JPH09299885A - Air current classifying device for manufacture of toner - Google Patents

Air current classifying device for manufacture of toner

Info

Publication number
JPH09299885A
JPH09299885A JP13971896A JP13971896A JPH09299885A JP H09299885 A JPH09299885 A JP H09299885A JP 13971896 A JP13971896 A JP 13971896A JP 13971896 A JP13971896 A JP 13971896A JP H09299885 A JPH09299885 A JP H09299885A
Authority
JP
Japan
Prior art keywords
raw material
classification
classifying
toner
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.)
Pending
Application number
JP13971896A
Other languages
Japanese (ja)
Inventor
Youko Goka
洋子 五箇
Hitoshi Kanda
仁志 神田
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.)
Canon Inc
Original Assignee
Canon Inc
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 Canon Inc filed Critical Canon Inc
Priority to JP13971896A priority Critical patent/JPH09299885A/en
Publication of JPH09299885A publication Critical patent/JPH09299885A/en
Pending legal-status Critical Current

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  • Developing Agents For Electrophotography (AREA)
  • Combined Means For Separation Of Solids (AREA)

Abstract

PROBLEM TO BE SOLVED: To make it possible to set a correct classification point and thereby enable high accuracy classification by using at least, part of a raw material feed pipe, a classifying edge and an air intake edge formed of a resin molding composed mainly of polybenzoimidazole, in a classifying device for classifying a pulverized raw material by the centrifugal force of a curved air current. SOLUTION: An air current classifying device for classifying powder into a particle by an air current is equipped with knife edge-type classifying edges 17, 18 on a lateral wall 23 and a lower wall 25 respectively. In addition, a coanda block 26 is installed at the lower part of a raw material feed pipe 16 with an open part in a classifying chamber 32, and the knife edge-type air intake edge 19 is provided toward the lower part of a classifying chamber 32 in the upper block 27 of the classifying chamber 32. In this case, this inner wall face of the raw material feed pipe 16, the classifying edges 17, 18 and further, the outer wall face of the air intake edge 19 are formed in resin composed mainly of plastic polybenzoimidazole. Thus the lubricity of a streaming particle is improved and the wear resistance of these parts in enhanced.

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、コアンダ効果を利
用し、静電荷像現像用トナーを製造する際に用いられる
気流式分級装置に関する。更に詳しくは、本発明は、重
量平均粒子径20μm以下の粒子を50個数%以上含有
する粉体原料を効率よく分級する気流式分級装置に関
し、特に、重量平均粒子径が8μm以下の粉体原料を効
率よく分級し得る、粉体を気流に乗せて運ぶと共に、コ
アンダ効果、前記粉体中の各粒子の粒子径に応じた慣性
力及び遠心力等の差に基づいて所定の粒度を有する粒子
に分級し、静電荷像現像用トナーを効率よく製造する為
の気流式分級装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an airflow classifying device used for producing a toner for developing an electrostatic charge image by utilizing the Coanda effect. More specifically, the present invention relates to an airflow classifier for efficiently classifying a powder raw material containing 50 number% or more of particles having a weight average particle diameter of 20 μm or less, and particularly to a powder raw material having a weight average particle diameter of 8 μm or less. The particles having a predetermined particle size based on the difference between the Coanda effect, the inertial force according to the particle size of each particle in the powder, the centrifugal force, etc. can be efficiently classified. The present invention relates to an airflow classifier for efficiently classifying toner for electrostatic image development.

【0002】[0002]

【従来の技術】電子写真法による画像形成に用いられる
トナー又は着色樹脂粉体には、通常、結着樹脂及び着色
剤又は磁性粉が少なくとも含有されている。この様なト
ナーによって、潜像担持体上に形成された静電荷像を現
像してトナー画像とし、次に、該画像を普通紙、又はプ
ラスチックフィルムの如き被転写材へと転写し、更に、
得られた転写画像を、加熱定着手段、加圧ローラ定着手
段、又は加熱加圧ローラ定着手段の如き定着装置によっ
て定着して画像が形成される。従って、トナーを形成す
る結着樹脂としては、熱及び/又は圧力が付加されると
塑性変形する特性を有する樹脂が使用される。又、上記
の様な画像形成に用いられるトナー或いはトナー用着色
樹脂粉体は、現在、主に、結着樹脂と、着色剤又は磁性
粉とを少なくとも含有する混合物(必要により、更に第
3成分を含有する)を溶融混練し、該溶融混練物を冷却
し冷却物とし、得られた冷却物を粉砕し、更に粉砕物を
分級することによって製造される。
2. Description of the Related Art Toner or colored resin powder used for image formation by electrophotography usually contains at least a binder resin and a colorant or magnetic powder. With such a toner, the electrostatic charge image formed on the latent image carrier is developed into a toner image, and then the image is transferred to a transfer material such as plain paper or a plastic film, and further,
The obtained transferred image is fixed by a fixing device such as heat fixing means, pressure roller fixing means, or heat pressure roller fixing means to form an image. Therefore, as the binder resin forming the toner, a resin having a characteristic of being plastically deformed when heat and / or pressure is applied is used. Further, the toner or the colored resin powder for toner used for the image formation as described above is currently a mixture mainly containing at least a binder resin and a colorant or a magnetic powder (and, if necessary, a third component). Is melted and kneaded, the melt-kneaded product is cooled to obtain a cooled product, the obtained cooled product is pulverized, and the pulverized product is further classified.

【0003】一方、粉体の分級については、各種の気流
式分級機及び気流式分級方法が提案されているが、この
中で回転翼を用いる分級機と可動部分を有しない分級機
がある。このうち、可動部分のない分級機として、固定
壁遠心式分級機と慣性力分級機がある。慣性力を利用す
る分級機としては、Loffier F. and K. Maly:Symposi
um on Powder Technology D-2(1981)に例示され、日鉄
鉱業製として商品化されているエルボジェット分級機
や、Okuda S.and Yasukuni J.:Proc. Inter. Symposi
um on Powder Technology'81,771(1981)で例示される分
級機が提案されている。
On the other hand, for classifying powders, various airflow classifiers and airflow classifying methods have been proposed. Among them, there are classifiers using rotary blades and classifiers having no moving parts. Among them, a classifier without a movable part includes a fixed wall centrifugal classifier and an inertial force classifier. As a classifier utilizing inertial force, Loffier F. and K. Maly: Symposi
um on Powder Technology D-2 (1981), the elbow jet classifier commercialized by Nippon Steel Mining Co., Ltd., and Okuda S. and Yasukuni J .: Proc. Inter. Symposi
A classifier exemplified by um on Powder Technology '81, 771 (1981) has been proposed.

【0004】図5及び図6に、従来の慣性力を利用した
気流式分級装置の断面図を示す。この気流式分級装置
は、粉体原料を、分級装置内の分級域に開口されている
開口部を有する原料供給管116から高速で気流と共に
分級域内へと噴出させ、噴出された気流中の粉体原料
を、粒子の慣性力及びコアンダ効果による湾曲気流の遠
心力によって分級する。即ち、図5及び図6に示した様
に、気流式分級装置の分級室132内にはコアンダブロ
ック126が設けられており、且つ噴出させる気流と角
度の交叉する気流を導入することによって、コアンダブ
ロック126に沿って流れる湾曲気流の遠心力によって
粗粉体と微粉体とに分離し、先端の細くなった分級エッ
ジ117及び118により、粗粉体と微粉体との分級、
若しくは粗粉体と中粉体と微粉体との分級を行ってい
る。この時、分級エッジ117及び118と入気エッジ
119の先端位置を調節し、それに応じて分級の為の気
流の流量を調整することにより、分級点(即ち、分級し
た粒子の大きさの境界となる点)を所定の位置に設定し
ていた。更に、粉体原料の比重及び所望の分級点に応じ
た分級エッジの先端位置を検知して移動させ、それに応
じて気流が所定流量になる様に制御していた。
FIG. 5 and FIG. 6 show cross-sectional views of a conventional airflow classifying apparatus utilizing inertial force. This airflow type classifier ejects the powder raw material at high speed into the classification area together with the airflow from a raw material supply pipe 116 having an opening that is opened in the classification area in the classification apparatus, and the powder in the ejected airflow is discharged. The body material is classified by the inertial force of the particles and the centrifugal force of the curved air flow due to the Coanda effect. That is, as shown in FIGS. 5 and 6, a Coanda block 126 is provided in the classification chamber 132 of the airflow classifier, and the Coanda block 126 is introduced to introduce the airflow whose angle intersects with the airflow to be jetted. The coarse powder and the fine powder are separated by the centrifugal force of the curved air stream flowing along the block 126, and the fine powder is classified by the classifying edges 117 and 118 having a thin tip.
Alternatively, the coarse powder, the medium powder, and the fine powder are classified. At this time, the tip positions of the classification edges 117 and 118 and the air intake edge 119 are adjusted, and the flow rate of the air flow for classification is adjusted accordingly, so that the classification point (that is, the boundary of the size of the classified particles and Point) was set at a predetermined position. Further, the tip position of the classification edge corresponding to the specific gravity of the powder raw material and the desired classification point is detected and moved, and the air flow is controlled so as to have a predetermined flow rate accordingly.

【0005】しかしながら、近年、静電荷像現像用トナ
ーのニーズとしては、省エネルギーという観点から、よ
り低い温度で結着樹脂を溶融させることが近年特に要求
されている為、溶融温度の低い結着樹脂を使用したもの
が使用されてきている。この様な樹脂が含有された粉体
原料を、上記した様な気流分級装置に導入して分級を行
う場合、原料供給管116や分級エッジ117及び11
8や入気エッジ119で生じる微小の摩擦熱や衝突熱に
よって、これらの部分に融着物や付着物を生じることに
なる。そして、連続運転時に、これらの付着と剥離が繰
り返されると、分級品の中に粗粒子となって混入し、精
度のよい分級品が得られない場合が生じ、本来であれば
大きさが均一でなければならない粒子群の中に他の粒子
群に入るべき大きさの粒子が混入してしまうという場合
があった。又、分級精度も低下する等の改善すべき問題
も生じる。
However, in recent years, as a need for a toner for developing an electrostatic image, it has been particularly required in recent years to melt the binder resin at a lower temperature from the viewpoint of energy saving. Therefore, the binder resin having a low melting temperature is required. Have been used. When the powder raw material containing such a resin is introduced into the air stream classifying apparatus as described above for classification, the raw material supply pipe 116 and the classification edges 117 and 11 are used.
The minute frictional heat or collision heat generated at 8 or the air inlet edge 119 causes a fused substance or an adhered substance at these portions. Then, during continuous operation, if these adhesion and peeling are repeated, coarse particles may be mixed into the classified product, and it may not be possible to obtain an accurate classified product. In some cases, particles having a size that should be included in another particle group are mixed into the particle group that must be. There is also a problem to be improved such as a decrease in classification accuracy.

【0006】特に、分級する際にトナー製造用の粉体材
料が激しく接触する箇所である原料供給管116、分級
エッジ117及び118、そして入気エッジ119にお
いて、トナー融着の現象が起こり易い。その様な場合、
通常、原料供給管116及び分級エッジ117及び11
8の材質を滑り性のよいもの、例えば、フッ素樹脂製に
する、或いはフッ素樹脂を表面にコーティングする等が
検討されてきた。しかし、トナー製造用の粉体材料には
磁性粉が含まれる場合もあり、かかる場合には摩耗とい
う問題が生じ、フッ素樹脂製の部材、或いはフッ素樹脂
を表面にコーティングした部材では耐摩耗性に劣る為、
使用することが出来なかった。特に、複写機やプリンタ
ー等に用いられる静電荷像現像用トナーを製造する為の
分級の際に、かかる問題が顕著であった。そこで、耐融
着性や耐摩耗性の両方を満足し得る分級装置の開発が望
まれている。
In particular, the phenomenon of toner fusion is likely to occur at the raw material supply pipe 116, the classification edges 117 and 118, and the air intake edge 119, which are locations where the powder material for toner production comes into heavy contact during classification. In such a case,
Usually, the raw material supply pipe 116 and the classification edges 117 and 11
It has been considered that the material of No. 8 has a good slipperiness, for example, it is made of fluororesin, or the surface is coated with fluororesin. However, magnetic powder is sometimes contained in the powder material for toner production, and in such a case, a problem of abrasion occurs, and a member made of fluororesin or a member whose surface is coated with fluororesin has abrasion resistance. Inferior,
I couldn't use it. In particular, such a problem was remarkable in the classification for producing the electrostatic charge image developing toner used in a copying machine, a printer or the like. Therefore, it is desired to develop a classifying device that can satisfy both fusion resistance and wear resistance.

【0007】一般に、トナーには数多くの異なった性質
が要求され、かかる要求性質を得る為には、使用する粉
体原料は勿論のこと、トナーの特性が製造方法によって
影響されることも多い。例えば、トナーを製造する為の
分級工程においては、分級された粒子群がシャープな粒
度分布を有することが要求される。又、低コストで効率
よく安定的に品質のよいトナーを作り出すことが望まれ
ている。
Generally, toners are required to have many different properties, and in order to obtain such required properties, not only the powder raw material used but also the properties of the toner are often influenced by the manufacturing method. For example, in a classification process for producing a toner, classified particle groups are required to have a sharp particle size distribution. Further, it is desired to efficiently and stably produce high-quality toner at low cost.

【0008】又、近年、例えば、複写機の省エネルギー
対策として、圧力によって被転写材にトナー画像を定着
する為にトナーの結着樹脂としてワックスの様な軟質の
ものを使用したり、加熱式定着の場合であっても、定着
スピードを速くしたり、定着に要する消費電力を少なく
且つ低温で定着させる為に、低ガラス転移点の、又は、
低軟化点、低融点の結着樹脂をトナーに使用する様にな
ってきている。この様な樹脂を含有するトナーの粉体原
料を前記した従来の分級装置に導入して分級すると、特
に分級装置内での付着や融着が発生し易かった。
Further, in recent years, for example, as an energy saving measure for a copying machine, a soft binder such as wax is used as a binder resin of toner in order to fix a toner image on a transfer material by pressure, or a heat fixing method is used. Even in the case of, in order to increase the fixing speed or to fix at a low temperature with low power consumption required for fixing, a low glass transition point, or
Binder resins having a low softening point and a low melting point have been used for toners. When the powder raw material of the toner containing such a resin is introduced into the above-described conventional classifying device and classified, adhesion and fusion are particularly likely to occur in the classifying device.

【0009】更には、近年、複写機やプリンターにおけ
る画質向上の為に、トナー粒子が徐々に微細化の方向に
進んで来ている。一般に、物質は細かくなるに従い粒子
間力の働きが大きくなっていくが、樹脂粒子やトナー粒
子も同様で、微小サイズになると粒子同士の凝集性が大
きくなっていき、凝集体を生じ易い。又、粒子同士の質
量差も小さくなっていく。この様な凝集体に、分級の際
の衝撃力や摩擦力等の外力が働くと、粒子が分級装置内
に融着し易い。特に、分級エッジ先端部分への融着が起
こり易く、この様な現象が発生すると分級精度が悪化
し、安定した状態で分級装置が稼働しなくなる為、長期
にわたり安定的に良質の分級品を得ることが困難とな
る。
Further, in recent years, in order to improve image quality in copying machines and printers, toner particles are gradually becoming finer. Generally, as the substance becomes finer, the action of interparticle force increases, but the same applies to resin particles and toner particles, and when the substance has a small size, the cohesiveness of the particles increases, and aggregates are likely to occur. Further, the mass difference between the particles also becomes smaller. When an external force such as an impact force or a frictional force at the time of classification acts on such an agglomerate, the particles are easily fused in the classifier. In particular, fusion is likely to occur at the tip of the classification edge, and if such a phenomenon occurs, the classification accuracy will deteriorate and the classifier will not operate in a stable state, so a stable, high-quality classified product can be obtained over a long period of time. Becomes difficult.

【0010】特に、重量平均粒子径が10μm以下のト
ナー製造用の粉体原料から、シャープな粒度分布を有す
るトナーを得ようとする場合には、従来の装置では分級
収率の低下を引き起こす。更に、重量平均粒子径が8μ
m以下のトナー製造用粉体原料からシャープな粒度分布
を有するトナーを得ようとする場合には、従来の装置で
は分級収率の低下を引き起こすことが一層顕著となる。
この様な点から、微粉体、特にトナー如き樹脂微粉体を
安定的、且つ効率的に分級する静電荷像現像用トナーを
製造する為の気流式分級装置が望まれている。特に、重
量平均粒子径8μm以下のトナーを安定的、且つ効率的
に分級する為の気流式分級装置が待望されている。
In particular, when a toner having a sharp particle size distribution is to be obtained from a powder raw material for producing a toner having a weight average particle diameter of 10 μm or less, a conventional apparatus causes a reduction in classification yield. Furthermore, the weight average particle size is 8μ.
When a toner having a sharp particle size distribution is to be obtained from a powder raw material for producing a toner having a particle size of m or less, it becomes more remarkable that the conventional apparatus causes a decrease in classification yield.
From this point of view, there is a demand for an airflow classifying apparatus for producing a toner for developing an electrostatic charge image, which classifies fine powder, particularly resin fine powder such as toner, stably and efficiently. In particular, an airflow type classifying device for stably and efficiently classifying a toner having a weight average particle diameter of 8 μm or less is desired.

【0011】[0011]

【発明が解決しようとする課題】従って、本発明の目的
は、上記した各種の問題点が解決された静電荷像現像用
トナーを製造し得る気流式分級装置を提供することにあ
る。即ち、本発明の目的は、正確な分級点を設定し、こ
れを保持することにより、より高精度の分級を可能に
し、精緻な粒度分布を有する粉体を効率よく生成し得る
静電荷像現像用トナーを製造する気流式分級装置、特
に、装置内で粉体原料の融着や部材の摩耗を有効に防止
することによって、装置内での分級点の変動を抑制し、
安定的な分級を可能とする静電荷像現像用トナーを製造
する為の気流式分級装置を提供することにある。
SUMMARY OF THE INVENTION It is, therefore, an object of the present invention to provide an air flow type classifying apparatus capable of producing an electrostatic charge image developing toner in which the above-mentioned various problems are solved. That is, an object of the present invention is to set an accurate classification point and hold it to enable more accurate classification, and electrostatic charge image development capable of efficiently producing powder having a fine particle size distribution. Air flow type classifying device for producing toner for use, in particular, by effectively preventing the fusion of the powder raw material and the wear of the members in the device, the fluctuation of the classification point in the device is suppressed,
An object of the present invention is to provide an air flow type classification device for producing a toner for developing an electrostatic charge image that enables stable classification.

【0012】更に、本発明の他の目的は、長時間稼働し
ても分級装置内に付着物が発生することのない静電荷像
現像用トナーを製造する為の気流式分級装置を提供する
ことにある。又、本発明の目的は、重量平均粒子径が1
0μm以下のトナー製造用の粉体原料から、特に、重量
平均粒子径が8μm以下のトナー製造用の粉体原料から
シャープな粒度分布を有する静電荷像現像用トナーを効
率よく得ることが出来る気流式分級装置を提供すること
にある。
Still another object of the present invention is to provide an air flow type classifying apparatus for producing a toner for developing an electrostatic charge image which does not cause deposits in the classifying apparatus even when operated for a long time. It is in. Further, an object of the present invention is that the weight average particle diameter is 1
An air flow that can efficiently obtain a toner for electrostatic image development having a sharp particle size distribution from a powder raw material for toner production having a particle size of 0 μm or less, particularly a powder raw material for toner production having a weight average particle size of 8 μm or less. The purpose is to provide a classifier.

【0013】[0013]

【課題を解決するための手段】上記目的は、以下の本発
明により達成される。即ち、本発明は、トナー製造用粉
体原料を気流によって分級する為の気流式分級装置であ
って、少なくともコアンダブロック、個壁ブロック及び
複数の分級エッジにより形成された分級域が設けられて
おり、該分級域に分級装置内に開口部を有する原料供給
管中を流動する気流によって粉体原料を噴出させ、噴出
された気流中の粉体原料を、粒子の慣性力及びコアンダ
効果による湾曲気流の遠心力によって複数の粒子径の異
なる粒体群に分級させる気流式分級装置において、粉体
原料の比重、目標分級点及び原料供給速度に合わせ、原
料供給管、分級エッジ及び入気エッジの少なくとも一部
がプラスチック系ポリベンゾイミダゾールを主成分とす
る樹脂成形品、又はプラスチック系ポリベンゾイミダゾ
ールを主成分とする樹脂で表面がコーティングされた部
材によって構成されていることを特徴とする気流式分級
装置。
The above object is achieved by the present invention described below. That is, the present invention is an air flow type classification device for classifying a powder raw material for toner production by an air flow, which is provided with at least a Coanda block, individual wall blocks and a classification area formed by a plurality of classification edges. The powder raw material is jetted by an air flow flowing in a raw material supply pipe having an opening in the classifying device in the classification area, and the powder raw material in the jetted air flow is curved air flow due to the inertial force of the particles and the Coanda effect. In the airflow type classifying device for classifying into a plurality of particle groups having different particle sizes by the centrifugal force of, at least the specific gravity of the powder raw material, the target classification point and the raw material supply speed, the raw material supply pipe, the classification edge and the intake edge A part is a resin molded product whose main component is plastic-based polybenzimidazole, or a resin whose main component is plastic-based polybenzimidazole Air classifier, characterized by being constituted by a ring has been member.

【0014】[0014]

【発明の実施の形態】以下に、本発明のトナー製造用気
流式分級装置を添付図面に基づいて詳細に説明する。図
1に、本発明の気流式分級装置の一例として、3分割の
場合の分級装置の断面図を示し、図2に、その斜視図を
示す。これらの図からわかる様に、本発明のトナー製造
用気流式分級装置は、基本的な構成は、先に説明した従
来のものと同様である。
BEST MODE FOR CARRYING OUT THE INVENTION The airflow classifying apparatus for producing toner according to the present invention will be described in detail below with reference to the accompanying drawings. FIG. 1 shows a sectional view of a classifying device in the case of dividing into three parts as an example of the airflow type classifying device of the present invention, and FIG. 2 shows a perspective view thereof. As can be seen from these figures, the basic structure of the airflow type classification apparatus for toner production of the present invention is the same as the conventional one described above.

【0015】図1及び図2において、側壁は、22、2
3及び24で示される形状を有し、下部壁は25で示さ
れる形状を有し、側壁23と下部壁25にはそれぞれナ
イフエッジ型の分級エッジ17及び18を具備してお
り、この分級エッジ17及び18よって分級室32の分
級ゾーンは3分画されている。側壁22の下の部分に
は、分級室32に開口部を有する原料供給管16が設け
られており、該原料供給管16の下部には、底部接線の
延長方向に対して下方に折り曲げて長楕円弧を描いたコ
アンダブロック26が設置されている。分級室32の上
部にある上部ブロック27には、分級室32の下部方向
に向けてナイフエッジ型の入気エッジ19が具備され、
更に分級室32の上部には、分級室に開口する入気管1
4及び15を設けられている。又、入気口14及び15
には、ダンパーの如き第1及び第2の気体導入調節手段
20及び21と静圧計28及び29が設けられている。
分級エッジ17及び18の位置は、被分級処理原料であ
る粉体原料の種類により、又、所望する粒子径により、
夫々のエッジの軸17a及び18aを回動させることに
よって適宜に調節される。
In FIGS. 1 and 2, the side walls are 22, 2
3 and 24, the lower wall has a shape shown by 25, and the side wall 23 and the lower wall 25 are provided with knife-edge type classification edges 17 and 18, respectively. 17 and 18, the classification zone of the classification chamber 32 is divided into three. A raw material supply pipe 16 having an opening in a classification chamber 32 is provided at a lower portion of the side wall 22, and a lower portion of the raw material supply pipe 16 is bent downward in a direction in which a bottom tangent line extends and is long. A Coanda block 26 that draws an elliptic arc is installed. The upper block 27 above the classification chamber 32 is provided with a knife-edge type air intake edge 19 toward the lower part of the classification chamber 32.
Further, at the upper part of the classification chamber 32, an intake pipe 1 opening to the classification chamber
4 and 15 are provided. Also, the air inlets 14 and 15
The first and second gas introduction adjusting means 20 and 21 such as dampers and the static pressure gauges 28 and 29 are provided in the.
The positions of the classification edges 17 and 18 depend on the type of powder raw material that is the raw material to be classified and the desired particle size.
It is adjusted appropriately by rotating the shafts 17a and 18a of the respective edges.

【0016】分級室32の底面には、夫々の分画域に対
応させて、分級室32内に開口した排出口11、12及
び13が設けられている。排出口11、12及び13に
は、パイプの如き連通手段が接続されており、これらの
連通手段には、夫々にバルブ手段の如き開閉手段を設け
てもよい。原料供給管16は、直管筒部36と角錐筒部
35から成っており、直管筒部36の内径と角錐筒部3
5の最も狭い箇所の内径との比を20:1〜1:1、好
ましくは10:1〜2:1に設定すると、良好な導入速
度が得られる。これらの形状及び設置方法は処理される
粉体原料の性状により決定すればよく、限定されるもの
ではない。上記の様な本発明の気流式分級装置は、トナ
ー製造用の粉体原料を分級する場合においては、粉体原
料の重量粒子径は10μm以下の場合に効果的であり、
特に、8μm以下の場合に一層効果的である。
The bottoms of the classification chamber 32 are provided with discharge ports 11, 12 and 13 which are opened in the classification chamber 32 so as to correspond to the respective fractionation areas. A communication means such as a pipe is connected to the discharge ports 11, 12 and 13, and each of these communication means may be provided with an opening / closing means such as a valve means. The raw material supply pipe 16 is composed of a straight pipe cylinder portion 36 and a pyramidal cylinder portion 35. The inner diameter of the straight pipe cylinder portion 36 and the pyramidal cylinder portion 3 are formed.
When the ratio of the inner diameter of the narrowest part of 5 to 20: 1 to 1: 1, preferably 10: 1 to 2: 1 is set, a good introduction speed can be obtained. These shapes and installation methods may be determined according to the properties of the powder raw material to be treated, and are not limited. The airflow classifier of the present invention as described above is effective in classifying powder raw materials for toner production, when the weight particle size of the powder raw materials is 10 μm or less,
Particularly, it is more effective when the thickness is 8 μm or less.

【0017】又、粉体原料を気流と共に原料供給管16
へと投入する手段としては、0.1〜3kg/cm2
圧を加えて送る方法、分級ゾーンの下流側にある送風機
を大型化し分級ゾーンの負圧をより大きくすることで外
気と粉体原料とを自然に吸引する方法、或いは、粉体原
料投入口にインジェクションフィーダーを装着し、これ
によって粉体原料と外気を吸引せしめると共に原料供給
管16を経て分級室32へ送る方法、等がある。本発明
においては、上記3つの粉体原料の投入手段のうち、分
級室32の負圧を大きくして外気と粉体原料とを自然に
吸引する方法、及びインジェクションフィーダーによる
方法が、装置面や運転条件にも特に好ましい影響が出て
くる為、好ましい。
Further, the raw material supply pipe 16 is used together with the powder raw material for the air flow.
As a means for feeding into the air, a method of sending by applying a pressure of 0.1 to 3 kg / cm 2 and an air blower on the downstream side of the classification zone are enlarged to increase the negative pressure in the classification zone to increase the outside air and powder. There is a method of naturally sucking the raw material, or a method of attaching an injection feeder to the powder raw material input port to suck the powder raw material and the outside air and sending it to the classification chamber 32 through the raw material supply pipe 16. . In the present invention, among the above-mentioned three powder raw material charging means, the method of increasing the negative pressure in the classification chamber 32 to naturally suck the outside air and the powder raw material, and the method using the injection feeder are This is preferable because it has a particularly favorable influence on the operating conditions.

【0018】以上の様な構成を有する気流式分級装置の
多分割分級域での分級操作は、例えば次の様にして行
う。先ず、排出口11、12及び13の少なくとも1つ
を介して分級室32内を減圧にし、この減圧によって生
じる分級室32内に開口している原料供給管16内を流
動する気流によって、好ましくは流速50〜300m/
秒の速度で粉体原料を原料供給管16を介して分級室3
2内に供給する。次に、供給された粉体原料は、コアン
ダブロック26の作用によるコアンダ効果と、その際に
流入する空気の如き気体の作用とにより湾曲線30を描
いて移動し、夫々粒子の粒子径及び慣性力の大小に応じ
て、大きい粒子(粗粒子)は気流の外側、即ち、分級エ
ッジ18の左側の第1分画に、中間の大きさの粒子(規
格内粒子径の粒子)は分級エッジ17と18との間の第
2分画に、小さい粒子(規格粒子径以下の粒子)は分級
エッジ17の右側の第3分画に夫々分割され、大きい粒
子は排出口11より、中間の大きさの粒子は排出口12
より、そして小さい粒子は排出口13よりそれぞれ排出
される。
The classification operation in the multi-division classification zone of the airflow type classification device having the above-mentioned structure is carried out, for example, as follows. First, the inside of the classifying chamber 32 is decompressed through at least one of the outlets 11, 12 and 13, and it is preferable that the air flow flowing in the raw material supply pipe 16 opening in the classifying chamber 32 caused by this depressurization causes Flow velocity 50-300m /
The powder material is classified at a rate of 2 seconds through the material supply pipe 16
Supply within 2. Next, the supplied powder raw material moves along the curved line 30 by the Coanda effect due to the action of the Coanda block 26 and the action of gas such as air flowing in at that time, and the particle diameter and the inertia of the particles are respectively generated. Depending on the magnitude of the force, large particles (coarse particles) are on the outside of the air flow, that is, on the first fraction on the left side of the classification edge 18, and particles of intermediate size (particles with a standard particle size) are on the classification edge 17. In the second fraction between No. 18 and 18, small particles (particles having a standard particle size or less) are respectively divided into the third fraction on the right side of the classification edge 17, and large particles have an intermediate size from the outlet 11. Particles are discharged from the outlet 12
The smaller and smaller particles are discharged from the discharge port 13, respectively.

【0019】本例による粉体原料の分級において、分級
点は、粉体が分級室32内へ飛び出す位置であるコアン
ダブロック26の左端部分に対する分級エッジ17及び
18の先端位置、入気エッジ19の先端位置によって主
に決定される。更に、分級点は、分級気流の流量或いは
原料供給管16からの粉体原料の噴出速度等によっても
影響を受ける。
In the classification of the powder raw material according to this example, the classification points are the tip positions of the classification edges 17 and 18 and the air intake edge 19 with respect to the left end portion of the Coanda block 26 where the powder jumps out into the classification chamber 32. It is mainly determined by the tip position. Further, the classification point is also affected by the flow rate of the classification air flow, the ejection speed of the powder raw material from the raw material supply pipe 16, and the like.

【0020】本発明の気流式分級装置において、分級室
32内に粉体原料が導入されると、粉体中の粒子の大き
さに応じて分散して粒子流が形成されるので、その流線
に沿って粗粒子からなる粗粉体群と、規格内粒子径の粒
子からなる中粉体群とを分画する分級エッジ18の位置
を変更すれば、所定の分級点に設定することが出来る。
即ち、分級エッジ17及び18を移動させることによっ
て、分級エッジ17及び18の向きをコアンダブロック
26に沿って飛翔する粒子群の流れ方向に合わせれば、
精度のよい分級が可能となる。
In the gas stream classifier of the present invention, when the powder raw material is introduced into the classifying chamber 32, a particle flow is formed by being dispersed according to the size of the particles in the powder. By changing the position of the classification edge 18 that separates the coarse powder group consisting of coarse particles and the medium powder group consisting of particles having the standard particle size along the line, it is possible to set a predetermined classification point. I can.
That is, by moving the classification edges 17 and 18 so that the orientations of the classification edges 17 and 18 are aligned with the flow direction of the particle group flying along the Coanda block 26,
It enables accurate classification.

【0021】図4に、図1の気流式分級装置の分級域部
の拡大図を示し、以下、これについて説明する。例え
ば、原料供給管16の先端開口部の下部に対応するコア
ンダブロック26中の、例えば、図中に示した位置Oを
基点とし、点Oと夫々のエッジの先端とを結んだ場合、
先ず、分級エッジ17の先端とコアンダブロック26の
壁面との距離aは、分級エッジ17の先端を軸17aを
中心に回動させることによって調節可能である。同様に
分級エッジ18の先端とコアンダブロック26の壁面と
の距離bは、分級エッジ18の先端を軸18aを中心と
して回動させるこにより調節可能である。更に、入気エ
ッジ19の先端とコアンダブロック26の側面との距離
cも、同様に入気エッジ19先端を軸19aを中心とし
て回動させることにより調節可能である。これらの結
果、分級室32の分級域の形状を任意に変化させて分級
点を容易に調整することによって、精度のよい分級が可
能となる。
FIG. 4 shows an enlarged view of the classification area of the airflow type classification apparatus of FIG. 1, which will be described below. For example, when a point O in the Coanda block 26 corresponding to the lower portion of the tip opening of the raw material supply pipe 16 is connected as a base point, and the point O is connected to the tip of each edge,
First, the distance a between the tip of the classification edge 17 and the wall surface of the Coanda block 26 can be adjusted by rotating the tip of the classification edge 17 around the shaft 17a. Similarly, the distance b between the tip of the classification edge 18 and the wall surface of the Coanda block 26 can be adjusted by rotating the tip of the classification edge 18 about the shaft 18a. Further, the distance c between the tip of the air intake edge 19 and the side surface of the Coanda block 26 can be adjusted by rotating the tip of the air intake edge 19 about the shaft 19a. As a result of these, by accurately changing the shape of the classification area of the classification chamber 32 and adjusting the classification point, accurate classification can be performed.

【0022】しかしながら、上記の様な分級域を有する
分級装置内では粉体原料は高速で移動する為、粉体原料
が接する面において、瞬間的に高熱になり、トナー融着
という問題が発生する。特に、トナー粒子が流動してい
く軌跡上にある原料供給管16の壁面、分級エッジ17
及び18の壁面部分、更には入気エッジ19の壁面部分
においては、その問題が一層顕著である。
However, since the powder raw material moves at a high speed in the classifying device having the above-mentioned classification area, the surface which the powder raw material comes into contact with is instantaneously heated to a high temperature, causing a problem of toner fusion. . In particular, the wall surface of the raw material supply pipe 16 and the classification edge 17 on the trajectory of the toner particles flowing.
The problem is more remarkable in the wall surface portions of Nos. 18 and 18, and further in the wall surface portion of the intake edge 19.

【0023】そこで、本発明のトナー製造用気流式分級
装置においては、これらの壁面へのトナー融着の問題を
解決する為、特に原料供給管16の内壁面、分級エッジ
17及び18、更に入気エッジ19の外壁面を、プラス
チック系ポリベンゾイミダゾールを主成分とする樹脂で
構成し、上記問題の解決を図る。即ち、これらの部材
を、プラスチック系ポリベンゾイミダゾールを主成分と
する樹脂成形品で構成するか、若しくはプラスチック系
ポリベンゾイミダゾールを主成分とする樹脂を表面にコ
ーティングした部材で構成することにより、上記問題点
が解決される。即ち、この様な構成を採ることにより、
原料供給管16の内面、分級エッジ17及び18や入気
エッジ19の表面において、優れた摺動特性が得られ、
流動する粒子の滑り性がよくなり、且つ耐摩耗性をも満
足することが出来る。特に、トナー用の粉体原料を製造
する場合において、これらの部材の壁面におけるトナー
融着物の発生が抑えられ、且つ装置を構成する部材の摩
耗をも低減させることが出来る。
Therefore, in order to solve the problem of toner fusion to these wall surfaces, the air flow classifying apparatus for toner production according to the present invention, in particular, the inner wall surface of the raw material supply pipe 16, the classification edges 17 and 18, and further includes The outer wall surface of the air edge 19 is made of a resin containing plastic-based polybenzimidazole as a main component to solve the above problem. That is, by configuring these members with a resin molded product containing plastic-based polybenzimidazole as a main component, or with a member whose surface is coated with a resin containing plastic-based polybenzimidazole as a main component, The problem is solved. That is, by adopting such a configuration,
Excellent sliding characteristics are obtained on the inner surface of the raw material supply pipe 16, the classification edges 17 and 18 and the surface of the air intake edge 19,
Sliding property of flowing particles is improved, and abrasion resistance can be satisfied. In particular, in the case of producing a powder raw material for toner, it is possible to suppress the generation of toner fusion products on the wall surfaces of these members, and it is possible to reduce the wear of the members constituting the apparatus.

【0024】本発明においては、原料供給管16、分級
エッジ17及び18、更に入気エッジ19の構成部材と
して、プラスチック系ポリベンゾイミダゾール樹脂を主
成分とする樹脂成形品を用いてもよいし、又、金属材料
等の表面にプラスチック系ポリベンゾイミダゾール樹脂
を主成分とする樹脂をコーティングした部材を用いても
よい。これは、使用する状況に応じて、適宜選択すれば
よい。
In the present invention, a resin molded product containing a plastic polybenzimidazole resin as a main component may be used as the constituent members of the raw material supply pipe 16, the classification edges 17 and 18, and the air intake edge 19. Further, a member in which the surface of a metal material or the like is coated with a resin containing a plastic polybenzimidazole resin as a main component may be used. This may be appropriately selected depending on the situation of use.

【0025】又、上記のプラスチック系ポリベンゾイミ
ダゾール樹脂を主成分とする樹脂としては、該樹脂を単
独で用いてもよいが、例えば、使用するトナー製造用の
粉体原料の材料特性等に応じて、適宜、その他の材料を
プラスチック系ポリベンゾイミダゾール樹脂にブレンド
して用いてもよい。尚、本発明で使用するポリベンゾイ
ミダゾール樹脂は、ベンゾイミダゾール環を有する耐熱
性高分子の総称であって、例えば、ポリ−p−フェニレ
ンベンゾイミダゾールやポリアルキレンベンゾイミダゾ
ールがある。又、上記した部材にプラスチック系ポリベ
ンゾイミダゾール樹脂を主成分とする樹脂をコーティン
グする方法としては種々の方法があるが、例えば、樹脂
を適当な溶剤に溶解せしめ部材表面に塗布する方法や、
樹脂を部材表面に直接熱溶融接着する、或いはプラスチ
ック系樹脂含有テープを部材の該当部分に添付する等の
公知の方法を用いればよい。
As the resin containing the above-mentioned plastic-based polybenzimidazole resin as a main component, the resin may be used alone. For example, it depends on the material characteristics of the powder raw material for toner production to be used. Therefore, other materials may be appropriately blended with the plastic-based polybenzimidazole resin and used. The polybenzimidazole resin used in the present invention is a general term for heat-resistant polymers having a benzimidazole ring, and examples thereof include poly-p-phenylenebenzimidazole and polyalkylenebenzimidazole. Further, there are various methods for coating the above-mentioned member with a resin containing a plastic-based polybenzimidazole resin as a main component, for example, a method of dissolving the resin in an appropriate solvent and applying it on the surface of the member,
A publicly known method such as directly heat-melting and adhering a resin to the surface of a member or attaching a plastic resin-containing tape to a corresponding portion of the member may be used.

【0026】更に、本発明においては、排出口11、1
2及び13を介しての減圧による吸引流の流量を調整す
ることで粒子の飛翔速度を増加させて分級域での粉体の
分散をより向上させ、より高い粉塵濃度でも良好な分級
精度が得られ、製品の収率の低下を防止することができ
るだけでなく、同じ粉塵濃度の場合に、より良好な分級
精度で、且つ製品の収率を向上させることが可能とな
る。
Further, in the present invention, the discharge ports 11, 1 are
By adjusting the flow rate of the suction flow due to the reduced pressure via 2 and 13, the flight speed of particles is increased to improve the dispersion of powder in the classification area, and good classification accuracy is obtained even at higher dust concentrations. Therefore, it is possible not only to prevent the product yield from decreasing but also to improve the product yield with better classification accuracy when the dust concentration is the same.

【0027】本発明の気流式分級装置は、上記の構成の
他、その形状や構成材料、或いはこれを用いる装置シス
テム等によって何ら限定されるものではなく、処理され
る粉体原料の性状により適宜に決定すればよい。又、本
発明の気流式分級装置は、特に、トナー製造用の粉体原
料を分級する場合において、粉体原料の重量粒子径が1
0μm以下の場合に効果的であり、更に、粉体原料の重
量粒子径が8μm以下の場合に一層効果的である。
The airflow classifying apparatus of the present invention is not limited to the above-mentioned constitution, its shape and constituent materials, the apparatus system using the same, etc., and may be appropriately selected depending on the properties of the powder raw material to be treated. You can decide to. Further, the airflow classifying apparatus of the present invention has a weight particle size of 1 when the powder raw material for toner production is classified.
It is effective when it is 0 μm or less, and is more effective when the weight particle size of the powder raw material is 8 μm or less.

【0028】本発明の気流式分級装置は、通常、相互の
機器をパイプの如き連通手段で連結して一体装置システ
ムとして使用する。そうした一体装置システムの好まし
い例を図3に示す。図3に示す一体装置システムは、本
発明の気流式分級装置の一例である3分割分級装置1
(図1及び2に示されるもの。詳細は既に説明の通りで
ある。)、定量供給機2、振動フィーダー3、捕集サイ
クロン4、5及び6を適当な連通手段で連結してなるも
のである。
The airflow classifier according to the present invention is usually used as an integrated device system by connecting mutual devices by a communicating means such as a pipe. A preferred example of such an integrated device system is shown in FIG. The integrated device system shown in FIG. 3 is a three-division classifier 1 which is an example of the airflow classifier of the present invention.
(Shown in FIGS. 1 and 2; details have already been described). The constant quantity feeder 2, the vibration feeder 3, and the collecting cyclones 4, 5 and 6 are connected by an appropriate communicating means. is there.

【0029】この一体装置システムにおいて、先ず粉体
原料は、適宜の手段により定量供給機2に送り込まれ、
次いで振動フィーダー3を介して原料供給管16により
3分割分級装置1内へと導入される。このとき、粉体原
料は、50〜300m/秒程度の流速で3分割分級装置
1内に導入される。3分割分級装置1の分級室32の大
きさは、通常[10〜50cm]×[10〜50cm]
程度とされているので、粉体原料が0.1秒以下、或い
は0.01秒以下の瞬時に3種以上の粒子群に分割され
る。例えば、図3に示した例では、3分割分級装置1に
よって、大きい粒子(粗粒子)、中間の大きさの粒子
(規定内粒子径の粒子)、小さい粒子(規定粒子径以下
の粒子)に夫々分割される。その後、大きい粒子は排出
口11を介して系外に排出され、捕集サイクロン6で粗
粉体として回収される。中間の大きさの粒子は排出口1
2を介して系外に排出され、捕集サイクロン5で製品
(トナー)になるべく回収される。小さい粒子は排出口
13を介して系外に排出され、捕集サイクロン4で微粉
体として回収される。上記で説明した例では、捕集サイ
クロン4、5及び6は、粉体原料を原料供給管16を介
して分級室32に吸引導入する為の吸引減圧手段として
の働きをしている。
In this integrated device system, first, the powder raw material is fed to the constant quantity feeder 2 by an appropriate means,
Then, the raw material supply pipe 16 is introduced into the three-division classifier 1 through the vibrating feeder 3. At this time, the powder raw material is introduced into the three-division classifier 1 at a flow rate of about 50 to 300 m / sec. The size of the classification chamber 32 of the three-division classification device 1 is usually [10 to 50 cm] × [10 to 50 cm].
The powder raw material is instantly divided into three or more kinds of particle groups for 0.1 seconds or less, or 0.01 seconds or less. For example, in the example shown in FIG. 3, the three-division classifier 1 converts the particles into large particles (coarse particles), intermediate particles (particles having a prescribed particle diameter), and small particles (particles having a prescribed particle diameter or less). Each is divided. After that, the large particles are discharged to the outside of the system through the discharge port 11 and recovered as coarse powder by the collecting cyclone 6. Particles of medium size are outlet 1
It is discharged to the outside of the system through 2 and is collected as much as a product (toner) by the collecting cyclone 5. The small particles are discharged out of the system through the discharge port 13 and are collected as fine powder by the collection cyclone 4. In the example described above, the collection cyclones 4, 5 and 6 function as suction decompression means for sucking and introducing the powder raw material into the classification chamber 32 via the raw material supply pipe 16.

【0030】本発明の気流式分級装置は、特に電子写真
法による画像形成に用いられるトナー又は着色樹脂粉体
を分級する場合に有効に用いられる。特に、低融点、低
軟化点、或いは低ガラス転移点を有する結着樹脂からな
るトナー組成物を分級する場合に有効である。この様な
樹脂が用いられているトナー製造用の粉体原料を従来の
分級装置にて分級すると、分級エッジ先端に融着物が発
生し易く、融着物の発生によって分級点が適切な範囲か
ら外れる傾向にある。この場合に、吸引減圧による流量
調節を行ったとしても要求される粉体の粒度分布は得ら
れにくく、分級効率が大幅に低下することが生じる。
又、分級した粉体の中に融着物が混入し、品質のよい製
品が得られなくなるという問題もあり、従来の分級装置
では、品質が一定の製品を得る為に、長時間安定的に稼
動させることは難しかった。
The airflow classifier of the present invention is effectively used especially for classifying toner or colored resin powder used for image formation by electrophotography. In particular, it is effective when classifying a toner composition composed of a binder resin having a low melting point, a low softening point, or a low glass transition point. When a powder raw material for toner production using such a resin is classified by a conventional classifying device, a fused substance is easily generated at the tip of the classification edge, and the classification point is out of an appropriate range due to the generation of the fused substance. There is a tendency. In this case, even if the flow rate is adjusted by suction decompression, it is difficult to obtain the required particle size distribution of the powder, and the classification efficiency may be significantly reduced.
In addition, there is a problem that fused materials are mixed in the classified powder, and it becomes impossible to obtain high-quality products. With conventional classification equipment, stable operation for a long time is required to obtain products of constant quality. It was difficult to get me to do it.

【0031】これに対し、本発明の気流式分級装置を用
いることによって、分級エッジ先端及び近傍での融着が
防止又は抑制される為、分級収率が良好になり、且つ高
精度な分級が出来る。又、本発明の気流式分級装置は、
分級装置内に融着物や付着物が殆ど発生しない為、長時
間の稼動が可能となり、分級処理を長時間にわたり安定
的に行うことが出来る。
On the other hand, by using the airflow classifier of the present invention, fusion at the tip of the classification edge and in the vicinity thereof is prevented or suppressed, so that the classification yield is improved and highly accurate classification is achieved. I can. Further, the airflow type classification device of the present invention,
Almost no fused substances or deposits are generated in the classifying device, so that it is possible to operate for a long time, and the classification process can be stably performed for a long time.

【0032】例えば、本発明の気流式分級装置を用いて
粉体原料を分級すれば、特に重量平均粒子径が10μm
以下のトナー製造用の粉体原料からシャープな粒度分布
を有するトナーを得ることが出来、従来に比べ効率よく
分級を行うことが可能となる。特に、本発明の気流式分
級装置を用いれば、重量平均粒子径が8μm以下のトナ
ー製造用の粉体原料からシャープな粒度分布を有するト
ナーを得ることが出来る。この為、ジェット・ミルによ
り粉砕する粉体原料の処理量を多くしようとする場合
や、粒子径の小さな粉砕品を得ようとする場合には著し
い効果が期待できる。
For example, when the powder raw material is classified by using the gas stream classifier of the present invention, the weight average particle diameter is particularly 10 μm.
A toner having a sharp particle size distribution can be obtained from the following powder raw materials for toner production, and classification can be performed more efficiently than in the past. In particular, if the airflow classifier of the present invention is used, a toner having a sharp particle size distribution can be obtained from a powder raw material for producing a toner having a weight average particle size of 8 μm or less. Therefore, a remarkable effect can be expected in the case of increasing the amount of the powder raw material to be crushed by the jet mill or in the case of obtaining a crushed product having a small particle size.

【0033】[0033]

【実施例】次に、本発明の実施例を挙げて本発明を更に
詳細に説明する。実際にトナー製造用の粉体原料を用い
て、製品(トナー)を得た具体例を示す。実施例1 ・スチレン−ブチルアクリレート−ジビニルベンゼン共重合体(モノマー重合 重量比80.0/19.0/1.0、重量平均分子量=35万) 100重量部 ・磁性酸化鉄(平均粒径0.18μm) 100重量部 ・ニグロシン 2重量部 ・低分子量エチレン−プロピレン共重合体 4重量部 上記の処方の材料を、ヘンシェルミキサー(FM−75
型、三井三池化工業(株)製)でよく混合した後、温度
150℃に設定した2軸混練機(PCM−30型、池貝
鉄工(株)製)にて混練した。得られた混練物を冷却
し、ハンマーミルにて1mm以下に粗粉砕し、1mmス
クリーン通過品を衝突式気流粉砕機ジェット・ミルで微
粉砕し、粉体原料とした。
EXAMPLES The present invention will be described in more detail with reference to Examples of the present invention. A specific example in which a product (toner) is actually obtained by using a powder raw material for toner production will be shown. Example 1 -Styrene-butyl acrylate-divinylbenzene copolymer (monomer polymerization weight ratio 80.0 / 19.0 / 1.0, weight average molecular weight = 350,000) 100 parts by weight-Magnetic iron oxide (average particle size 0 .18 μm) 100 parts by weight Nigrosine 2 parts by weight Low molecular weight ethylene-propylene copolymer 4 parts by weight A material of the above formulation was applied to a Henschel mixer (FM-75).
Type, well mixed by Mitsui Miike Chemical Industry Co., Ltd., and then kneaded by a twin-screw kneader (PCM-30 type, manufactured by Ikegai Iron Works Co., Ltd.) set at a temperature of 150 ° C. The obtained kneaded product was cooled, coarsely pulverized with a hammer mill to 1 mm or less, and a 1 mm screen passing product was finely pulverized with a jet mill of a collision type airflow pulverizer to obtain a powder raw material.

【0034】上記の様にして得られたトナー原料を、図
3に示す装置システムで下記の様にして分級を行った。
先ず、上記で得られた粉体原料を定量供給機2を介し
て、振動フィーダー3及び原料供給管16を介して、コ
アンダ効果を利用して粗粉体、中粉体及び微粉体の3種
に分級すべく、図1に示す3分割分級装置1に導入し
た。導入に際しては、排出口11、12及び13に連通
している捕集サイクロン4、5及び6の吸引による系内
の減圧から派生する吸引力と、原料供給管16に取付け
たインクジェクションフィーダー31からの圧縮空気を
利用した。本実施例においては、原料供給管16、分級
エッジ17及び18、更に入気エッジ19の部材に、プ
ラスチック系ポリベンゾイミダゾール樹脂成形品が用い
られた装置を使用した。
The toner raw material obtained as described above was classified as follows using the apparatus system shown in FIG.
First, the powder raw material obtained above is categorized into three types, that is, a coarse powder, a medium powder and a fine powder by utilizing the Coanda effect through the constant quantity feeder 2, the vibration feeder 3 and the raw material supply pipe 16. In order to carry out classification, it was introduced into the three-division classification device 1 shown in FIG. At the time of introduction, the suction force derived from the reduced pressure in the system by the suction of the collection cyclones 4, 5 and 6 communicating with the discharge ports 11, 12 and 13 and the ink injection feeder 31 attached to the raw material supply pipe 16 Of compressed air was used. In the present embodiment, an apparatus in which a plastic polybenzimidazole resin molded product was used for the members of the raw material supply pipe 16, the classification edges 17 and 18, and the air intake edge 19 was used.

【0035】上記の構成の装置システムを使用して1ケ
月間連続運転を行った後、気流式分級装置を分解して原
料供給管16、分級エッジ17及び18、更に入気エッ
ジ19の状態を観察したところ、部材の摩耗及び部材へ
の融着現象は全く見られなかった。又、1ケ月間の連続
運転中に得られた分級品の粒度は安定していた。
After carrying out continuous operation for one month using the apparatus system having the above-mentioned constitution, the air flow type classifying apparatus is disassembled and the state of the raw material supply pipe 16, the classifying edges 17 and 18, and further the state of the intake edge 19 are changed. As a result of observation, neither wear of the member nor fusion phenomenon to the member was observed at all. The particle size of the classified product obtained during the continuous operation for one month was stable.

【0036】比較例1 実施例1と同じトナー製造用の粉体原料を用いて、図7
に示す従来の一体装置システムで分級を行った。即ち、
粉体原料を、定量供給機102、振動フィーダー103
及び原料供給管116を介して導入し、コアンダ効果を
利用して粗粉体、中粉体及び微粉体の3種に分級すべ
く、図5に示した3分割分級装置101に導入した。導
入に際しては、実施例1と同様に、排出口111、11
2及び113に連通している捕集サイクロン104、1
05及び106の吸引による系内の減圧から派生する吸
引力と、原料供給管116に取付けたインクジェクショ
ンフィーダー131からの圧縮空気を利用した。比較例
においては、原料供給管116、分級エッジ117及び
118、更に入気エッジ119の部材としてフッ素樹脂
成形品を使用した。
Comparative Example 1 Using the same powder raw material for toner production as in Example 1, FIG.
The classification was performed by the conventional integrated device system shown in. That is,
The powder raw material is supplied in a constant quantity by a feeder 102 and a vibration feeder 103.
Then, it was introduced through the raw material supply pipe 116, and was introduced into the three-division classification device 101 shown in FIG. 5 in order to classify into three types of coarse powder, medium powder and fine powder by utilizing the Coanda effect. At the time of introduction, as in the first embodiment, the discharge ports 111, 11
Collection cyclones 104, 1 communicating with 2 and 113
The suction force derived from the reduced pressure in the system by the suction of 05 and 106 and the compressed air from the ink injection feeder 131 attached to the raw material supply pipe 116 were used. In the comparative example, a fluororesin molded product was used as the material for the raw material supply pipe 116, the classification edges 117 and 118, and the air inlet edge 119.

【0037】実施例1と同様に、原料粉体を3つの粒子
群に分級する為、連続運転を行ったところ、2日後に分
級品の粒度が非常に粗くなった。そこで、気流式分級装
置101を分解し、原料供給管116の内面、分級エッ
ジ117及び118、更に入気エッジ119表面の状態
を観察したところ、原料供給管116の内壁面及び入気
エッジ119の先端部には融着は殆ど見られなかった
が、分級エッジ117及び118の表面に融着物がこび
りついていた。この為、運転を続けるには分級エッジ1
17及び118の両部材を交換せざるを得なかった。
In the same manner as in Example 1, in order to classify the raw material powder into three particle groups, continuous operation was carried out, and after 2 days, the particle size of the classified product became very coarse. Then, the airflow classifier 101 was disassembled, and the state of the inner surface of the raw material supply pipe 116, the classification edges 117 and 118, and the surface of the air intake edge 119 were observed, and the inner wall surface of the raw material supply pipe 116 and the air intake edge 119 were observed. Almost no fusion was observed at the tip portion, but the fusion material was stuck to the surfaces of the classification edges 117 and 118. Therefore, to continue driving, classification edge 1
Both members 17 and 118 had to be replaced.

【0038】比較例2 実施例1で用いたと同じトナー製造用の粉体原料を用い
て、図7に示す従来の一体装置システムを使用して分級
を行った。本実施例では、3分割分級機の原料供給管1
16、分級エッジ117及び118、更に入気エッジ1
19の構成部材がSUS304で形成されているものを
使用した。実施例1と同様に、連続運転を行ったとこ
ろ、2日後に得られた分級品の粒度に異常が見られた
為、運転を取り止め、気流式分級装置101を分解して
原料供給管116、分級エッジ117及び118、そし
て入気エッジ119の状態を目視により観察した。この
結果、分級エッジ117及び118表面、更に入気エッ
ジ119表面に、トナーの融着物が層になってこびりつ
いており、原料供給管116内はかなり摩耗していた。
その為、これ以上の運転を続けることは不可能であっ
た。
Comparative Example 2 The same powder raw material for toner production as used in Example 1 was used to perform classification using a conventional integrated device system shown in FIG. In this embodiment, the raw material supply pipe 1 of the three-division classifier
16, classification edges 117 and 118, and intake edge 1
19 constituent members formed of SUS304 were used. When continuous operation was performed in the same manner as in Example 1, an abnormality was found in the particle size of the classified product obtained after 2 days. Therefore, the operation was stopped, the airflow classification device 101 was disassembled, and the raw material supply pipe 116, The states of the classification edges 117 and 118 and the air intake edge 119 were visually observed. As a result, on the surfaces of the classification edges 117 and 118, and further on the surface of the air inlet edge 119, a fused substance of the toner was stuck as a layer, and the inside of the raw material supply pipe 116 was considerably worn.
Therefore, it was impossible to continue driving any further.

【0039】[0039]

【発明の効果】以上説明した様に、本発明の静電荷像用
トナーの製造用気流式分級装置によれば、原料供給管、
分級エッジ及び入気エッジの材質を適宜に特定のものに
することによって、分級装置内へのトナー成分の融着が
軽減され、且つ、装置内の部材の摩耗が防止される為、
様々な粉体原料の比重及び分級気流条件に応じて正確な
分級点が得られ、シャープな粒度分布のトナーが高い分
級収率で得られ、且つ連続して安定したトナー製品の生
産を行うことが可能となる。更には、分級機内の原料供
給管、分級エッジ及び入気エッジに融着物が発生せず、
又、装置内の摩耗も防止できる。この結果、これらの交
換頻度を減らすことが出来、本発明によればコストダウ
ンも可能となる。又、本発明の気流式分級装置が用いら
れているトナー製造装置システムにより、従来の装置に
比べ、画像濃度が安定して高く、耐久性が高く、カブリ
やクリーニング不良等の画像欠陥のない所定の粒度を有
する優れた静電荷像現像用トナーが得られる。
As described above, according to the airflow classifying apparatus for producing an electrostatic image toner of the present invention, a raw material supply pipe,
By appropriately selecting the materials of the classification edge and the air intake edge, the fusion of the toner component into the classification device is reduced, and the wear of the members in the device is prevented,
Accurate classification points can be obtained according to the specific gravity and classification airflow conditions of various powder raw materials, toners with a sharp particle size distribution can be obtained with high classification yield, and continuous stable toner product production can be achieved. Is possible. Furthermore, the raw material supply pipe in the classifier, no fusion material is generated on the classification edge and the air intake edge,
In addition, wear inside the device can be prevented. As a result, the frequency of replacement of these can be reduced, and the cost can be reduced according to the present invention. Further, the toner manufacturing apparatus system in which the airflow classifying apparatus of the present invention is used, the image density is stable and high as compared with the conventional apparatus, the durability is high, and there is no image defect such as fog or cleaning failure. An excellent electrostatic image developing toner having a particle size of

【0040】特に、本発明の気流式分級装置によれば、
重量平均粒子径10μm以下のトナー製造用の粉体原料
から、シャープな粒度分布を有するトナーを効率よく得
ることが可能であり、更には、重量平均粒子径が8μm
以下のトナー製造用の粉体原料からシャープな粒度分布
を有するトナーを効率よく得ることが出来る。
Particularly, according to the airflow type classification apparatus of the present invention,
It is possible to efficiently obtain a toner having a sharp particle size distribution from a powder raw material for producing a toner having a weight average particle diameter of 10 μm or less, and further, a weight average particle diameter of 8 μm.
A toner having a sharp particle size distribution can be efficiently obtained from the following powder raw materials for toner production.

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

【図1】本発明の気流式分級装置の一例を表す断面図で
ある。
FIG. 1 is a cross-sectional view showing an example of an airflow classification device of the present invention.

【図2】図1の気流式分級装置の側面図及び斜視図であ
る。
2A and 2B are a side view and a perspective view of the airflow classification device of FIG.

【図3】図1に示す気流式分級装置を用いた装置システ
ムを表す図である。
FIG. 3 is a diagram showing an apparatus system using the airflow classifier shown in FIG.

【図4】図1の気流式分級装置の分級域部の拡大図であ
る。
FIG. 4 is an enlarged view of a classification area portion of the airflow classification device of FIG.

【図5】従来の気流式分級装置の一例を表す断面図であ
る。
FIG. 5 is a cross-sectional view showing an example of a conventional airflow classifier.

【図6】図5の気流式分級装置の側面図及び斜視図であ
る。
6A and 6B are a side view and a perspective view of the airflow classification device of FIG.

【図7】図5に示す気流式分級装置を用いた装置システ
ムを表す図である。
7 is a diagram showing an apparatus system using the airflow type classification apparatus shown in FIG.

【符号の説明】[Explanation of symbols]

1、101:気流式3分割分級装置 2:定量供給機 3:振動フィーダー 4、5、6、104、105、106:捕集サイクロン 11、12、13、111、112、113:排出口 14、15、114、115:入気口 16、116:原料供給管 16a:原料供給管の開口部 17、117:中粉体群と微粉体群とを分画する分級エ
ッジ 18、118:粗粉体群と中粉体群とを分画する分級エ
ッジ 17a:分級エッジ17の軸 18a:分級エッジ18の軸 19、119:入気エッジ 19a:入気エッジの軸 20、120:第1気体導入調節手段 21、121:第2気体導入調節手段 22、122:入気側側壁 23、24、123、124:側壁 25、125:下部壁 26、126:コアンダブロック 27、127:上部壁 28、29、128、129:静圧計 30:粒子飛散軌跡(湾曲線) 31、131:インジェクションフィーダー 32、132:分級室
1, 101: Air flow type three-division classifier 2: Fixed amount feeder 3: Vibratory feeder 4, 5, 6, 104, 105, 106: Collection cyclone 11, 12, 13, 111, 112, 113: Discharge port 14, 15, 114, 115: Inlet port 16, 116: Raw material supply pipe 16a: Opening of raw material supply pipe 17, 117: Classification edge for separating a medium powder group and a fine powder group 18, 118: Coarse powder Classifying edge 17a: axis of classifying edge 17 18a: axis of classifying edge 18, 19: 119: inlet edge 19a: axis of inlet edge 20, 120: first gas introduction control Means 21, 121: Second gas introduction adjusting means 22, 122: Air inlet side wall 23, 24, 123, 124: Side wall 25, 125: Lower wall 26, 126: Coanda block 27, 127: Upper wall 28, 9,128,129: static pressure meter 30: particles scattering trajectory (curved line) 31, 131: Injection feeder 32, 132: classifying chamber

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 トナー製造用粉体原料を気流によって分
級する為の気流式分級装置であって、少なくともコアン
ダブロック、個壁ブロック及び複数の分級エッジにより
形成された分級域が設けられており、該分級域に分級装
置内に開口部を有する原料供給管中を流動する気流によ
って粉体原料を噴出させ、噴出された気流中の粉体原料
を、粒子の慣性力及びコアンダ効果による湾曲気流の遠
心力によって複数の粒子径の異なる粒体群に分級させる
気流式分級装置において、粉体原料の比重、目標分級点
及び原料供給速度に合わせ、原料供給管、分級エッジ及
び入気エッジの少なくとも一部がプラスチック系ポリベ
ンゾイミダゾールを主成分とする樹脂成形品、又はプラ
スチック系ポリベンゾイミダゾールを主成分とする樹脂
で表面がコーティングされた部材によって構成されてい
ることを特徴とする気流式分級装置。
1. An airflow type classifying device for classifying a powder raw material for toner production by an airflow, comprising a classification area formed by at least a Coanda block, individual wall blocks and a plurality of classification edges, The powder raw material is jetted by an air flow flowing in a raw material supply pipe having an opening in the classifying device in the classification area, and the powder raw material in the jetted air flow is converted into a curved air flow due to the inertia force of the particles and the Coanda effect. At least one of a raw material supply pipe, a classification edge and an air intake edge is selected in accordance with the specific gravity of the powder raw material, the target classification point and the raw material supply speed in an air flow type classification device for classifying into a plurality of particle groups having different particle sizes by centrifugal force. Part is a resin molded product containing plastic-based polybenzimidazole as a main component, or the surface is coated with a resin containing plastic-based polybenzimidazole as a main component An airflow classifier characterized by being constituted by a bent member.
JP13971896A 1996-05-10 1996-05-10 Air current classifying device for manufacture of toner Pending JPH09299885A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13971896A JPH09299885A (en) 1996-05-10 1996-05-10 Air current classifying device for manufacture of toner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13971896A JPH09299885A (en) 1996-05-10 1996-05-10 Air current classifying device for manufacture of toner

Publications (1)

Publication Number Publication Date
JPH09299885A true JPH09299885A (en) 1997-11-25

Family

ID=15251798

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13971896A Pending JPH09299885A (en) 1996-05-10 1996-05-10 Air current classifying device for manufacture of toner

Country Status (1)

Country Link
JP (1) JPH09299885A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012115782A (en) * 2010-12-02 2012-06-21 Ricoh Co Ltd Production apparatus and container for powder
CN106733643A (en) * 2016-11-29 2017-05-31 德米特(苏州)电子环保材料有限公司 Powder classifier

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012115782A (en) * 2010-12-02 2012-06-21 Ricoh Co Ltd Production apparatus and container for powder
CN106733643A (en) * 2016-11-29 2017-05-31 德米特(苏州)电子环保材料有限公司 Powder classifier
CN106733643B (en) * 2016-11-29 2024-01-05 德米特(苏州)电子环保材料有限公司 Powder classifier

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