JP2005075374A - Fine powder filling apparatus - Google Patents

Fine powder filling apparatus Download PDF

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JP2005075374A
JP2005075374A JP2003305477A JP2003305477A JP2005075374A JP 2005075374 A JP2005075374 A JP 2005075374A JP 2003305477 A JP2003305477 A JP 2003305477A JP 2003305477 A JP2003305477 A JP 2003305477A JP 2005075374 A JP2005075374 A JP 2005075374A
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fine powder
filling
pipe
gas
container
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Kazuyoshi Morii
和好 森井
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Ricoh Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a fine powder filling apparatus, which is easy to handle, inexpensive, need not to be stopped at every time when a stored powder in a container is transferred out, offers superior work efficiency, and can be operated consecutively. <P>SOLUTION: The fine powder filling apparatus at least has a closed housing unit in which fine powder is enclosed airtightly, a fine powder fluidizing means for guiding a gas into the housing unit to fluidize the fine powder, and a filling means for discharging the fluidized powder from the housing unit and filling it into a fine powder filling container. The housing unit has a fine powder supply pipe arranged above and a fine powder transfer container arranged below. The supply pipe has a fine powder inlet, which is provided with an enclosing means. The fine powder transfer container has the fine powder fluidizing means, the fine powder filling means consisting of a pressurizing means using a gas and a fine powder discharge pipe, and a pressure adjusting means. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、微粉体の小口径容器、少容量容器への微粉体の充填装置に関し、特に静電潜像現像用トナーを複写機のカートリッジや、複写機現像部へ直接充填する充填装置に関する。   The present invention relates to an apparatus for filling fine powder into a small-diameter container and a small-capacity container for fine powder, and more particularly to a filling apparatus for directly filling toner for developing an electrostatic latent image into a cartridge of a copying machine or a developing unit of a copying machine.

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。これらの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。   Examples of powder filling machines include rotary valves, screw feeders, and auger type filling machines. To fill the powder container from these devices, use the powder's own weight, place the powder container directly under the filling machine, increase the bulk density of the powder in the filling machine, and cut it out. A method of filling these powders into the containers by gravity is a general method for efficiently filling powders into a constant volume filling container. In addition, after introducing gas into the powder in the powder feeder and improving the fluidity, it is transported from the powder feeder to the vicinity of the receiving container by the subordinate pipe and degassed from the powder in the transport pipe by the deaeration pipe. Then, a method (Japanese Patent Laid-Open No. 9-193902) for filling the container with high density has been proposed.

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ないことから製作が難かしい上に重量が大で持ち運びに難があった。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た。   However, these systems have to be provided with a deaeration pipe accurately and coaxially provided in the filling pipe, so that they are difficult to manufacture and are heavy and difficult to carry. In addition, it is effective when the filling container has a large filling diameter and is located directly under the filling machine. However, in a small-diameter filling container or a filling container having various structures inside, the filling machine or the transport pipe is separated. It was difficult to replace the powder in the container with the air inside the container, and there was a problem that the powder was blown up from the filling port and the movement of the powder was blocked by the structure in the container, so that the desired amount could not be filled.

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、粉塵が舞ったり、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するという問題も生じていた。   In addition, if you try to replenish toner used in copiers and printers directly to the toner bottle and the developing part of the machine in the general office where the machine is installed, dust may be scattered, even if it can be replenished However, when filling in a low density state containing a lot of air or directly into a complicated developing part, there is a problem that an image forming problem occurs in a part where the toner enters and a part where the toner does not enter. Also occurred.

これらの問題を解決するために、例えば、特開2002−337801号公報(特許文献1)に記載の発明が開示されている。特許文献1に記載の発明においては、図2に示すように、充填用微粉体及び気体を収納する密閉構造の充填用粉体収納装置(1)中で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充填用粉体収納装置から充填ノズルまで移送し、該充填ノズルの先端を粉体充填用容器(9)内に挿入し、気体により流動化された微粉体を該容器内に吐出して充填する方法であって、充填ノズルの先端が、該容器内に滞留する微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というものである。   In order to solve these problems, for example, an invention described in JP-A-2002-337801 (Patent Document 1) is disclosed. In the invention described in Patent Document 1, as shown in FIG. 2, after powder is fluidized with gas in a sealed powder storage device (1) that stores fine powder and gas for filling, The fluidized powder is transferred from the filling powder storage device to the filling nozzle, the tip of the filling nozzle is inserted into the powder filling container (9), and the fine powder fluidized by the gas is obtained. In this method, the container is discharged and filled, and the container is filled with the powder in a state where the tip of the filling nozzle is surrounded by the fine powder staying in the container.

特許文献1に記載の方法により、粉体中に均一に気体を導入し最少の気体量で制御して微粉体を流動状態にして、小口径充填容器や複雑な形状の充填容器の奥や底部に流動微粉体を流入させ、容器内で充填ノズルから容器開口間の微粉体の層により充填後の微粉体から脱気させ、簡単に高密度、無粉塵で充填できるようになった。さらに、特許文献1に記載の装置は、持ち運びができ、操作が簡単で、誰でも、どんな場所でも充填できるものである。   By the method described in Patent Document 1, gas is uniformly introduced into the powder and controlled with a minimum amount of gas so that the fine powder is in a fluid state, and the back and bottom of a small-diameter filling container or a complicated-shaped filling container Flowing fine powder was allowed to flow into the container, and the fine powder after filling was degassed by a layer of fine powder between the filling nozzle and the opening of the container in the container, so that it could be filled easily with high density and no dust. Furthermore, the device described in Patent Document 1 is portable, easy to operate, and can be filled by anyone at any location.

しかしながら、特許文献1に記載の装置は、圧送装置自体が微粉体の貯蔵容器を兼ねているため、流動床が大型にならざるを得ず、高価で取扱いが不自由であるという欠点を有していた。また、容器内の貯蔵粉体を搬出するたびに、装置の稼動を停止し、新たな貯蔵容器と交換しなければならないので、作業効率が悪いという問題も有していた。   However, the apparatus described in Patent Document 1 has a disadvantage that the fluidized bed is inevitably large because the pressure feeding apparatus itself also serves as a storage container for fine powder, and is expensive and inconvenient to handle. It was. In addition, every time the stored powder in the container is carried out, the operation of the apparatus must be stopped and replaced with a new storage container, which has a problem of poor work efficiency.

特開2002−337801号公報JP 2002-337801 A

本発明は、流動床が小型であって、取扱いが容易且つ安価で、容器内の貯蔵粉体を搬出するたびに、装置の稼動を停止する必要がなく、作業効率に優れ、連続して稼動させることができる微粉体充填用装置を提供することを目的とする。   The present invention has a small fluidized bed, is easy to handle, is inexpensive, and does not need to stop the operation every time the stored powder in the container is carried out. It is an object of the present invention to provide a fine powder filling device that can be made to operate.

本発明によれば、以下に示す微粉体充填用装置が提供される。
〔1〕微粉体を密閉して収納する密閉収納装置と、該収納装置に気体を導入して微粉体を流動化させる微粉体の流動化手段と、該密閉収納装置から流動化された微粉体を吐出させて微粉体充填用容器に充填する充填手段とを少なくとも有する微粉体の充填用装置であって、該密閉収納装置が上部の微粉体供給管と下部の微粉体圧送容器とを有し、該微粉体供給管の微粉体投入口に微粉体の密閉手段が設けられ、該微粉体圧送容器に前記微粉体の流動化手段と、気体による加圧手段と微粉体の吐出管からなる微粉体の充填手段と、圧力調整手段とが設けられていることを特徴とする微粉体充填用装置。
〔2〕該微粉体圧送容器の容量が、該微粉体供給管の容量に対して1.5倍以上であることを特徴とする前記〔1〕に記載の微粉体充填用装置。
〔3〕該微粉体の密閉手段が、微粉体供給調整バルブであることを特徴とする前記〔1〕又は〔2〕に記載の微粉体充填用装置。
〔4〕該微粉体の密閉手段が、微粉体投入口への配管と該配管にフィルタを介して設けられた気体の導入・吸引バルブとからなることを特徴とする前記〔1〕又は〔2〕に記載の微粉体充填用装置。
〔5〕該微粉体圧送容器の上部に絞り部が設けられ、該絞り部を含む微粉体圧送容器に微粉体の第一の流動化手段が設けられていることを特徴とする前記〔1〕〜〔4〕のいずれかに記載の微粉体充填用装置。
〔6〕該絞り部の頂角が6〜70度であることを特徴とする前記〔5〕に記載の微粉体充填用装置。
〔7〕該第一の流動化手段が、微粉体圧送容器の絞り部を含む部分に設けられた第一流動床と第一空気ヘッダと、該第一空気ヘッダへの気体配管とを有し、該気体配管にフィルタを介して気体の導入・吸引バルブが設けられていることを特徴とする前記〔5〕又は〔6〕に記載の微粉体充填用装置。
〔8〕該流動化手段が、微粉体圧送容器の底部に設けられた第二流動床と、第二流動床の下に設けられた第二空気ヘッダと、該第二空気ヘッダへの気体導入管と、該気体導入管に設けられた気体圧力調整弁とからなる第二の流動化手段であることを特徴とする前記〔1〕〜〔7〕のいずれかに記載の微粉体充填用装置。
〔9〕該気体による加圧手段が、微粉体圧送容器への気体導入管と、該気体導入管に設けられている開閉バルブであることをことを特徴とする前記〔1〕〜〔8〕のいずれかに記載の微粉体充填用装置。
〔10〕該粉体吐出管の入り口が気体導入管の出口より下方に設けられていることを特徴とする前記〔1〕〜〔9〕のいずれかに記載の微粉体充填用装置。
〔11〕該圧力調整手段が、気体放出管と、該気体放出管に設けられたフィルタと圧抜きバルブと気体配管とからなり、該気体配管に開閉バルブが設けられていることを特徴とする前記〔1〕〜〔10〕のいずれかに記載の微粉体充填用装置。
〔12〕該微粉体供給管と微粉体圧送容器との間に振動篩が設けられていることを特徴とする前記〔1〕〜〔11〕のいずれかに記載の微粉体充填用装置。
〔13〕装置各部が、フェルール製の簡易配管締結具で密閉連結されていることを特徴とする前記〔1〕〜〔12〕のいずれかに記載の微粉体充填用装置。
According to the present invention, the following apparatus for filling fine powder is provided.
[1] A hermetic storage device for hermetically storing fine powder, a fluidizing means for fine powder that fluidizes the fine powder by introducing gas into the storage device, and a fine powder fluidized from the hermetic storage device A fine powder filling device having at least a filling means for discharging into the fine powder filling container, wherein the hermetic storage device has an upper fine powder supply pipe and a lower fine powder pressure feed container. A fine powder sealing means is provided at the fine powder inlet of the fine powder supply pipe, and the fine powder is composed of the fine powder fluidizing means, a gas pressurizing means, and a fine powder discharge pipe in the fine powder feed container. An apparatus for filling fine powder, characterized in that a body filling means and a pressure adjusting means are provided.
[2] The apparatus for filling fine powder according to [1], wherein the capacity of the fine powder feeding container is 1.5 times or more the capacity of the fine powder supply pipe.
[3] The fine powder filling apparatus according to [1] or [2], wherein the fine powder sealing means is a fine powder supply adjusting valve.
[4] The above [1] or [2], wherein the fine powder sealing means comprises a pipe to the fine powder inlet and a gas introduction / suction valve provided in the pipe via a filter. ] The apparatus for fine powder filling described in the above.
[5] The above-mentioned [1], wherein a throttle part is provided in an upper part of the fine powder feeding container, and a first fluidizing means for fine powder is provided in the fine powder pressure feeding container including the throttle part. -The apparatus for fine powder filling in any one of [4].
[6] The fine powder filling device according to [5], wherein the apex angle of the narrowed portion is 6 to 70 degrees.
[7] The first fluidizing means includes a first fluidized bed, a first air header, and a gas pipe to the first air header provided in a portion including the throttle portion of the fine powder pressure feeding container. The apparatus for filling fine powder according to [5] or [6], wherein the gas pipe is provided with a gas introduction / suction valve through a filter.
[8] The fluidizing means includes a second fluidized bed provided at the bottom of the fine powder pressure container, a second air header provided under the second fluidized bed, and gas introduction into the second air header. The fine powder filling apparatus according to any one of [1] to [7], wherein the fine fluid filling means is a second fluidizing means comprising a pipe and a gas pressure regulating valve provided in the gas introduction pipe. .
[9] The above [1] to [8], wherein the gas pressurizing means is a gas introduction pipe to the fine powder pressure feeding container and an opening / closing valve provided in the gas introduction pipe. The apparatus for filling fine powder according to any one of the above.
[10] The fine powder filling apparatus according to any one of [1] to [9], wherein an inlet of the powder discharge pipe is provided below an outlet of the gas introduction pipe.
[11] The pressure adjusting means includes a gas release pipe, a filter provided in the gas release pipe, a pressure release valve, and a gas pipe, and the gas pipe is provided with an open / close valve. The apparatus for filling fine powder according to any one of [1] to [10].
[12] The apparatus for filling fine powder according to any one of [1] to [11], wherein a vibrating sieve is provided between the fine powder supply pipe and the fine powder pumping container.
[13] The apparatus for filling fine powder according to any one of [1] to [12], wherein each part of the apparatus is hermetically connected with a simple pipe fastener made of ferrule.

本発明の微粉体充填用装置は、流動床が小型なので、取扱いが容易且つ安価である。また、容器内の貯蔵粉体を搬出するたびに、装置の稼動を停止する必要がないことから、作業効率に優れ、連続して稼動させることができる。   The apparatus for filling fine powder of the present invention is easy and inexpensive to handle because the fluidized bed is small. Moreover, since it is not necessary to stop the operation of the apparatus every time the stored powder in the container is carried out, it is excellent in work efficiency and can be operated continuously.

本発明の微粉体充填用装置は、微粉体を密閉して収納する密閉収納装置と、該収納装置に気体を導入して微粉体を流動化させる微粉体の流動化手段と、該密閉収納装置から流動化された微粉体を吐出させて微粉体充填用容器に充填する充填手段とを少なくとも有する。かかる構成の微粉体充填用装置は従来公知であるが、本発明における特徴的な部分は、該密閉収納装置が上部の微粉体供給管1と下部の微粉体圧送容器2とに分かれていることである。このように構成すると、微粉体圧送容器2の内径を微粉体供給管1の内径より小さくすることにより、流動床の面積を小さくすることができるので低コストで作製することができ、小型かつ軽量なので取扱いが容易である。   The apparatus for filling fine powder of the present invention includes a sealed storage device for sealing and storing fine powder, a fluidizing means for fine powder that introduces gas into the storage device to fluidize the fine powder, and the sealed storage device. And a filling means for discharging the fluidized fine powder into the fine powder filling container. A fine powder filling apparatus having such a configuration is conventionally known, but the characteristic part of the present invention is that the hermetic storage device is divided into an upper fine powder supply pipe 1 and a lower fine powder pressure feeding container 2. It is. If comprised in this way, since the area of a fluidized bed can be made small by making the internal diameter of the fine powder pumping container 2 smaller than the internal diameter of the fine powder supply pipe | tube 1, it can produce at low cost, and is small and lightweight. So it is easy to handle.

上記微粉体圧送容器2の容量は、微粉体供給管1の容量に対し1.5倍以上であることが好ましい。微粉体圧送容器2の容量が、微粉体供給管1の容量に対し1.5倍未満の場合は、微粉体圧送容器2における微粉体の流動化が効率よく行なえない虞がある。   The capacity of the fine powder feeding container 2 is preferably 1.5 times or more the capacity of the fine powder supply pipe 1. When the capacity of the fine powder feeding container 2 is less than 1.5 times the capacity of the fine powder supply pipe 1, there is a possibility that the fine powder in the fine powder feeding container 2 cannot be fluidized efficiently.

本発明における密閉収納装置は全体が密閉構造になっている。そのためには、本発明の装置各部は、フェルール製の簡易配管締結具で密閉連結されていることが好ましい。このように構成されていると、微粉体の品種切替の際に装置各部を容易に着脱することができるので、生産性が向上する。   The hermetic storage device in the present invention has a hermetic structure as a whole. For that purpose, it is preferable that each part of the apparatus of the present invention is hermetically connected with a simple pipe fastener made of ferrule. If comprised in this way, since each part of an apparatus can be easily attached or detached at the time of the kind change of a fine powder, productivity will improve.

また、密閉収納装置を構成する微粉体供給管1の微粉体投入口15に微粉体の密閉手段が設けられている。微粉体投入口15に設けられる密閉手段としては、図1に示すように、微粉体供給調整バルブ3を微粉体投入口15に設けることが挙げられる。但し、微粉体供給調整バルブ3を設けると、微粉体の凝集体が形成されるので、後述するように、振動篩を設けて凝集体を取り除くことが好ましい。   Further, a fine powder sealing means is provided at the fine powder inlet 15 of the fine powder supply pipe 1 constituting the hermetic storage device. As the sealing means provided at the fine powder inlet 15, as shown in FIG. 1, the fine powder supply adjustment valve 3 is provided at the fine powder inlet 15. However, since a fine powder aggregate is formed when the fine powder supply adjustment valve 3 is provided, it is preferable to provide a vibrating sieve to remove the aggregate as described later.

また、微粉体投入口15の密閉化手段として、図示はしないが、微粉体投入口15に気体吸引管を取り付け、該気体吸引管にフィルタを介して開閉バルブを設けることが挙げられる。このように構成すると、開閉バルブを開いて気体を吸引すると、微粉体が粉体投入口15に集積して粉体ブロックを形成するので、密閉収納装置内部を密閉化することができる。この構成の場合は微粉体の凝集体が形成されないので、微粉体の凝集体を取り除く手段を設けなくてもよい。   As a means for sealing the fine powder inlet 15, although not shown, a gas suction pipe is attached to the fine powder inlet 15, and an open / close valve is provided on the gas suction pipe via a filter. With this configuration, when the gas is sucked by opening the opening / closing valve, the fine powder accumulates in the powder inlet 15 to form a powder block, so that the inside of the hermetic storage device can be sealed. In the case of this configuration, since the fine powder aggregates are not formed, it is not necessary to provide means for removing the fine powder aggregates.

本発明における密閉収納装置を構成する微粉体圧送容器2には、微粉体の流動化手段と、気体による加圧手段と微粉体の吐出管からなる微粉体の充填手段と、圧力調整手段とが設けられている。即ち、微粉体圧送容器2において、微粉体を流動化し、流動化した微粉体を気体による加圧手段と微粉体の吐出管からなる充填手段により少容量容器23へ吐出して、充填することができる。その際、圧力調整手段により微粉体圧送容器内の圧力を調整することにより、充填手段による微粉体の吐出を安定して行なうことがができる。   The fine powder feeding container 2 constituting the hermetic storage device in the present invention includes a fine powder fluidizing means, a fine pressure filling means comprising a gas pressurizing means and a fine powder discharge pipe, and a pressure adjusting means. Is provided. That is, in the fine powder feeding container 2, the fine powder is fluidized, and the fluidized fine powder is discharged and filled into the small-capacity container 23 by the filling means including the gas pressurizing means and the fine powder discharge pipe. it can. At that time, by adjusting the pressure in the fine powder feeding container by the pressure adjusting means, it is possible to stably discharge the fine powder by the filling means.

微粉体圧送容器2に設けられる微粉体の流動化手段には、第一の流動化手段と第二の流動化手段がある。これらの流動化手段により、空気を緩やかに微粉体内に導入して、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微粉体は高い流動性を有するため、充填用粉体収納装置内の圧力を外圧より僅かに高くするだけで、粉体を充填用粉体収納装置外に排出でき、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。   As the fluidizing means for the fine powder provided in the fine powder feeding container 2, there are a first fluidizing means and a second fluidizing means. By these fluidization means, air can be gently introduced into the fine powder to achieve fluidization with a low Brownian motion of the powder. Since the fine powder has high fluidity after fluidization, the powder can be discharged out of the filling powder storage device by transferring the pressure in the filling powder storage device slightly higher than the external pressure. Pneumatic transport can be smoothly performed in the path to the tip of the filling nozzle, and filling can be performed without extra stirring in the filling container.

微粉体圧送容器2の上部に絞り部4が設けられていることが好ましく、絞り部4を含む微粉体圧送容器2に第一の流動化手段が設けられていることが好ましい。即ち、微粉体を絞り部4で重力により滑り落としながら、流動化させることが好ましい。
絞り部4の頂角は、微粉体が安定して滑り落ちるという観点から、6〜70度であることが好ましく、15〜60度がより好ましく、30〜50度が更に好ましい。頂角が6度未満の場合は絞りが小さすぎて微粉体が垂直に近い状態で落下するので、滑り落とすという効果が得られない虞があり、70度を超える場合は絞りが大きすぎて微粉体がスムースに落下しない虞がある。
It is preferable that the throttle part 4 is provided in the upper part of the fine powder pumping container 2, and it is preferable that the first fluidization means is provided in the fine powder pumping container 2 including the throttle part 4. That is, it is preferable to fluidize the fine powder while sliding it down by the gravity at the throttle portion 4.
The apex angle of the narrowed portion 4 is preferably 6 to 70 degrees, more preferably 15 to 60 degrees, and further preferably 30 to 50 degrees, from the viewpoint that the fine powder stably slides down. If the apex angle is less than 6 degrees, the aperture is too small and the fine powder falls in a state of being nearly vertical, so there is a possibility that the effect of sliding down may not be obtained. There is a risk that the body will not fall smoothly.

該第一の流動化手段においては、装置外から気体を微粉体に均等に導入するために、具体的には、絞り部4を含む微粉体圧送容器2に設けられた第一流動床5aと、第一流動床5aの下部に設けられた第一空気ヘッダ5bと、第一空気ヘッダ5bへの気体配管6とを有し、該気体配管6にフィルタ8を介して気体の導入・吸引バルブ7が設けられていることが好ましい。
第一流動床5aは気体分配手段としての機能を有し、例えば、焼結金属板、焼結樹脂板、目の細かい金網などが挙げられ、流動床5aの下には空気ヘッダ5bが設けられているので、装置外から導入された気体は微粉体圧送容器2に均等に導入される。また、微粉体が絞り部4を落下している際に気体を吸引して微粉体を絞り部4に集積させて粉体ブロックを形成することにより、微粉体の流れを止めて絞り部4より下方部分を密閉化することができる。
In the first fluidizing means, in order to uniformly introduce gas into the fine powder from outside the apparatus, specifically, a first fluidized bed 5a provided in the fine powder pressure feeding container 2 including the throttle portion 4; And a first air header 5b provided at the lower part of the first fluidized bed 5a and a gas pipe 6 to the first air header 5b. A gas introduction / suction valve is connected to the gas pipe 6 through a filter 8. 7 is preferably provided.
The first fluidized bed 5a has a function as a gas distribution means, and includes, for example, a sintered metal plate, a sintered resin plate, a fine wire mesh, and the like, and an air header 5b is provided under the fluidized bed 5a. Therefore, the gas introduced from outside the apparatus is equally introduced into the fine powder pressure feeding container 2. Further, when the fine powder is falling on the throttle portion 4, the flow of fine powder is stopped from the throttle portion 4 by sucking gas and accumulating the fine powder in the throttle portion 4 to form a powder block. The lower part can be sealed.

上記第二の流動化手段においては、微粉体圧送容器2の底部に設けられた第二流動床17aと、第二流動床17aの下に設けられた第二空気ヘッダと17b、第二空気ヘッダ17bへの気体導入管18と、該気体導入管に設けられた気体圧力調整弁19とからなることが好ましい。第二流動床17aは、上記流動床5aと同様に構成され、気体圧力調整弁19としては第一気体圧力調整弁19aと第二気体圧力調整弁19bが設けられていることがより好ましく、第1調整弁19aと第2調整弁19bの間には第1圧力計(p1)を、第2調整弁19bと微粉体圧送容器2の底部との間には第2圧力計(p2)を設けることが好ましく、第2圧力計(p2)と粉体搬送管2の底部との間には空気流量計20を設けることが好ましい。   In the second fluidizing means, a second fluidized bed 17a provided at the bottom of the fine powder pressure container 2, a second air header and 17b provided under the second fluidized bed 17a, and a second air header. It is preferable to consist of the gas introduction pipe | tube 18 to 17b and the gas pressure control valve 19 provided in this gas introduction pipe | tube. The second fluidized bed 17a is configured in the same manner as the fluidized bed 5a, and it is more preferable that the first gas pressure regulating valve 19a and the second gas pressure regulating valve 19b are provided as the gas pressure regulating valve 19, A first pressure gauge (p1) is provided between the first adjustment valve 19a and the second adjustment valve 19b, and a second pressure gauge (p2) is provided between the second adjustment valve 19b and the bottom of the fine powder feeding container 2. It is preferable that an air flow meter 20 is provided between the second pressure gauge (p2) and the bottom of the powder transport pipe 2.

上記微粉体圧送容器2には、気体による加圧手段と微粉体の吐出管9からなる微粉体の充填手段と、圧力調整手段とが設けられている。該充填手段を構成する加圧手段としては、微粉体圧送容器へ気体導入管10を配管し、気体導入管10に開閉バルブ11aを設けることが好ましく挙げられる。また、圧力調整手段としては、微粉体圧送容器2へ気体配管12を配管し、気体配管12にフィルタ14と圧抜きバルブ13を設け、気体配管12に開閉バルブ11bが設けられた気体導入管16を設けることが好ましく挙げられる。尚、開閉バルブ11aと開閉バルブ11bは別々のバルブを設けてもよければ、一のバルブに統合してもよい。   The fine powder feeding container 2 is provided with a fine powder filling means composed of a gas pressurizing means and a fine powder discharge pipe 9, and a pressure adjusting means. As the pressurizing means constituting the filling means, it is preferable to connect the gas introduction pipe 10 to the fine powder feeding container and to provide the gas introduction pipe 10 with an opening / closing valve 11a. Further, as a pressure adjusting means, a gas pipe 12 is piped to the fine powder pressure feeding container 2, a filter 14 and a pressure relief valve 13 are provided in the gas pipe 12, and a gas introduction pipe 16 provided with an opening / closing valve 11b in the gas pipe 12. It is preferable to provide. Note that the opening / closing valve 11a and the opening / closing valve 11b may be provided as separate valves or may be integrated into one valve.

このように構成されていると、加圧手段と圧力調整手段で、微粉体圧送容器2内の圧力を調節、制御して、微粉体に適度の圧力を加え、吐出管から微粉体を充填容器23内に吐出することができる。また、流動化した微粉体を排出し、容器23に充填するときの開始および終了の制御を、微粉体圧送容器2内の圧力を調節することにより行うことができる。微粉体圧送容器2内の圧力の制御は、開閉バルブ11aと圧抜きバルブ13の調整によって行なうことができ、開閉バルブ11bによって補助することができる。また粉体充填操作中で微粉体圧送容器2内の圧力を変更し、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うことができる。   When configured in this manner, the pressure in the fine powder feeding container 2 is adjusted and controlled by the pressurizing means and the pressure adjusting means to apply an appropriate pressure to the fine powder, and the fine powder is filled from the discharge pipe. 23 can be discharged. Further, the start and end of the fluidized fine powder discharged and filled in the container 23 can be controlled by adjusting the pressure in the fine powder pressure feed container 2. Control of the pressure in the fine powder pressure feeding container 2 can be performed by adjusting the on-off valve 11a and the pressure release valve 13, and can be assisted by the on-off valve 11b. In addition, the pressure in the fine powder feeding container 2 can be changed during the powder filling operation, and fine pressure adjustment can be performed to change the powder outflow state, for example, at the beginning and midway of the powder filling operation.

なお、微粉体をスムースに吐出するためには、粉体吐出管9の入り口が気体導入管10の出口より下方に設けられていることが好ましい。   In order to smoothly discharge the fine powder, the inlet of the powder discharge pipe 9 is preferably provided below the outlet of the gas introduction pipe 10.

微粉体圧送容器2における加圧の程度は、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、微粉体圧送容器2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。微粉体圧送容器2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は、2〜1500ゲージヘクトpa、好ましくは3〜800ゲージヘクトpa、より好ましくは10〜500ゲージヘクトpaである。2ゲージヘクトpa未満の加圧では、充填に長時間を要する。   The degree of pressurization in the fine powder feeding container 2 may be slightly higher than the normal pressure, and if it is pressurized too much, the trapping effect by the fine powder cloud staying in the fine powder feeding container 2 is impaired. There is. Generally, the degree of pressurization is 2 to 1500 gauge hectopas, preferably 3 to 800, although it depends on the amount of the fine powder cloud staying in the fine powder feeding container 2 and the filling mode of the fluidized fine powder. Gauge hectopa, more preferably 10 to 500 gauge hectopa. When the pressure is less than 2 gauge hectares, filling takes a long time.

本発明においては、微粉体供給管1と微粉体圧送容器2との間に振動篩21が設けられていることが好ましい。特に、密閉手段として、微粉体供給調整バルブ3を微粉体投入口15に設けた場合、振動篩21を設けて凝集体を取り除くことが好ましい。また、振動篩21は激しい振動を装置本体に与えないために、スプリング22を用いて装置に取付けられていることが好ましい。   In the present invention, it is preferable that a vibrating sieve 21 is provided between the fine powder supply pipe 1 and the fine powder pumping container 2. In particular, when the fine powder supply adjusting valve 3 is provided at the fine powder inlet 15 as a sealing means, it is preferable to provide the vibrating sieve 21 to remove the aggregate. Further, the vibration sieve 21 is preferably attached to the apparatus using a spring 22 in order not to give intense vibration to the apparatus main body.

本発明の微粉体充填用装置は、広く微粉体の充填に使用することができるが、静電潜像現像用の粉体トナーの充填に好適に使用することができる。   The fine powder filling apparatus of the present invention can be widely used for filling fine powder, but can be suitably used for filling powder toner for developing an electrostatic latent image.

本発明の微粉体充填用装置の説明図である。It is explanatory drawing of the apparatus for fine powder filling of this invention. 従来の微粉体充填用装置の説明図である。It is explanatory drawing of the conventional apparatus for fine powder filling.

符号の説明Explanation of symbols

1 微粉体供給管
2 微粉体圧送容器
3 微粉体供給調整バルブ
4 絞り部
5a 第一流動床
5b 第一空気ヘッダ
6 気体配管
7 気体の導入・吸引バルブ
8 フィルタ
9 吐出管
10 気体導入管
11a 開閉バルブ
11b 開閉バルブ
12 気体配管
13 圧抜きバルブ
14 フィルタ
15 微粉体投入口
16 気体導入管
17a 第二流動床
17b 第二空気ヘッダ
18 気体導入管
19 気体圧力調整弁
19a 第一気体圧力調整弁
19b 第二気体圧力調整弁
20 流量計
21 振動篩
22 スプリング
23 少容量容器
DESCRIPTION OF SYMBOLS 1 Fine powder supply pipe 2 Fine powder pumping container 3 Fine powder supply adjustment valve 4 Restriction part 5a First fluidized bed 5b First air header 6 Gas pipe 7 Gas introduction / suction valve 8 Filter 9 Discharge pipe 10 Gas introduction pipe 11a Opening and closing Valve 11b Open / close valve 12 Gas pipe 13 Pressure release valve 14 Filter 15 Fine powder inlet 16 Gas introduction pipe 17a Second fluidized bed 17b Second air header 18 Gas introduction pipe 19 Gas pressure adjustment valve 19a First gas pressure adjustment valve 19b First Two gas pressure control valve 20 Flow meter 21 Vibrating sieve 22 Spring 23 Small capacity container

Claims (13)

微粉体を密閉して収納する密閉収納装置と、該収納装置に気体を導入して微粉体を流動化させる微粉体の流動化手段と、該密閉収納装置から流動化された微粉体を吐出させて微粉体充填用容器に充填する充填手段とを少なくとも有する微粉体の充填用装置であって、該密閉収納装置が上部の微粉体供給管と下部の微粉体圧送容器とを有し、該微粉体供給管の微粉体投入口に微粉体の密閉手段が設けられ、該微粉体圧送容器に前記微粉体の流動化手段と、気体による加圧手段と微粉体の吐出管からなる前記微粉体の充填手段と、圧力調整手段とが設けられていることを特徴とする微粉体充填用装置。   A hermetically sealed storage device for storing fine powder in a sealed manner, a fluidizing means for fluidizing the fine powder by introducing gas into the storage device, and discharging the fluidized fine powder from the sealed storage device. A fine powder filling apparatus having at least a filling means for filling the fine powder filling container, wherein the hermetic storage device has an upper fine powder supply pipe and a lower fine powder pressure feed container, A fine powder sealing means is provided at the fine powder inlet of the body supply pipe, and the fine powder fluidization means, a gas pressure means, and a fine powder discharge pipe are provided in the fine powder feed container. An apparatus for filling fine powder, characterized in that filling means and pressure adjusting means are provided. 該微粉体圧送容器の容量が、該微粉体供給管の容量に対して1.5倍以上であることを特徴とする請求項1に記載の微粉体充填用装置。   2. The apparatus for filling fine powder according to claim 1, wherein the capacity of the fine powder feeding container is 1.5 times or more the capacity of the fine powder supply pipe. 該微粉体の密閉手段が、微粉体供給調整バルブであることを特徴とする請求項1又は2に記載の微粉体充填用装置。   The fine powder filling apparatus according to claim 1 or 2, wherein the fine powder sealing means is a fine powder supply adjusting valve. 該微粉体の密閉手段が、微粉体投入口への配管と該配管にフィルタを介して設けられた気体の導入・吸引バルブとからなることを特徴とする請求項1又は2に記載の微粉体充填用装置。   3. The fine powder according to claim 1, wherein the fine powder sealing means comprises a pipe to the fine powder inlet and a gas introduction / suction valve provided in the pipe via a filter. Filling device. 該微粉体圧送容器の上部に絞り部が設けられ、該絞り部を含む微粉体圧送容器に微粉体の第一の流動化手段が設けられていることを特徴とする請求項1〜4のいずれかに記載の微粉体充填用装置。   The throttle part is provided in the upper part of this fine powder pumping container, The 1st fluidization means of fine powder is provided in the fine powder pumping container containing this throttle part, The any one of Claims 1-4 characterized by the above-mentioned. A device for filling fine powder according to claim 1. 該絞り部の頂角が6〜70度であることを特徴とする請求項5に記載の微粉体充填用装置。   6. The fine powder filling apparatus according to claim 5, wherein the apex angle of the narrowed portion is 6 to 70 degrees. 該第一の流動化手段が、微粉体圧送容器の絞り部を含む部分に設けられた第一流動床と第一空気ヘッダと、該第一空気ヘッダへの気体配管とを有し、該気体配管にフィルタを介して気体の導入・吸引バルブが設けられていることを特徴とする請求項5又は6に記載の微粉体充填用装置。   The first fluidizing means has a first fluidized bed, a first air header, and a gas pipe to the first air header provided in a portion including the throttle portion of the fine powder pressure feeding container. The apparatus for filling fine powder according to claim 5 or 6, wherein a gas introduction / suction valve is provided in the pipe via a filter. 該流動化手段が、微粉体圧送容器の底部に設けられた第二流動床と、第二流動床の下に設けられた第二空気ヘッダと、該第二空気ヘッダへの気体導入管と、該気体導入管に設けられた気体圧力調整弁とからなる第二の流動化手段であることを特徴とする請求項1〜7のいずれかに記載の微粉体充填用装置。   The fluidizing means includes a second fluidized bed provided at the bottom of the fine powder pressure feeding container, a second air header provided under the second fluidized bed, a gas introduction pipe to the second air header, The apparatus for filling fine powder according to any one of claims 1 to 7, which is a second fluidizing means comprising a gas pressure adjusting valve provided in the gas introduction pipe. 該気体による加圧手段が、微粉体圧送容器への気体導入管と、該気体導入管に設けられている開閉バルブであることをことを特徴とする請求項1〜8のいずれかに記載の微粉体充填用装置。   9. The gas pressurizing means is a gas introduction pipe to a fine powder pressure feeding container and an open / close valve provided in the gas introduction pipe. Equipment for fine powder filling. 該粉体吐出管の入り口が気体導入管の出口より下方に設けられていることを特徴とする請求項1〜9のいずれかに記載の微粉体充填用装置。   The apparatus for filling fine powder according to any one of claims 1 to 9, wherein an inlet of the powder discharge pipe is provided below an outlet of the gas introduction pipe. 該圧力調整手段が、気体放出管と、該気体放出管に設けられたフィルタと圧抜きバルブと気体配管とからなり、該気体配管に開閉バルブが設けられていることを特徴とする請求項1〜10のいずれかに記載の微粉体充填用装置。   2. The pressure adjusting means comprises a gas discharge pipe, a filter provided in the gas discharge pipe, a pressure release valve, and a gas pipe, and an open / close valve is provided in the gas pipe. The apparatus for fine powder filling in any one of -10. 該微粉体供給管と微粉体圧送容器との間に振動篩が設けられていることを特徴とする請求項1〜11のいずれかに記載の微粉体充填用装置。   The apparatus for filling fine powder according to any one of claims 1 to 11, wherein a vibrating sieve is provided between the fine powder supply pipe and the fine powder pumping container. 装置各部が、フェルール製の簡易配管締結具で密閉連結されていることを特徴とする請求項1〜12のいずれかに記載の微粉体充填用装置。   The apparatus for filling fine powder according to any one of claims 1 to 12, wherein each part of the apparatus is hermetically connected by a simple pipe fastener made of ferrule.
JP2003305477A 2003-08-28 2003-08-28 Fine powder filling apparatus Pending JP2005075374A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007123169A1 (en) * 2006-04-20 2007-11-01 National Institute Of Advanced Industrial Science And Technology Process and apparatus for producing granular silicon
CN102582853A (en) * 2012-03-07 2012-07-18 中联重科股份有限公司 Material packaging machine
CN102778830A (en) * 2011-05-09 2012-11-14 株式会社理光 Fluid transferer, fluid filling apparatus and fluid transfer method
CN103293912A (en) * 2012-02-28 2013-09-11 株式会社理光 Powder filling system and powder filling method
CN103616809A (en) * 2013-11-29 2014-03-05 亿和精密工业(苏州)有限公司 Carbon powder filling machine

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007123169A1 (en) * 2006-04-20 2007-11-01 National Institute Of Advanced Industrial Science And Technology Process and apparatus for producing granular silicon
CN102778830A (en) * 2011-05-09 2012-11-14 株式会社理光 Fluid transferer, fluid filling apparatus and fluid transfer method
US8931524B2 (en) 2011-05-09 2015-01-13 Ricoh Company, Ltd. Fluid transferer, fluid filling apparatus and fluid transfer method
CN103293912A (en) * 2012-02-28 2013-09-11 株式会社理光 Powder filling system and powder filling method
CN102582853A (en) * 2012-03-07 2012-07-18 中联重科股份有限公司 Material packaging machine
CN103616809A (en) * 2013-11-29 2014-03-05 亿和精密工业(苏州)有限公司 Carbon powder filling machine

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