JP2004057843A - Classifier and production method of toner using the same - Google Patents

Classifier and production method of toner using the same Download PDF

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Publication number
JP2004057843A
JP2004057843A JP2002215584A JP2002215584A JP2004057843A JP 2004057843 A JP2004057843 A JP 2004057843A JP 2002215584 A JP2002215584 A JP 2002215584A JP 2002215584 A JP2002215584 A JP 2002215584A JP 2004057843 A JP2004057843 A JP 2004057843A
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Japan
Prior art keywords
classification
powder
classifier
ring
powder material
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JP2002215584A
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Japanese (ja)
Inventor
Tetsuya Tanaka
田中 哲也
Nobuyasu Makino
牧野 信康
Hideyuki Santo
山東 秀行
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Ricoh Co Ltd
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Ricoh Co Ltd
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Application filed by Ricoh Co Ltd filed Critical Ricoh Co Ltd
Priority to JP2002215584A priority Critical patent/JP2004057843A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a classifier which enhances the efficiency of dispersion in its dispersion chamber, highly efficiently separates particles in the range of required sizes and enhances the recovery of a product, and to provide a production method using the classifier. <P>SOLUTION: A deposition prevention means 11 having a rugged shape is disposed on the upper part of a conical member 7 and a ring-like member 12 is disposed on the lower part of the conical member 7. The ring-like member 12 can be disposed in a plurality of number and the thickness and diameter can be changed in accordance with classification conditions. A deposition preventing means 11 and the ring-like member 12 are attachable and detachable with respect to the conical member 7. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、電子写真、静電記録、静電印刷などにおける、静電荷像を現像するための乾式トナーの製造に用いる分級装置に関するものであって、所望の粒径を得るために粒子の篩い分けを行う分級装置およびこれを用いるトナーの製造方法に関するものである。
【0002】
【従来の技術】
従来、ミクロンオーダーの粉体材料を粗粉と微粉に分離させるための分級装置は、円筒形状の分散室と分級室によって構成されている。分散室と分級室との間には円錐状部材が設けられ、分散室の上部外側表面一端の口から粉体材料を供給し、当該分散室内部に形成された旋回流によって分散作用を受け、さらに当該分級室へと導かれ遠心分離によって、微粉排出口又は粗粉排出口へと排出され、粉体材料が粗粉と微粉に分離される。
【0003】
図8は従来の分級装置の構成を示す断面図である。図8に示す分級装置は、1次搬送空気である流入エアーと粉体材料が供給される供給管1と、エアーと共に超微粉が排出される排気管2と、分散室3と、分散室3に送り込まれる2次搬送空気であるエアー流入口4と、エアーと共に微粉が排出される微粉排出口5と、エアーと共に粗粉を排出する粗粉排出口6と、分散室3の下部に設けられ、分散室3内の旋回流場を増長させる円錐状部材7と、その下部に設けられた分級板8と、円錐状部材7と分級板8により区画される分級室9とを含んで構成されている。なお、分級装置本体全体は略円筒状の筐体からなる。
【0004】
次に、図8に示す従来の分級装置の動作について説明する。
先ず、供給管1およびエアー流入口4からエアーが供給され、同時に排気管2、微粉排出口5および粗粉排出口6からエアーが排出されることにより、分散室3および分級室9の各内部には旋回流場が形成される。そこに、供給管1より粉体材料がエアーと共に供給され、分散室3の内部に導かれ、エアーの旋回流場による遠心分離作用を受けながら、粉体材料は回転しながら落下していく。この時、粉体材料の中でも非常に小さい粒径の超微粉は分散室3の中心方向に導かれ、吸引ファン等による吸引器(図示せず)と連通する排気管2より排出されることとなる。分散室3内で回転しながら落下した粉体材料は環状の間隙Aを通過して分級室9に導かれ、ここでも遠心分離作用を受けることにより、粉体材料の中でも大きい粗粉は遠心力によって分級室9の中心から遠ざかり、分級板8と分級室9の各内壁面との環状の間隙Bを通過して吸引ファン等による吸引器(図示せず)と連通する粗粉排出口6より排出される。一方、微粉は向心力によって分級室9の中心へと導かれ、吸引ファン等による吸引器(図示せず)と連通する微粉排出口5より排出される。
【0005】
【発明が解決しようとする課題】
しかしながら、前記のような従来の分級装置においては、分級装置を連続的に運転させた場合、分散室と分級室の間に設けられた円錐状部材の上部表面に、供給された粉体材料が堆積する場合がある。これは供給する粉体材料に対する製品の回収率を低下させる原因の一つとなっている。さらに、円錐状部材の上部表面に粉体材料が堆積することによって、分散室の気流が乱れたり、分散室と分級室との隙間を狭くしてしまう場合があり、これによって分級精度が低下してしまうという不具合も発生する。
また、分級装置の分級室内部には分布を持った流れが形成されており、特に円錐状部材下部壁面付近は他の場所に比べて速度が速くなっているため、粗粉回収側へと回収されるべき粉体材料が、分級装置中心部の微粉回収側へと導かれ、分級精度を低下してしまうという不具合もあった。
【0006】
なお、本発明者らは、これらの不具合を解決するために、特開平2000−218236号公報等に、円錐状部材上に段差を設けるなどした技術を開示している。
【0007】
本発明はこれらの不具合を解決するためのものであり、分級装置の分散室内での分散効率向上を達成し、必要とする大きさの範囲の粒子を高効率で分離し、製品の回収率を向上した分級装置およびこれを用いるトナーの製造方法を提供することを目的とする。
【0008】
【課題を解決するための手段】
上記課題を解決するために、請求項1に記載の本発明は、粉体材料を分散する分散室と、分散室の下方に連続して設けられて分散室から流入する粉体材料を遠心分級する分級室と、分散室と分級室とを区画する円錐状部材と、分級室を区画する分級板とを有し、分散室上部に設けられた粉体材料供給口から搬送空気と共に供給される粉体材料を、分散室内部の旋回流によって超微粉と微粉とに分級して超微粉を排出し、分級室へと導かれた粉体材料を遠心分離によって粗粉と微粉とに分級して粗粉を排出する分級装置において、前記分級装置は、円錐状部材上部に堆積防止手段を備えることを特徴とする分級装置である。
請求項2に記載の本発明は、前記堆積防止手段は、上部に凹凸形状を有することを特徴とする請求項1記載の分級装置である。
請求項3に記載の本発明は、前記堆積防止手段は、円錐状部材に対して着脱可能であることを特徴とする請求項1又は2記載の分級装置である。
【0009】
請求項4に記載の本発明は、前記分級装置は、円錐状部材下部にリング状部材を備えることを特徴とする請求項1ないし3のいずれかに記載の分級装置である。
請求項5に記載の本発明は、前記リング状部材は、複数設けられることを特徴とする請求項4記載の分級装置である。
請求項6に記載の本発明は、前記リング状部材は、厚みおよび直径を分級条件に応じて可変することを特徴とする請求項4又は5に記載の分級装置である。
請求項7に記載の本発明は、前記リング状部材は、円錐状部材に対して着脱可能であることを特徴とする請求項4ないし6のいずれかに記載の分級装置である。
【0010】
請求項8に記載の本発明は、電子写真方式の画像形成装置に使用するトナーの製造方法において、粉体材料を粉砕化した後に、請求項1ないし7のいずれかに記載の分級装置で分級してトナーを製造することを特徴とするトナーの製造方法である。
【0011】
【発明の実施の形態】
以下より、本発明の実施の形態について図に基づき説明する。
本発明の分級装置は、分散室の上部に設けられた粉体材料供給口から供給された粉体材料は分散室内部に形成された旋回流によって旋回分散作用を受けて超微粉を排出し、更に分級室へと導かれて遠心分離によって粉体材料を粗粉と微粉に分級する。そして、分散室に設けられた堆積防止手段は、円錐状部材上部の速度分布を変化させ、粉体材料が円錐状部材上部に堆積しにくくすることができるため、分散室での分散効率を向上することができる。
【0012】
図1は本発明の一実施形態に係る分級装置の構成を示す断面図である。本発明の分級装置は、円錐状部材7の上部に堆積防止手段11を有し、下部にリング状部材12を有している。図1に示すように、この堆積防止手段11は円錐状部材7の上部にて、分散室3の内部に形成されている旋回流によって回転するように設置されている。このように設定されることで、分散室3に供給された粉体材料が分散室3を旋回しながら下降して分級室9へと導かれる際に、分散室3の内部において堆積防止手段11により粉体材料が円錐状部材7の上部に堆積することを防止する。つまり、この堆積防止手段11が設けられたことにより、堆積防止手段11が回転し、円錐状部材7上部の速度分布が変化し、回転方向の流れが強くなり、円錐状部材7上部に粉体材料が堆積しにくくなる。よって、分散室3での分散効率が向上し、精度の良い分級が可能となる。
【0013】
図2は堆積防止手段11の平面図であり、図3は円錐状部材7の側面断面図である。
堆積防止手段11は、脱着機構13により円錐状部材7に対して脱着可能となっている。これにより、粉体材料の処理量、平均粒径等の条件変更に対して容易に対応でき、切り替え時間の短縮化も図ることができる。堆積防止手段11は、特にその形状を問わないが、凹凸部10は旋回方向の流れを受け、堆積防止手段11が回転するような羽根形状が好ましい。
また、円錐状部材7下部壁面付近は他の場所に比べて速度が速くなっているため、図3に示すように、円錐状部材7の下部にリング状部材12を設けることにより、円錐状部材7下部壁面に沿う流れを変化させて、粗粉回収側へと回収されるべき粉体材料が微粉回収側へと導かれ分級精度を低下させる作用を防止する。なお、リング状部材12は、特にその形状を問わないが、特に真円形状のものが好ましい。
【0014】
また、図4に示すように、リング状部材12を複数設けることにより、壁面に沿う流れが更に変化し、粗粉回収側に導かれるべき粒径を持つ粉体材料が微粉回収側に導かれる作用をより一層防ぐことができる。
【0015】
図5は、分級室9に対するリング状部材12の高さhを示す図である。図5に示すように、リング状部材12の高さhを分級室9の高さHの1/2以下が好ましい。これは、リング状部材12の高さhが高すぎると、分級室9内部の流れが大きく変化し、粉体材料の回収率が低下する等の問題が発生するので、これを防止するためである。なお、リング状部材12の高さhは分級条件に応じて可変できるものである。
【0016】
図6は、円錐状部材7に対するリング状部材12の構成を示す図である。図6に示すように、リング状部材12の厚みdを円錐状部材7の下部半径aの30%以下が好ましい。これは、リング状部材12の厚みが厚すぎると、高さの条件と同様に、分級室9内部の流れが大きく変化し、粉体材料の回収率が低下する等の問題が発生するので、これを防止するためである。なお、リング状部材12の厚みdは分級条件に応じて可変できるものである。
また、リング状部材12の直径bを、円錐状部材7の下部凸部の直径c以上が好ましい。これは、円錐状部材7の下部凸部の直径c以下に設定しても、壁面に沿う流れは大きく変化せず、その結果、粉体材料の動きもほとんど変わらないため、粗粉回収側に導かれるべき粒径を持つ粉体材料が、微粉回収側に導かれる作用を防ぐような効果が得られないからである。
【0017】
また、図中矢印eに示すように、リング状部材12の上部外側および/又は内側を曲面形状部とすることが好ましい。これは、円錐状部材7の下部にリング状部材12を設けた取り付け部分に流れが淀みやすくなり、連続運転をする場合粉体材料が堆積しやすくなり、回収率が低下し、清掃性が悪くなる等の不具合を防止するためである。
【0018】
更に、図7に示すリング状部材12を脱着機構14、例えばネジ止めなどによって円錐状部材7に取り付けることによって、取り付けが容易となり、リング状部材12の切り替え作業の短縮化を図ることができ、高さ・幅調整等も容易となる。
【0019】
更に、上述した分級装置を用いてトナーを分級して製造することにより、得られるトナーの分級精度が向上し、トナーの高品質化を図ることができる。
【0020】
【実施例】
次に、本実施形態の実施例による具体例を説明する。なお、本発明は下記実施例に限定されるものではなく、特許請求の範囲内の記載であれば多種の変形や置換可能であることは言うまでもない。
スチレン−アクリル共重合体樹脂85重量部とカーボンブラック15重量部の混合物を溶融混練、冷却し、これをハンマーミルで粗粉砕した後、ジェットミルにて微粉砕された粉体材料を、以下に示す構成の分級装置によって分級を行った。
【0021】
分級精度試験
(実施例1)
円錐状状部材の上部に堆積防止手段を設置した分級装置に、上記組成の粉体材料を供給し、排気ブロワー圧15.9kPa(1620mmAq)、堆積防止手段の凸部羽根を8枚に設定し、体積平均粒径7.5μm(コールターカウンタによる測定)の粉体を回収できるように分級を実施したところ、フィード量10.5kg/hに対して、体積平均粒径7.30μm、4μm以下の微粉含有率(重量%)6.61%、12.7μm以上の粗粉含有率(重量%)2.05%であり、シャープな粒度分布が得られた。
【0022】
(実施例2)
円錐状部材の下部にリング状部材を設けた分級装置に、上記組成の粉体材料を供給し、排気ブロワー圧15.9kPa(1620mmAq)、リング状部材の高さhを分級室高さHの約1/20、リング状部材の厚みdを1.5mm、直径bを170mmに設定し、他は実施例1と同条件で処理した。その結果、フィード量10.5kg/hに対して、体積平均粒径7.50μm、4μm以下の微粉含有率(重量%)4.50%、12.7μm以上の粗粉含有率(重量%)2.52%であり、シャープな粒度分布が得られた。
【0023】
(実施例3)
円錐状部材の下部にリング状部材を2つ設けた分級装置に、上記組成の粉体材料を供給し、リング状部材の直径bを170mmと150mmとして、他は実施例1と同条件で処理した。その結果、フィード量10.5kg/hに対して、体積平均粒径7.55μm、4μm以下の微粉含有率(重量%)4.07、12.7μm以上の粗粉含有率(重量%)2.60%であり、シャープな粒度分布が得られた。
【0024】
(比較例)
上記組成の粉体材料を供給して、図8に示す構成の従来の分級装置を用い、排気ブロワー圧15.9kPa(1620mmAq)に設定し、体積平均粒径7.5μm(コールターカウンタによる測定)の粉体を回収できるように分級を実施した。その結果、フィード量10.5kg/hに対して、体積平均粒径7.15μm、4μm以下の微粉含有率(重量%)10.87%、12.7μm以上の粗粉含有率(重量%)1.30%であり、実施例1〜3に比べてシャープな粒度分布が得られなかった。
【0025】
リング状部材の形状による清掃性
 円錐状部材の下部にリング状部材を設けた分級装置に、上記組成の粉体材料を供給し、リング状部材の上部外側を曲面形状として、他は実施例1と同条件で処理した。その結果、円錐状部材下部取り付け部分の粉体材料の堆積が減少し、清掃性も改善された。
【0026】
円錐状部材の下部にリング状部材を設けた分級装置に、上記組成の粉体材料を供給し、リング状部材の上部内側を曲面形状として、他は実施例1と同条件で処理した。その結果、円錐状部材下部取り付け部分の粉体材料の堆積が減少し、清掃性も改善された。
【0027】
部材脱着による清掃性
 円錐状状部材の上部に堆積防止手段を設置した分級装置に、上記組成の粉体材料を供給し、堆積防止手段11を脱着可能として、他は実施例1と同条件で処理した後、清掃切替を実施した。その結果、清掃切替時間について、実施例1に比べ約10%の短縮が可能となった。
【0028】
円錐状部材の下部にリング状部材を設けた分級装置に、上記組成の粉体材料を供給し、リング状部材12を脱着可能として、他は実施例1と同条件で処理した後、清掃切替を実施した。その結果、清掃切替時間について、実施例1に比べ約15%の短縮が可能となった。
【0029】
【発明の効果】
以上説明したように、本発明によれば、円錐状部材上部に、旋回流によって回転する堆積防止手段を設けることで、円錐状部材上部に粉体材料が堆積するのを防止することができ、分級精度を向上した分級装置を提供することができる。
更に、円錐状部材の下部にリング状部材を設けることにより、円錐状部材の下部における流れを変化させ、良好な分級性を向上した分級装置を提供することができる。
更に、リング状部材の厚みや直径を分級条件に応じて可変することにより、分級条件に柔軟に対応可能な分級装置を提供することができる。
更に、堆積防止手段とリング状部材とを着脱可能とすることで、粉体材料の処理量、平均粒径等の条件変更に対して容易に対応でき、清掃性を向上し、切り替え時間の短縮化も可能な分級装置を提供することができる。
更に、上記分級装置をトナーの製造に用いることで、粒度分布がシャープで高品質なトナーを得ることが可能なトナー製造方法を提供することができる。
【図面の簡単な説明】
【図1】本発明の一実施形態に係る分級装置の構成を示す断面図である。
【図2】堆積防止手段の平面図である。
【図3】円錐状部材の構成を示す側面断面図である。
【図4】複数のリング状部材の構成を示す側面断面図である。
【図5】分級室9に対するリング状部材の高さhを示す図である。
【図6】円錐状部材に対するリング状部材の構成を示す図である。
【図7】リング状部材の取り付け部分を示す部分断面図である。
【図8】従来の分級装置の構成を示す断面図である。
【図9】従来の分級装置における円錐状部材の構成を示す断面図である。
【符号の説明】
1 供給管
2 排気管
3 分散室
4 エアー流入口
5 微粉排出口
6 粗粉排出口
7 円錐状部材
8 分級板
9 分級室
10 凸部(凹部)
11 堆積防止手段
12 リング状部材
13、14 脱着機構
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a classifier used for producing a dry toner for developing an electrostatic image in electrophotography, electrostatic recording, electrostatic printing, and the like, and relates to a particle sieve for obtaining a desired particle size. The present invention relates to a classification device for performing classification and a method for producing a toner using the classification device.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, a classifier for separating a micron-order powder material into a coarse powder and a fine powder includes a cylindrical dispersion chamber and a classification chamber. A conical member is provided between the dispersion chamber and the classifying chamber, and the powder material is supplied from an opening at one end of the upper outer surface of the dispersion chamber, and is subjected to a dispersion action by a swirling flow formed inside the dispersion chamber. Further, the powder is guided to the classifying chamber and discharged to a fine powder discharge port or a coarse powder discharge port by centrifugal separation, whereby the powder material is separated into coarse powder and fine powder.
[0003]
FIG. 8 is a cross-sectional view showing a configuration of a conventional classification device. The classifier shown in FIG. 8 includes a supply pipe 1 through which inflow air as primary transport air and a powder material are supplied, an exhaust pipe 2 through which ultrafine powder is discharged together with air, a dispersion chamber 3, and a dispersion chamber 3. An air inlet 4, which is a secondary conveying air fed to the air, a fine powder outlet 5 for discharging fine powder with air, a coarse powder outlet 6 for discharging coarse powder with air, and a lower portion of the dispersion chamber 3. A conical member 7 for increasing the swirling flow field in the dispersion chamber 3, a classifying plate 8 provided below the conical member 7, and a classifying chamber 9 defined by the conical member 7 and the classifying plate 8. ing. In addition, the whole classification apparatus main body consists of a substantially cylindrical housing.
[0004]
Next, the operation of the conventional classifier shown in FIG. 8 will be described.
First, air is supplied from the supply pipe 1 and the air inlet 4, and at the same time, air is discharged from the exhaust pipe 2, the fine powder discharge port 5, and the coarse powder discharge port 6. , A swirling flow field is formed. There, the powder material is supplied together with air from the supply pipe 1, guided into the dispersion chamber 3, and falls while rotating while undergoing centrifugal action by the swirling flow field of air. At this time, the ultrafine powder having a very small particle size among the powder materials is guided toward the center of the dispersion chamber 3 and discharged from the exhaust pipe 2 communicating with a suction device (not shown) such as a suction fan. Become. The powder material that has fallen while rotating in the dispersion chamber 3 passes through the annular gap A and is guided to the classification chamber 9, where the powder material is also subjected to the centrifugal separation operation. From the center of the classifying chamber 9, passing through the annular gap B between the classifying plate 8 and each inner wall surface of the classifying chamber 9, from the coarse powder discharge port 6 communicating with a suction device (not shown) such as a suction fan or the like. Is discharged. On the other hand, the fine powder is guided to the center of the classification chamber 9 by centripetal force, and is discharged from the fine powder discharge port 5 communicating with a suction device (not shown) such as a suction fan.
[0005]
[Problems to be solved by the invention]
However, in the conventional classifier as described above, when the classifier is operated continuously, the supplied powder material is supplied to the upper surface of the conical member provided between the dispersion chamber and the classifier. May accumulate. This is one of the causes for lowering the product recovery rate for the supplied powder material. Further, the accumulation of the powder material on the upper surface of the conical member may disturb the airflow in the dispersion chamber or narrow the gap between the dispersion chamber and the classification chamber, thereby lowering the classification accuracy. There is also a problem that this will happen.
In addition, a flow with distribution is formed inside the classification chamber of the classification device, and the speed is particularly high near the lower wall surface of the conical member compared to other places, so it is collected to the coarse powder collection side. There is also a problem that the powder material to be performed is guided to the fine powder collecting side in the center of the classification device, and the classification accuracy is reduced.
[0006]
In order to solve these problems, the present inventors disclose a technique in which a step is provided on a conical member, for example, in Japanese Patent Application Laid-Open No. 2000-218236.
[0007]
The present invention is intended to solve these problems, and achieves improved dispersion efficiency in the dispersion chamber of the classifier, separates particles in a required size range with high efficiency, and improves the product recovery rate. An object of the present invention is to provide an improved classifier and a method for producing a toner using the same.
[0008]
[Means for Solving the Problems]
In order to solve the above-mentioned problem, the present invention according to claim 1 provides a dispersion chamber for dispersing a powder material, and a powder material provided continuously below the dispersion chamber and flowing from the dispersion chamber by centrifugal classification. Classifying chamber, a conical member for dividing the classifying chamber and the classifying chamber, and a classifying plate for classifying the classifying chamber, and are supplied together with carrier air from a powder material supply port provided in the upper part of the classifying chamber. The powder material is classified into ultrafine powder and fine powder by the swirling flow inside the dispersion chamber, the ultrafine powder is discharged, and the powder material guided to the classification chamber is classified into coarse powder and fine powder by centrifugal separation. In a classifier for discharging coarse powder, the classifier is provided with a deposition preventing means above the conical member.
According to a second aspect of the present invention, there is provided the classification device according to the first aspect, wherein the accumulation preventing means has an uneven shape on an upper portion.
According to a third aspect of the present invention, there is provided the classification device according to the first or second aspect, wherein the accumulation preventing unit is detachable from the conical member.
[0009]
The present invention according to claim 4 is the classification device according to any one of claims 1 to 3, wherein the classification device includes a ring-shaped member below the conical member.
According to a fifth aspect of the present invention, there is provided the classification device according to the fourth aspect, wherein a plurality of the ring-shaped members are provided.
According to a sixth aspect of the present invention, there is provided the classification device according to the fourth or fifth aspect, wherein the ring-shaped member varies a thickness and a diameter according to a classification condition.
The present invention according to claim 7 is the classification device according to any one of claims 4 to 6, wherein the ring-shaped member is detachable from the conical member.
[0010]
According to an eighth aspect of the present invention, in the method for producing a toner used in an electrophotographic image forming apparatus, after the powder material is pulverized, the classification is performed by the classification apparatus according to any one of the first to seventh aspects. And a method for producing a toner.
[0011]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
The classifier of the present invention, the powder material supplied from the powder material supply port provided in the upper part of the dispersion chamber is subjected to a swirling dispersion action by a swirling flow formed inside the dispersion chamber to discharge ultrafine powder, Further, the powder material is guided to a classification room, and the powder material is classified into coarse powder and fine powder by centrifugal separation. The accumulation preventing means provided in the dispersion chamber can change the velocity distribution of the upper part of the conical member, thereby making it difficult for the powder material to accumulate on the upper part of the conical member, thereby improving the dispersion efficiency in the dispersion chamber. can do.
[0012]
FIG. 1 is a cross-sectional view illustrating a configuration of a classification device according to an embodiment of the present invention. The classifier according to the present invention has the accumulation preventing means 11 at the upper part of the conical member 7 and the ring-shaped member 12 at the lower part. As shown in FIG. 1, the accumulation preventing means 11 is installed above the conical member 7 so as to be rotated by a swirling flow formed inside the dispersion chamber 3. With this setting, when the powder material supplied to the dispersion chamber 3 descends while rotating in the dispersion chamber 3 and is guided to the classification chamber 9, the accumulation preventing means 11 is disposed inside the dispersion chamber 3. This prevents the powder material from being deposited on the upper part of the conical member 7. That is, the provision of the accumulation preventing means 11 causes the accumulation preventing means 11 to rotate, the velocity distribution in the upper part of the conical member 7 changes, the flow in the rotational direction becomes stronger, and the powder Material is less likely to deposit. Therefore, the dispersion efficiency in the dispersion chamber 3 is improved, and classification with high accuracy is possible.
[0013]
FIG. 2 is a plan view of the accumulation preventing means 11, and FIG. 3 is a side sectional view of the conical member 7.
The deposition preventing means 11 is detachable from the conical member 7 by a detachment mechanism 13. Accordingly, it is possible to easily cope with a change in conditions such as the processing amount of the powder material and the average particle diameter, and it is possible to shorten the switching time. Although the shape of the accumulation preventing means 11 is not particularly limited, a blade shape in which the unevenness portion 10 receives a flow in the turning direction and the accumulation preventing means 11 rotates is preferable.
In addition, since the speed near the lower wall surface of the conical member 7 is higher than that of other places, as shown in FIG. 3, by providing the ring-shaped member 12 below the conical member 7, (7) The flow along the lower wall surface is changed to prevent the powder material to be recovered to the coarse powder recovery side from being guided to the fine powder recovery side and to reduce the classification accuracy. The shape of the ring-shaped member 12 is not particularly limited, but is preferably a perfect circle.
[0014]
As shown in FIG. 4, by providing a plurality of ring-shaped members 12, the flow along the wall surface is further changed, and the powder material having a particle diameter to be guided to the coarse powder collection side is guided to the fine powder collection side. The effect can be further prevented.
[0015]
FIG. 5 is a diagram illustrating the height h of the ring-shaped member 12 with respect to the classification chamber 9. As shown in FIG. 5, the height h of the ring-shaped member 12 is preferably equal to or less than の of the height H of the classifying chamber 9. This is because if the height h of the ring-shaped member 12 is too high, the flow inside the classification chamber 9 changes greatly, and a problem such as a reduction in the recovery rate of the powder material occurs. is there. In addition, the height h of the ring-shaped member 12 can be changed according to classification conditions.
[0016]
FIG. 6 is a diagram showing a configuration of the ring-shaped member 12 with respect to the conical member 7. As shown in FIG. 6, the thickness d of the ring-shaped member 12 is preferably 30% or less of the lower radius a of the conical member 7. This is because if the thickness of the ring-shaped member 12 is too large, as in the case of the height condition, the flow inside the classification chamber 9 greatly changes, and a problem such as a reduction in the recovery rate of the powder material occurs. This is to prevent this. In addition, the thickness d of the ring-shaped member 12 can be changed according to classification conditions.
Further, the diameter b of the ring-shaped member 12 is preferably equal to or larger than the diameter c of the lower convex portion of the conical member 7. This is because, even if the diameter is set to be equal to or less than the diameter c of the lower convex portion of the conical member 7, the flow along the wall surface does not change significantly, and as a result, the movement of the powder material hardly changes. This is because a powder material having a particle diameter to be guided cannot obtain an effect of preventing an action guided to the fine powder recovery side.
[0017]
Further, as shown by an arrow e in the figure, it is preferable that the outer side and / or the inner side of the upper part of the ring-shaped member 12 is a curved part. This is because the flow tends to stagnate at the mounting portion where the ring-shaped member 12 is provided below the conical member 7, and the powder material is easily deposited in continuous operation, the recovery rate is reduced, and the cleaning property is poor. This is for preventing such troubles as becoming.
[0018]
Furthermore, by attaching the ring-shaped member 12 shown in FIG. 7 to the conical member 7 by the detachment mechanism 14, for example, screwing, the attachment becomes easy, and the switching work of the ring-shaped member 12 can be shortened. Adjustment of height and width becomes easy.
[0019]
Furthermore, by classifying and manufacturing the toner using the above-described classifier, the classification accuracy of the obtained toner is improved, and the quality of the toner can be improved.
[0020]
【Example】
Next, a specific example according to an example of the present embodiment will be described. It should be noted that the present invention is not limited to the following embodiments, and it goes without saying that various modifications and substitutions can be made within the scope of the claims.
A mixture of 85 parts by weight of a styrene-acrylic copolymer resin and 15 parts by weight of carbon black was melt-kneaded, cooled, coarsely ground with a hammer mill, and then finely ground with a jet mill. Classification was performed by a classification device having the configuration shown.
[0021]
Classification accuracy test (Example 1)
The powder material having the above composition is supplied to a classifier having a deposition preventing means provided above the conical member, the exhaust blower pressure is set to 15.9 kPa (1620 mmAq), and the number of the convex blades of the deposition preventing means is set to eight. The powder was classified so that a powder having a volume average particle diameter of 7.5 μm (measured by a Coulter counter) could be recovered, and the volume average particle diameter was 7.30 μm and 4 μm or less for a feed amount of 10.5 kg / h. The fine powder content (% by weight) was 6.61%, and the coarse powder content (% by weight) of 12.7 μm or more was 2.05%, and a sharp particle size distribution was obtained.
[0022]
(Example 2)
The powder material having the above composition is supplied to a classification device having a ring-shaped member provided below the conical member, the exhaust blower pressure is 15.9 kPa (1620 mmAq), and the height h of the ring-shaped member is set to the classification chamber height H. About 1/20, the thickness d of the ring-shaped member was set to 1.5 mm, and the diameter b was set to 170 mm. As a result, with respect to the feed amount of 10.5 kg / h, the content of fine powder having a volume average particle size of 7.50 μm and 4 μm or less (% by weight) 4.50%, and the content of coarse powder having a volume average particle size of 12.7 μm or more (% by weight) 2.52%, and a sharp particle size distribution was obtained.
[0023]
(Example 3)
The powder material having the above composition was supplied to a classifier having two ring members provided below the conical member, and the diameter b of the ring members was set to 170 mm and 150 mm, and the other conditions were the same as in Example 1. did. As a result, with respect to the feed amount of 10.5 kg / h, the content of fine powder having a volume average particle size of 7.55 μm and 4 μm or less (% by weight) 4.07, and the content of coarse powder having a content of 12.7 μm or more (% by weight) 2 .60%, and a sharp particle size distribution was obtained.
[0024]
(Comparative example)
The powder material having the above composition is supplied, the exhaust blower pressure is set to 15.9 kPa (1620 mmAq) using a conventional classifier having the configuration shown in FIG. 8, and the volume average particle size is 7.5 μm (measured by a Coulter counter). Classification was performed so that the powder of the above could be recovered. As a result, for a feed amount of 10.5 kg / h, the content of fine powder having a volume average particle size of 7.15 μm and 4 μm or less (% by weight) 10.87%, and the content of coarse powder having a volume average particle size of 12.7 μm or more (% by weight) 1.30%, and a sharper particle size distribution was not obtained as compared with Examples 1 to 3.
[0025]
Cleanability by the Shape of the Ring Member The powder material having the above composition was supplied to a classifier provided with a ring member below the conical member, and the upper outside of the ring member was formed into a curved surface. It processed on the same conditions as. As a result, the accumulation of the powder material in the lower attachment portion of the conical member was reduced, and the cleaning property was also improved.
[0026]
The powder material having the above composition was supplied to a classification device having a ring-shaped member provided below the conical member, and the inside of the upper portion of the ring-shaped member was formed into a curved surface. As a result, the accumulation of the powder material in the lower attachment portion of the conical member was reduced, and the cleaning property was also improved.
[0027]
The powder material having the above composition is supplied to a classifying apparatus in which the deposition preventing means is provided on the upper part of the conical member having a cleaning property by detaching the member, and the deposition preventing means 11 is detachable. After processing, a cleaning switch was performed. As a result, the cleaning switching time can be reduced by about 10% as compared with the first embodiment.
[0028]
The powdery material having the above composition is supplied to a classifier having a ring-shaped member provided below the conical member, and the ring-shaped member 12 is detachable. Was carried out. As a result, the cleaning switching time can be reduced by about 15% as compared with the first embodiment.
[0029]
【The invention's effect】
As described above, according to the present invention, it is possible to prevent the powder material from being deposited on the upper portion of the conical member by providing the upper portion of the conical member with the deposition prevention unit that rotates by the swirling flow, A classifier with improved classification accuracy can be provided.
Further, by providing the ring-shaped member below the conical member, the flow in the lower part of the conical member can be changed, and a classifier having improved classification can be provided.
Further, by varying the thickness and the diameter of the ring-shaped member according to the classification conditions, it is possible to provide a classification device that can flexibly respond to the classification conditions.
Further, by making the deposition preventing means and the ring-shaped member detachable, it is possible to easily cope with a change in conditions such as a processing amount of powder material, an average particle diameter, etc., thereby improving cleanability and reducing switching time. It is possible to provide a classifying device that can be used.
Further, by using the classifier for the production of a toner, it is possible to provide a toner production method capable of obtaining a high quality toner having a sharp particle size distribution.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view illustrating a configuration of a classification device according to an embodiment of the present invention.
FIG. 2 is a plan view of a deposition preventing unit.
FIG. 3 is a side sectional view showing a configuration of a conical member.
FIG. 4 is a side sectional view showing a configuration of a plurality of ring-shaped members.
FIG. 5 is a view showing a height h of a ring-shaped member with respect to a classifying chamber 9;
FIG. 6 is a diagram showing a configuration of a ring-shaped member with respect to a conical member.
FIG. 7 is a partial cross-sectional view showing a mounting portion of a ring-shaped member.
FIG. 8 is a cross-sectional view showing a configuration of a conventional classification device.
FIG. 9 is a cross-sectional view showing a configuration of a conical member in a conventional classifier.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Supply pipe 2 Exhaust pipe 3 Dispersion chamber 4 Air inflow port 5 Fine powder discharge port 6 Coarse powder discharge port 7 Conical member 8 Classification plate 9 Classification chamber 10 Convex part (recess)
DESCRIPTION OF SYMBOLS 11 Deposition prevention means 12 Ring-shaped members 13 and 14 Detachment mechanism

Claims (8)

粉体材料を分散する分散室と、分散室の下方に連続して設けられて分散室から流入する粉体材料を遠心分級する分級室と、分散室と分級室とを区画する円錐状部材と、分級室を区画する分級板とを有し、
分散室上部に設けられた粉体材料供給口から搬送空気と共に供給される粉体材料を、分散室内部の旋回流によって超微粉と微粉とに分級して超微粉を排出し、分級室へと導かれた粉体材料を遠心分離によって粗粉と微粉とに分級して粗粉を排出する分級装置において、
前記分級装置は、円錐状部材上部に堆積防止手段を備える
ことを特徴とする分級装置。
A dispersion chamber for dispersing the powder material, a classification chamber that is provided continuously below the dispersion chamber and classifies the powder material flowing from the dispersion chamber by centrifugal classification, and a conical member that partitions the dispersion chamber and the classification chamber. , Having a classification plate for partitioning the classification room,
The powder material supplied along with the carrier air from the powder material supply port provided in the upper part of the dispersion chamber is classified into ultrafine powder and fine powder by the swirling flow inside the dispersion chamber, and the ultrafine powder is discharged. In a classifier that classifies the guided powder material into coarse powder and fine powder by centrifugation and discharges the coarse powder,
The classifier is characterized in that the classifier is provided with a deposition preventing means above the conical member.
前記堆積防止手段は、上部に凹凸形状を有する
ことを特徴とする請求項1記載の分級装置。
2. The classification device according to claim 1, wherein the accumulation preventing means has an uneven shape on an upper part.
前記堆積防止手段は、円錐状部材に対して着脱可能である
ことを特徴とする請求項1又は2記載の分級装置。
The classification device according to claim 1, wherein the accumulation preventing unit is detachable from the conical member.
前記分級装置は、円錐状部材下部にリング状部材を備える
ことを特徴とする請求項1ないし3のいずれかに記載の分級装置。
The classification device according to any one of claims 1 to 3, wherein the classification device includes a ring-shaped member below the conical member.
前記リング状部材は、複数設けられる
ことを特徴とする請求項4記載の分級装置。
The classifier according to claim 4, wherein a plurality of the ring-shaped members are provided.
前記リング状部材は、厚みおよび直径を分級条件に応じて可変する
ことを特徴とする請求項4又は5に記載の分級装置。
The classifier according to claim 4, wherein the ring-shaped member has a thickness and a diameter that are variable according to a classification condition.
前記リング状部材は、円錐状部材に対して着脱可能である
ことを特徴とする請求項4ないし6のいずれかに記載の分級装置。
The classifier according to any one of claims 4 to 6, wherein the ring-shaped member is detachable from the conical member.
電子写真方式の画像形成装置に使用するトナーの製造方法において、
粉体材料を粉砕化した後に、請求項1ないし7のいずれかに記載の分級装置で分級してトナーを製造する
ことを特徴とするトナーの製造方法。
In a method for producing a toner used in an electrophotographic image forming apparatus,
A method for producing a toner, comprising: pulverizing a powder material; and then classifying the powder material with the classifier according to claim 1 to produce a toner.
JP2002215584A 2002-07-24 2002-07-24 Classifier and production method of toner using the same Pending JP2004057843A (en)

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006289349A (en) * 2005-03-14 2006-10-26 Ricoh Co Ltd Air current type classifier, vibrating device
US8404425B2 (en) 2009-01-07 2013-03-26 Ricoh Company, Limited Apparatus and method for manufacturing toner
KR20150027525A (en) * 2013-09-04 2015-03-12 삼성전기주식회사 Centrifugal classifier
KR101576989B1 (en) * 2014-04-25 2015-12-14 대한민국 mixture particle separating system
CN105300108A (en) * 2015-10-22 2016-02-03 桐乡市耀润电子有限公司 Blanking equipment used for feeding ferrite spherical particle raw materials into pre-sintering kiln
CN105300107A (en) * 2015-10-22 2016-02-03 桐乡市耀润电子有限公司 Blanking device used for feeding ferrite spherical particle raw materials into pre-sintering kiln
CN105333737A (en) * 2015-10-22 2016-02-17 桐乡市耀润电子有限公司 Discharging device used before ferrite spherical particle raw materials enter presintering kiln
CN108465637A (en) * 2018-02-09 2018-08-31 赵云红 A kind of centrifugal soil screening plant of soil remediation

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006289349A (en) * 2005-03-14 2006-10-26 Ricoh Co Ltd Air current type classifier, vibrating device
US8404425B2 (en) 2009-01-07 2013-03-26 Ricoh Company, Limited Apparatus and method for manufacturing toner
KR20150027525A (en) * 2013-09-04 2015-03-12 삼성전기주식회사 Centrifugal classifier
KR102057912B1 (en) 2013-09-04 2019-12-20 삼성전기주식회사 Centrifugal classifier
KR101576989B1 (en) * 2014-04-25 2015-12-14 대한민국 mixture particle separating system
CN105300108A (en) * 2015-10-22 2016-02-03 桐乡市耀润电子有限公司 Blanking equipment used for feeding ferrite spherical particle raw materials into pre-sintering kiln
CN105300107A (en) * 2015-10-22 2016-02-03 桐乡市耀润电子有限公司 Blanking device used for feeding ferrite spherical particle raw materials into pre-sintering kiln
CN105333737A (en) * 2015-10-22 2016-02-17 桐乡市耀润电子有限公司 Discharging device used before ferrite spherical particle raw materials enter presintering kiln
CN105300107B (en) * 2015-10-22 2017-07-21 桐乡市耀润电子有限公司 Enter the doffer of pre- firing for ferrite ball type particulate material
CN105300108B (en) * 2015-10-22 2017-07-21 桐乡市耀润电子有限公司 Enter the blanking device of pre- firing for ferrite ball type particulate material
CN108465637A (en) * 2018-02-09 2018-08-31 赵云红 A kind of centrifugal soil screening plant of soil remediation

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