JP2000254589A - Classifier and production of toner using it - Google Patents

Classifier and production of toner using it

Info

Publication number
JP2000254589A
JP2000254589A JP6331099A JP6331099A JP2000254589A JP 2000254589 A JP2000254589 A JP 2000254589A JP 6331099 A JP6331099 A JP 6331099A JP 6331099 A JP6331099 A JP 6331099A JP 2000254589 A JP2000254589 A JP 2000254589A
Authority
JP
Japan
Prior art keywords
coarse powder
guide member
classification
solid substance
fine powder
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
JP6331099A
Other languages
Japanese (ja)
Other versions
JP3632098B2 (en
Inventor
Tetsuya Tanaka
哲也 田中
Yoshihiro Saito
芳浩 斎藤
Kazuyoshi Morii
和好 森井
Eisuke Sugisawa
英輔 杉沢
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 JP6331099A priority Critical patent/JP3632098B2/en
Publication of JP2000254589A publication Critical patent/JP2000254589A/en
Application granted granted Critical
Publication of JP3632098B2 publication Critical patent/JP3632098B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a classifier which recovers solids of at least a desired particle size to a fine powder recovery side, or solids of a desired particle size or below to a coarse powder recovery side and is small in classification errors and high in classification precision and a method for producing toner using the classifier. SOLUTION: An apparatus is composed of a solid supply means 1 for supplying solids, a classification chamber 4 formed from a guide member 2 in a main body 0a and a classification member 3 arranged below the guide member 2, a fine powder discharging means 5 for discharging fine powder from a middle part in the fine powder recovery direction for recovering the fine powder of the solids by a revolving flow formed in the classification chamber 4, a coarse powder discharging means 6 for discharging coarse powder from a clearance in the coarse powder recovery direction for recovering the coarse powder of the solids by a revolving flow formed in the classification chamber 4, and a coarse powder flow hindrance means 7 for hindering the flow of the coarse powder in the fine powder recovery direction on the lower part wall surface 2a of the guide member 2.

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、分級装置に関し、
固体物質の、特に電子写真、静電記録、静電印刷等にお
ける静電荷像の潜像を顕像化する現像の為の画像形成装
置に使用する乾式トナーを製造する際に、分級室内に旋
回流を形成し、固体物質のトナーを遠心分離して分級す
る分級装置及びそれを使用するトナーの製造方法に関す
る。
TECHNICAL FIELD The present invention relates to a classification device,
When manufacturing a dry toner used in an image forming apparatus for developing a solid material, in particular, a latent image of an electrostatic image in electrophotography, electrostatic recording, electrostatic printing, etc., it is rotated into a classifying chamber. The present invention relates to a classifying apparatus for forming a flow and classifying a solid substance toner by centrifugal separation, and a method for producing a toner using the same.

【0002】[0002]

【従来の技術】従来、分級装置は、例えば、電子写真複
写方式による画像形成装置の複写機、ファクシミリ装
置、プリンター及びそれらの複合機においては、画像担
持体のドラム感光体上に形成された静電荷像にトナーを
付着させて、当該静電荷像の潜像を顕像化してトナー現
像し、そのトナー像を転写紙に転写することにより画像
を形成している。このような画像形成装置に使用される
トナーは、通常、固体物質の原材料を混練して固めた状
態で粉砕して、所定のトナーを分級装置によって分級し
ている。
2. Description of the Related Art Conventionally, for example, in a copying machine, a facsimile machine, a printer, and a multifunction machine of an image forming apparatus based on an electrophotographic copying method, a classifier is a static image formed on a drum photosensitive member of an image carrier. Toner is attached to the charge image, the latent image of the electrostatic charge image is visualized, developed with toner, and the toner image is transferred to transfer paper to form an image. Usually, a toner used in such an image forming apparatus is pulverized in a state where raw materials of a solid substance are kneaded and solidified, and a predetermined toner is classified by a classifier.

【0003】このような、電子写真複写方式の画像形成
装置に使用されるトナーは、製造工程の最終段階で、ト
ナー中の粗粒や紙粉等をスクリーンを介して除去するこ
とにより、画像を形成した時に、画像上に砂状のカブ
リ、縦筋状のムラ、転写不良等の異常画像の発生を防止
するようにすることは公知である(特開平5―2934
43号の公報を参照)。
[0003] The toner used in such an electrophotographic image forming apparatus is formed by removing coarse particles and paper dust from the toner through a screen at the final stage of the manufacturing process. It is known to prevent the occurrence of abnormal images such as sand-like fog, vertical streak-like unevenness, and transfer failure on an image when formed (Japanese Patent Laid-Open No. 5-2934).
No. 43).

【0004】図6において、従来、ミクロンオーダの固
体物質(T)を粗粉(Tl)と微粉(Ts)に分離する
分級装置100は、固体物質(T)を分散室101か
ら、本体100aの円筒形状内の円錐状部材の案内部材
102と分級板103により形成される分級室104に
供給し、分散室101内部に形成される旋回流によって
分散作用を受け、さらに分級室104へと導かれ遠心分
離によって、微粉排出口105と粗粉排出口106へと
排出され、固体物質(T)は微粉(Ts)と粗粉(T
l)に分離するようになっている。
[0004] In FIG. 6, conventionally, a classifier 100 for separating a micron-order solid substance (T) into a coarse powder (Tl) and a fine powder (Ts) is provided. It is supplied to a classifying chamber 104 formed by a guide member 102 of a conical member in a cylindrical shape and a classifying plate 103, receives a dispersion action by a swirling flow formed inside the dispersion chamber 101, and is further guided to the classifying chamber 104. By centrifugal separation, the solid substance (T) is discharged to the fine powder discharge port 105 and the coarse powder discharge port 106, and the fine powder (Ts) and the coarse powder (T
l).

【0005】このような分級装置において、エアーが分
級室内へ吸引される際に、エアーの流入位置や流入方向
を変更して、分級限界粒径を変更することも公知である
(特開平6−154709号及び特開平10−2021
91号等の公報を参照)。
In such a classifier, it is also known that, when air is sucked into a classifying chamber, the classifying limit particle diameter is changed by changing the position and direction of air flow (Japanese Patent Laid-Open No. Hei 6-1994). No. 154709 and JP-A-10-2021
No. 91, etc.).

【0006】従来のこのような分級装置は、回収される
固体物質の粒径は、所定の分布幅にばらついている。例
えば、図6に記載の従来の分級装置において、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に、ジェットミルにて微粉砕した
固体物質を供給して、排気ブロワー圧1620mmAq
の条件で、コールターカウンターによる測定で体積平均
粒径7.8μmになるように分級した。その結果、体積
平均粒径7.88μm、4μm以下の微粉含有率(重量
%)は10.71であった。理想とする分布は、所望の
粒径以上の固体物質は全て粗粉回収側へ、所望の粒径以
下の固体物質は全て微粉回収側へ回収されることであ
る。然し、従来のこのような分級装置においては、所望
の粒径以上の固体物質が微粉回収側へ、又、所望の粒径
以下の固体物質が粗粉回収側へ回収される分級誤差が大
きく分級精度が低いと言う不具合が発生していた。
[0006] In such a conventional classifier, the particle size of the recovered solid substance varies in a predetermined distribution width. For example, in the conventional classifier shown in FIG. 6, a mixture of 85 parts by weight of a styrene-acrylic copolymer resin and 15 parts by weight of carbon black is melt-kneaded, cooled, roughly crushed by a hammer mill, and then jet-milled. Is supplied with a finely pulverized solid material at an exhaust blower pressure of 1620 mmAq.
Under the conditions described above, the particles were classified so as to have a volume average particle size of 7.8 μm as measured by a Coulter counter. As a result, the content (% by weight) of fine powder having a volume average particle size of 7.88 μm and 4 μm or less was 10.71. The ideal distribution is that all the solid substances having a desired particle size or more are collected to the coarse powder collecting side, and all the solid substances having a desired particle size or less are collected to the fine powder collecting side. However, in such a conventional classifier, the classification error in which solid substances having a desired particle size or more are collected to the fine powder collection side and solid substances having a desired particle size or less are collected to the coarse powder collection side is large. A problem that accuracy was low occurred.

【0007】[0007]

【発明が解決しようとする課題】前述した従来のかかる
分級装置及びそれを使用するトナーの製造方法は、所望
の粒径以上の固体物質が微粉回収側へ、又は、所望の粒
径以下の固体物質が粗粉回収側へ回収される分級誤差が
大きく分級精度が低いと言う問題が発生していた。
In the above-described conventional classifying apparatus and the method for producing a toner using the same, a solid substance having a desired particle size or more is transferred to a fine powder collecting side or a solid substance having a desired particle size or less is used. There has been a problem that the classification error in which the substance is recovered to the coarse powder recovery side is large and the classification accuracy is low.

【0008】そこで本発明の課題は、このような問題点
を解決するものである。即ち、所望の粒径以上の固体物
質が微粉回収側へ、又は、所望の粒径以下の固体物質が
粗粉回収側へ回収される分級誤差が小さく分級精度が高
い分級装置及びそれを使用するトナーの製造方法を提供
することを目的とする。
Therefore, an object of the present invention is to solve such a problem. That is, a solidifying material having a desired particle size or more is collected on the fine powder collecting side, or a solid material having a desired particle size or less is collected on the coarse powder collecting side. An object of the present invention is to provide a method for manufacturing a toner.

【0009】[0009]

【課題を解決するための手段】上記目的を達成するため
に、請求項1の本発明は、分級室内に旋回流を形成し、
固体物質を遠心分離して分級する分級装置において、分
級する固体物質を供給する固体物質供給手段と、上記固
体物質供給手段により供給された固体物質を案内する案
内部材と、上記案内部材の下方に配置された分級部材
と、本体内の上記案内部材と上記分級部材により形成さ
れる分級室と、上記分級室内に形成される旋回流により
固体物質の微粉が回収される微粉回収方向の中央部から
微粉を排出する微粉排出手段と、上記分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を排出する粗粉排出手段と、上記案
内部材の下部壁面での粗粉の微粉回収方向への流れを阻
止する粗粉流阻止手段とからなる分級装置であることを
最も主要な特徴とする。
To achieve the above object, according to the present invention, a swirling flow is formed in a classification chamber.
In a classifier that classifies a solid substance by centrifugation, a solid substance supply means for supplying a solid substance to be classified, a guide member for guiding the solid substance supplied by the solid substance supply means, A classifying member arranged, a classifying chamber formed by the guide member and the classifying member in the main body, and a central portion in a fine powder collecting direction in which fine powder of a solid substance is collected by a swirling flow formed in the classifying chamber. Fine powder discharging means for discharging fine powder, coarse powder discharging means for discharging coarse powder from a gap in a coarse powder collecting direction in which coarse powder of a solid substance is recovered by a swirling flow formed in the classification chamber, The most main feature of the present invention is a classification device including a coarse powder flow preventing means for preventing the flow of coarse powder in the direction of collecting fine powder on the lower wall surface.

【0010】請求項2の本発明は、請求項1記載の分級
装置において、粗粉流阻止手段は、リング形状部材から
なる分級装置であることを主要な特徴とする。
A second aspect of the present invention is characterized in that, in the classifying apparatus according to the first aspect, the coarse powder flow preventing means is a classifying apparatus comprising a ring-shaped member.

【0011】請求項3の本発明は、請求項1又は2記載
の分級装置において、粗粉流阻止手段は、複数のリング
形状部材からなる分級装置であることを主要な特徴とす
る。
According to a third aspect of the present invention, in the classification apparatus according to the first or second aspect, the coarse powder flow preventing means is a classification apparatus including a plurality of ring-shaped members.

【0012】請求項4の本発明は、請求項2又は3記載
の分級装置において、粗粉流阻止手段のリング形状部材
の高さは、分級室の高さの1/2以下である分級装置で
あることを主要な特徴とする。
According to a fourth aspect of the present invention, in the classification device according to the second or third aspect, the height of the ring-shaped member of the coarse powder flow preventing means is not more than 1/2 of the height of the classification chamber. Is the main feature.

【0013】請求項5の本発明は、請求項2、3又は4
記載の分級装置において、粗粉流阻止手段のリング形状
部材の厚さは、案内部材の下部壁面半径の30%以下で
ある分級装置であることを主要な特徴とする。
The present invention of claim 5 is the invention of claim 2, 3 or 4.
In the classification device described above, the main feature is that the thickness of the ring-shaped member of the coarse powder flow preventing means is 30% or less of the radius of the lower wall surface of the guide member.

【0014】請求項6の本発明は、請求項2、3、4又
は5記載の分級装置において、粗粉流阻止手段のリング
形状部材の直径は、案内部材の下部壁面中央に形成され
た凸形状部の直径以上である分級装置であることを主要
な特徴とする。
According to a sixth aspect of the present invention, in the classification device according to the second, third, fourth or fifth aspect, the diameter of the ring-shaped member of the coarse powder flow preventing means is a convex formed at the center of the lower wall surface of the guide member. The main feature is that it is a classification device having a diameter equal to or larger than the diameter of the shape portion.

【0015】請求項7の本発明は、請求項2、3、4、
5又は6記載の分級装置において、粗粉流阻止手段のリ
ング形状部材の上部外側は、曲面形状部からなる分級装
置であることを主要な特徴とする。
The present invention according to claim 7 is based on claims 2, 3, 4,
7. The classification device according to 5 or 6, wherein the upper outer side of the ring-shaped member of the coarse powder flow preventing means is a classification device including a curved surface portion.

【0016】請求項8の本発明は、請求項2、3、4、
5、6又は7記載の分級装置において、粗粉流阻止手段
のリング形状部材の上部内側は、曲面形状部からなる分
級装置であることを主要な特徴とする。
The present invention according to claim 8 is the invention according to claims 2, 3, 4,
The classification device according to 5, 6, or 7, is characterized in that the inside of the upper portion of the ring-shaped member of the coarse powder flow preventing means is a classification device having a curved surface portion.

【0017】請求項9の本発明は、請求項1乃至8のい
ずれかに記載の分級装置において、粗粉流阻止手段は、
着脱手段により案内部材に着脱可能である分級装置であ
ることを主要な特徴とする。
According to a ninth aspect of the present invention, in the classification device according to any one of the first to eighth aspects, the coarse powder flow preventing means comprises:
The main feature is that it is a classifier that can be attached to and detached from the guide member by attaching and detaching means.

【0018】請求項10の本発明は、電子写真方式の画
像形成装置に使用する潜像を顕像化するトナーの製造方
法において、固体物質を粉砕化した後に、請求項1乃至
9のいずれかに記載の分級装置で分級してトナーを製造
するトナーの製造方法であることを最も主要な特徴とす
る。
According to a tenth aspect of the present invention, in the method for producing a toner for visualizing a latent image used in an electrophotographic image forming apparatus, any one of the first to ninth aspects after pulverizing a solid substance. The most main feature of the present invention is a method for producing a toner in which a toner is produced by classifying with a classifying apparatus described in (1).

【0019】[0019]

【作用】上記のように構成された分級装置及びそれを使
用するトナーの製造方法は、請求項1においては、固体
物質供給手段により供給された固体物質を案内する案内
部材と案内部材の下方に配置された分級部材と本体内の
案内部材と分級部材により形成される分級室内に形成さ
れる旋回流により固体物質の微粉が回収される微粉回収
方向の中央部から微粉を微粉排出手段で排出し、分級室
内に形成される旋回流により固体物質の粗粉が回収され
る粗粉回収方向の間隙から粗粉を粗粉排出手段で排出す
るようにして、案内部材の下部壁面での粗粉の微粉回収
方向への流れを粗粉流阻止手段で阻止するようにして、
所望の粒径以上の固体物質が微粉回収側へ、又は、所望
の粒径以下の固体物質が粗粉回収側へ回収される分級誤
差が小さく分級精度が高い分級装置を提供することが出
来るようにする。
According to the first aspect of the present invention, there is provided a classifying apparatus and a method of manufacturing a toner using the classifying apparatus, wherein a guide member for guiding the solid material supplied by the solid material supply means and a guide member below the guide member are provided. Fine powder of solid material is recovered by a swirling flow formed in a classification chamber formed by the disposed classification member, the guide member in the main body, and the classification member. The coarse powder on the lower wall surface of the guide member is discharged from the gap in the coarse powder collection direction in which the coarse powder of the solid substance is recovered by the swirling flow formed in the classification chamber. By blocking the flow in the fine powder collection direction with coarse powder flow prevention means,
It is possible to provide a classification apparatus in which a solid substance having a desired particle size or more is collected to a fine powder collecting side or a solid substance having a desired particle size or less is collected to a coarse powder collecting side, and the classification error is small and the classification accuracy is high. To

【0020】請求項2においては、固体物質供給手段に
より供給された固体物質を案内する案内部材と案内部材
の下方に配置された分級部材と本体内の案内部材と分級
部材により形成される分級室内に形成される旋回流によ
り固体物質の微粉が回収される微粉回収方向の中央部か
ら微粉を微粉排出手段で排出し、分級室内に形成される
旋回流により固体物質の粗粉が回収される粗粉回収方向
の間隙から粗粉を粗粉排出手段で排出するようにして、
案内部材の下部壁面での粗粉の微粉回収方向への流れを
粗粉流阻止手段のリング形状部材で阻止するようにし
て、簡単な構造で、所望の粒径以上の固体物質が微粉回
収側へ、又は、所望の粒径以下の固体物質が粗粉回収側
へ回収される分級誤差が小さく分級精度が高い分級装置
を提供することが出来るようにする。
In a second aspect, a classifying chamber formed by a guide member for guiding the solid material supplied by the solid material supply means, a classifying member disposed below the guide member, a guide member in the main body and the classifying member. The fine powder of the solid substance is collected by the swirl flow formed in the fine powder. The fine powder is discharged from the central part in the fine powder recovery direction by the fine powder discharge means, and the coarse powder of the solid substance is collected by the swirl flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the powder collecting direction,
The ring-shaped member of the coarse powder flow preventing means prevents the coarse powder from flowing in the fine powder collecting direction on the lower wall surface of the guide member, and the solid substance having a desired particle size or more has a simple structure. Or a classifier having a small classification error and a high classification accuracy in which a solid substance having a desired particle size or less is recovered to a coarse powder recovery side.

【0021】請求項3においては、固体物質供給手段に
より供給された固体物質を案内する案内部材と案内部材
の下方に配置された分級部材と本体内の案内部材と分級
部材により形成される分級室内に形成される旋回流によ
り固体物質の微粉が回収される微粉回収方向の中央部か
ら微粉を微粉排出手段で排出し、分級室内に形成される
旋回流により固体物質の粗粉が回収される粗粉回収方向
の間隙から粗粉を粗粉排出手段で排出するようにして、
案内部材の下部壁面での粗粉の微粉回収方向への流れを
粗粉流阻止手段の複数のリング形状部材で阻止するよう
にして、簡単な構造で、所望の粒径以上の固体物質が微
粉回収側へ、又は、所望の粒径以下の固体物質が粗粉回
収側へ回収される分級誤差が更に小さく分級精度が更に
高い分級装置を提供することが出来るようにする。
In a third aspect, a classifying chamber formed by a guide member for guiding the solid substance supplied by the solid substance supply means, a classifying member disposed below the guide member, a guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirl flow formed in the fine powder. The fine powder is discharged from the central part in the fine powder recovery direction by the fine powder discharge means, and the coarse powder of the solid substance is collected by the swirl flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the powder collecting direction,
The solid material having a desired particle size or more has a simple structure in which the flow of coarse powder in the direction of collecting fine powder on the lower wall surface of the guide member is blocked by the plurality of ring-shaped members of the coarse powder flow blocking means. It is possible to provide a classification device having a smaller classification error and a higher classification accuracy, in which a solid substance having a desired particle size or less is recovered to a coarse powder collection side.

【0022】請求項4においては、固体物質供給手段に
より供給された固体物質を案内する案内部材と案内部材
の下方に配置された分級部材と本体内の案内部材と分級
部材により形成される分級室内に形成される旋回流によ
り固体物質の微粉が回収される微粉回収方向の中央部か
ら微粉を微粉排出手段で排出し、分級室内に形成される
旋回流により固体物質の粗粉が回収される粗粉回収方向
の間隙から粗粉を粗粉排出手段で排出するようにして、
案内部材の下部壁面での粗粉の微粉回収方向への流れを
粗粉流阻止手段のリング形状部材で阻止するようにする
と共にリング形状部材の高さを分級室の高さの1/2以
下になるようにして、分級室内部の旋回流が大きく変化
して固体物質の回収率が低下することなく、簡単な構造
で、所望の粒径以上の固体物質が微粉回収側へ、又は、
所望の粒径以下の固体物質が粗粉回収側へ回収される分
級誤差が小さく分級精度が高い分級装置を提供すること
が出来るようにする。
According to a fourth aspect of the present invention, there is provided a classification chamber formed by a guide member for guiding the solid substance supplied by the solid substance supply means, a classification member disposed below the guide member, a guide member in the main body, and the classification member. The fine powder of the solid substance is collected by the swirl flow formed in the fine powder. The fine powder is discharged from the central part in the fine powder recovery direction by the fine powder discharge means, and the coarse powder of the solid substance is collected by the swirl flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the powder collecting direction,
The flow of the coarse powder in the direction of collecting the fine powder on the lower wall surface of the guide member is prevented by the ring-shaped member of the coarse-flow preventing means, and the height of the ring-shaped member is not more than half the height of the classification chamber. In such a manner, the swirl flow inside the classification chamber is largely changed and the solid matter recovery rate is not reduced, and the solid matter having a desired particle size or more is supplied to the fine powder collection side with a simple structure, or
A classification apparatus which has a small classification error and a high classification accuracy in which a solid substance having a desired particle size or less is recovered to a coarse powder recovery side can be provided.

【0023】請求項5においては、固体物質供給手段に
より供給された固体物質を案内する案内部材と案内部材
の下方に配置された分級部材と本体内の案内部材と分級
部材により形成される分級室内に形成される旋回流によ
り固体物質の微粉が回収される微粉回収方向の中央部か
ら微粉を微粉排出手段で排出し、分級室内に形成される
旋回流により固体物質の粗粉が回収される粗粉回収方向
の間隙から粗粉を粗粉排出手段で排出するようにして、
案内部材の下部壁面での粗粉の微粉回収方向への流れを
粗粉流阻止手段のリング形状部材で阻止するようにする
と共にリング形状部材の厚さを案内部材の下部壁面半径
の30%以下になるようにして、分級室内部の旋回流が
大きく変化して固体物質の回収率が低下することなく、
簡単な構造で、所望の粒径以上の固体物質が微粉回収側
へ、又は、所望の粒径以下の固体物質が粗粉回収側へ回
収される分級誤差が小さく分級精度が高い分級装置を提
供することが出来るようにする。
In a fifth aspect, a classification member formed by a guide member for guiding the solid substance supplied by the solid substance supply means, a classification member disposed below the guide member, a guide member in the main body and the classification member. The fine powder of the solid substance is collected by the swirl flow formed in the fine powder. The fine powder is discharged from the central part in the fine powder recovery direction by the fine powder discharge means, and the coarse powder of the solid substance is collected by the swirl flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the powder collecting direction,
The flow of the coarse powder in the direction of collecting the fine powder on the lower wall surface of the guide member is prevented by the ring-shaped member of the coarse powder flow preventing means, and the thickness of the ring-shaped member is 30% or less of the radius of the lower wall surface of the guide member. So that the swirl flow inside the classification chamber changes greatly and the solid matter recovery rate does not decrease,
Provides a classification device that has a simple structure and has a small classification error and a high classification accuracy in which a solid substance with a desired particle size or more is collected to the fine powder collection side or a solid substance with a desired particle size or less is collected to the coarse powder collection side. To be able to

【0024】請求項6においては、固体物質供給手段に
より供給された固体物質を案内する案内部材と案内部材
の下方に配置された分級部材と本体内の案内部材と分級
部材により形成される分級室内に形成される旋回流によ
り固体物質の微粉が回収される微粉回収方向の中央部か
ら微粉を微粉排出手段で排出し、分級室内に形成される
旋回流により固体物質の粗粉が回収される粗粉回収方向
の間隙から粗粉を粗粉排出手段で排出するようにして、
案内部材の下部壁面での粗粉の微粉回収方向への流れを
粗粉流阻止手段のリング形状部材で阻止するようにする
と共にリング形状部材の直径を案内部材の下部壁面中央
に形成された凸形状部の直径以上になるようにして、案
内部材の下部壁面に沿う旋回流が大きく変化せず固体物
質の動きも殆どかわらなくなることはなく、簡単な構造
で、所望の粒径以上の固体物質が微粉回収側へ、又は、
所望の粒径以下の固体物質が粗粉回収側へ回収される分
級誤差が小さく分級精度が高い分級装置を提供すること
が出来るようにする。
According to a sixth aspect of the present invention, there is provided a classification chamber formed by a guide member for guiding the solid substance supplied by the solid substance supply means, a classification member disposed below the guide member, a guide member in the main body, and the classification member. The fine powder of the solid substance is collected by the swirl flow formed in the fine powder. The fine powder is discharged from the central part in the fine powder recovery direction by the fine powder discharge means, and the coarse powder of the solid substance is collected by the swirl flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the powder collecting direction,
The flow of coarse powder in the direction of collecting fine powder on the lower wall surface of the guide member is prevented by the ring-shaped member of the coarse powder flow preventing means, and the diameter of the ring-shaped member is formed at the center of the lower wall surface of the guide member. By making the diameter of the solid portion larger than the diameter of the shape portion, the swirling flow along the lower wall surface of the guide member does not greatly change and the movement of the solid material hardly changes, and the solid material having a simple structure and a desired particle size or more is obtained. To the fine powder collection side, or
A classification apparatus which has a small classification error and a high classification accuracy in which a solid substance having a desired particle size or less is recovered to a coarse powder recovery side can be provided.

【0025】請求項7においては、固体物質供給手段に
より供給された固体物質を案内する案内部材と案内部材
の下方に配置された分級部材と本体内の案内部材と分級
部材により形成される分級室内に形成される旋回流によ
り固体物質の微粉が回収される微粉回収方向の中央部か
ら微粉を微粉排出手段で排出し、分級室内に形成される
旋回流により固体物質の粗粉が回収される粗粉回収方向
の間隙から粗粉を粗粉排出手段で排出するようにして、
案内部材の下部壁面での粗粉の微粉回収方向への流れを
粗粉流阻止手段のリング形状部材で阻止するようにする
と共にリング形状部材の上部外側は曲面形状部からなる
ようにして、リング形状部材の上部の取り付け部外側で
の旋回流の淀みや連続運転時の固体物質の堆積を防止し
て固体物質の回収率が向上して清掃性も良く、簡単な構
造で、所望の粒径以上の固体物質が微粉回収側へ、又
は、所望の粒径以下の固体物質が粗粉回収側へ回収され
る分級誤差が小さく分級精度が高い分級装置を提供する
ことが出来るようにする。
In a seventh aspect, a classifying chamber formed by a guide member for guiding the solid substance supplied by the solid substance supply means, a classifying member disposed below the guide member, a guide member in the main body and the classifying member. The fine powder of the solid substance is collected by the swirl flow formed in the fine powder. The fine powder is discharged from the central part in the fine powder recovery direction by the fine powder discharge means, and the coarse powder of the solid substance is collected by the swirl flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the powder collecting direction,
The ring-shaped member of the coarse-particle flow preventing means prevents the coarse powder from flowing in the fine powder collecting direction on the lower wall surface of the guide member, and the upper outer side of the ring-shaped member is formed of a curved surface portion. Prevents stagnation of swirling flow outside the mounting part on the top of the shaped member and solid material accumulation during continuous operation, improves the recovery rate of solid material, improves cleanability, has a simple structure, and has a desired particle size It is possible to provide a classification apparatus which has a small classification error and a high classification accuracy in which the solid substance is collected on the fine powder collection side or the solid substance having a desired particle size or less is collected on the coarse powder collection side.

【0026】請求項8においては、固体物質供給手段に
より供給された固体物質を案内する案内部材と案内部材
の下方に配置された分級部材と本体内の案内部材と分級
部材により形成される分級室内に形成される旋回流によ
り固体物質の微粉が回収される微粉回収方向の中央部か
ら微粉を微粉排出手段で排出し、分級室内に形成される
旋回流により固体物質の粗粉が回収される粗粉回収方向
の間隙から粗粉を粗粉排出手段で排出するようにして、
案内部材の下部壁面での粗粉の微粉回収方向への流れを
粗粉流阻止手段のリング形状部材で阻止するようにする
と共にリング形状部材の上部内側は曲面形状部からなる
ようにして、リング形状部材の上部の取り付け部内側で
の旋回流の淀みや連続運転時の固体物質の堆積を防止し
て固体物質の回収率が向上して清掃性も良く、簡単な構
造で、所望の粒径以上の固体物質が微粉回収側へ、又
は、所望の粒径以下の固体物質が粗粉回収側へ回収され
る分級誤差が小さく分級精度が高い分級装置を提供する
ことが出来るようにする。
In a preferred embodiment, a classifying chamber formed by a guide member for guiding the solid substance supplied by the solid substance supply means, a classifying member disposed below the guide member, a guide member in the main body and the classifying member. The fine powder of the solid substance is collected by the swirl flow formed in the fine powder. The fine powder is discharged from the central part in the fine powder recovery direction by the fine powder discharge means, and the coarse powder of the solid substance is collected by the swirl flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the powder collecting direction,
The flow of coarse powder in the direction of collecting fine powder on the lower wall surface of the guide member is prevented by the ring-shaped member of the coarse powder flow preventing means, and the inside of the upper portion of the ring-shaped member is formed of a curved surface portion. Prevents stagnation of swirling flow inside the upper part of the shaped member and accumulation of solid substances during continuous operation, improves the recovery rate of solid substances, improves cleanability, has a simple structure, and has a desired particle size. It is possible to provide a classification apparatus which has a small classification error and a high classification accuracy in which the solid substance is collected on the fine powder collection side or the solid substance having a desired particle size or less is collected on the coarse powder collection side.

【0027】請求項9においては、固体物質供給手段に
より供給された固体物質を案内する案内部材と案内部材
の下方に配置された分級部材と本体内の案内部材と分級
部材により形成される分級室内に形成される旋回流によ
り固体物質の微粉が回収される微粉回収方向の中央部か
ら微粉を微粉排出手段で排出し、分級室内に形成される
旋回流により固体物質の粗粉が回収される粗粉回収方向
の間隙から粗粉を粗粉排出手段で排出するようにして、
案内部材の下部壁面での粗粉の微粉回収方向への流れを
粗粉流阻止手段のリング形状部材で阻止するようにする
と共に粗粉流阻止手段を着脱手段により案内部材に着脱
可能になるようにして、案内部材の下部壁面に粗粉流阻
止手段のリング形状部材の取り付けの切り替え作業も短
縮化され粗粉流阻止手段のリング形状部材の高さの調整
も容易に行うことが出来る、簡単な構造で、所望の粒径
以上の固体物質が微粉回収側へ、又は、所望の粒径以下
の固体物質が粗粉回収側へ回収される分級誤差が小さく
分級精度が高い分級装置を提供することが出来るように
する。
In a ninth aspect, a classifying chamber formed by a guide member for guiding the solid material supplied by the solid material supply means, a classifying member disposed below the guide member, a guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirl flow formed in the fine powder. The fine powder is discharged from the central part in the fine powder recovery direction by the fine powder discharge means, and the coarse powder of the solid substance is collected by the swirl flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the powder collecting direction,
The flow of coarse powder in the direction of collecting the fine powder on the lower wall surface of the guide member is prevented by the ring-shaped member of the coarse powder flow prevention means, and the coarse powder flow prevention means can be detachably attached to the guide member by the detachable means. In addition, the work of switching the attachment of the ring-shaped member of the coarse powder flow prevention means to the lower wall surface of the guide member is also shortened, and the height of the ring-shaped member of the coarse powder flow prevention means can be easily adjusted. Provided is a classifier having a simple structure, a solid substance having a desired particle size or more is collected to a fine powder collecting side, or a solid substance having a desired particle size or less is collected to a coarse powder collecting side, the classification error is small and the classification accuracy is high. To be able to

【0028】請求項10においては、固体物質を粉砕化
した後に、請求項1乃至9記載の分級装置で分級してト
ナーを製造するようにして、簡単な製造方法で、所望の
粒径以上の固体物質が微粉回収側へ、又は、所望の粒径
以下の固体物質が粗粉回収側へ回収される分級誤差が小
さく分級精度が高いトナーを製造するトナー製造方法を
提供することが出来るようにする。
In the tenth aspect, after the solid substance is pulverized, the toner is produced by classifying the solid substance with the classifier according to the first to ninth aspects. To provide a toner production method for producing a toner having a small classification error and high classification accuracy in which a solid substance is collected on a fine powder collection side or a solid substance having a desired particle size or less is collected on a coarse powder collection side. I do.

【0029】[0029]

【発明の実施の形態】次に、本発明の実施の形態を図面
を参照して詳細に説明する。図1又は図2において、分
級装置0は、固体物質供給手段1の供給管1a及び2次
気体流入口1bから、気体の空気が図示の矢印A方向と
矢印B方向から供給され、同時に排気管1c、微粉排出
手段5の微粉排出口5a、粗粉排出手段6の粗粉排出口
6aからは、気体の空気が図示の矢印C方向、図示の矢
印D方向、図示の矢印E方向から排出されることによっ
て、分散室1d及び本体0a内の円錐形状の案内部材2
と分級部材3の分級板により形成される分級室4内部に
旋回流場が形成される。
Next, embodiments of the present invention will be described in detail with reference to the drawings. In FIG. 1 or FIG. 2, the classifying apparatus 0 is configured such that gaseous air is supplied from the supply pipe 1 a and the secondary gas inlet 1 b of the solid substance supply means 1 in the directions of arrows A and B shown in FIG. 1c, gaseous air is discharged from the fine powder discharge port 5a of the fine powder discharge means 5 and the coarse powder discharge port 6a of the coarse powder discharge means 6 in the illustrated arrow C direction, the illustrated arrow D direction, and the illustrated arrow E direction. The conical guide member 2 in the dispersion chamber 1d and the main body 0a
A swirling flow field is formed inside the classification chamber 4 formed by the classification plate of the classification member 3.

【0030】そこに、上記供給管1aより、粒径がミク
ロンオーダの固体物質(T)が図示の矢印A方向に供給
され、上記分散室1d内部に導かれ、遠心分離作用を受
けながら、固体物質(T)は回転しながら図示の矢印F
方向に落下する。この際、固体物質(T)の非常に小さ
い粒径の微粉は、上記分散室1dの中心方向に導かれ、
上記排気管1cから図示の矢印C方向に排出される。
A solid substance (T) having a particle size on the order of microns is supplied from the supply pipe 1a in the direction of the arrow A shown in the drawing, guided into the dispersion chamber 1d, and subjected to centrifugal separation. The substance (T) rotates while the arrow F shown in the figure.
Fall in the direction. At this time, the fine powder having a very small particle diameter of the solid substance (T) is guided toward the center of the dispersion chamber 1d,
It is discharged from the exhaust pipe 1c in the direction of arrow C shown in the figure.

【0031】上記分散室1dより回転しながら落下した
固体物質(T)は間隙4aを通過して、上記分級室4内
部に導かれ、ここでも遠心分離作用を受け、固体物質
(T)の粗粉(Tl)は遠心力によって上記分級室4の
中心から遠ざかる図示の矢印G方向の粗粉回収方向の上
記分級部材3の分級板の端部と上記本体0aの内壁面と
の間隙4bを通過して、上記粗粉排出手段6の上記粗粉
排出口6aから排出される。
The solid substance (T) that has fallen while rotating from the dispersion chamber 1d passes through the gap 4a and is guided into the classification chamber 4, where the solid substance (T) is also subjected to a centrifugal separation action, and the solid substance (T) is coarsened. The powder (Tl) passes through the gap 4b between the end of the classifying plate of the classifying member 3 and the inner wall surface of the main body 0a in the coarse powder collecting direction in the direction of arrow G shown in the figure, which moves away from the center of the classifying chamber 4 by centrifugal force. Then, the powder is discharged from the coarse powder discharge port 6a of the coarse powder discharging means 6.

【0032】上記案内部材2の下部壁面2aには、粗粉
(Tl)の図示の矢印H方向の微粉回収方向への流れを
阻止する粗粉流阻止手段7の好ましくは真円のリング形
状のリング形状部材7aが配置されている。上記案内部
材2の上記下部壁面2aへの上記粗粉流阻止手段7のリ
ング形状の上記リング形状部材7aの配置によって、上
記分級室4内には分布を持った流れが形成されており、
特に、上記案内部材2の上記下部壁面2a付近には、他
の場所に比べて図示の矢印H方向の流れの速度が早く、
上記分級室4内に導かれる固体物質(T)は上記分級室
4の中心に近づく図示の矢印H方向の微粉回収方向へと
導かれ易く、矢印G方向の粗粉回収方向へと回収される
べき固体物質(T)の粗粉(Tl)が図示の矢印H方向
の微粉回収方向へと導かれる流れが阻止されて、固体物
質(T)の微粉(Ts)は向心力によって上記分級室4
の中心に近づく図示の矢印H方向の微粉回収方向へと導
かれ上記微粉排出手段5の上記微粉排出5aから排出さ
れて分級が行われるようになっている。
On the lower wall surface 2a of the guide member 2, a coarse powder flow preventing means 7 for preventing the coarse powder (Tl) from flowing in the fine powder recovery direction in the direction of arrow H shown in the figure, preferably in the form of a perfect circular ring. A ring-shaped member 7a is arranged. Due to the arrangement of the ring-shaped member 7 a of the ring shape of the coarse powder flow preventing means 7 on the lower wall surface 2 a of the guide member 2, a distributed flow is formed in the classification chamber 4,
In particular, near the lower wall surface 2a of the guide member 2, the speed of the flow in the direction of the arrow H shown in the figure is higher than in other places,
The solid substance (T) introduced into the classifying chamber 4 is easily guided in the direction of the fine powder collection in the direction of the arrow H shown in the drawing approaching the center of the classifying chamber 4 and is collected in the direction of the coarse powder collection in the direction of the arrow G. The flow of the coarse powder (Tl) of the solid substance (T) to be guided to the fine powder collection direction in the direction of the arrow H shown in the drawing is prevented, and the fine powder (Ts) of the solid substance (T) is centrifugally applied to the classification chamber 4.
And is discharged from the fine powder discharge 5a of the fine powder discharge means 5 to perform classification.

【0033】固体物質(T)は、例えば、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、これを図示しない
ハンマーミルの粉砕装置で粗粉砕した後に、図示しない
ジェットミルの粉砕装置にて微粉砕した後に、上記分級
装置0の上記固体物質供給手段1により上記分級室4内
に供給して、排気ブロワー圧1620mmAq、上記リ
ング形状部材7aの高さが高すぎると上記分級室4内部
の旋回流が大きく変化して固体物質(T)の回収率が低
下するので上記分級室4の高さの約1/2で好ましくは
1/2以下、上記リング形状部材7aの厚さが厚過ぎる
と上記分級室4内部の旋回流が大きく変化して固体物質
(T)の回収率が低下するので上記案内部材2の上記下
部壁面2aの半径の好ましくは30%以下で1.5m
m、上記リング形状部材7aの直径は上記案内部材2の
上記下部壁面2a中央に形成された凸形状部2bの直径
以下に設定すると、上記案内部材2の上記下部壁面2a
に沿う旋回流が変化せず、固体物質(T)の動きも殆ど
かわらないので上記凸形状部2bの直径以上である17
0mmの条件で、コールターカウンターによる測定で体
積平均粒径が7.8μmになるように分級した結果、フ
イード量が10.5Kg/hに対して、体積平均粒径が
7.66μm、4μm以下の微粉含有率(重量%)が
6.67であり、従来の分級装置100よりもシャープ
な粒度分布となり、分級誤差が小さく分級精度が高いト
ナーを分級する分級装置0及びそれを使用するトナーの
製造方法を提供することが出来るようになった。
The solid substance (T) is, for example, 85 parts by weight of a styrene-acrylic copolymer resin and 15 parts of carbon black 15
The mixture of parts by weight is melt-kneaded, cooled, coarsely pulverized by a hammer mill (not shown), finely pulverized by a jet mill (not shown), and then supplied with the solid material supply means of the classifier 0. If the exhaust blower pressure is 1620 mmAq and the height of the ring-shaped member 7a is too high, the swirling flow inside the classification chamber 4 changes greatly, and the solid substance (T) recovery rate is increased. When the thickness of the ring-shaped member 7a is too large, the swirling flow inside the classifying chamber 4 is greatly changed, and the solid is formed. Since the recovery rate of the substance (T) decreases, the radius of the lower wall surface 2a of the guide member 2 is preferably 30% or less and 1.5 m
m, if the diameter of the ring-shaped member 7a is set to be equal to or less than the diameter of the convex portion 2b formed at the center of the lower wall surface 2a of the guide member 2, the lower wall surface 2a of the guide member 2
And the movement of the solid substance (T) hardly changes, so that the diameter is equal to or larger than the diameter of the convex portion 2b.
As a result of classification under the condition of 0 mm so that the volume average particle size becomes 7.8 μm as measured by a Coulter counter, the volume average particle size was 7.66 μm and 4 μm or less for a feed amount of 10.5 kg / h. The fine powder content (% by weight) is 6.67, the particle size distribution is sharper than that of the conventional classifier 100, the classification error is small, and the classification device 0 for classifying the toner with high classification accuracy and the production of the toner using the same. A method can now be provided.

【0034】従って、所望の粒径以上の固体物質(T)
が微粉回収方向側へ、又は、所望の粒径以下の固体物質
(T)が粗粉回収方向側へ回収される分級誤差が小さく
分級精度が高い分級装置0及びそれを使用するトナーの
製造方法を提供するが出来るようになった。
Therefore, the solid substance (T) having a desired particle size or more
Classifier 0 having high classification accuracy with a small classification error in which solid substance (T) having a desired particle size or less is collected in the coarse powder collection direction, and a method of manufacturing a toner using the same. Can now be provided.

【0035】図3において、上記案内部材2の上記下部
壁面2aには、粗粉(Tl)の図示の矢印H方向の微粉
回収方向への流れを阻止する上記粗粉流阻止手段7の好
ましくは真円のリング形状の複数の上記リング形状部材
7a、上記リング形状部材7a、例えば、図示のよ
うに内側と外側に配置されている。
In FIG. 3, preferably, the coarse powder flow preventing means 7 for preventing the coarse powder (Tl) from flowing in the fine powder collecting direction in the direction indicated by arrow H on the lower wall surface 2a of the guide member 2 is preferable. The plurality of ring-shaped members 7a 1 and 7a 2 having a perfect circular ring shape are arranged on the inside and outside as shown in the figure.

【0036】固体物質(T)は、例えば、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、これを図示しない
ハンマーミルの粉砕装置で粗粉砕した後に、図示しない
ジェットミルの粉砕装置にて微粉砕した後に、上記分級
装置0の上記固体物質供給手段1により上記分級室4内
に供給して、排気ブロワー圧1620mmAq、複数の
上記リング形状部材7aの直径が150mmと上記リ
ング形状部材7aの直径が170mmの高さを上記分
級室4の高さの約1/2、複数の上記リング形状部材7
の直径が150mmと上記リング形状部材7a
直径が170mmの厚さ1.5mmの条件で、コールタ
ーカウンターによる測定で体積平均粒径が7.80μm
になるよう分級した結果、フイード量が10.5Kg/
hに対して、体積平均粒径が7.70μm、4μm以下
の微粉含有率(重量%)が4.59であり、更にシャー
プな粒度分布となり、分級誤差が小さく分級精度が高い
トナーを分級する分級装置0及びそれを使用するトナー
の製造方法を提供することが出来るようになった。
The solid substance (T) is, for example, 85 parts by weight of a styrene-acrylic copolymer resin and 15 parts of carbon black 15
The mixture of parts by weight is melt-kneaded, cooled, coarsely pulverized by a hammer mill (not shown), finely pulverized by a jet mill (not shown), and then supplied with the solid material supply means of the classifier 0. 1 is supplied to the classification chamber 4 by an exhaust blower pressure 1620MmAq, the diameter of the plurality of the ring-shaped member 7a 1 is 150mm and the ring-shaped member 7a 2 diameter of 170mm and height of the classifying chamber 4 high About one-half of the ring-shaped members 7
The diameter of a 1 is 150mm and the diameter of the ring-shaped member 7a 2 of 170mm under conditions of thickness 1.5 mm, the volume average particle diameter measured by a Coulter counter is 7.80μm
As a result, the feed amount was 10.5 kg /
With respect to h, the content of fine powder having a volume average particle size of 7.70 μm and 4 μm or less (weight%) is 4.59, and a sharper particle size distribution is obtained, and a classification error is small and a classification accuracy is high. It has become possible to provide a classifier 0 and a method for producing a toner using the same.

【0037】従って、所望の粒径以上の固体物質(T)
が微粉回収方向側へ、又は、所望の粒径以下の固体物質
(T)が粗粉回収方向側へ回収される分級誤差が更に小
さく分級精度が更に高い分級装置0及びそれを使用する
トナーの製造方法を提供するが出来るようになった。
Therefore, a solid substance (T) having a desired particle size or more
Is smaller in the direction of collecting fine powder or solid substance (T) having a desired particle size or less is collected in the direction of collecting coarse powder. Manufacturing methods can now be provided.

【0038】図4において、上記案内部材2の上記下部
壁面2aには、粗粉(Tl)の図示の矢印H方向の微粉
回収方向への流れを阻止する上記粗粉流阻止手段7の好
ましくは真円のリング形状の上記リング形状部材7aの
上部外側にR形状の曲面形状部7b、上部内側にR形状
の曲面形状部7cが設けてある。従って、上記案内部材
2の上記下部壁面2aの上記粗粉流阻止手段7の上記リ
ング形状部材7aの上部の取り付け部での旋回流の淀み
や連続運転時の固体物質(T)の堆積を防止して、固体
物質(T)の回収率が向上して清掃性も良く、所望の粒
径以上の固体物質(T)が微粉回収方向側へ、又は、所
望の粒径以下の固体物質(T)が粗粉回収方向側へ回収
される分級誤差が更に小さく分級精度が更に高い分級装
置0及びそれを使用するトナーの製造方法を提供するが
出来るようになった。
In FIG. 4, preferably, the coarse powder flow preventing means 7 for preventing the coarse powder (Tl) from flowing in the fine powder collection direction in the direction of arrow H shown in the drawing on the lower wall surface 2a of the guide member 2. An R-shaped curved surface portion 7b is provided on the upper outer side of the ring-shaped member 7a having a perfect circular shape, and an R-shaped curved surface portion 7c is provided on the upper inner side. Therefore, the stagnation of the swirl flow at the upper portion of the ring-shaped member 7a of the coarse powder flow preventing means 7 on the lower wall surface 2a of the guide member 2 and the accumulation of the solid substance (T) during continuous operation are prevented. As a result, the recovery rate of the solid substance (T) is improved and the cleaning property is also good, and the solid substance (T) having a desired particle size or more is moved toward the fine powder collection direction or the solid substance (T) having a desired particle size or less. ) Can provide a classification device 0 having a smaller classification error collected in the coarse powder collection direction and a higher classification accuracy, and a method for producing a toner using the same.

【0039】図5において、上記案内部材2の上記下部
壁面2aには、粗粉(Tl)の図示の矢印H方向の微粉
回収方向への流れを阻止する上記粗粉流阻止手段7の好
ましくは真円のリング形状の上記リング形状部材7a
が、着脱手段7dの着脱裸子7dと着脱裸子穴7d
の着脱により、着脱可能になっている。従って、上記案
内部材2の上記下部壁面2aに、上記粗粉流阻止手段7
の上記リング形状部材7aの取り付けの切り替え作業も
短縮化され、上記粗粉流阻止手段7の上記リング形状部
材7aの高さの調整も容易に行うことが出来、所望の粒
径以上の固体物質(T)が微粉回収方向側へ、又は、所
望の粒径以下の固体物質(T)が粗粉回収方向側へ回収
される分級誤差が更に小さく分級精度が更に高い分級装
置0及びそれを使用するトナーの製造方法を提供するが
出来るようになった。
In FIG. 5, preferably, the coarse powder flow preventing means 7 for preventing the coarse powder (Tl) from flowing in the fine powder collecting direction in the direction indicated by arrow H on the lower wall surface 2a of the guide member 2 is preferable. The above-mentioned ring-shaped member 7a having a perfect circular ring shape
But detachment of the detachable unit 7d Hadakako 7d 1 and detachable Hadakako hole 7d 2
It can be attached and detached by attaching and detaching. Accordingly, the coarse powder flow preventing means 7 is provided on the lower wall surface 2a of the guide member 2.
The work of switching the mounting of the ring-shaped member 7a is also shortened, the height of the ring-shaped member 7a of the coarse powder flow preventing means 7 can be easily adjusted, and a solid substance having a desired particle size or more can be obtained. (T) is collected in the fine powder collection direction, or a solid substance (T) having a desired particle size or less is collected in the coarse powder collection direction. It is possible to provide a method for producing a toner that is less susceptible.

【0040】[0040]

【発明の効果】本発明は、以上説明したように構成され
ているので、請求項1の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段で阻止するようにしたので、所望の
粒径以上の固体物質が微粉回収側へ、又は、所望の粒径
以下の固体物質が粗粉回収側へ回収される分級誤差が小
さく分級精度が高い分級装置を提供することが出来るよ
うになった。
According to the present invention, as described above, according to the first aspect of the present invention, there is provided a guide member for guiding the solid substance supplied by the solid substance supply means, and a guide member provided below the guide member. Fine powder of solid material is recovered by a swirling flow formed in a classification chamber formed by the disposed classification member, the guide member in the main body, and the classification member. The coarse powder on the lower wall surface of the guide member is discharged from the gap in the coarse powder collection direction in which the coarse powder of the solid substance is recovered by the swirling flow formed in the classification chamber. Since the flow in the fine powder recovery direction is blocked by the coarse powder flow prevention means, solid substances having a desired particle size or more are directed to the fine powder recovery side, or solid substances having a desired particle diameter or less are directed to the coarse powder recovery side. Recovered classification error is small and classification accuracy is high It has become possible to provide a classification device.

【0041】請求項2の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段のリング形状部材で阻止するように
したので、簡単な構造で、所望の粒径以上の固体物質が
微粉回収側へ、又は、所望の粒径以下の固体物質が粗粉
回収側へ回収される分級誤差が小さく分級精度が高い分
級装置を提供することが出来るようになった。
According to the second aspect of the present invention, the guide member is formed by the guide member for guiding the solid material supplied by the solid material supply means, the classifying member disposed below the guide member, the guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirling flow formed in the classification chamber. The fine powder is discharged from the center in the fine powder collection direction by the fine discharge means, and the coarse powder of the solid substance is collected by the swirling flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the coarse powder collecting direction, and the flow of the coarse powder in the fine powder collecting direction at the lower wall surface of the guide member is performed by the ring-shaped member of the coarse powder flow preventing means. Since it is prevented, solid substances with a desired particle size or more are collected to the fine powder collection side or solid substances with a desired particle size or less are collected to the coarse powder collection side with a simple structure. Providing a highly accurate classification device Theft has become to be able to.

【0042】請求項3の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段の複数のリング形状部材で阻止する
ようにしたので、簡単な構造で、所望の粒径以上の固体
物質が微粉回収側へ、又は、所望の粒径以下の固体物質
が粗粉回収側へ回収される分級誤差が更に小さく分級精
度が更に高い分級装置を提供することが出来るようにな
った。
According to the third aspect of the present invention, the guide member is formed by the guide member for guiding the solid material supplied by the solid material supply means, the classifying member disposed below the guide member, the guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirling flow formed in the classification chamber. The fine powder is discharged from the center in the fine powder collection direction by the fine discharge means, and the coarse powder of the solid substance is collected by the swirling flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the coarse powder collecting direction, and the flow of the coarse powder in the fine powder collecting direction on the lower wall surface of the guide member is formed by a plurality of ring shapes of coarse powder flow preventing means. Since the material is blocked by a member, the classification error in which a solid substance having a desired particle size or more is collected to the fine powder collecting side or a solid substance having a desired particle size or less is collected to the coarse powder collecting side with a simple structure. Classification smaller and higher classification accuracy It has become to be able to provide a location.

【0043】請求項4の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段のリング形状部材で阻止するように
すると共にリング形状部材の高さを分級室の高さの1/
2以下になるようにしたので、分級室内部の旋回流が大
きく変化して固体物質の回収率が低下することなく、簡
単な構造で、所望の粒径以上の固体物質が微粉回収側
へ、又は、所望の粒径以下の固体物質が粗粉回収側へ回
収される分級誤差が小さく分級精度が高い分級装置を提
供することが出来るようになった。
According to the fourth aspect of the present invention, the guide member is formed by the guide member for guiding the solid substance supplied by the solid substance supply means, the classifying member disposed below the guide member, the guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirling flow formed in the classification chamber. The fine powder is discharged from the center in the fine powder collection direction by the fine discharge means, and the coarse powder of the solid substance is collected by the swirling flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the coarse powder collecting direction, and the flow of the coarse powder in the fine powder collecting direction at the lower wall surface of the guide member is performed by the ring-shaped member of the coarse powder flow preventing means. So that the height of the ring-shaped member is 1 / the height of the classification chamber.
2 or less, so that the swirl flow inside the classification chamber does not greatly change and the solid matter recovery rate does not decrease. Alternatively, it is possible to provide a classification device having a small classification error and a high classification accuracy in which a solid substance having a desired particle size or less is recovered to a coarse powder recovery side.

【0044】請求項5の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段のリング形状部材で阻止するように
すると共にリング形状部材の厚さを案内部材の下部壁面
半径の30%以下になるようにしたので、分級室内部の
旋回流が大きく変化して固体物質の回収率が低下するこ
となく、簡単な構造で、所望の粒径以上の固体物質が微
粉回収側へ、又は、所望の粒径以下の固体物質が粗粉回
収側へ回収される分級誤差が小さく分級精度が高い分級
装置を提供することが出来るようになった。
According to the fifth aspect of the present invention, the guide member is formed by the guide member for guiding the solid material supplied by the solid material supply means, the classifying member disposed below the guide member, the guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirling flow formed in the classification chamber. The fine powder is discharged from the center in the fine powder collection direction by the fine discharge means, and the coarse powder of the solid substance is collected by the swirling flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the coarse powder collecting direction, and the flow of the coarse powder in the fine powder collecting direction at the lower wall surface of the guide member is performed by the ring-shaped member of the coarse powder flow preventing means. Since the thickness of the ring-shaped member is set to be 30% or less of the radius of the lower wall surface of the guide member, the swirling flow inside the classification chamber is greatly changed, and the solid matter recovery rate is reduced. No simple structure Thus, it is possible to provide a classification device in which a solid substance having a desired particle size or more is collected to a fine powder collecting side, or a solid substance having a desired particle size or less is collected to a coarse powder collecting side and the classification error is small and the classification accuracy is high. I can do it.

【0045】請求項6の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段のリング形状部材で阻止するように
すると共にリング形状部材の直径を案内部材の下部壁面
中央に形成された凸形状部の直径以上になるようにした
ので、案内部材の下部壁面に沿う旋回流が大きく変化せ
ず固体物質の動きも殆どかわらなくなることはなく、簡
単な構造で、所望の粒径以上の固体物質が微粉回収側
へ、又は、所望の粒径以下の固体物質が粗粉回収側へ回
収される分級誤差が小さく分級精度が高い分級装置を提
供することが出来るようになった。
According to the sixth aspect of the present invention, the guide member is formed by the guide member for guiding the solid material supplied by the solid material supply means, the classifying member disposed below the guide member, the guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirling flow formed in the classification chamber. The fine powder is discharged from the center in the fine powder collection direction by the fine discharge means, and the coarse powder of the solid substance is collected by the swirling flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the coarse powder collecting direction, and the flow of the coarse powder in the fine powder collecting direction at the lower wall surface of the guide member is performed by the ring-shaped member of the coarse powder flow preventing means. Since the diameter of the ring-shaped member is made larger than the diameter of the convex portion formed in the center of the lower wall surface of the guide member, the swirling flow along the lower wall surface of the guide member does not change significantly and Movement of matter The solid material with the desired particle size or more is collected to the fine powder collection side or the solid material with the desired particle size or less is collected to the coarse powder collection side with a simple structure. It has become possible to provide a highly accurate classification device.

【0046】請求項7の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段のリング形状部材で阻止するように
すると共にリング形状部材の上部外側は曲面形状部から
なるようにしたので、リング形状部材の上部の取り付け
部外側での旋回流の淀みや連続運転時の固体物質の堆積
を防止して固体物質の回収率が向上して清掃性も良く、
簡単な構造で、所望の粒径以上の固体物質が微粉回収側
へ、又は、所望の粒径以下の固体物質が粗粉回収側へ回
収される分級誤差が小さく分級精度が高い分級装置を提
供することが出来るようになった。
According to the present invention, the guide member is formed by the guide member for guiding the solid material supplied by the solid material supply means, the classifying member disposed below the guide member, the guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirling flow formed in the classification chamber. The fine powder is discharged from the center in the fine powder collection direction by the fine discharge means, and the coarse powder of the solid substance is collected by the swirling flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the coarse powder collecting direction, and the flow of the coarse powder in the fine powder collecting direction at the lower wall surface of the guide member is performed by the ring-shaped member of the coarse powder flow preventing means. The upper part of the ring-shaped member is formed with a curved surface so as to prevent stagnation of the swirling flow outside the mounting part of the upper part of the ring-shaped member and the accumulation of solid substances during continuous operation. Solid May be cleaning of the recovery rate is improved,
Provides a classification device that has a simple structure and has a small classification error and a high classification accuracy in which a solid substance with a desired particle size or more is collected to the fine powder collection side or a solid substance with a desired particle size or less is collected to the coarse powder collection side. Now you can do it.

【0047】請求項8の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段のリング形状部材で阻止するように
すると共にリング形状部材の上部内側は曲面形状部から
なるようにしたので、リング形状部材の上部の取り付け
部内側での旋回流の淀みや連続運転時の固体物質の堆積
を防止して固体物質の回収率が向上して清掃性も良く、
簡単な構造で、所望の粒径以上の固体物質が微粉回収側
へ、又は、所望の粒径以下の固体物質が粗粉回収側へ回
収される分級誤差が小さく分級精度が高い分級装置を提
供することが出来るようになった。
According to the eighth aspect of the present invention, the guide member is formed by the guide member for guiding the solid material supplied by the solid material supply means, the classifying member disposed below the guide member, the guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirling flow formed in the classification chamber. The fine powder is discharged from the center in the fine powder collection direction by the fine discharge means, and the coarse powder of the solid substance is collected by the swirling flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the coarse powder collecting direction, and the flow of the coarse powder in the fine powder collecting direction at the lower wall surface of the guide member is performed by the ring-shaped member of the coarse powder flow preventing means. The upper part of the ring-shaped member is made of a curved surface so as to prevent stagnation of the swirling flow inside the upper part of the ring-shaped member and the accumulation of solid matter during continuous operation. Solid May be cleaning of the recovery rate is improved,
Provides a classification device that has a simple structure and has a small classification error and a high classification accuracy in which a solid substance with a desired particle size or more is collected to the fine powder collection side or a solid substance with a desired particle size or less is collected to the coarse powder collection side. Now you can do it.

【0048】請求項9の発明によれば、固体物質供給手
段により供給された固体物質を案内する案内部材と案内
部材の下方に配置された分級部材と本体内の案内部材と
分級部材により形成される分級室内に形成される旋回流
により固体物質の微粉が回収される微粉回収方向の中央
部から微粉を微粉排出手段で排出し、分級室内に形成さ
れる旋回流により固体物質の粗粉が回収される粗粉回収
方向の間隙から粗粉を粗粉排出手段で排出するようにし
て、案内部材の下部壁面での粗粉の微粉回収方向への流
れを粗粉流阻止手段のリング形状部材で阻止するように
すると共に粗粉流阻止手段を着脱手段により案内部材に
着脱可能になるようにしたので、案内部材の下部壁面に
粗粉流阻止手段のリング形状部材の取り付けの切り替え
作業も短縮化され粗粉流阻止手段のリング形状部材の高
さの調整も容易に行うことが出来る、簡単な構造で、所
望の粒径以上の固体物質が微粉回収側へ、又は、所望の
粒径以下の固体物質が粗粉回収側へ回収される分級誤差
が小さく分級精度が高い分級装置を提供することが出来
るようになった。
According to the ninth aspect of the present invention, the guide member is formed by the guide member for guiding the solid substance supplied by the solid substance supply means, the classifying member disposed below the guide member, the guide member in the main body, and the classifying member. The fine powder of the solid substance is collected by the swirling flow formed in the classification chamber. The fine powder is discharged from the center in the fine powder collection direction by the fine discharge means, and the coarse powder of the solid substance is collected by the swirling flow formed in the classification chamber. The coarse powder is discharged by the coarse powder discharging means from the gap in the coarse powder collecting direction, and the flow of the coarse powder in the fine powder collecting direction at the lower wall surface of the guide member is performed by the ring-shaped member of the coarse powder flow preventing means. In addition, the coarse powder flow preventing means can be attached to and detached from the guide member by the attaching / detaching means, so that the work of switching the attachment of the ring-shaped member of the coarse powder flow preventing means to the lower wall surface of the guide member is also shortened. Is The height of the ring-shaped member of the powder flow prevention means can be easily adjusted, and the solid substance having a desired particle size or more is transferred to the fine powder collecting side or a solid substance having a desired particle size or less with a simple structure. It has become possible to provide a classification device which has a small classification error and a high classification accuracy collected to the coarse powder collection side.

【0049】請求項10の発明によれば、固体物質を粉
砕化した後に、請求項1乃至9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ようにしたので、簡単
な製造方法で、所望の粒径以上の固体物質が微粉回収側
へ、又は、所望の粒径以下の固体物質が粗粉回収側へ回
収される分級誤差が小さく分級精度が高いトナーを製造
することが出来るトナー製造方法を提供することが出来
るようになった。
According to the tenth aspect of the present invention, after the solid substance is pulverized, the toner is produced by classifying the solid substance with the classifying apparatus according to any one of the first to ninth aspects. Thus, it is possible to produce a toner having a small classification error and a high classification accuracy in which a solid substance having a desired particle size or more is collected to a fine powder collecting side or a solid substance having a desired particle size or less is collected to a coarse powder collecting side. A method for producing a toner can be provided.

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

【図1】本発明の実施の形態例を示す分級装置を説明す
る説明図である。
FIG. 1 is an explanatory diagram illustrating a classification device according to an embodiment of the present invention.

【図2】本発明の実施の形態例を示す分級装置の主要部
を説明する説明図である。
FIG. 2 is an explanatory diagram illustrating a main part of a classification device according to an embodiment of the present invention.

【図3】本発明の他の実施の形態例を示す分級装置の主
要部を説明する拡大説明図である。
FIG. 3 is an enlarged explanatory view for explaining a main part of a classification device according to another embodiment of the present invention.

【図4】本発明の他の実施の形態例を示す回収トナー分
級装置の主要部を説明する拡大説明図である。
FIG. 4 is an enlarged explanatory view illustrating a main part of a collected toner classification device according to another embodiment of the present invention.

【図5】本発明の他の実施の形態例を示す回収トナー分
級装置の主要部を説明する拡大説明図である。
FIG. 5 is an enlarged explanatory view illustrating a main part of a collected toner classification device according to another embodiment of the present invention.

【図6】従来技術の分級装置を説明する説明図である。FIG. 6 is an explanatory diagram for explaining a classifier according to the related art.

【符号の説明】[Explanation of symbols]

0 分級装置、0a 本体 1 固体物質供給手段、1a 供給管、1b 2次気体
流入口、1c 排気管、1d 分散室 2 案内部材、2a 下部壁面、2b 凸形状部 3 分級部材 4 分級室、4a 間隙、4b 間隙 5 微粉排出手段、5a 微粉排出口 6 粗粉排出手段、6a 粗粉排出口 7 粗粉流阻止手段、7a リング形状部材、7a
リング形状部材、7a リング形状部材、7a
ング形状部材、7b 曲面形状部、7c 曲面形状部、
7d 着脱手段、7d 着脱裸子、7d 着脱裸子
穴 100 分級装置、100a 本体 101 分散室 102 案内部材 103 分級板 104 分級室 105 微粉排出口 106 粗粉排出口
0 classifier, 0a main body 1 solid substance supply means, 1a supply pipe, 1b secondary gas inlet, 1c exhaust pipe, 1d dispersion chamber 2 guide member, 2a lower wall surface, 2b convex shape 3 classification member 4 classification chamber, 4a Gap 4b gap 5 fine powder discharge means, 5a fine powder discharge port 6 coarse powder discharge means, 6a coarse powder discharge port 7 coarse powder flow prevention means, 7a ring-shaped member, 7a 1
Ring-shaped member, 7a 2 ring-shaped member, 7a n ring-shaped member, 7b curved portion, 7c curved portion,
7d attachment / detachment means, 7d 1 attachment / detachment element, 7d 2 attachment / detachment hole 100 Classifier, 100a Main body 101 Dispersion chamber 102 Guide member 103 Classification plate 104 Classification chamber 105 Fine powder discharge port 106 Coarse powder discharge port

───────────────────────────────────────────────────── フロントページの続き (72)発明者 森井 和好 東京都大田区中馬込1丁目3番6号 株式 会社リコー内 (72)発明者 杉沢 英輔 東京都大田区中馬込1丁目3番6号 株式 会社リコー内 Fターム(参考) 2H005 AB04 EA05 4D021 FA25 GA02 GA03 GA05 GA06 GA08 GA18 GA29 GA30 HA01 HA10  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Kazuyoshi Morii 1-3-6 Nakamagome, Ota-ku, Tokyo Inside Ricoh Co., Ltd. (72) Eiji Sugisawa 1-3-6 Nakamagome, Ota-ku, Tokyo F-term in Ricoh Co., Ltd. (reference) 2H005 AB04 EA05 4D021 FA25 GA02 GA03 GA05 GA06 GA08 GA18 GA29 GA30 HA01 HA10

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 分級室内に旋回流を形成し、固体物質を
遠心分離して分級する分級装置において、分級すべき固
体物質を供給する固体物質供給手段と、上記固体物質供
給手段により供給された固体物質を案内する案内部材
と、上記案内部材の下方に配置された分級部材と、本体
内の上記案内部材と上記分級部材により形成される分級
室と、上記分級室内に形成される旋回流により固体物質
の微粉が回収される微粉回収方向の中央部から微粉を排
出する微粉排出手段と、上記分級室内に形成される旋回
流により固体物質の粗粉が回収される粗粉回収方向の間
隙から粗粉を排出する粗粉排出手段と、上記案内部材の
下部壁面での粗粉の微粉回収方向への流れを阻止する粗
粉流阻止手段とからなることを特徴とする分級装置。
1. A classifying device for forming a swirling flow in a classifying chamber and centrifuging and classifying a solid substance, wherein the solid substance supply means for supplying a solid substance to be classified and the solid substance supply means. A guide member for guiding the solid substance, a classifying member disposed below the guide member, a classifying chamber formed by the guide member and the classifying member in the main body, and a swirling flow formed in the classifying chamber. A fine powder discharging means for discharging fine powder from a central portion in a fine powder collecting direction in which fine powder of solid substance is collected, and a gap in a coarse powder collecting direction in which coarse powder of solid substance is recovered by a swirling flow formed in the classification chamber. A classifier comprising: a coarse powder discharging means for discharging coarse powder; and a coarse powder flow preventing means for preventing a flow of coarse powder in a direction of collecting fine powder on a lower wall surface of the guide member.
【請求項2】 請求項1記載の分級装置において、粗粉
流阻止手段は、リング形状部材からなることを特徴とす
る分級装置。
2. The classification device according to claim 1, wherein the coarse powder flow preventing means comprises a ring-shaped member.
【請求項3】 請求項1又は2記載の分級装置におい
て、粗粉流阻止手段は、複数のリング形状部材からなる
ことを特徴とする分級装置。
3. A classifier according to claim 1, wherein the coarse powder flow preventing means comprises a plurality of ring-shaped members.
【請求項4】 請求項2又は3記載の分級装置におい
て、粗粉流阻止手段のリング形状部材の高さは、分級室
の高さの1/2以下であることを特徴とする分級装置。
4. The classification device according to claim 2, wherein the height of the ring-shaped member of the coarse powder flow preventing means is equal to or less than half the height of the classification chamber.
【請求項5】 請求項2、3又は4記載の分級装置にお
いて、粗粉流阻止手段のリング形状部材の厚さは、案内
部材の下部壁面半径の30%以下であることを特徴とす
る分級装置。
5. The classification device according to claim 2, wherein the thickness of the ring-shaped member of the coarse powder flow preventing means is not more than 30% of the radius of the lower wall surface of the guide member. apparatus.
【請求項6】 請求項2、3、4又は5記載の分級装置
において、粗粉流阻止手段のリング形状部材の直径は、
案内部材の下部壁面中央に形成された凸形状部の直径以
上であることを特徴とする分級装置。
6. The classifier according to claim 2, 3, 4 or 5, wherein the diameter of the ring-shaped member of the coarse powder flow preventing means is:
A classifier characterized in that the diameter is equal to or greater than the diameter of a convex portion formed in the center of the lower wall surface of the guide member.
【請求項7】 請求項2、3、4、5又は6記載の分級
装置において、粗粉流阻止手段のリング形状部材の上部
外側は、曲面形状部からなることを特徴とする分級装
置。
7. The classifying apparatus according to claim 2, wherein an upper outer side of the ring-shaped member of the coarse powder flow preventing means comprises a curved surface portion.
【請求項8】 請求項2、3、4、5、6又は7記載の
分級装置において、粗粉流阻止手段のリング形状部材の
上部内側は、曲面形状部からなることを特徴とする分級
装置。
8. The classification device according to claim 2, wherein the inside of the upper part of the ring-shaped member of the coarse powder flow preventing means is formed of a curved surface portion. .
【請求項9】 請求項1乃至8のいずれかに記載の分級
装置において、粗粉流阻止手段は、着脱手段により案内
部材に着脱可能であることを特徴とする分級装置。
9. The classifying apparatus according to claim 1, wherein the coarse powder flow preventing means is detachable from the guide member by attaching and detaching means.
【請求項10】 電子写真方式の画像形成装置に使用す
る潜像を顕像化するトナーの製造方法において、固体物
質を粉砕化した後に、請求項1乃至9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。
10. A method for producing a toner for visualizing a latent image used in an electrophotographic image forming apparatus, comprising the steps of: A method for producing a toner, comprising producing a toner by classification.
JP6331099A 1999-03-10 1999-03-10 Classification device and method for producing toner using the same Expired - Fee Related JP3632098B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6331099A JP3632098B2 (en) 1999-03-10 1999-03-10 Classification device and method for producing toner using the same

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Publication Number Publication Date
JP2000254589A true JP2000254589A (en) 2000-09-19
JP3632098B2 JP3632098B2 (en) 2005-03-23

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ID=13225596

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Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010181868A (en) * 2009-01-07 2010-08-19 Ricoh Co Ltd Method for manufacturing toner
CN108262255A (en) * 2017-12-01 2018-07-10 共同科技开发有限公司 A kind of rotary type sieves sandbox
CN109483751A (en) * 2018-11-20 2019-03-19 禹州市华盛钧窑有限公司 A kind of anti-jamming mechanism of Ceramic manufacturing device for recovering powder

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010181868A (en) * 2009-01-07 2010-08-19 Ricoh Co Ltd Method for manufacturing toner
CN108262255A (en) * 2017-12-01 2018-07-10 共同科技开发有限公司 A kind of rotary type sieves sandbox
CN108262255B (en) * 2017-12-01 2020-10-09 安徽嘉诚建设工程有限公司 Rotary sand screening box
CN109483751A (en) * 2018-11-20 2019-03-19 禹州市华盛钧窑有限公司 A kind of anti-jamming mechanism of Ceramic manufacturing device for recovering powder

Also Published As

Publication number Publication date
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