lower limit detection sensor 10b, the automatic opening / closing valve 8a is closed and the automatic opening / closing valve 8c is opened at that time, and the inside of the container 3 and the powder are The inside of the grain storage hopper 4 may be returned to the atmospheric pressure state and an alarm may be generated. Such control can also be executed by the controller 12a.

【0027】容器3とガス圧縮機1とは配管5を介して
相互に接続されているが、容器3に対する配管5の接続
位置は、容器3内の粉粒体mの上限レベルよりも上方と
されている。配管5の途中には、ガス圧縮機1から容器
3側へ供給される圧縮空気の圧力を所定の誤差の範囲又
は許容範囲内で一定化させるための圧力設定器7や自動
開閉バルブ8aが設けられている。この自動開閉バルブ
8aは、容器3の上部に取付けられた圧力検知センサ1
1で検出される容器3内の圧力値が所定の一定値となる
ようにコントローラ12aの制御によって開閉されるも
ので、容器3内の圧力値が所定の圧力値よりも低くなる
と、開状態とされて容器3内へ圧縮空気の供給を行わせ
る。そして、容器3内が所定の圧力値に達すると、その
時点で閉状態とされて容器3内への圧縮空気の供給を停
止させるように制御されている。
The container 3 and the gas compressor 1 are connected to each other via a pipe 5, but the connecting position of the pipe 5 to the container 3 is above the upper limit level of the powder m in the container 3. Has been done. A pressure setter 7 and an automatic opening / closing valve 8a for keeping the pressure of the compressed air supplied from the gas compressor 1 to the container 3 side constant within a predetermined error range or an allowable range are provided in the middle of the pipe 5. Has been. This automatic opening / closing valve 8a is a pressure detection sensor 1 attached to the upper part of the container 3.
It is opened and closed under the control of the controller 12a so that the pressure value in the container 3 detected in 1 becomes a predetermined constant value. When the pressure value in the container 3 becomes lower than the predetermined pressure value, the open state is established. Then, the compressed air is supplied into the container 3. Then, when the inside of the container 3 reaches a predetermined pressure value, the container 3 is closed at that time, and the supply of the compressed air into the container 3 is controlled to be stopped.

【0028】ガス圧縮機1からの圧縮空気は、容器3内
へ供給されるだけではなく、分岐配管6を介して粉粒体
貯蔵ホッパー4内にも供給される。これは、粉粒体貯蔵
ホッパー4内と容器3内との圧力差をなくし、自動開放
バルブ8bが開放された際に容器3内の粉粒体mが粉粒
体貯蔵ホッパー4側へ逆流するのを防止するためであ
る。
The compressed air from the gas compressor 1 is supplied not only into the container 3 but also into the granular material storage hopper 4 through the branch pipe 6. This eliminates the pressure difference between the inside of the powder storage hopper 4 and the inside of the container 3, and when the automatic opening valve 8b is opened, the powder m in the container 3 flows back to the side of the powder storage hopper 4. This is to prevent this.

【0029】次に、上記粉粒体の吐出装置Aを用いた場
合の本発明に係る粉粒体の吐出方法の一例について説明
する。先ず、容器3内に適量の粉粒体mを充填させた状
態において、自動開閉バルブ8aを開放させて、ガス圧
縮機1から容器3内に圧縮空気を連続的に供給し、容器
3内が所定の一定圧に達した時点で自動開閉バルブ8a
を閉じればよい。これにより、容器3に供給された圧縮
空気がノズル2から排気され、これに伴って粉粒体mも
ノズル2から外部に吐出されることとなる。
Next, an example of a method for discharging powdery or granular material according to the present invention when the above-mentioned powdery or granular material discharging apparatus A is used will be described. First, while the container 3 is filled with an appropriate amount of the granular material m, the automatic opening / closing valve 8a is opened and the compressed air is continuously supplied from the gas compressor 1 into the container 3 to Automatic opening / closing valve 8a when a predetermined constant pressure is reached
Just close. As a result, the compressed air supplied to the container 3 is exhausted from the nozzle 2 and, along with this, the granular material m is also discharged from the nozzle 2 to the outside.

【0030】この粉粒体mの吐出量は、ノズル2等の各
部の形状や寸法的な条件を一定化させた条件下では、容
器3内の圧力を所定の値にすることにより定量化するこ
とができる。そして、この圧力値を所望の値に制御する
ことにより、粉粒体mの吐出量を任意の所望量に加減し
た上で、連続的に且つ定量的に微量吐出させることがで
きる。ノズル2から圧縮空気が順次排気されると容器3
内の圧力値は低下するが、この圧力値が一定値以下にな
ると自動開閉バルブ8aが開放して圧縮空気が容器3内
に補充されるので、容器3内の圧力は略一定値に維持さ
れることとなり、粉粒体mの定量的な微量吐出を継続し
て実行することが可能である。
The discharge amount of the powder or granular material m is quantified by setting the pressure in the container 3 to a predetermined value under the condition that the shape and dimensional conditions of each part such as the nozzle 2 are made constant. be able to. By controlling this pressure value to a desired value, it is possible to continuously and quantitatively eject a small amount of the powder m after adjusting the ejection amount of the powder m to any desired amount. When the compressed air is sequentially discharged from the nozzle 2, the container 3
Although the internal pressure value decreases, when the internal pressure value falls below a certain value, the automatic opening / closing valve 8a opens and the compressed air is replenished in the container 3, so that the internal pressure of the container 3 is maintained at a substantially constant value. As a result, it is possible to continuously carry out the quantitative minute discharge of the powder m.

【0031】また、本発明では、ガス圧縮機1から容器
3内に連続的に圧縮空気を供給させるだけではなく、自
動開閉バルブ8aを一定時間の間隔で開閉させて、圧縮
空気を容器3内へ断続的に供給させるようにしてもよ
い。かかる断続的な圧縮空気の供給によれば、容器3内
にパルス的な圧力波を生じさせて、粉粒体mを強制的に
振動させることができるので、粉粒体mがノズル2の内
部に詰まりを生じるようなことを極力防止することが可
能である。
Further, in the present invention, not only is compressed air continuously supplied from the gas compressor 1 into the container 3, but the automatic opening / closing valve 8a is opened / closed at regular time intervals so that the compressed air is contained in the container 3. May be supplied intermittently. By such intermittent supply of compressed air, it is possible to generate a pulsed pressure wave in the container 3 and forcibly vibrate the granular material m, so that the granular material m is inside the nozzle 2. It is possible to prevent the occurrence of clogging in the interior.

【0032】表1に、本実施例に係る粉粒体の吐出方法
の試験条件を示す。圧縮ガスの断続供給は50〔mse
c〕ごとに自動開閉バルブ8aを開閉させ、設定圧力に
達するまでこれを繰り返す方法で試験を行った。
Table 1 shows the test conditions of the discharging method of the powdery or granular material according to the present embodiment. The intermittent supply of compressed gas is 50 [mse
The automatic opening / closing valve 8a was opened / closed every c], and this was repeated until the set pressure was reached.

【表1】 [Table 1]

【0033】表2に、上記表1で示した試験を10分間
連続して試験し、それを5回繰り返した場合の1分間あ
たりの平均吐出量、及び変動係数(標準偏差÷平均吐出
量×100〔%〕)を示す。
In Table 2, the test shown in Table 1 above is continuously tested for 10 minutes, and the average discharge amount per minute when the test is repeated 5 times and the variation coefficient (standard deviation ÷ average discharge amount ×) 100 [%]) is shown.

【表2】 [Table 2]

【0034】表1に示す試験条件において、ノズル2の
目詰まりは認められなかった。また、圧縮空気の吐出方
法を連続と断続の何れに変えた場合にも、変動係数に大
きな変化は認められず、粉粒体吐出の定量性に悪影響を
与えなかった。更に、圧縮空気の供給圧力やノズル径を
適切に選択することにより、定量的に任意の微量吐出量
が得られることが確認された。
Under the test conditions shown in Table 1, the nozzle 2 was not clogged. Further, when the method of discharging the compressed air was changed to either continuous or intermittent, no large change was observed in the coefficient of variation, and there was no adverse effect on the quantitativeness of discharge of the granular material. Furthermore, it was confirmed that an appropriate minute discharge amount can be quantitatively obtained by appropriately selecting the supply pressure of compressed air and the nozzle diameter.

【0035】〔第2実施例(請求項6、8、9に対
応)〕図2は、本発明の第2実施例に係る粉粒体の吐出
装置Aaを示す要部断面図である(第1実施例と同一部
位は同一符号で示す。他の図も同様)。この吐出装置A
aは、ガス流供給手段18から供給されてくるガス流の
ガイドを行うための吐出管16、この吐出管16の上部
に連設された短管部17内に一部挿入した状態に設けら
れた容器13、及びこの容器13に自動開閉バルブ8b
を介して接続された粉粒体貯蔵ホッパー4等を具備して
いる。
[Second Embodiment (corresponding to Claims 6, 8 and 9)] FIG. 2 is a sectional view of a main part showing a powdery or granular material discharge device Aa according to a second embodiment of the present invention (first embodiment). The same parts as those in the first embodiment are designated by the same reference numerals, and the same applies to other drawings). This discharge device A
a is provided in a state in which it is partially inserted into the discharge pipe 16 for guiding the gas flow supplied from the gas flow supply means 18 and the short pipe portion 17 connected to the upper part of the discharge pipe 16. Container 13 and automatic opening / closing valve 8b for this container 13
It is provided with a powder and granular material storage hopper 4 and the like connected via.

【0036】上記のうち、ガス流供給手段18として
は、例えば圧縮空気を一定時間間隔で断続的に供給する
ことにより圧縮空気をパルス的な噴流状態で供給すべく
構成された装置、又は空気圧が周期的に変動する脈動状
態の空気供給を行う装置が適用されている。
Of the above, the gas flow supply means 18 is, for example, a device configured to supply compressed air in a pulsed jet state by intermittently supplying compressed air at fixed time intervals, or an air pressure. A device that supplies air in a pulsating state that changes periodically is applied.

【0037】容器13は、内部に粉粒体mを収容するた
めの空間部30aを形成した筒状の容器本体13の下端
先端部に、可撓性を有する軟質な袋状に形成されたフッ
素樹脂(商品名:テフロン)製の濾布15がクランプバ
ンド14aによってクランプされて取付けられている。
この濾布15は、例えば150メッシュに相当するメッ
シュ状のもので、本発明の小孔15aを多数形成した多
孔部に相当し、この袋状に形成された濾布15内にも粉
粒体mが充填される。容器13は、その外周に取付けら
れたフランジ部31が短管部17のフランジ部17a上
に載置されてクランパー32によってクランプされるこ
とにより短管部17内に挿入された状態に取付けられ、
これにより容器13の下端先端部に位置する濾布15が
吐出管16内に配置されている。
The container 13 has a flexible soft bag-like fluorine formed at the lower end of a cylindrical container body 13 having a space 30a for accommodating the powder or granular material m therein. A filter cloth 15 made of resin (trade name: Teflon) is clamped and attached by a clamp band 14a.
The filter cloth 15 has a mesh shape corresponding to, for example, 150 mesh, and corresponds to a porous portion having a large number of small holes 15a according to the present invention. m is filled. The container 13 is mounted in a state in which the flange portion 31 attached to the outer periphery of the container 13 is placed on the flange portion 17a of the short pipe portion 17 and clamped by the clamper 32 so that the container 13 is inserted into the short pipe portion 17.
As a result, the filter cloth 15 located at the lower end of the container 13 is arranged in the discharge pipe 16.

【0038】容器13への粉粒体mの投入は、容器13
内の粉粒体mの充填レベルが検知センサ19よりも下降
した時点で自動開閉バルブ8bが開放し、粉粒体貯蔵ホ
ッパー4内の粉粒体mが容器13内へ落下することによ
りなされ、容器13内には常に一定量以上の粉粒体mが
収容された状態となるように構成されている。これによ
り、容器13の最下部に位置する濾布15内の粉粒体m
には、常に一定の粉粒体圧が作用した状態となってい
る。尚、上記のような容器13内への粉粒体mの投入動
作はコントローラ12bによって自動制御される。
The powder m is introduced into the container 13 in the container 13
The automatic opening / closing valve 8b is opened at the time when the filling level of the powder or granules m therein falls below the detection sensor 19, and the powder or granules m in the powder or granule storage hopper 4 falls into the container 13, The container 13 is configured to always contain a certain amount or more of the granular material m. As a result, the granular material m in the filter cloth 15 located at the bottom of the container 13
Is always in a state in which a constant granular material pressure is applied. It should be noted that the operation of charging the powder or granular material m into the container 13 as described above is automatically controlled by the controller 12b.

【0039】上記構成の粉粒体の吐出装置Aaでは、容
器13内へ粉粒体mを収容させた状態において、ガス流
供給手段18から吐出管16内へ圧縮空気を一定時間間
隔で断続的に供給し、或いは脈動状態の空気供給を行わ
せて、吐出管16内に空気圧が変動するガス流を生じさ
せると、このガス流によって濾布15を左右に揺動させ
た状態に振動させることができる。すると、この濾布1
5内に収容されている粉粒体mは、濾布15の振動動作
によって濾布15の多数の小孔15a(メッシュ孔)を
通過して吐出管16内へ微量ずつ連続して定量的に流出
することとなる。従って、吐出管16からは、圧縮空気
のガス流と共に、微量の粉粒体mを連続して定量的に吐
出させることができる。
In the powdery or granular material discharge device Aa having the above structure, compressed air is intermittently supplied from the gas flow supply means 18 into the discharge pipe 16 at regular time intervals while the powdery or granular material m is contained in the container 13. Or a pulsating air supply to generate a gas flow in which the air pressure fluctuates in the discharge pipe 16, the filter cloth 15 is oscillated in a left-right oscillated state by this gas flow. You can Then, this filter cloth 1
The granular material m accommodated in 5 passes through a large number of small holes 15a (mesh holes) of the filter cloth 15 by the vibration operation of the filter cloth 15 and is continuously and quantitatively transferred into the discharge pipe 16 in small amounts. It will be leaked. Therefore, it is possible to continuously and quantitatively discharge a minute amount of the granular material m from the discharge pipe 16 together with the gas flow of the compressed air.

【0040】本実施例では、ガス流として脈動空気を用
いて、表3に示す条件で試験を行った。評価方法は、第
1実施例と同様である。
In this example, pulsating air was used as the gas flow, and the test was conducted under the conditions shown in Table 3. The evaluation method is the same as in the first embodiment.

【表3】 [Table 3]

【0041】表4に試験結果を示す。試験結果におい
て、濾布15に目詰まりは認められず、脈動空気の脈動
周期や吐出量を変えることにより、粉粒体の吐出濃度を
任意に変化させることができた。また、脈動周期を変え
ても変動係数に大きなばらつきは認められず、吐出の定
量性に悪影響を与えなかった。
Table 4 shows the test results. In the test results, no clogging was found in the filter cloth 15, and the discharge concentration of the powdery or granular material could be arbitrarily changed by changing the pulsation cycle or discharge amount of the pulsating air. Further, even if the pulsation cycle was changed, no large variation was found in the coefficient of variation, and there was no adverse effect on the quantitativeness of ejection.

【表4】 [Table 4]

【0042】〔第3実施例(請求項6、7、9に対
応)〕図3は、本発明の第3実施例に係る粉粒体の吐出
装置Abの一部切欠断面図である。この吐出装置Ab
は、その基本的な構成は第2実施例で示した吐出装置A
aと共通するが、容器13には、この容器13に対して
振動を付与するためのバイブレータ33が取付けられ、
このバイブレータ33の作動によって容器13に振動を
付与し、その先端部の濾布15を振動させ得るように構
成されている。尚、好ましくは、容器13は短管部17
に対してフレキシブルな状態に取付けられ、濾布15が
バイブレータ33の振動によって充分に大きな振幅で振
動するように配慮されている。吐出管16内にガス流を
供給するためのガス流供給手段18Aとしては、第2実
施例の場合とは異なり、空気圧変動のない連続した通常
の送風動作(空気供給)を行うものが適用されている。
[Third Embodiment (Corresponding to Claims 6, 7, and 9)] FIG. 3 is a partially cutaway sectional view of a powdery or granular material discharging device Ab according to a third embodiment of the present invention. This discharge device Ab
The basic structure of the discharging device A is shown in the second embodiment.
Although it is common to a, a vibrator 33 for applying vibration to the container 13 is attached to the container 13,
Vibration is applied to the container 13 by the operation of the vibrator 33, and the filter cloth 15 at the tip of the container 13 can be vibrated. In addition, preferably, the container 13 has a short tube portion 17
The filter cloth 15 is mounted in a flexible state with respect to the filter cloth 15 so that the filter cloth 15 vibrates with a sufficiently large amplitude by the vibration of the vibrator 33. Unlike the case of the second embodiment, as the gas flow supply means 18A for supplying the gas flow into the discharge pipe 16, a device for performing a continuous normal blow operation (air supply) without air pressure fluctuation is applied. ing.

【0043】上記構成の吐出装置Abにあっては、ガス
流供給手段18Aで発生されるガス流によって濾布15
を積極的に振動させることはできないものの、濾布15
をバイブレータ33の振動付与作用によって吐出管16
内のガス流中において振動させることができる。従っ
て、かかる装置構成であっても、第2実施例の場合と同
様に、濾布15の多数の小孔15aから粉粒体mを連続
的に且つ定量的に吐出させることができ、この粉粒体m
をガス流によって所定の位置へ適切に導くことが可能で
ある。
In the discharge device Ab having the above structure, the filter cloth 15 is supplied by the gas flow generated by the gas flow supply means 18A.
Although it cannot vibrate positively, the filter cloth 15
The discharge pipe 16 is provided by the vibration applying action of the vibrator 33.
It can be vibrated in the gas flow inside. Therefore, even with such a device configuration, as in the case of the second embodiment, it is possible to continuously and quantitatively discharge the granular material m from the large number of small holes 15a of the filter cloth 15. Grain m
Can be properly guided to a predetermined position by the gas flow.

【0044】〔他の実施例〕尚、上記構成の吐出装置A
bにあっては、バイブレータ33に代えて、容器13に
対してハンマリング動作を行う装置を設けた場合にも同
様な作用が得られる。また、請求項6乃至9に記載の本
発明では、容器13の全体を振動させるように構成して
もよいが、必ずしもこれに限定されず、例えば濾布15
の部分に機械的振動を直接付与させて、この濾布15の
箇所のみを部分的に振動させるようにしてもよい。
[Other Embodiments] Incidentally, the discharge device A having the above construction
In the case of b, the same effect can be obtained when a device for performing a hammering operation is provided for the container 13 instead of the vibrator 33. Further, in the present invention described in claims 6 to 9, the whole container 13 may be configured to vibrate, but the invention is not necessarily limited to this, and for example, the filter cloth 15
It is also possible to directly apply mechanical vibration to the part to partially vibrate only the portion of the filter cloth 15.

【0045】更に、本発明では、濾布15を必ずしも袋
状に形成する必要もない他、多孔部を濾布によって形成
する必要もない。例えば図4に示すように、容器13A
の底部にフィルター15Aを設けて、このフィルター孔
から粉粒体mが吐出されるように構成してもよい。ま
た、かかるフィルター15A以外として、例えば容器1
3Aにパンチング孔を施すようにしても構わない。
Further, in the present invention, the filter cloth 15 does not necessarily have to be formed in a bag shape, and the porous portion need not be formed by the filter cloth. For example, as shown in FIG. 4, the container 13A
A filter 15A may be provided at the bottom of the filter, and the powder m may be discharged from this filter hole. In addition to the filter 15A, for example, the container 1
A punching hole may be provided in 3A.

【0046】上記した第1〜第3の各実施例では、圧縮
ガス又はガス流の媒体として空気を用いているが、本発
明はこれに限定されず、空気以外の気体(例えば不活性
ガス等)を用いてもよいことは言うまでもない。その
他、本発明では、粉粒体mの具体的な種類も決して限定
されない。
In each of the above-mentioned first to third embodiments, air is used as the medium of the compressed gas or gas flow, but the present invention is not limited to this, and a gas other than air (for example, an inert gas or the like). It goes without saying that) may be used. Besides, in the present invention, the specific type of the powder or granular material m is by no means limited.

【0047】[0047]

【発明の効果】以上の説明から理解されるように、請求
項1、2、及び6乃至8に記載の本発明に係る粉粒体の
吐出方法によれば、粉粒体を作業員の人手によることな
く高精度で且つ定量的に微量吐出させることができるの
で、食品や医薬品等の各種分野において微量添加物を人
手によって秤量することなく、所望の主成分に対しての
正確な微量添加が行えることとなり、微量添加作業の作
業能率の向上が図れるという格別な効果が得られる。
As can be understood from the above description, according to the method for discharging powdery particles according to the present invention described in claims 1, 2, and 6 to 8, the powdery particles can be manually handled by a worker. Since it is possible to accurately and quantitatively discharge a small amount of trace additive without depending on, it is possible to accurately add a trace amount to a desired main component without manually weighing a trace amount additive in various fields such as foods and pharmaceuticals. As a result, it is possible to obtain a special effect that the work efficiency of the small amount addition work can be improved.

【0048】特に、請求項2に記載の本発明によれば、
容器内への圧縮ガスの供給を断続的に行わせた場合に
は、粉粒体がノズルに詰まりを生じるようなことも極力
解消できて好ましい。また、請求項8に記載の本発明に
よれば、ガス流によって容器の多孔部を振動させること
ができるので、振動付与手段としてバイブレータ等の機
械的手段を採用する必要がなくなり、装置構成の簡素化
が図れる利点も得られる。
Particularly, according to the present invention as set forth in claim 2,
When the supply of the compressed gas into the container is intermittently performed, it is preferable that the powder particles can clog the nozzle as much as possible. Further, according to the present invention described in claim 8, since the porous portion of the container can be vibrated by the gas flow, it is not necessary to employ a mechanical means such as a vibrator as the vibration imparting means, and the device configuration is simple. There is also an advantage that it can be realized.

【0049】請求項3乃至5、及び9に記載の本発明に
係る粉粒体の吐出装置によれば、上記した本発明の粉粒
体の吐出方法を適切に実施でき、有用である。
According to the discharging apparatus for powder or granules according to the present invention as defined in claims 3 to 5 and 9, the above-mentioned method for discharging powder or granules according to the present invention can be appropriately carried out and is useful.

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

【図1】本発明に係る粉粒体の吐出装置の一例を示す一
部切欠断面図。
FIG. 1 is a partially cutaway sectional view showing an example of a powdery or granular material discharge device according to the present invention.

【図2】本発明に係る粉粒体の吐出装置の他の例を示す
一部切欠断面図。
FIG. 2 is a partially cutaway cross-sectional view showing another example of a powder or granular material discharge device according to the present invention.

【図3】本発明に係る粉粒体の吐出装置の他の例を示す
一部切欠断面図。
FIG. 3 is a partially cutaway cross-sectional view showing another example of a powder or granular material discharge device according to the present invention.

【図4】本発明に係る粉粒体の吐出装置に適用される容
器の他の実施例を示す要部断面図。
FIG. 4 is a cross-sectional view of essential parts showing another embodiment of the container applied to the discharging device for powdery particles according to the present invention.

【符号の説明】[Explanation of symbols]

1 圧縮ガス源 2 ノズル 2a パイプ部 3 容器 4 粉粒体貯蔵ホッパー 5 配管 6 分岐配管 7 圧力設定器 8a〜8c 自動開閉バルブ 9 上限検知センサ 10a,10b 下限検知センサ 11 圧力検知センサ 12a,12b コントローラ 13,13A 容器 14a クランプバンド 15 濾布(多孔部) 15a 小孔 15 フィルター 16 吐出管 17 短管部 17a フランジ部 18,18A ガス流供給手段 19 検知センサ 20 配管部 30,30a 空間部 31 フランジ部 32 クランパー 33 バイブレーター m 粉粒体 A,Aa,Ab 粉粒体の吐出装置 1 Compressed gas source 2 Nozzle 2a Pipe part 3 Container 4 Powder granule storage hopper 5 Piping 6 Branch piping 7 Pressure setting device 8a-8c Automatic opening / closing valve 9 Upper limit detection sensor 10a, 10b Lower limit detection sensor 11 Pressure detection sensor 12a, 12b Controller 13, 13A Container 14a Clamp band 15 Filter cloth (perforated part) 15a Small hole 15 Filter 16 Discharge pipe 17 Short pipe part 17a Flange part 18,18A Gas flow supply means 19 Detection sensor 20 Piping part 30,30a Space part 31 Flange part 32 Clamper 33 Vibrator m Particles A, Aa, Ab Discharge device for particles

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】先端にノズルを備えた容器内に圧縮ガスを
供給し、この容器内圧力を一定の圧力範囲内に維持させ
ることにより、容器内の粉粒体を前記ノズルから連続的
に且つ定量的に吐出させることを特徴とする粉粒体の吐
出方法。
1. A compressed gas is supplied into a container having a nozzle at its tip, and the internal pressure of the container is maintained within a constant pressure range, so that powder particles in the container are continuously and continuously discharged from the nozzle. A method for discharging a granular material, which comprises discharging quantitatively.
【請求項2】請求項1において、上記容器内への圧縮ガ
スの供給を、粉粒体の物性に応じて連続的又は断続的に
行わせることを特徴とする粉粒体の吐出方法。
2. The method for discharging a granular material according to claim 1, wherein the compressed gas is supplied into the container continuously or intermittently according to the physical properties of the granular material.
【請求項3】内部に粉粒体を収容するための空間部を形
成し且つ先端側にノズルを備えた容器と、この容器内へ
圧縮ガスを供給するための圧縮ガス源と、この圧縮ガス
源から容器内へ供給される圧縮ガスの圧力を所定の圧力
範囲内に維持させるための圧力設定手段とを備えている
ことを特徴とする粉粒体の吐出装置。
3. A container having a space portion for accommodating powder and granules therein and having a nozzle on the tip side, a compressed gas source for supplying compressed gas into the container, and the compressed gas. And a pressure setting means for maintaining the pressure of the compressed gas supplied from the source into the container within a predetermined pressure range.
【請求項4】請求項3において、上記圧力設定手段は、
容器内の圧力値の検出を行うための圧力センサと、この
圧力センサで検出された圧力値を所定の圧力範囲内に維
持させるべく圧縮ガス源から容器内への圧縮ガスの供給
の制御を行う自動開閉バルブとから構成されていること
を特徴とする粉粒体の吐出装置。
4. The pressure setting means according to claim 3,
Controls the supply of compressed gas from the compressed gas source into the container to maintain the pressure value detected by this pressure sensor within the specified pressure range and the pressure sensor for detecting the pressure value inside the container. An apparatus for discharging a powder or granular material, comprising an automatic opening / closing valve.
【請求項5】請求項3又は4において、上記容器内の粉
粒体の充填量を所定の一定量に維持させるべく容器に連
結された粉粒体貯蔵ホッパーから容器内への粉粒体の供
給制御を行う粉粒体の供給制御手段を備えていることを
特徴とする粉粒体の吐出装置。
5. The powder or granular material according to claim 3, wherein the powder or granular material is transferred from the powder or granular material storage hopper connected to the container to maintain the filling amount of the powder or granular material in the container at a predetermined fixed amount. A discharge device for powder or granular material, comprising a supply control means for powder or granular material for performing supply control.
【請求項6】多数の小孔を形成した多孔部を備えた容器
中に粉粒体を充填させた状態で、この容器の少なくとも
多孔部をガス流中で振動させることにより、この容器内
の粉粒体を前記多孔部の小孔から連続的に且つ定量的に
ガス流中に吐出させることを特徴とする粉粒体の吐出方
法。
6. A container provided with a porous part having a large number of small holes filled with a powder or granular material, and at least the porous part of the container is vibrated in a gas flow, whereby A method for discharging a powder or granular material, which comprises discharging the powder or granular material continuously and quantitatively into a gas flow from the small holes of the porous portion.
【請求項7】請求項6において、上記容器の少なくとも
多孔部を振動させる手段が、ハンマリング又はバイブレ
ータ等による機械的手段によって容器に振動を付与する
手段であることを特徴とする粉粒体の吐出方法。
7. The powdery or granular material according to claim 6, wherein the means for vibrating at least the porous portion of the container is means for vibrating the container by mechanical means such as hammering or a vibrator. Discharge method.
【請求項8】請求項6において、上記容器の少なくとも
多孔部を振動させる手段が、上記ガス流を脈動流又は圧
縮ガスのパルス的な噴流とする手段であることを特徴と
する粉粒体の吐出方法。
8. The powdery or granular material according to claim 6, wherein the means for vibrating at least the porous portion of the container is means for making the gas flow a pulsating flow or a pulsed jet of compressed gas. Discharge method.
【請求項9】内部に粉粒体を収容するための空間部を形
成し且つ少なくとも先端側に多数の小孔を形成した多孔
部を備えた容器と、この容器の多孔部が配置される位置
へガス流を供給させるためのガス流供給手段とを備え、
前記容器の多孔部がガス流内で振動することによりこの
容器内の粉粒体が多孔部の小孔から連続的に且つ定量的
にガス流中へ吐出されるように構成されていることを特
徴とする粉粒体の吐出装置。
9. A container provided with a porous portion having a space portion for accommodating powder and granules therein and having a large number of small holes formed at least on the tip side, and a position where the porous portion of the container is arranged. A gas flow supply means for supplying a gas flow to
By vibrating the porous part of the container in the gas flow, it is configured that the powder or granular material in the container is continuously and quantitatively discharged into the gas flow from the small holes of the porous part. Discharge device for powder particles.
JP6010187A 1994-02-01 1994-02-01 Method and apparatus for discharging powder and granules Expired - Fee Related JP2816527B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6010187A JP2816527B2 (en) 1994-02-01 1994-02-01 Method and apparatus for discharging powder and granules

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6010187A JP2816527B2 (en) 1994-02-01 1994-02-01 Method and apparatus for discharging powder and granules

Publications (2)

Publication Number Publication Date
JPH07213887A true JPH07213887A (en) 1995-08-15
JP2816527B2 JP2816527B2 (en) 1998-10-27

Family

ID=11743288

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005035793A (en) * 2003-06-30 2005-02-10 Sinto Brator Co Ltd Device and method for supplying powdery and granular material
JP2009300652A (en) * 2008-06-12 2009-12-24 Bridgestone Corp Device and method for manufacturing information display panel
CN118992613A (en) * 2024-10-21 2024-11-22 山东劳动职业技术学院(山东劳动技师学院) Fluidized bed device of powder material transport vehicle
CN121513720A (en) * 2026-01-16 2026-02-13 云鹏医药集团有限公司 A wet mixing granulation machine and method for a pharmaceutical product

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5235438A (en) * 1975-09-12 1977-03-18 Sankyo Alum Ind Co Ltd Double window
JPS6049928U (en) * 1983-09-13 1985-04-08 株式会社 松井製作所 Material supply device to pressure tank

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5235438A (en) * 1975-09-12 1977-03-18 Sankyo Alum Ind Co Ltd Double window
JPS6049928U (en) * 1983-09-13 1985-04-08 株式会社 松井製作所 Material supply device to pressure tank

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005035793A (en) * 2003-06-30 2005-02-10 Sinto Brator Co Ltd Device and method for supplying powdery and granular material
JP2009300652A (en) * 2008-06-12 2009-12-24 Bridgestone Corp Device and method for manufacturing information display panel
CN118992613A (en) * 2024-10-21 2024-11-22 山东劳动职业技术学院(山东劳动技师学院) Fluidized bed device of powder material transport vehicle
CN121513720A (en) * 2026-01-16 2026-02-13 云鹏医药集团有限公司 A wet mixing granulation machine and method for a pharmaceutical product

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