JP2002293301A - Method and device for filling fine powder - Google Patents

Method and device for filling fine powder

Info

Publication number
JP2002293301A
JP2002293301A JP2001102264A JP2001102264A JP2002293301A JP 2002293301 A JP2002293301 A JP 2002293301A JP 2001102264 A JP2001102264 A JP 2001102264A JP 2001102264 A JP2001102264 A JP 2001102264A JP 2002293301 A JP2002293301 A JP 2002293301A
Authority
JP
Japan
Prior art keywords
powder
gas
filling
fluidizing
fluidized
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
JP2001102264A
Other languages
Japanese (ja)
Other versions
JP3549051B2 (en
Inventor
Kunio Makino
邦夫 牧野
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.)
Ricoh Co Ltd
Original Assignee
Ricoh 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 Ricoh Co Ltd filed Critical Ricoh Co Ltd
Priority to JP2001102264A priority Critical patent/JP3549051B2/en
Priority to US10/095,268 priority patent/US6679301B2/en
Priority to CNB021071756A priority patent/CN1275827C/en
Priority to EP02005321A priority patent/EP1254835A3/en
Publication of JP2002293301A publication Critical patent/JP2002293301A/en
Application granted granted Critical
Publication of JP3549051B2 publication Critical patent/JP3549051B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method and device by which a gas is uniformly led into a powder, thereby obtaining a fluidized state of the powder in which the powder is controlled with the smallest amount of gas, by which the fluidized powder is caused to flow into a filling container of a small diameter or into the back or bottom of the filling container of a complicated shape, and by which the device can be miniaturized and carried, is made easy to operate, can degas from the powder after filling and is capable of highly densely filling the powder without including dust. SOLUTION: Powder-gas separation sieves, which allow passage of the gas but do not allow passage of the powder, are respectively provided in an air inlet opening in the upstream section of a stored-powder fluidization means and in a gas outlet opening in the downstream section of a filling nozzle. The fluidized powder is sealed in a space between the stored-powder fluidizing means and the filling container. The area of a gas outlet opening 12 of the stored-powder fluidizing means is made 1.002 times or larger than the area of the air outlet opening 16 of the filling nozzle. Thus, the current velocity of the gas in the gas outlet opening is made greater than the current velocity of the gas in the gas discharge opening. Accordingly, the fluidized powder is naturally discharged from the stored-powder fluidization means, via a fluidized-powder path and the filling nozzle, into the filling container.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、20ミクロン以下
の静電潜像現像用トナーのような微小粉体の小口径容
器、小容量容器への充填、あるいは従来の重力を利用し
た充填方法では充填不可能な容器状部分への粉体充填方
法及び粉体充填装置に関し、特に、複写機中のトナーカ
ートリッジ、あるいは複写機現像部への乾式トナーの直
接充填技術に関する。
BACKGROUND OF THE INVENTION The present invention relates to a method for filling fine powder such as toner for developing an electrostatic latent image having a size of 20 microns or less into a small-diameter container or a small-capacity container, or a conventional filling method using gravity. More particularly, the present invention relates to a technique for directly filling dry toner into a toner cartridge in a copying machine or a developing unit of a copying machine.

【0002】[0002]

【従来の技術】粉体の充填機として、ロータリーバル
ブ、スクリューフィーダー、オーガー式充填機などがあ
るが、これら装置から粉体受け容器に粉体を充填するに
は粉体の自重を利用し、充填機の直下に粉体の受け容器
を置き、充填機内で粉体の嵩密度を上げ、切出された粉
体を重力によりこれら容器内に充填される方法をとるの
が、一定容積の充填容器に粉体を効率よく充填する方法
として一般的である。また、粉体供給機中の粉体に気体
を導入し流動性を高めた後、従属する配管により粉体供
給機から受け容器近傍に輸送し脱気配管により輸送管中
の粉体から脱気した後、これを受け容器に高密度充填す
る方法(特開平9−193902号公報)が提案されて
いる。
2. Description of the Related Art As a powder filling machine, there are a rotary valve, a screw feeder, an auger-type filling machine, and the like. A method of placing a powder receiving container directly under the filling machine, increasing the bulk density of the powder in the filling machine, and filling the cut powder into these containers by gravity is a method of filling a fixed volume. This is a common method for efficiently filling a container with powder. Also, after gas is introduced into the powder in the powder feeder to increase the fluidity, the powder is transported from the powder feeder to the vicinity of the receiving container by a dependent pipe, and degassed from the powder in the transport pipe by a degassing pipe. After that, a method of receiving this and filling the container with high density (Japanese Patent Application Laid-Open No. 9-193902) has been proposed.

【0003】しかしながら、これらの方式は、充填管に
同軸状に正確に設けた脱気用配管付きのものとせねなば
ならず製作が難かしい上に重量が大で持ち運びに難があ
り、また、充填容器の充填口径が大きく充填機の真下に
充填容器が位置するときには有効であるが、小口径充填
容器や、内部に様々な構造物のある充填容器では、充填
機あるいは輸送管を離れた粉体が容器内部の空気と置換
され難く、充填口からの吹き上げや容器内の構造物に粉
体の動きを阻害され、所望の量を充填できないなどの問
題が生じている。
[0003] However, these systems have to be provided with a deaeration pipe accurately provided coaxially with the filling pipe, which is difficult to manufacture, and is heavy in weight and difficult to carry. It is effective when the filling diameter of the filling container is large and the filling container is located directly below the filling machine.However, in the case of a small-diameter filling container or a filling container having various structures inside, the filling machine or the transport pipe is separated. There is a problem that the powder is not easily replaced by the air inside the container, the powder is blown up from the filling port or the structure in the container hinders the movement of the powder, and the desired amount cannot be filled.

【0004】また、複写機やプリンタ-で使用されるト
ナーを、機械が設置されている一般のオフィスで、トナ
ーボトルや、機械の現像部に直接補給しようとすると、
粉塵が舞うことや、たとえ補給できたとしても、空気を
多く含んだ低密度の状態での充填であったり、複雑な現
像部に直接入れる場合には、トナーが入る部分と、入ら
ない部分で、画像形成上の問題が発生してしまってい
た。
[0004] Further, when an attempt is made to directly supply toner used in a copying machine or a printer to a toner bottle or a developing unit of a machine in a general office where the machine is installed,
Even if dust is flying, or even if it can be replenished, if it is filled in a low-density state with a lot of air, or if it is directly put into a complicated developing section, the part where toner enters and the part where it does not enter However, a problem in image formation has occurred.

【0005】そこで我々は、先に、特願2001−71
152号において「粉体を容器に充填する方法におい
て、粉体充填用容器内に挿入し、気体により流動化され
た粉体を該容器内に吐出して充填する充填ノズルの先端
が、該容器内に滞留する前記粉体により囲繞された状態
で、該粉体を該容器内に充填することを特徴とする粉体
の充填方法」及び「少なくとも粉体充填用容器内に滞留
する流動化された粉体により吐出先端が囲繞される位置
に挿入される充填ノズル、粉体流動化のための気体導入
手段、及び流動化された粉体の前記充填ノズルへの移送
路を、密閉可能な充填用粉体収納装置に設けたことを特
徴とする粉体充填装置」を提案した。そして、この粉体
充填技術について、特に粉体流動化のための気体の導入
態様及び排出態様と充填効率との関係を中心に更に検討
を続けた結果、今般、流体粘度、装置内壁との摩擦及び
流体体積変化等によるヘッド圧損を加味した上で、気体
が導入され排出されるまでの効果的な挙動制御、効果的
な流速及び流量制御法、したがって、粉体が流動化され
ていることに起因する充填系内での暴れがより少なく、
より効率的な粉体充填技術を開発するに到った。
[0005] Therefore, we first described in Japanese Patent Application No. 2001-71.
No. 152, "in the method of filling powder into a container, the tip of a filling nozzle which is inserted into a powder filling container and discharges and charges powder fluidized by a gas into the container is provided in the container. A method of filling the powder, characterized in that the powder is filled in the container while being surrounded by the powder that is retained in the container; and Filling nozzle inserted at a position where the discharge tip is surrounded by the powder, gas introduction means for fluidizing the powder, and a transfer path for fluidizing the powder to the filling nozzle, which can be sealed. Powder filling device, which is provided in a powder storage device for use ". As a result of further study on the powder filling technology, especially focusing on the relationship between the gas introduction and discharge modes for powder fluidization and the filling efficiency, the fluid viscosity, friction with the inner wall of the apparatus have been recently investigated. In consideration of the head pressure loss due to fluid volume change, etc., effective behavior control until gas is introduced and discharged, effective flow rate and flow rate control method, and therefore, powder is fluidized Less runaway in the filling system due to
A more efficient powder filling technology has been developed.

【0006】[0006]

【発明が解決しようとする課題】従って、本発明の目的
は、上記従来技術に鑑みて、粉体中に均一に気体を導入
し最少の気体量で制御された粉体の流動状態を得て、小
口径充填容器や複雑な形状の充填容器の奥または底部に
流動粉体を流入し、小型で持ち運びができ、操作が簡単
で、容器内で充填ノズルから容器開口間の粉体の層によ
り充填後の粉体から脱気させ、簡単に高密度、無粉塵で
充填できる方法及び装置を提供することにある。さら
に、誰でもどんな場所でも作業汚れなしにトナー等の粉
体を充填できるように、小型で持ち運びができ、操作が
簡単な充填機を提供することにある。
SUMMARY OF THE INVENTION Accordingly, it is an object of the present invention to provide a method of introducing a gas uniformly into a powder and obtaining a controlled flow state of the powder with a minimum amount of gas in view of the above prior art. The flowing powder flows into the inner or bottom of a small-diameter or complicated-shaped filling container, is small and portable, easy to operate, and has a powder layer between the filling nozzle and the container opening inside the container. It is an object of the present invention to provide a method and an apparatus which can be degassed from powder after filling and can be easily filled with high density and no dust. Another object of the present invention is to provide a compact, portable, and easy-to-operate filling machine so that anyone can fill powder such as toner in any place without any work contamination.

【0007】[0007]

【課題を解決するための手段】上記課題は、本発明の
(1)「粉体の流動化のための気体が導入される気体導
入開口部を上流部に有する密閉可能な容器状の収納粉体
流動化手段と、該気体が排出される気体排出開口部を下
流部に有する充填ノズルと、前記収納粉体流動化手段と
充填ノズルを連結し、排出される流動化粉体の経路とを
有し、該充填ノズルは充填用容器の口を密閉可能である
粉体充填手段を用いた微細粉体の充填方法であって、該
収納粉体流動化手段上流の気体導入開口部及び充填ノズ
ル下流部の気体排出開口部に、共に気体を通過させるが
粉体は通過させない粉体−気体分離篩を設けたものとす
ることにより、流動化粉体を該収納粉体流動化装置及び
充填用容器の間に封じ込め、前記収納粉体流動化装置の
気体排出開口部の開口面積を、前記充填ノズルの気体排
出開口部の開口面積の1.002倍以上とすることによ
り、該気体排出開口部の気体の流速が前記気体排出開口
部の気体の流速よりも高くされて、流動化粉体が前記収
納粉体流動化装置から流動化粉体の経路及び充填ノズル
を経由して前記充填用容器に自然排出されることを特徴
とする微細粉体の充填方法」により達成される。
SUMMARY OF THE INVENTION The object of the present invention is to provide (1) a hermetically sealable container-like storage powder having a gas introduction opening for introducing a gas for fluidizing powder at an upstream portion. Body fluidizing means, a filling nozzle having a gas discharge opening for discharging the gas at a downstream portion, and connecting the stored powder fluidizing means and the filling nozzle to form a path for the fluidized powder to be discharged. The filling nozzle is a method for filling fine powder using a powder filling means capable of closing the mouth of a filling container, wherein a gas introduction opening upstream of the stored powder fluidizing means and a filling nozzle By providing a powder-gas separation sieve that allows gas to pass through but does not allow powder to pass through the gas discharge opening at the downstream part, the fluidized powder can be used as the stored powder fluidizing device and for filling. The container is sealed between the containers, and the gas discharge opening of the stored powder fluidizer is opened. By setting the area to be 1.002 times or more the opening area of the gas discharge opening of the filling nozzle, the gas flow rate of the gas discharge opening is made higher than the gas flow rate of the gas discharge opening, Fluidized powder is spontaneously discharged from the storage powder fluidizer through the fluidized powder path and the filling nozzle to the filling container, thereby achieving a fine powder filling method. You.

【0008】また、上記課題は、本発明の(2)「充填
用粉体及び気体を収納する前記密閉可能な容器状の収納
粉体流動化手段中の該粉体を気体により流動化した後、
該流動化された粉体を該収納粉体流動化手段から前記経
路を介して前記充填ノズルまで排出することを特徴とす
る前記第(1)項に記載の微細粉体の充填方法」により
達成される。
The object of the present invention is to provide (2) the method of the present invention, wherein after the powder in the hermetically sealable container-like stored powder fluidizing means for storing the filling powder and gas is fluidized by gas. ,
Discharging the fluidized powder from the storage powder fluidizing means to the filling nozzle via the path, to achieve the fine powder filling method according to the above mode (1). Is done.

【0009】また、上記課題は、本発明の(3)「前記
収納粉体流動化手段内への追加気体の導入により、前記
粉体の流動化が行なわれることを特徴とする前記第
(1)項に記載の微細粉体の充填方法」により達成され
る。
[0009] The object of the present invention is also described in (3) of the present invention, wherein the powder is fluidized by introducing an additional gas into the stored powder fluidizing means. )).

【0010】また、上記課題は、本発明の(4)「前記
収納粉体流動化手段が振動されることにより、前記気体
による粉体の流動化が行なわれることを特徴とする前記
第(1)項又は第(2)項に記載の粉体の微細充填方
法」により達成される。
[0010] The object of the present invention is also described in (4) of the present invention, wherein the powder is fluidized by the gas by vibrating the stored powder fluidizing means. ) Or the method for finely filling powder according to the item (2) ”.

【0011】また、上記課題は、本発明の(5)「前記
粉体の前記粉体流動化手段から前記充填ノズルまでの排
出が、前記粉体流動化手段内の圧力を昇圧することによ
り行なわれることを特徴とする前記第(2)項乃至第
(4)項のいずれか1に記載の充填方法」により達成さ
れる。
[0011] The object of the present invention is also achieved in (5) of the present invention, wherein the discharging of the powder from the powder fluidizing means to the filling nozzle is performed by increasing the pressure in the powder fluidizing means. The filling method according to any one of the above items (2) to (4). "

【0012】また、上記課題は、本発明の(6)「前記
粉体の前記粉体流動化手段から前記充填ノズルまでの排
出が、該粉体流動化手段に外部圧力を加えて該粉体流動
化手段の内容積を減容させることにより行なわれること
を特徴とする前記第(2)項乃至第(5)項のいずれか
1に記載の充填方法」により達成される。
[0012] The object of the present invention is also described in (6) of the present invention, wherein the discharge of the powder from the powder fluidizing means to the filling nozzle is performed by applying an external pressure to the powder fluidizing means. The filling method according to any one of the above items (2) to (5), which is performed by reducing the internal volume of the fluidizing means.

【0013】また、上記課題は、本発明の(7)「前記
粉体流動化手段が、導入気体の流速を加減可能な導入気
体調節弁と、前記流動化粉体の排出経路の排出粉体の流
速を調節可能な排出粉体流速調節弁とを有し、前記流動
化粉体の排出量及び排出程度が、該導入気体調節弁の開
閉程度の調節又は/及び該排出粉体流速調節弁の開閉程
度の調節により制御されることを特徴とする前記第
(2)項乃至第(6)項のいずれか1に記載の充填方
法」により達成される。
The above object is also achieved by (7) the present invention, wherein the powder fluidizing means is capable of adjusting the flow rate of the introduced gas, and the discharge powder in the discharge path of the fluidized powder. The flow rate of the fluidized powder is controlled by controlling the opening / closing degree of the introduction gas control valve and / or the discharge powder flow rate control valve. The charging method according to any one of the above items (2) to (6), wherein the filling is controlled by adjusting the degree of opening and closing.

【0014】また、上記課題は、本発明の(8)「前記
粉体流動化手段が更に、全開及び全閉自在な圧力開放弁
を有し、前記流動化粉体の排出の開始及び終了が該圧力
開放弁の開閉により迅速に行なわれることを特徴とする
前記第(7)項に記載の充填方法」により達成される。
[0014] The object of the present invention is also described in (8) of the present invention, wherein the powder fluidizing means further has a pressure release valve that can be fully opened and fully closed, and the start and end of discharge of the fluidized powder can be determined. This is achieved by the filling method according to the above mode (7), characterized in that the charging is quickly performed by opening and closing the pressure release valve.

【0015】また、上記課題は、本発明の(9)「前記
粉体流動化手段が更に、前記粉体流動化のための気体導
入手段を有し、該気体導入手段が、気体を前記粉体流動
化手段に送出可能に収納する圧力容器であることを特徴
とする前記第(2)項乃至第(8)項のいずれか1に記
載の充填方法」により達成される。
The object of the present invention is also described in (9) of the present invention, wherein the powder fluidizing means further includes a gas introducing means for fluidizing the powder, and the gas introducing means converts the gas into the powder. The filling method according to any one of the above items (2) to (8), wherein the pressure container is housed in a body fluidizing means so as to be able to be sent out.

【0016】また、上記課題は、本発明の(10)「前
記粉体流動化手段が更に、前記粉体流動化のための気体
導入手段を有し、該気体導入手段が、逆止弁付きの送気
ポンプであることを特徴とする前記第(2)項乃至第
(8)項のいずれか1に記載の充填方法」により達成さ
れる。
The object of the present invention is also described in (10) of the present invention, wherein the powder fluidizing means further has a gas introducing means for fluidizing the powder, and the gas introducing means has a check valve. The charging method according to any one of the above items (2) to (8), "which is the air supply pump described above.

【0017】また、上記課題は、本発明の(11)「前
記粉体流動化手段が更に、前記粉体流動化のための気体
導入手段との間に、気体を該粉体流動化手段内に均一に
導入するための気体分配手段を有することを特徴とする
前記第(7)項乃至第(10)項のいずれか1に記載の
充填方法」により達成される。
The object of the present invention is also described in (11) of the present invention, wherein the powder fluidizing means further includes a gas between the powder fluidizing means and the gas introducing means for fluidizing the powder. (7) The charging method according to any one of the above (7) to (10), further comprising a gas distribution means for uniformly introducing the gas into the container.

【0018】また、上記課題は、本発明の(12)「前
記粉体が、平均体積粒径0.2μm〜20μmの静電潜
像現像用トナーであることを特徴とする前記第(2)項
乃至第(11)項のいずれか1に記載の充填方法」によ
り達成される。
The object of the present invention is also described in (12) of the present invention, wherein the (powder) is a toner for developing an electrostatic latent image having an average volume particle diameter of 0.2 μm to 20 μm. Or the filling method according to any one of the items (11) to (11).

【0019】また、上記課題は、本発明の(13)「粉
体の流動化のための気体が導入される気体導入開口部を
上流部に有する密閉可能な収納粉体流動化装置と、該気
体が排出される気体排出開口部を下流部に有する充填ノ
ズルと、前記収納粉体流動化装置と充填ノズルを連結せ
る流動化粉体の経路とを有し、該充填ノズルは充填用容
器の口を密閉可能である微細粉体充填装置であって、該
収納粉体流動化装置上流の気体導入開口部及び充填ノズ
ル下流部の気体排出開口部は、共に気体を通過させるが
粉体は通過させない粉体−気体分離篩を備えることによ
り、流動化粉体を該収納粉体流動化装置及び充填用容器
の間に封じ込め、前記収納粉体流動化装置の気体排出開
口部の開口面積が、前記充填ノズルの気体排出開口部の
開口面積の1.002倍以上であることにより、該気体
排出開口部の気体の流速が前記気体排出開口部の気体の
流速よりも高くされて、流動化粉体が前記収納粉体流動
化装置から流動化粉体の経路及び充填ノズルを経由して
前記充填用容器に自然排出されることを特徴とする微細
粉体充填装置」により達成される。
The object of the present invention is to provide (13) a sealable powder storage fluidizer having a gas inlet opening for introducing a gas for fluidizing powder at an upstream portion thereof. A filling nozzle having a gas discharge opening at a downstream portion from which gas is discharged, and a path of fluidized powder for connecting the filled powder fluidizing device and the filled nozzle, wherein the filled nozzle is provided in a filling container. A fine powder filling device capable of closing the mouth, wherein a gas introduction opening upstream of the storage powder fluidization device and a gas discharge opening downstream of the filling nozzle both allow gas to pass, but powder pass through. By providing a powder-gas separation sieve that does not allow the fluidized powder to be sealed between the stored powder fluidizer and the filling container, the gas discharge opening of the stored powder fluidizer has an opening area of 1.0 of the opening area of the gas discharge opening of the filling nozzle By being twice or more, the flow velocity of the gas at the gas discharge opening is made higher than the flow velocity of the gas at the gas discharge opening, and the fluidized powder is removed from the stored powder fluidizer by the fluidized powder. , And is naturally discharged into the filling container via the filling path and the filling nozzle.

【0020】また、上記課題は、本発明の(14)「充
填用粉体及び気体を収納する前記密閉可能な容器状の収
納粉体流動化装置中の該粉体を気体により流動化した
後、該流動化された粉体を該収納粉体流動化装置から前
記経路を介して前記充填ノズルまで排出することを特徴
とする前記第(13)項に記載の微細粉体充填装置」に
より達成される。
[0020] The above object is also achieved by (14) the present invention, wherein after the powder is fluidized by gas in the hermetically sealed container-like stored powder fluidizer for storing powder and gas for filling. Discharging the fluidized powder from the storage powder fluidizing device to the filling nozzle via the path, to achieve the fine powder filling device according to the above mode (13). Is done.

【0021】また、上記課題は、本発明の(15)「前
記収納粉体流動化装置内への追加気体の導入により、前
記粉体の流動化が行なわれることを特徴とする前記第
(14)項に記載の微細粉体充填装置」により達成され
る。
The object of the present invention is also described in (15) of the present invention, wherein the fluidization of the powder is performed by introducing an additional gas into the fluidized storage device. )).

【0022】また、上記課題は、本発明の(16)「前
記収納粉体流動化装置が振動されることにより、前記気
体による粉体の流動化が行なわれることを特徴とする前
記第(14)項又は第(15)項に記載の微細粉体充填
装置」により達成される。
[0022] The object of the present invention is also described in (16) of the present invention, wherein the powder is fluidized by the gas by vibrating the stored powder fluidizer. ) Or (15).

【0023】また、上記課題は、本発明の(17)「前
記粉体の前記粉体流動化装置から前記充填ノズルまでの
排出が、前記粉体流動化装置内の圧力を昇圧することに
より行なわれることを特徴とする前記第(14)項乃至
第(16)項のいずれか1に記載の微細粉体充填装置」
により達成される。
The object of the present invention is also achieved in (17) of the present invention, wherein the discharging of the powder from the powder fluidizing device to the filling nozzle is performed by increasing the pressure in the powder fluidizing device. The fine powder filling device according to any one of the above items (14) to (16), "
Is achieved by

【0024】また、上記課題は、本発明の(18)「前
記粉体の前記粉体流動化装置から前記充填ノズルまでの
排出が、該粉体流動化手段に外部圧力を加えて該粉体流
動化装置の内容積を減容させることにより行なわれるこ
とを特徴とする前記第(14)項乃至第(17)項のい
ずれか1に記載の微細粉体充填装置」により達成され
る。
The object of the present invention is also described in (18) of the present invention, wherein the discharge of the powder from the powder fluidizing device to the filling nozzle is performed by applying an external pressure to the powder fluidizing means. The fine powder filling apparatus according to any one of the above (14) to (17), which is performed by reducing the internal volume of the fluidization apparatus.

【0025】また、上記課題は、本発明の(19)「前
記粉体流動化装置が、導入気体の流速を加減可能な導入
気体調節弁と、前記流動化粉体の排出経路の排出粉体の
流速を調節可能な排出粉体流速調節弁とを有し、前記流
動化粉体の排出量及び排出程度が、該導入気体調節弁の
開閉程度の調節又は/及び該排出粉体流速調節弁の開閉
程度の調節により制御されることを特徴とする前記第
(14)項乃至第(18)項のいずれか1に記載の微細
粉体充填装置」により達成される。
[0025] The above object is also achieved by (19) the present invention relates to "the powder fluidizing device, wherein the introduced gas control valve capable of adjusting the flow rate of the introduced gas, and the discharge powder in the discharge path of the fluidized powder. The flow rate of the fluidized powder is controlled by controlling the opening / closing degree of the introduction gas control valve and / or the discharge powder flow rate control valve. The fine powder filling apparatus according to any one of the above (14) to (18), wherein the fine powder filling apparatus is controlled by adjusting the opening / closing degree of the fine powder.

【0026】また、上記課題は、本発明の(20)「前
記粉体流動化装置が更に、全開及び全閉自在な圧力開放
弁を有し、前記流動化粉体の排出の開始及び終了が該圧
力開放弁の開閉により迅速に行なわれることを特徴とす
る前記第(19)項に記載の微細粉体充填装置」により
達成される。
[0026] The object of the present invention is also described in (20) of the present invention, wherein the powder fluidizer further has a pressure release valve that can be fully opened and fully closed, and the start and end of discharge of the fluidized powder can be determined. This is achieved by the fine powder filling apparatus according to the above mode (19), wherein the operation is performed promptly by opening and closing the pressure release valve.

【0027】また、上記課題は、本発明の(21)「前
記粉体流動化装置が更に、前記粉体流動化のための気体
導入手段を有し、該気体導入手段が、気体を前記粉体流
動化装置に送出可能に収納する圧力容器であることを特
徴とする前記第(14)項乃至第(20)項のいずれか
1に記載の微細粉体充填装置」により達成される。
[0027] The object of the present invention is also described in (21) of the present invention, wherein the powder fluidizing apparatus further includes gas introducing means for fluidizing the powder, and the gas introducing means converts the gas into the powder. The fine powder filling apparatus according to any one of the above (14) to (20), wherein the pressure vessel is a pressure vessel housed in a body fluidizing device so as to be able to be sent out.

【0028】また、上記課題は、本発明の(22)「前
記粉体流動化装置が更に、前記粉体流動化のための気体
導入手段を有し、該気体導入手段が、逆止弁付きの送気
ポンプであることを特徴とする前記第(14)項乃至第
(20)項のいずれか1に記載の微細粉体充填装置」に
より達成される。
The above object is also achieved by the present invention as defined in (22) of the present invention, wherein the powder fluidizing device further comprises gas introducing means for fluidizing the powder, wherein the gas introducing means has a check valve. The fine powder filling apparatus according to any one of the above items (14) to (20), "

【0029】また、上記課題は、本発明の(23)「前
記粉体流動化装置が更に、前記粉体流動化のための気体
導入手段との間に、気体を該粉体流動化装置内に均一に
導入するための気体分配手段を有することを特徴とする
前記第(14)項乃至第(22)項のいずれか1に記載
の微細粉体充填装置」により達成される。
[0029] The above object is also achieved in (23) of the present invention in that the above-mentioned powder fluidizing device further comprises a gas introduced into the powder fluidizing device between the powder fluidizing device and the gas introducing means. The fine powder filling apparatus according to any one of the above (14) to (22), further comprising a gas distribution means for uniformly introducing the fine powder into the powder.

【0030】また、上記課題は、本発明の(24)「前
記粉体が、平均体積粒径0.2μm〜20μmの静電潜
像現像用トナーであることを特徴とする前記第(14)
項乃至第(23)項のいずれか1に記載の微細粉体充填
装置」により達成される。
The object of the present invention is also described in (24) of the present invention, wherein the powder is a toner for developing an electrostatic latent image having an average volume particle diameter of 0.2 μm to 20 μm.
Item to the fine powder filling apparatus according to any one of the items (23) to (23) ".

【0031】以下、本発明を詳細に説明する。粉体を流
動化し、例えばパイプによりニューマティック輸送する
ことは、気体と粉体の混合により可能であることが良く
知られている。しかし、流動化した直径20μm以下の
粉体、特に直径10μm以下のトナーのような極微粉体
を単に例えば容器中に排出するだけでは、粉体(粉塵)
の飛散防止や充填後の脱気が不十分で、工場内の大型の
設備では粉塵対策や脱気用の設備を追加して実施可能で
あっても、一般のオフィスなどの環境では、実用的では
ない。トナーのような極微粉体は、体積に対する表面積
比が極めて大であるため通常は2次凝集していることが
多いが、例えばアジテータ等により2次凝集が解かれた
極微粉体は、極微粉化する前の塊状材質の比重にほとん
ど関係なく、表面状態のみが主に反映されて、気体中を
ブラウン運動し続け、したがってトナーのような極微粉
体をニューマティック輸送した場合には、随伴する気体
から極微粉体を自然沈降により分離するには一般的に途
方もない長時間を要することが経験上知られている。
Hereinafter, the present invention will be described in detail. It is well known that fluidizing powders and pneumatically transporting them by, for example, pipes is possible by mixing gas and powder. However, merely discharging a fluidized powder having a diameter of 20 μm or less, particularly an ultrafine powder such as a toner having a diameter of 10 μm or less into, for example, a container may result in a powder (dust).
Insufficient prevention of scattering and deaeration after filling, and large-scale equipment in the factory can be implemented with additional dust control and deaeration equipment. is not. Ultrafine powders such as toners usually have secondary agglomeration in many cases because the surface area ratio to the volume is extremely large. Irrespective of the specific gravity of the agglomerated material before the formation, only the surface state is mainly reflected and continues Brownian motion in the gas, so it accompanies when ultrafine powder such as toner is pneumatically transported. It has been known from experience that it generally takes a tremendous amount of time to separate ultrafine powder from gas by natural sedimentation.

【0032】図1には、本発明による微粉体の充填系が
説明のため簡略化されて示されている。この微粉体の充
填系において、微粉体は、充填操作中、粉体流動化装置
(A)の上流に設けられた粉体−気体分離篩(a)と、
充填用容器(B)下流に設けられた粉体−気体分離篩
(b)との間にのみ存在でき、分離篩(a)又は(b)
から系外に出ることができない。しかし、本発明におい
て実際には、分離篩(b)は充填用容器(B)に設けら
れるのではなく、充填ノズルに設けられている。
FIG. 1 schematically shows a fine powder filling system according to the present invention for explanation. In this fine powder filling system, the fine powder is filled with a powder-gas separation sieve (a) provided upstream of the powder fluidization device (A) during the filling operation;
It can exist only between the powder-gas separation sieve (b) provided downstream of the filling container (B), and is a separation sieve (a) or (b).
Can not get out of the system. However, in the present invention, the separation sieve (b) is not provided in the filling container (B) but is provided in the filling nozzle.

【0033】そして、分離篩(b)の部分の開口面積
(S2)に対する分離篩(a)の部分の開口面積(S1
の比が大きい場合には、その比の程度に応じて、開口面
積(S2)の箇所では開口面積(S1)の箇所よりも気体
の流速を大にすることができ、したがって、開口面積
(S1)の箇所における気体流速が小さくても、気体に
より流動化された粉体を速やかに充填用容器(B)まで
排出できるような流速が得られることを意味する。これ
は、最近のようにOA機器の小型化、軽量化と高性能化
に対する要求が高まる中で必然的にトナーや現像剤のた
めの充填容器及び充填口径、つまり開口面積(S2)を
小さく押さえざるを得ない状況下では、特に有利であ
る。また、本発明における流動化された粉体のこのよう
な速やかな充填用容器(B)への排出は、粉体流動化装
置(A)と充填用容器(B)とを連結する途中経路が、
図中点線で示されるように充分太い途中経路(C1)で
あっても、或いは1点鎖線で示されるように充分細い途
中経路(C2)であっても変わらない。
The opening area (S 1 ) of the portion of the separation sieve (a) relative to the opening area (S 2 ) of the portion of the separation sieve (b)
Is large, the flow velocity of the gas can be made larger at the location of the opening area (S 2 ) than at the location of the opening area (S 1 ), depending on the degree of the ratio. This means that even if the gas flow velocity at the point (S 1 ) is small, a flow velocity that can quickly discharge the powder fluidized by the gas to the filling container (B) is obtained. This is inevitably due to the recent increase in demand for downsizing, weight reduction and high performance of OA equipment, inevitably reducing the filling container and filling opening for toner and developer, that is, the opening area (S 2 ). This is particularly advantageous in situations where it must be suppressed. In addition, the rapid discharge of the fluidized powder to the filling container (B) according to the present invention is performed by a path on the way connecting the powder fluidizing device (A) and the filling container (B). ,
It does not change whether the route is a sufficiently thick middle route (C 1 ) as shown by the dotted line or a sufficiently thin middle route (C 2 ) as shown by the one-dot chain line.

【0034】したがって、本発明における分離篩(a)
の部分への粉体流動化のための流入気体は、開口面積
(S1)が開口面積(S2)よりも大きいときには、理屈
上では、分離篩(b)部分における排出圧力、即ち1気
圧よりも僅かでも高い圧力で流入させればよいことにな
るが、実際には充填系の中の流体粘度、装置内壁との摩
擦及び流体体積減少等によるヘッド圧損が生じ得る。
Therefore, the separation sieve (a) in the present invention
When the opening area (S 1 ) is larger than the opening area (S 2 ), the inflowing gas for fluidizing the powder into the portion (a) theoretically has the discharge pressure at the separation sieve (b) portion, that is, 1 atm. In this case, it is sufficient that the pressure is made to flow at a slightly higher pressure, but in practice, head pressure loss may occur due to fluid viscosity in the filling system, friction with the inner wall of the apparatus, and decrease in fluid volume.

【0035】本発明における粉体流動化のための流入気
体の加圧の程度は、上記のように、常圧より僅かに高い
程度でよく、あまり高圧に加圧すると反って、容器内に
滞留する微粉体雲による捕捉効果が損なわれることがあ
る。容器中に滞留する微粉体雲の量や流動化済みの微粉
体の充填態様にもよるが、一般的には加圧の程度(粉体
排出路として3.5m以内の長さのウレタンチューブを
用いた場合)は、2〜1500ゲージヘクトpa/cm
2、好ましくは3〜800ゲージヘクトpa/cm2、よ
り好ましくは10〜500ゲージヘクトpa/cm2
ある。2ゲージヘクトpa/cm2未満の加圧では、充
填に長時間を要する。
In the present invention, the degree of pressurization of the inflow gas for fluidizing the powder may be slightly higher than the normal pressure as described above. In some cases, the capturing effect due to the fine powder cloud is impaired. Although it depends on the amount of the fine powder cloud staying in the container and the filling mode of the fluidized fine powder, in general, the degree of pressurization (a urethane tube having a length of 3.5 m or less as a powder discharge path is used). 2) 1500 gauge hectare pa / cm
2 , preferably 3 to 800 gauge hectares pa / cm 2 , more preferably 10 to 500 gauge hectares pa / cm 2 . At a pressure of less than 2 gauge hectares pa / cm 2 , it takes a long time to fill.

【0036】さらに、本発明においては、分離篩(a)
及び分離篩(b)は、同一の微粉体を対象とする粉体−
気体分離篩であるので、材質を変える必要がない。本発
明における分離篩(通気板)としては、例えば焼結金属
板、金属メッシュ、焼結樹脂パネルのようなものが挙げ
られる。
Further, in the present invention, the separation sieve (a)
And the separation sieve (b) is a powder intended for the same fine powder.
Since it is a gas separation sieve, there is no need to change the material. Examples of the separation sieve (vent plate) in the present invention include a sintered metal plate, a metal mesh, and a sintered resin panel.

【0037】このような篩材料の中で、篩材料の選択は
重要であり、特にトナーのような微粉体を対象として、
支障なく均一な通気ができ長期間目詰りを生ぜず、比較
的低圧での送風が可能であるような全ての要件を満たす
篩材料の選択は困難なことでもある。本発明において
は、分離篩(通気多孔板)として焼結樹脂製のパネル
(商品名:フィルタレン)をアクリル円筒と下部フラン
ジ間に挟む構造としたときに最も良好な結果が得られた
ので、粉体の均質で安定的な流動状態を維持するため
に、焼結樹脂板(商品名:フィルタレン)を用いた場合
について、以下説明している。通気多孔板としてはゴア
テックス、焼結金属板などもあるが、焼結樹脂板フィル
タレンからの空気流入が一番均一であったことも理由の
1つである。
Among such sieve materials, selection of the sieve material is important, and particularly for fine powder such as toner.
It is also difficult to select a sieve material that satisfies all requirements such that uniform and uniform ventilation is possible, does not cause clogging for a long period of time, and can be blown at a relatively low pressure. In the present invention, the best results were obtained when a panel made of a sintered resin (trade name: Filterlen) was sandwiched between an acrylic cylinder and a lower flange as a separation sieve (aerated porous plate). The case where a sintered resin plate (trade name: Filterlen) is used to maintain a homogeneous and stable flow state of the powder will be described below. There are also Gore-Tex and sintered metal plates as the perforated porous plate, and one of the reasons is that the air flow from the sintered resin plate filter is most uniform.

【0038】また、本発明においては、密閉可能な充填
用粉体流動化装置(粉体切出し装置)中の充填用粉体に
気体を、導入気体調節弁により導入程度を調節し、充填
用粉体流動化装置(粉体切出し装置)内の圧力を調節、
制御し、また、気体を均等に導入する手段により、均一
に流動化した後、粉体を充填用粉体流動化装置外に排出
して容器に充填することが好ましい。この気体の均等導
入手段により、空気を緩やかに充填用粉体流動化装置に
導入して必要最小限度の、したがって粉体の例えばブラ
ウン運動を低く抑えた流動化を達成することができる。
流動化された後には粉体が高い流動性を有するため、充
填用粉体流動化装置内の圧力を外圧より僅かに高くする
だけで、粉体を充填用粉体流動化装置外に排出でき、排
出、移送路中を充填ノズル先端まで円滑にニューマティ
ック輸送し、充填用容器中で余分な撹拌を伴うことなく
充填することができる。
In the present invention, the degree of introduction of the gas into the filling powder in the sealable filling fluidization device (powder cutting device) is adjusted by an introduction gas control valve, and the filling powder is controlled. Adjust the pressure inside the body fluidizer (powder cutting device),
It is preferable that the powder is discharged out of the filling powder fluidizing apparatus and then filled in a container after the fluid is uniformly fluidized by means for controlling and uniformly introducing the gas. By means of this uniform introduction of gas, air can be gently introduced into the filling powder fluidizer to achieve the required minimum fluidization, thus minimizing the powder, for example, Brownian motion.
Since the powder has high fluidity after fluidization, the powder can be discharged out of the filling powder fluidizer only by slightly increasing the pressure in the powder fluidizer for filling from the external pressure. Pneumatic transport to the tip of the filling nozzle smoothly through the discharge, transfer and transfer paths, and filling can be performed in the filling container without extra stirring.

【0039】気体により粉体を流動化する際、充填用粉
体流動化装置の気体のみを用いるのでなく、装置外から
気体を導入する場合には、気体を均一に導入することが
重要であり、そのためには、例えばヘッド圧損をあまり
激しく生じない目の細かい金網などの気体分配手段を通
して気体を導入することが特に好ましい。流動化した粉
体を排出し、容器に充填するときの開始および終了の制
御は、充填用粉体流動化装置内の圧力を速やかに調節す
ることにより行なうことができ、これは、例えば充填用
粉体流動化装置に設けた圧力開放弁によって行なうこと
ができ、また、外部の加圧手段等によって補助すること
ができる。また、別に設けられ圧力微調整に適した粉体
流速調節弁により、粉体充填操作中で充填用粉体流動化
装置及び/又は粉体排出路中の圧力を変更することがで
き、さらに、粉体の流出状態を例えば粉体充填操作の最
初と途中で変化させる圧力微調整を行なうこともでき
る。
When fluidizing the powder with gas, it is important not only to use the gas of the filling powder fluidization device but also to introduce the gas uniformly when introducing the gas from outside the device. For this purpose, it is particularly preferable to introduce the gas through a gas distribution means such as a fine wire mesh which does not cause a head pressure loss so intensely. The control of the start and end of discharging the fluidized powder and filling the container can be performed by quickly adjusting the pressure in the filling powder fluidizing device. It can be performed by a pressure release valve provided in the powder fluidization device, and can be assisted by an external pressurizing means or the like. In addition, a separately provided powder flow rate adjusting valve suitable for fine pressure adjustment can change the pressure in the powder fluidizing device for filling and / or the powder discharge path during the powder filling operation, It is also possible to perform fine pressure adjustment to change the outflow state of the powder between the beginning and the middle of the powder filling operation, for example.

【0040】また、本発明は、粉体と気体とが封入され
密閉された充填用粉体収納装置を揺り動かすことで流動
化した後、充填用粉体収納装置内を加圧することができ
るが、装置内の加圧は、外部圧力により充填用粉体収納
装置の内容積を減少させることにより行なうことがで
き、例えば、押し潰して内容積を減容化し、粉体を装置
外に排出して、充填ノズル先端までニューマティック輸
送し、充填容器に充填する。この方法によれば、粉体を
流動化するための装置が不要又は少なくとも小型化で
き、排出するための手段を可能な限り省略できる。充填
用粉体収納装置は、手で振ることができる大きさ、重さ
であってもよく、また、加圧空気導入用のポンプ動力に
より容易に振動又は揺動できる大きさ、重さであっても
よい。充填用粉体収納装置は、小型化することにより、
あらかじめ必要量を秤量しておくと、使い切りタイプの
簡易充填機としても利用することができる。
Further, according to the present invention, after the powder and gas are sealed and the sealed powder storage device is fluidized by rocking, the inside of the powder storage device can be pressurized. Pressurization in the device can be performed by reducing the internal volume of the filling powder storage device by external pressure, for example, crushing to reduce the internal volume, and discharging the powder outside the device. Pneumatic transportation to the tip of the filling nozzle and filling in the filling container. According to this method, a device for fluidizing the powder is unnecessary or at least miniaturized, and a means for discharging the powder can be omitted as much as possible. The filling powder storage device may have a size and weight that can be shaken by hand, and a size and weight that can be easily vibrated or rocked by the power of a pump for introducing pressurized air. You may. The powder storage device for filling is downsized,
If the required amount is weighed in advance, it can also be used as a single-use type simple filling machine.

【0041】[0041]

【発明の実施の形態】[装置例1]図2に、本発明の装
置の一例の概要を示す。この例の粉体充填装置(1)
は、密閉可能な(通常密閉)充填用粉体流動化装置(1
0)、この粉体流動化装置(10)の下部に、フランジ
で、取付取外し自在に結合され、粉体の流動層を形成す
るための空気の通気多孔板としての気体粉体分離篩
(2)(焼結金属板、焼結樹脂板、目の細かい金網な
ど)を取外し自在に収納し、導入気体調節弁(20)が
付された通気管としての圧縮空気配管(7)、圧縮空気
配管(7)が取付取外し自在に嵌め込まれた気体導入手
段としての空気ヘッダ(3)、閉鎖弁付粉体の投入口
(11)、内部圧力の開放及び密封のための圧力開放弁
(13)、圧力微調整用の粉体流速調節弁(15)、粉
体流動化装置(10)内部の圧力をチェックするための
圧力計(14)、粉体導出管(24)に連なる流動粉体
輸送管(12)としてのポリウレタンチューブの先に取
外自在に結合された粉体充填用ノズル(17)から構成
され、粉体充填用ノズル(17)の根本には粉体充填用
の粉体容器(18)の口部に嵌合する程度の大きさの、
この例では裁頭円錐形のポリプロピレン環からなる軟質
パッキン(19)で周囲が巻かれた形の気体粉体分離篩
(16)が設けられている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS [Example 1 of Apparatus] FIG. 2 shows an outline of an example of the apparatus of the present invention. Powder filling device of this example (1)
Is a sealable (usually closed) powder fluidizer for filling (1
0), a gas powder separation sieve (2) which is detachably connected to a lower portion of the powder fluidization device (10) by a flange so as to be attached and detached and serves as an air-permeable porous plate for forming a fluidized bed of powder. ) (Sintered metal plate, sintered resin plate, fine wire mesh, etc.) are removably housed, and compressed air piping (7) and compressed air piping as ventilation pipes provided with an introduction gas control valve (20) (7) an air header (3) as a gas introduction means fitted in a detachable manner, a powder inlet (11) with a closing valve, a pressure release valve (13) for releasing and sealing internal pressure, Powder flow rate control valve (15) for fine adjustment of pressure, pressure gauge (14) for checking pressure inside powder fluidizer (10), fluidized powder transport pipe connected to powder outlet pipe (24) (12) A powder filler removably connected to the end of the polyurethane tube. Consists use a nozzle (17), the base of the powder filling nozzle (17) is enough to fit the mouth of the powder container for powder filling (18) the size of,
In this example, a gas-powder separating sieve (16) having a shape wound around a soft packing (19) made of a frusto-conical polypropylene ring is provided.

【0042】空気ヘッダ(3)は充填用粉体流動化装置
(10)内部の圧力の昇圧することができる程度の若干
耐圧性のものであり、空気ヘッダ(3)には第3圧力計
(p3)が設けられる。空気ヘッダ(3)に接続する圧
縮空気配管(7)には順に、第1減圧弁(25)、第2
減圧弁(26)、空気流量計(27)が設けられ、第1
減圧弁(25)と第2減圧弁(26)の間には第1圧力
計(p1)が、第2減圧弁(26)と空気流量計(2
7)の間には第2圧力計(p2)がそれぞれ設けられて
いる。また、この例の粉体充填装置における粉体充填用
容器(18)としては、透明の樹脂製のトナー容器のよ
うな容器を好ましく用いることができる。
The air header (3) is slightly pressure-resistant so that the pressure inside the filling powder fluidizer (10) can be increased, and the air header (3) has a third pressure gauge ( p3) is provided. A first pressure reducing valve (25) and a second pressure reducing valve (25) are sequentially connected to a compressed air pipe (7) connected to the air header (3).
A pressure reducing valve (26) and an air flow meter (27) are provided.
A first pressure gauge (p1) is provided between the pressure reducing valve (25) and the second pressure reducing valve (26), and the second pressure reducing valve (26) and the air flow meter (2).
A second pressure gauge (p2) is provided between 7). In addition, as the powder filling container (18) in the powder filling device of this example, a container such as a transparent resin toner container can be preferably used.

【0043】この例の装置においては、充填しようとす
る粉体を閉鎖弁付き粉体投入口(11)から充填用粉体
流動化装置(10)内に投入し、内部圧力の開放及び密
封のための圧力開放弁(13)を開放しておく。一方、
圧力微調整用の粉体流速調節弁(15)の操作は人力ま
たは電磁弁などで自動化されても良い。その後粉体投入
口(4)の圧力開放弁(13)を閉じ、気体導入手段と
しての加圧空気溜である空気ヘッダ(3)に通気管
(7)から気体を導入する。この気体の流入は圧力調
整、流量調整としての第1減圧弁(25)、第2減圧弁
(26)により調整されても良く装置が運転中は流入を
継続する。
In the apparatus of this embodiment, the powder to be filled is charged into the powder fluidizing device (10) for filling from the powder inlet (11) with a shut-off valve, and the internal pressure is released and sealed. Pressure relief valve (13) is opened. on the other hand,
The operation of the powder flow rate control valve (15) for fine pressure adjustment may be automated by human power or an electromagnetic valve. Thereafter, the pressure release valve (13) of the powder inlet (4) is closed, and gas is introduced from the ventilation pipe (7) into the air header (3) which is a pressurized air reservoir as gas introduction means. The inflow of this gas may be adjusted by a first pressure reducing valve (25) and a second pressure reducing valve (26) for pressure adjustment and flow rate adjustment, and the inflow is continued during operation of the apparatus.

【0044】導入された気体は、通気多孔板(2)で均
一に粉体中に分散され粉体を流動化する。先端が粉体容
器の底面に密着しないよう斜めまたは一部突起を備えた
粉体排出輸送導管(12)に連らなる充填ノズルとして
の充填管(17)の先端を粉体充填用容器(18)の内
部に挿入し圧力開放弁(13)を閉じると粉体はその流
動化に使用した気体の圧力で充填用粉体流動化装置(1
0)内から粉体輸送管(12)に押出され、先端を粉体
充填用容器(18)の内部に挿入された管状の充填ノズ
ル(17)の先端から粉体充填用容器(18)内に排出
される。
The introduced gas is uniformly dispersed in the powder by the gas-permeable porous plate (2) to fluidize the powder. The tip of a filling pipe (17) as a filling nozzle connected to a powder discharge / transport conduit (12) provided with a slant or a partial projection so that the tip does not adhere to the bottom surface of the powder container is connected to the powder filling container (18). ), And the pressure release valve (13) is closed, the powder is filled with the pressure of the gas used for fluidization of the powder (1).
0) from the inside of the powder filling container (18), which is extruded into the powder transport pipe (12) from the inside and the tip is inserted from the tip of a tubular filling nozzle (17) inserted into the inside of the powder filling container (18). Is discharged.

【0045】この例の装置においては、充填の最初、特
に、粉体充填用容器(18)の内部が完全に空である場
合には、最初、充填用粉体流動化装置(10)の粉体流
速調節弁(15)の開閉度を加減して、充填用粉体流動
化装置(10)からの粉体排出速度を控え目にして、充
填された流動性の粉体の粉体充填用容器(18)内部で
のアバレ、拡散を避け、次に、容器(18)中に滞留す
る微粉体雲の量が、管状充填ノズル(17)の先端から
吐出される流動化済み粉体流をほぼ囲繞できる程度に増
した後、粉体流速調節弁(15)をより開にして、充填
操作を続けることができる。
In the apparatus of this example, at the beginning of the filling, especially when the inside of the powder filling container (18) is completely empty, the powder of the powder fluidizing device (10) is first charged. The degree of opening and closing of the body flow rate control valve (15) is adjusted so that the speed of discharging the powder from the filling fluidizing device (10) is reduced, and the container for filling the filled fluid powder is filled with powder. (18) Avoid the ablation and diffusion inside, and the amount of the fine powder cloud remaining in the container (18) is almost equal to the fluidized powder flow discharged from the tip of the tubular filling nozzle (17). After increasing to the extent that it can be surrounded, the powder flow control valve (15) can be opened further and the filling operation can be continued.

【0046】充填管(17)は粉体充填用容器(18)
の充填口上部に置かれ、粉体充填用容器(18)のセッ
ト後に粉体充填用容器(18)内部に自動的に挿入され
ても手動で挿入されても良い。そして、圧力開放弁(1
3)を開放することにより輸送力となっていた充填用粉
体流動化装置(10)内の内圧がなくなり粉体の排出を
停止できる。
The filling tube (17) is a container for powder filling (18)
May be automatically or manually inserted into the powder filling container (18) after the setting of the powder filling container (18). Then, the pressure release valve (1
By opening 3), the internal pressure inside the powder fluidizing device for filling (10), which has become a transport force, disappears, and the discharge of powder can be stopped.

【0047】粉体の輸送原動力となっている充填用粉体
流動化装置(10)の内圧をすばやく上げるために、充
填用粉体流動化装置(10)には流動のための圧縮空気
導入口とは別の圧縮空気導入口が流動化した粉体の粉面
以上の位置に設けられても良い。粉体充填用容器(1
8)内の管状充填ノズル(17)は単純な配管として
も、また、図に示されるように二重管としての外壁の一
部を3000メッシュ以上の細かい金属スクリーンまた
は焼結プラスチック板で通気構造とし、内外壁間の圧力
を空気インクジェクション効果で減圧することにより、
二重管外壁の通気構造を介し充填した粉体中の気体を抜
き、粉体密度を更に上げても良い。
In order to quickly increase the internal pressure of the powder fluidizer for filling (10), which is the driving force for powder transport, the powder fluidizer for filling (10) has a compressed air inlet for fluidization. Alternatively, another compressed air inlet may be provided at a position higher than the powder surface of the fluidized powder. Container for powder filling (1
8) The tubular filling nozzle (17) in the inside can be a simple pipe, or a part of the outer wall as a double pipe as shown in the figure can be a vented structure with a fine metal screen or sintered plastic plate of 3000 mesh or more. By reducing the pressure between the inner and outer walls by the air injection effect,
The gas in the filled powder may be extracted through the ventilation structure of the outer wall of the double pipe to further increase the powder density.

【0048】[装置例2]図3には、本発明の装置の他
の一例の概要が示される。この例の粉体充填装置(1)
においては、軟質プラスチック等の可撓性材質で作成さ
れた充填用粉体流動化装置(10)、充填用粉体流動化
装置(10)の下部に、フランジで取付取外し自在に結
合され、粉体の流動層を形成するための空気の通気多孔
板(2)(焼結金属板、焼結樹脂板、目の細かい金網な
ど)を取外し自在に収納し、通気管(7)としての圧縮
空気配管、通気管(7)が取付取外し自在に嵌め込まれ
た気体導入手段としての空気ヘッダ(3)、閉鎖弁付粉
体の投入口(11)、内部圧力の開放及び密封のための
圧力開放弁(13)、圧力微調整用の粉体流速調節弁
(15)、流動粉体導出管(24)としてステンレス
管、流動化された粉体の前記充填ノズル(17)への排
出路(移送路)(12)としての取付取外し自在に接続
されたウレタンチューブ、排出路(12)(ウレタンチ
ューブ)に取付取外し自在に接続されたステンレス製の
充填ノズル(17)の根本には粉体充填用の粉体容器
(18)の口部に嵌合する程度の大きさの、この例では
裁頭円錐形のポリプロピレン環からなる軟質パッキン
(19)で周囲が巻かれた形の気体粉体分離篩(16)
が設けられている。
[Example 2 of Apparatus] FIG. 3 shows an outline of another example of the apparatus of the present invention. Powder filling device of this example (1)
In the above, the powder fluidizing device for filling (10) made of a flexible material such as a soft plastic is attached to a lower portion of the powder fluidizing device for filling (10) by a flange so as to be detachable and detachable. Perforated air-permeable plate (2) (sintered metal plate, sintered resin plate, fine mesh, etc.) for forming a fluidized bed of the body is detachably housed, and compressed air as ventilation tube (7) An air header (3) as a gas introduction means into which a pipe and a ventilation pipe (7) are detachably fitted and detached, an inlet (11) for powder with a closing valve, a pressure release valve for releasing and sealing internal pressure. (13) a powder flow rate control valve (15) for fine pressure adjustment, a stainless steel pipe as a fluidized powder outlet pipe (24), and a discharge path (transfer path) of the fluidized powder to the filling nozzle (17) ) (12) Urethane tube detachably connected The base of a stainless steel filling nozzle (17) removably connected to the discharge path (12) (urethane tube) is detachably connected to the mouth of a powder container (18) for powder filling. A gas powder separation sieve (16) of a size, in this example wound around a soft packing (19) consisting of a frustoconical polypropylene ring (19)
Is provided.

【0049】但し、例1の装置と異なり、気体導入手段
として、気体出口に逆止弁(8)を有し小型電動機
(5)により伸縮して空気ヘッダ(3)に空気を送る蛇
腹構造のポンプ(6)を有する。ポンプ(6)は保持枠
(9)中に取外自在に固定されており、小型電動機
(5)によりポンプ(6)が伸縮すると、保持枠(9)
を介して充填用粉体流動化装置(10)が振動され、こ
の振動により、充填用粉体流動化装置(10)中の粉体
が気体で流動化される。
However, unlike the apparatus of Example 1, the gas introduction means has a bellows structure having a check valve (8) at the gas outlet and having a small motor (5) to expand and contract to send air to the air header (3). It has a pump (6). The pump (6) is detachably fixed in the holding frame (9). When the pump (6) expands and contracts by the small electric motor (5), the holding frame (9)
The powder fluidizing device for filling (10) is vibrated through the, and the powder in the fluidizing device for filling fluid (10) is fluidized by gas by the vibration.

【0050】この例の装置においては、充填用粉体流動
化装置(10)も空気ヘッダ(3)も加圧容器特有の肉
厚材料で構成する必要がなく、装置全体の軽量化、小型
化を一層促進することができ、小型電動機(5)のため
の動力線用プラグ(21)を、例えば複写機に設けたコ
ンセントに差し込むだけで、稼働させることができる。
In the apparatus of this example, neither the powder fluidizing apparatus for filling (10) nor the air header (3) needs to be made of a thick material peculiar to the pressurized container. The power line plug (21) for the small electric motor (5) can be operated simply by plugging it into, for example, an outlet provided in the copying machine.

【0051】[装置例3]さらに、本発明においては、
粉体と共に気体が充填され、一本の配管接続口がついた
密閉容器で容器が人力で容易に変形するポリエチレンな
どの軟質プラスチックで形成し、外部から圧力を加えて
該プラスチック容器を変形させ、内圧を高めて配管接続
口に接続されたウレタンチューブなどを得て粉体を充填
容器の底部に導いても良い。または変形しない硬質プラ
スチック等の容器に少なくとも2本の配管接続口を設
け、一本には0.2Mpa以下の圧縮空気を接続し、他
の一本は粉体輸送管とし粉体をチューブを通して容器底
部に導くようにしても良い。圧縮空気元としては通常の
コンプレッサの他に、手動の例えば自転車の空気入れも
代用できる。
[Example 3 of Apparatus] Further, in the present invention,
Filled with gas together with powder, the container is made of a soft plastic such as polyethylene which is easily deformed by human power in a closed container with one pipe connection port, and deforms the plastic container by applying external pressure, The internal pressure may be increased to obtain a urethane tube or the like connected to the pipe connection port, and the powder may be guided to the bottom of the filling container. Alternatively, at least two pipe connection ports are provided in a container of hard plastic or the like that does not deform, one of which is connected to compressed air of 0.2 Mpa or less, and the other is a powder transport tube and the powder is passed through the tube. It may be guided to the bottom. As the source of the compressed air, a manual compressor, for example, a bicycle inflator can be used in place of the usual compressor.

【0052】このように、本発明においては、収納粉体
流動化装置(10)の通気多孔板としての気体排出開口
部(2)の開口面積を、充填ノズル(17)の通気多孔
板としての気体排出開口部(16)の開口面積の1.0
02倍以上とすることにより、気体排出開口部(16)
の気体の流速が気体排出開口部(2)の気体の流速より
も高くされて、流動化粉体を前記収納粉体流動化装置か
ら流動化粉体の経路及び充填ノズルを経由して前記充填
用容器に自然流出に近い状態で排出することができる。
無論、上記のように、粉体の粉体流動化装置(10)か
ら充填ノズル(17)までの排出を、粉体流動化装置
(10)内の圧力を昇圧することにより行なってもよ
く、また、粉体流動化装置(10)に外部圧力を加えて
粉体流動化装置(10)の内容積を減容させることによ
り行なってもよい。
As described above, in the present invention, the opening area of the gas discharge opening (2) as the gas-permeable porous plate of the stored powder fluidizing device (10) is set to be equal to the gas-permeable porous plate of the filling nozzle (17). 1.0 of the opening area of the gas discharge opening (16)
By making it 02 times or more, the gas discharge opening (16)
The flow velocity of the gas is higher than the flow velocity of the gas at the gas discharge opening (2), and the fluidized powder is filled from the storage powder fluidizer through the fluidized powder path and the filling nozzle. It can be discharged into a container for water in a state close to natural outflow.
Of course, as described above, the discharging of the powder from the powder fluidization device (10) to the filling nozzle (17) may be performed by increasing the pressure in the powder fluidization device (10). Alternatively, this may be performed by applying external pressure to the powder fluidization device (10) to reduce the internal volume of the powder fluidization device (10).

【0053】そしてこのような本発明は、前記のよう
に、充填される粉体が、平均体積粒径0.2μm〜20
μmの静電潜像現像用トナーである場合に特に効果的で
ある。
According to the present invention, as described above, the powder to be filled has an average volume particle size of 0.2 μm to 20 μm.
This is particularly effective when the toner is a toner for developing an electrostatic latent image of μm.

【0054】[0054]

【発明の効果】以上、詳細かつ具体的な説明から明らか
なように、本発明により、粉体中に均一に気体を導入し
最少の気体量で制御された粉体の流動状態を得て、小口
径充填容器や複雑な形状の充填容器の奥または底部に流
動粉体を流入し、容器内で充填ノズルに設けられた気体
粉体分離篩により充填後の粉体から脱気させ、簡単に高
密度、無粉塵で充填できる方法を提供でき、さらに、誰
でも、どんな場所でも充填できるように、小型で持ち運
びができ、操作が簡単である充填機を提供することがで
きるという極めて優れた効果を奏するものである。
As is apparent from the detailed and specific explanations above, according to the present invention, a gas is uniformly introduced into a powder to obtain a controlled flow state of the powder with a minimum gas amount. Fluid powder flows into the back or bottom of a small-diameter filling container or a complicated-shaped filling container, and is degassed from the filled powder by a gas-powder separation sieve provided at the filling nozzle inside the container. An excellent effect that it can provide a method that can be filled with high density and no dust, and can provide a compact, portable and easy-to-operate filling machine so that anyone can fill in any place. Is played.

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

【図1】本発明における微粉体の充填系を簡略化して示
した図である。
FIG. 1 is a simplified view of a fine powder filling system according to the present invention.

【図2】本発明における粉体充填装置の一例を示す概略
図である。
FIG. 2 is a schematic view showing an example of a powder filling device according to the present invention.

【図3】本発明における粉体充填装置の他の一例を示す
概略図である。
FIG. 3 is a schematic view showing another example of the powder filling apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 粉体充填装置 2 気体−粉体分離篩(通気多孔板) 3 空気ヘッダ 4 粉体投入口 5 小型電動機(モータ) 6 ポンプ 7 圧縮空気配管 8 逆止弁 9 保持枠 10 充填用粉体流動化装置 11 粉体の投入口 12 流動粉体輸送管(排出・移送路) 13 圧力開放弁 14 圧力計 15 粉体流速調節弁 16 気体−粉体分離篩(通気多孔板) 17 充填用ノズル 18 粉体容器 19 軟質パッキン 20 導入気体調節弁 21 動力線用プラグ 24 粉体導出管 25 第1減圧弁 26 第2減圧弁 27 空気流量計 A 粉体流動化装置 a 粉体−気体分離篩 B 充填用容器 b 粉体−気体分離篩 C1 途中経路 C2 途中経路 p1 第1圧力計 p2 第2圧力計 p3 第3圧力計 S1 開口面積 S2 開口面積DESCRIPTION OF SYMBOLS 1 Powder filling apparatus 2 Gas-powder separation sieve (porous perforated plate) 3 Air header 4 Powder input port 5 Small electric motor (motor) 6 Pump 7 Compressed air piping 8 Check valve 9 Holding frame 10 Powder flow for filling 11 Powder input port 12 Fluid powder transport pipe (discharge / transfer path) 13 Pressure release valve 14 Pressure gauge 15 Powder flow rate control valve 16 Gas-powder separation sieve (aerated porous plate) 17 Filling nozzle 18 Powder container 19 Soft packing 20 Introduced gas control valve 21 Power line plug 24 Powder outlet pipe 25 First pressure reducing valve 26 Second pressure reducing valve 27 Air flow meter A Powder fluidizer a Powder-gas separation sieve B Filling use container b powder - gas separating sieve C 1 intermediate path C 2 intermediate path p1 first pressure gauge p2 second pressure gauge p3 third pressure gauge S 1 opening area S 2 opening area

Claims (24)

【特許請求の範囲】[Claims] 【請求項1】 粉体の流動化のための気体が導入される
気体導入開口部を上流部に有する密閉可能な容器状の収
納粉体流動化手段と、該気体が排出される気体排出開口
部を下流部に有する充填ノズルと、前記収納粉体流動化
手段と充填ノズルを連結し、排出される流動化粉体の経
路とを有し、該充填ノズルは充填用容器の口を密閉可能
である粉体充填手段を用いた微細粉体の充填方法であっ
て、該収納粉体流動化手段上流の気体導入開口部及び充
填ノズル下流部の気体排出開口部に、共に気体を通過さ
せるが粉体は通過させない粉体−気体分離篩を設けたも
のとすることにより、流動化粉体を該収納粉体流動化装
置及び充填用容器の間に封じ込め、前記収納粉体流動化
装置の気体排出開口部の開口面積を、前記充填ノズルの
気体排出開口部の開口面積の1.002倍以上とするこ
とにより、該気体排出開口部の気体の流速が前記気体排
出開口部の気体の流速よりも高くされて、流動化粉体が
前記収納粉体流動化装置から流動化粉体の経路及び充填
ノズルを経由して前記充填用容器に自然排出されること
を特徴とする微細粉体の充填方法。
1. A sealable container-like storage powder fluidizing means having an upstream gas introduction opening for introducing a gas for fluidizing powder, and a gas discharge opening for discharging the gas. Nozzle at the downstream portion, and a path for fluidized powder to be discharged by connecting the stored powder fluidizing means and the filling nozzle, and the filling nozzle can seal the opening of the filling container. A method for filling fine powder using powder filling means, wherein gas is passed through both a gas introduction opening upstream of the stored powder fluidization means and a gas discharge opening downstream of the filling nozzle. By providing a powder-gas separation sieve through which the powder does not pass, the fluidized powder is sealed between the storage powder fluidization device and the filling container, and the gas of the storage powder fluidization device is sealed. Change the opening area of the discharge opening to the opening of the gas discharge opening of the filling nozzle. By setting the opening area to be 1.002 times or more, the flow velocity of the gas at the gas discharge opening is made higher than the flow velocity of the gas at the gas discharge opening, and the fluidized powder is stored in the storage powder fluidizing device. Characterized in that the powder is spontaneously discharged into the filling container through a fluidized powder path and a filling nozzle.
【請求項2】 充填用粉体及び気体を収納する前記密閉
可能な容器状の収納粉体流動化手段中の該粉体を気体に
より流動化した後、該流動化された粉体を該収納粉体流
動化手段から前記経路を介して前記充填ノズルまで排出
することを特徴とする請求項1に記載の微細粉体の充填
方法。
2. After the powder in the hermetically sealable container-like stored powder fluidizing means for storing a filling powder and a gas is fluidized by a gas, the fluidized powder is stored in the container. The method for filling fine powder according to claim 1, wherein the powder is discharged from the powder fluidizing means to the filling nozzle via the path.
【請求項3】 前記収納粉体流動化手段内への追加気体
の導入により、前記粉体の流動化が行なわれることを特
徴とする請求項2に記載の微細粉体の充填方法。
3. The method according to claim 2, wherein the fluidization of the powder is performed by introducing an additional gas into the fluidizing means.
【請求項4】 前記収納粉体流動化手段が振動されるこ
とにより、前記気体による粉体の流動化が行なわれるこ
とを特徴とする請求項2又は3に記載の微細粉体の充填
方法。
4. The method according to claim 2, wherein the powder is fluidized by the gas by vibrating the stored powder fluidizing means.
【請求項5】 前記粉体の前記粉体流動化手段から前記
充填ノズルまでの排出が、前記粉体流動化手段内の圧力
を昇圧することにより行なわれることを特徴とする請求
項2乃至4のいずれか1に記載の微細粉体の充填方法。
5. The discharge of the powder from the powder fluidizing means to the filling nozzle is performed by increasing the pressure in the powder fluidizing means. The method for filling a fine powder according to any one of the above.
【請求項6】 前記粉体の前記粉体流動化手段から前記
充填ノズルまでの排出が、該粉体流動化手段に外部圧力
を加えて該粉体流動化手段の内容積を減容させることに
より行なわれることを特徴とする請求項2乃至5のいず
れか1に記載の微細粉体の充填方法。
6. The discharging of the powder from the powder fluidizing means to the filling nozzle includes applying an external pressure to the powder fluidizing means to reduce the internal volume of the powder fluidizing means. The method for filling fine powder according to any one of claims 2 to 5, wherein the method is performed.
【請求項7】 前記粉体流動化手段が、導入気体の流速
を加減可能な導入気体調節弁と、前記流動化粉体の排出
経路の排出粉体の流速を調節可能な排出粉体流速調節弁
とを有し、前記流動化粉体の排出量及び排出程度が、該
導入気体調節弁の開閉程度の調節又は/及び該排出粉体
流速調節弁の開閉程度の調節により制御されることを特
徴とする請求項2乃至6のいずれか1に記載の微細粉体
の充填方法。
7. An introduction gas control valve capable of adjusting the flow rate of the introduced gas, and a discharge powder flow rate control capable of adjusting the flow rate of the discharge powder in the discharge path of the fluidized powder. And a discharge amount and a discharge degree of the fluidized powder are controlled by adjusting an opening / closing degree of the introduction gas control valve and / or an opening / closing degree of the discharge powder flow rate control valve. The method for filling fine powder according to any one of claims 2 to 6, characterized in that:
【請求項8】 前記粉体流動化手段が更に、全開及び全
閉自在な圧力開放弁を有し、前記流動化粉体の排出の開
始及び終了が該圧力開放弁の開閉により迅速に行なわれ
ることを特徴とする請求項7に記載の微細粉体の充填方
法。
8. The powder fluidizing means further includes a pressure release valve which can be fully opened and fully closed, and the discharge and start of the fluidized powder can be quickly started and closed by opening and closing the pressure relief valve. The method for filling fine powder according to claim 7, wherein:
【請求項9】 前記粉体流動化手段が更に、前記粉体流
動化のための気体導入手段を有し、該気体導入手段が、
気体を前記粉体流動化手段に送出可能に収納する圧力容
器であることを特徴とする請求項2乃至8のいずれか1
に記載の微細粉体の充填方法。
9. The powder fluidizing means further includes gas introducing means for fluidizing the powder, wherein the gas introducing means comprises:
9. A pressure vessel for accommodating gas so as to be able to be sent to said powder fluidization means.
The method for filling fine powder according to the above.
【請求項10】 前記粉体流動化手段が更に、前記粉体
流動化のための気体導入手段を有し、該気体導入手段
が、逆止弁付きの送気ポンプであることを特徴とする請
求項2乃至8のいずれか1に記載の微細粉体の充填方
法。
10. The powder fluidizing means further includes a gas introducing means for fluidizing the powder, and the gas introducing means is an air supply pump with a check valve. A method for filling a fine powder according to any one of claims 2 to 8.
【請求項11】 前記粉体流動化手段が更に、前記粉体
流動化のための気体導入手段との間に、気体を該粉体流
動化手段内に均一に導入するための気体分配手段を有す
ることを特徴とする請求項7乃至10のいずれか1に記
載の微細粉体の充填方法。
11. The powder fluidizing means further includes a gas distribution means for uniformly introducing a gas into the powder fluidizing means between the powder fluidizing means and the gas fluidizing means. The method for filling a fine powder according to any one of claims 7 to 10, wherein the method comprises:
【請求項12】 前記粉体が、平均体積粒径0.2μm
〜20μmの静電潜像現像用トナーであることを特徴と
する請求項2乃至11のいずれか1に記載の微細粉体の
充填方法。
12. The powder has an average volume particle size of 0.2 μm.
The method for filling fine powder according to any one of claims 2 to 11, wherein the toner is a toner for developing an electrostatic latent image having a size of from 20 to 20 µm.
【請求項13】 粉体の流動化のための気体が導入され
る気体導入開口部を上流部に有する密閉可能な収納粉体
流動化装置と、該気体が排出される気体排出開口部を下
流部に有する充填ノズルと、前記収納粉体流動化装置と
充填ノズルを連結せる流動化粉体の経路とを有し、該充
填ノズルは充填用容器の口を密閉可能である微細粉体充
填装置であって、該収納粉体流動化装置上流の気体導入
開口部及び充填ノズル下流部の気体排出開口部は、共に
気体を通過させるが粉体は通過させない粉体−気体分離
篩を備えることにより、流動化粉体を該収納粉体流動化
装置及び充填用容器の間に封じ込め、前記収納粉体流動
化装置の気体排出開口部の開口面積が、前記充填ノズル
の気体排出開口部の開口面積の1.002倍以上である
ことにより、該気体排出開口部の気体の流速が前記気体
排出開口部の気体の流速よりも高くされて、流動化粉体
が前記収納粉体流動化装置から流動化粉体の経路及び充
填ノズルを経由して前記充填用容器に自然排出されるこ
とを特徴とする微細粉体充填装置。
13. A sealable storage powder fluidizing device having an upstream gas introducing opening through which a gas for fluidizing powder is introduced, and a downstream gas discharging opening through which the gas is discharged. A fine powder filling device, comprising: a filling nozzle having a filling section; and a fluidized powder path connecting the storage powder fluidizing device and the filling nozzle, wherein the filling nozzle is capable of sealing a mouth of a filling container. The gas introduction opening upstream of the storage powder fluidization device and the gas discharge opening downstream of the filling nozzle are both provided with a powder-gas separation sieve that allows gas to pass through but does not allow powder to pass through. Enclosing the fluidized powder between the storage powder fluidizer and the filling container, wherein the opening area of the gas discharge opening of the storage powder fluidizer is the opening area of the gas discharge opening of the filling nozzle. 1.002 times or more of The flow velocity of the gas at the discharge opening is made higher than the flow velocity of the gas at the gas discharge opening, and the fluidized powder flows from the storage powder fluidizer through the fluidized powder path and the filling nozzle. A fine powder filling apparatus characterized by being naturally discharged into a filling container.
【請求項14】 充填用粉体及び気体を収納する前記密
閉可能な容器状の収納粉体流動化装置中の該粉体を気体
により流動化した後、該流動化された粉体を該収納粉体
流動化装置から前記経路を介して前記充填ノズルまで排
出することを特徴とする請求項13に記載の微細粉体充
填装置。
14. The powder in the hermetically sealable container-like powder fluidizing device for storing a filling powder and a gas is fluidized by a gas, and then the fluidized powder is stored in the container. 14. The fine powder filling apparatus according to claim 13, wherein the powder is discharged from the powder fluidizing apparatus to the filling nozzle via the path.
【請求項15】 前記収納粉体流動化装置内への追加気
体の導入により、前記粉体の流動化が行なわれることを
特徴とする請求項14に記載の微細粉体充填装置。
15. The fine powder filling apparatus according to claim 14, wherein the powder is fluidized by introducing an additional gas into the stored powder fluidizing apparatus.
【請求項16】 前記収納粉体流動化装置が振動される
ことにより、前記気体による粉体の流動化が行なわれる
ことを特徴とする請求項14又は請求項15に記載の微
細粉体充填装置。
16. The fine powder filling apparatus according to claim 14, wherein the powder is fluidized by the gas by vibrating the stored powder fluidizing apparatus. .
【請求項17】 前記粉体の前記粉体流動化装置から前
記充填ノズルまでの排出が、前記粉体流動化装置内の圧
力を昇圧することにより行なわれることを特徴とする請
求項14乃至16のいずれか1に記載の微細粉体充填装
置。
17. The discharge of the powder from the powder fluidization device to the filling nozzle is performed by increasing the pressure in the powder fluidization device. The fine powder filling apparatus according to any one of the above.
【請求項18】 前記粉体の前記粉体流動化装置から前
記充填ノズルまでの排出が、該粉体流動化手段に外部圧
力を加えて該粉体流動化装置の内容積を減容させること
により行なわれることを特徴とする請求項14乃至17
のいずれか1に記載の微細粉体充填装置。
18. The discharge of the powder from the powder fluidization device to the filling nozzle may include applying an external pressure to the powder fluidization means to reduce the internal volume of the powder fluidization device. 18. The method according to claim 14, wherein:
The fine powder filling apparatus according to any one of the above.
【請求項19】 前記粉体流動化装置が、導入気体の流
速を加減可能な導入気体調節弁と、前記流動化粉体の排
出経路の排出粉体の流速を調節可能な排出粉体流速調節
弁とを有し、前記流動化粉体の排出量及び排出程度が、
該導入気体調節弁の開閉程度の調節又は/及び該排出粉
体流速調節弁の開閉程度の調節により制御されることを
特徴とする請求項14乃至18のいずれか1に記載の微
細粉体充填装置。
19. An introduction gas control valve capable of adjusting a flow rate of an introduction gas, and a discharge powder flow rate control capable of adjusting a flow rate of a discharge powder in a discharge path of the fluidization powder. And a discharge amount and a discharge degree of the fluidized powder,
19. The fine powder filling according to claim 14, which is controlled by adjusting the opening / closing degree of the introduction gas control valve and / or adjusting the opening / closing degree of the discharge powder flow rate control valve. apparatus.
【請求項20】 前記粉体流動化装置が更に、全開及び
全閉自在な圧力開放弁を有し、前記流動化粉体の排出の
開始及び終了が該圧力開放弁の開閉により迅速に行なわ
れることを特徴とする請求項19に記載の微細粉体充填
装置。
20. The powder fluidizing device further includes a pressure release valve that can be fully opened and fully closed, and the start and end of discharge of the fluidized powder are quickly performed by opening and closing the pressure relief valve. 20. The fine powder filling apparatus according to claim 19, wherein:
【請求項21】 前記粉体流動化装置が更に、前記粉体
流動化のための気体導入手段を有し、該気体導入手段
が、気体を前記粉体流動化装置に送出可能に収納する圧
力容器であることを特徴とする請求項14乃至20のい
ずれか1に記載の微細粉体充填装置。
21. The powder fluidization device further includes a gas introduction unit for fluidizing the powder, and the gas introduction unit is configured to store a gas in the powder fluidization device such that the gas can be delivered to the powder fluidization device. The fine powder filling apparatus according to any one of claims 14 to 20, wherein the apparatus is a container.
【請求項22】 前記粉体流動化装置が更に、前記粉体
流動化のための気体導入手段を有し、該気体導入手段
が、逆止弁付きの送気ポンプであることを特徴とする請
求項14乃至20のいずれか1に記載の微細粉体充填装
置。
22. The powder fluidizing device further comprises gas introduction means for fluidizing the powder, wherein the gas introduction means is an air supply pump with a check valve. The fine powder filling apparatus according to any one of claims 14 to 20.
【請求項23】 前記粉体流動化装置が更に、前記粉体
流動化のための気体導入手段との間に、気体を該粉体流
動化装置内に均一に導入するための気体分配手段を有す
ることを特徴とする請求項14乃至22のいずれか1に
記載の微細粉体充填装置。
23. The powder fluidization device further includes a gas distribution unit for uniformly introducing gas into the powder fluidization device between the powder fluidization device and the gas fluidization device. The fine powder filling apparatus according to any one of claims 14 to 22, comprising:
【請求項24】 前記粉体が、平均体積粒径0.2μm
〜20μmの静電潜像現像用トナーであることを特徴と
する請求項14乃至23のいずれか1に記載の微細粉体
充填装置。
24. The powder according to claim 1, wherein the powder has an average volume particle size of 0.2 μm.
24. The fine powder filling apparatus according to claim 14, wherein the toner is a toner for developing an electrostatic latent image having a size of 20 to 20 [mu] m.
JP2001102264A 2001-03-13 2001-03-30 Filling method and filling device for powder toner Expired - Fee Related JP3549051B2 (en)

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JP2001102264A JP3549051B2 (en) 2001-03-30 2001-03-30 Filling method and filling device for powder toner
US10/095,268 US6679301B2 (en) 2001-03-13 2002-03-11 Powder packing method and apparatus therefor
CNB021071756A CN1275827C (en) 2001-03-13 2002-03-13 Power filling method and apparatus
EP02005321A EP1254835A3 (en) 2001-03-13 2002-03-13 Powder packing method and apparatus therefor

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