JPH07244399A - Production of electrostatic charge image developing toner - Google Patents

Production of electrostatic charge image developing toner

Info

Publication number
JPH07244399A
JPH07244399A JP6033739A JP3373994A JPH07244399A JP H07244399 A JPH07244399 A JP H07244399A JP 6033739 A JP6033739 A JP 6033739A JP 3373994 A JP3373994 A JP 3373994A JP H07244399 A JPH07244399 A JP H07244399A
Authority
JP
Japan
Prior art keywords
toner
crushing
resin
rotor
manufacturing
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
JP6033739A
Other languages
Japanese (ja)
Inventor
Shingo Ishiyama
慎吾 石山
Susumu Ikushima
暹 生嶋
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
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 Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP6033739A priority Critical patent/JPH07244399A/en
Publication of JPH07244399A publication Critical patent/JPH07244399A/en
Pending legal-status Critical Current

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  • Developing Agents For Electrophotography (AREA)
  • Crushing And Grinding (AREA)
  • Crushing And Pulverization Processes (AREA)

Abstract

PURPOSE:To prevent the deterioration of toner performance such as the deterioration of image quality at the time of taking photograph by making a toner spherical without heat processing. CONSTITUTION:This producing method has a pulverizing process for a toner material containing a resin and a coloring agent, and the pulverized toner is surface ground by an impact grinder to make the toner spherical. That is, the pulverized toner obtained in the pulverizing process is introduced into the impact grinder having grinding zone 4 formed between the outside surface of a rotor 1 rotating around a rotary shaft 2 and the inside surface of a liner 6. The corners or projections of breakage surface of the toner particle, which are generated by the collision of the toner particle with each other or with the wall surface of the a pulverizer, are removed or buried into the toner main body by surface grinding to make the shape spherical. The outside surface of the rotor 1 and the inside surface of the liner 6 has corrugated acute angled grinding blades. As a result, the producing method simple in the process and free from the thermal damage of the toner is obtained.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、電子写真法、静電記録
法等において使用される静電荷像現像用トナーの製造方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of producing an electrostatic charge image developing toner used in electrophotography, electrostatic recording and the like.

【0002】[0002]

【従来の技術】従来、静電荷像現像用トナーの製造方法
は、樹脂、着色剤等の原料を混合、混練し、冷却工程を
経た後、ジェットミルなどで微粉砕後分級し、必要であ
れば形状を球形化する処理が行われる。この球形化工程
の目的は、粉砕工程における機械的な破壊を受けたトナ
ー粒子の形状が不定形で突起を多数持つ構造となること
より生じる流動性の低下を改善することにある。この球
形化工程として一般には分級後のトナー粒子を、トナー
表面が軟化あるいは溶融する様な高温雰囲気下に通すこ
とよって行うが、工程の増加、表面が軟化あるいは溶融
したトナー粒子同士が付着・凝集することによる粗大粒
子の発生、熱によるトナーの性能低下等、様々な問題が
発生する。
2. Description of the Related Art Conventionally, a method for producing a toner for developing an electrostatic image includes mixing raw materials such as a resin and a colorant, kneading them, passing through a cooling step, finely pulverizing with a jet mill or the like, and classifying them. For example, the process of making the shape spherical is performed. The purpose of this spheronization step is to improve the decrease in fluidity caused by the shape of the toner particles that have been mechanically destroyed in the pulverization step and have an irregular shape having a large number of protrusions. This spheronization step is generally carried out by passing the toner particles after classification through a high-temperature atmosphere in which the toner surface softens or melts, but the number of steps increases, and the toner particles whose surfaces are softened or melted adhere and aggregate. As a result, various problems occur such as generation of coarse particles and deterioration of toner performance due to heat.

【0003】[0003]

【発明が解決しようとする課題】本発明は、トナーに熱
処理を加えることなく、トナー粒子形状を球形に調整し
得る方法を提供することにある。すなわち本発明の目的
はトナーを熱処理することなく球形化することにより、
流動性向上のみならず、粒子同士の付着・凝集による粗
大粒子の発生・粒度分布の変化、並びにトナー構成成分
中の熱的に弱い化学成分の劣化等から引き起こされる実
写時の画質低下等のトナーの性能低下の防止を達成する
トナー製造方法を提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method capable of adjusting the shape of toner particles into a spherical shape without applying heat treatment to the toner. That is, the object of the present invention is to make the toner spherical without heat treatment,
Not only the fluidity is improved, but also the generation of coarse particles due to the adhesion and aggregation of particles, the change in the particle size distribution, and the deterioration of the image quality during actual copying caused by the deterioration of the thermally weak chemical components in the toner components. Another object of the present invention is to provide a method for producing a toner, which achieves the prevention of the performance deterioration of

【0004】[0004]

【課題を解決する為の手段】しかして、かかる本発明の
目的は、樹脂及び着色剤を含有するトナー材料の粉砕工
程を有する静電荷像現像用トナーの製造方法において、
粉砕後、衝撃式粉砕機によって粉砕トナーを表面粉砕
し、球形化することを特徴とする製造方法を採用するこ
とにより達成される。
SUMMARY OF THE INVENTION The object of the present invention, however, is to provide a method for producing a toner for developing an electrostatic charge image, which comprises a step of pulverizing a toner material containing a resin and a colorant.
After the pulverization, the pulverized toner is surface pulverized by an impact type pulverizer to make it spherical, which is achieved by adopting a production method.

【0005】以下に本発明を詳細に説明する。本発明の
トナー製造方法においては、球形化工程以外は、通常の
製造方法を採用することができる。通常の製造方法とし
ては先ずトナー原料を混合し、溶融押し出し機などで混
練して板状に押し出して冷却固化しトナー材料を得る。
トナー原料としては、樹脂及び着色剤が必須成分として
使用されるが、必要に応じて例えば帯電制御剤やその他
のトナー特性付与剤を使用することができる。
The present invention will be described in detail below. In the toner manufacturing method of the present invention, an ordinary manufacturing method can be adopted except for the spheroidizing step. As a usual manufacturing method, first, toner raw materials are mixed, kneaded by a melt extruder or the like, extruded in a plate shape, cooled and solidified to obtain a toner material.
As the toner raw material, a resin and a colorant are used as essential components, but if necessary, for example, a charge control agent or another toner property imparting agent can be used.

【0006】樹脂としては、例えば、トナーに適した公
知の各種の樹脂を使用することが出来る。例えば、スチ
レン系樹脂、塩化ビニル樹脂、ロジン変成マレイン酸樹
脂、フェノール樹脂、エポキシ樹脂、ポリエステル樹
脂、ポリエチレン樹脂、ポリプロピレン樹脂、アイオノ
マー樹脂、ポリウレタン樹脂、シリコーン樹脂、ケトン
樹脂、エチレン−エチルアクリレート樹脂、キシレン樹
脂、ポリビニルブチラール樹脂、ポリカーボネート樹脂
などが挙げられる。これらの樹脂は2種以上を併用する
こともできる。特に、スチレン系樹脂、飽和または不飽
和ポリエステル樹脂およびエポキシ樹脂を主樹脂として
用いることが好ましい。
As the resin, for example, various known resins suitable for toner can be used. For example, styrene resin, vinyl chloride resin, rosin-modified maleic acid resin, phenol resin, epoxy resin, polyester resin, polyethylene resin, polypropylene resin, ionomer resin, polyurethane resin, silicone resin, ketone resin, ethylene-ethyl acrylate resin, xylene. Resin, polyvinyl butyral resin, polycarbonate resin and the like can be mentioned. These resins can be used in combination of two or more kinds. In particular, it is preferable to use a styrene resin, a saturated or unsaturated polyester resin and an epoxy resin as the main resin.

【0007】そして、樹脂のガラス転移温度は、熱分析
法(示唆熱分析装置、示唆走査熱量分析装置等)で測定
した時の転移開始温度(変曲点)が50℃以上であるこ
とが好ましい。ガラス転移温度が50℃未満の場合に
は、40℃以上の高温で長時間トナーを放置した時、ト
ナーの凝集或いは固着を招き使用上問題がある。トナー
用着色剤としては、公知の各種の着色剤を使用すること
が出来、例えばカーボンブラック、ニグロシン、ベンジ
ジンイエロー、キナクリドン、ローダミンB、フタロシ
アニンブルー等が好適に使用される。着色剤は、樹脂1
00重量部当たり、通常0.1〜30重量部、好ましく
は3〜15重量部の割合で使用される。
The glass transition temperature of the resin preferably has a transition start temperature (inflection point) of 50 ° C. or higher when measured by a thermal analysis method (indicative thermal analyzer, suggestive scanning calorimeter, etc.). . When the glass transition temperature is lower than 50 ° C., when the toner is left at a high temperature of 40 ° C. or higher for a long time, the toner agglomerates or adheres, which causes a problem in use. As the toner colorant, various known colorants can be used, and for example, carbon black, nigrosine, benzidine yellow, quinacridone, rhodamine B, phthalocyanine blue, etc. are preferably used. Colorant is resin 1
It is usually used in an amount of 0.1 to 30 parts by weight, preferably 3 to 15 parts by weight, per 00 parts by weight.

【0008】帯電制御剤としては、やはり公知の各種の
帯電制御剤を使用することが出来る。例えば、第4アン
モニウム塩、ニグロシン染料、トリフェニルメタン染
料、スチレン−アミノアクリレート共重合体、ポリアミ
ン樹脂などの正帯電制御剤や、モノアゾ系金属錯塩等の
負帯電制御剤が挙げられる。帯電制御剤は樹脂100重
量部当たり、通常0.1〜10重量部の割合で使用され
る。
As the charge control agent, various known charge control agents can be used. Examples thereof include positive charge control agents such as quaternary ammonium salts, nigrosine dyes, triphenylmethane dyes, styrene-aminoacrylate copolymers and polyamine resins, and negative charge control agents such as monoazo metal complex salts. The charge control agent is usually used in a proportion of 0.1 to 10 parts by weight per 100 parts by weight of the resin.

【0009】また、各種のトナー特性付与剤としては、
例えば、オフセット防止のため、ポリエチレンワック
ス、ポリプロピレンワックスなどのポリアルキレンワッ
クスを使用することができる。また、流動性および耐凝
集性の向上のために、チタニア、アルミナ、シリカ等の
無機微粒子を使用することができる。これらのトナー特
性付与剤は、樹脂100重量部当たり、通常0.1〜1
0重量部の割合で使用される。
Further, as various toner characteristic imparting agents,
For example, in order to prevent offset, a polyalkylene wax such as polyethylene wax or polypropylene wax can be used. Further, in order to improve fluidity and aggregation resistance, inorganic fine particles such as titania, alumina and silica can be used. These toner property imparting agents are usually used in an amount of 0.1 to 1 per 100 parts by weight of the resin.
Used in a proportion of 0 parts by weight.

【0010】更に、トナーが磁性トナーである場合に
は、フェライト、マグネタイトを始め、鉄、コバルト、
ニッケル等の強磁性元素を含む合金又は化合物などの磁
性粒子を含有することができる。磁性粒子は、バインダ
ー樹脂100重量部当たり、通常、20〜70重量部の
割合で使用される。次に、トナー材料は、公知の粉砕機
によって、重量平均粒径が好ましくは20μm以下の範
囲になるように粉砕される。ここに、重量平均粒径と
は、粒径−重量分布のメジアン値粒径であり、例えば、
コールターエレクトロニクス社製コールカウンタで測定
することが出来る。上記の粉砕工程は単一の粉砕機によ
って行うことも可能であるが、種々の粉砕機を適宜組合
わせて2段階以上に分けて粉砕を行うことも好ましい。
通常のトナー製造方法においては、ハンマーミル、ピー
ルミル、スクリーンミル、自由粉砕機、フェザーミル等
を用いた粗粉砕工程、ジェットミル、衝撃式粉砕機、流
動層式カウンタージェットミル、ファインミル等を用い
た微粉砕工程の2段階で粉砕を行う工程、粗粉砕工程と
微粉砕工程の間に衝撃式粉砕機、ACMパルベライザ
ー、クリプトロン、ピンミル等を用いた中粉砕工程を設
けて3段階で粉砕を行う工程等の粉砕工程が例示され
る。
Further, when the toner is a magnetic toner, ferrite, magnetite, iron, cobalt,
Magnetic particles such as alloys or compounds containing ferromagnetic elements such as nickel can be contained. The magnetic particles are usually used in a proportion of 20 to 70 parts by weight per 100 parts by weight of the binder resin. Next, the toner material is pulverized by a known pulverizer so that the weight average particle diameter is preferably in the range of 20 μm or less. Here, the weight average particle size is a median value particle size of particle size-weight distribution, for example,
It can be measured with a Coulter Electronics Coal Counter. The above crushing step can be performed by a single crusher, but it is also preferable to appropriately combine various crushers and perform crushing in two or more stages.
In the usual toner manufacturing method, a rough milling process using a hammer mill, peel mill, screen mill, free crusher, feather mill, etc., jet mill, impact crusher, fluidized bed type counter jet mill, fine mill, etc. are used. The crushing process is performed in two steps, the intermediate crushing process using an impact crusher, ACM pulsarizer, kryptron, pin mill, etc. is provided between the coarse crushing process and the fine crushing process, and the crushing is performed in three steps. A crushing process such as a process to be performed is exemplified.

【0011】本発明ではこうして得られた粉砕トナー
を、回転軸を中心に回転するローターの外側表面とライ
ナーの内側表面との間に形成された粉砕領域を有する衝
撃式粉砕機に導入し、トナー粒子同士の衝突・トナー粒
子と粉砕機壁面との衝突により体積粉砕(粒子自体が大
きく割れる粉砕)で発生した粒子の破断面に発生した角
・突起を削除又はトナー本体に機械的に埋め込む表面粉
砕により形状を球形化することにより達成される。図1
に本発明に用いる衝撃式粉砕機の一例を示す。
In the present invention, the pulverized toner thus obtained is introduced into an impact type pulverizer having a pulverization region formed between the outer surface of the rotor rotating about the rotation axis and the inner surface of the liner, and the toner is Surface crushing that removes the corners and protrusions generated on the fracture surface of the particles generated by volume crushing (crushing that the particles themselves are largely broken) due to collision of particles with each other and collision of the toner particles with the crusher wall surface Is achieved by making the shape spherical. Figure 1
An example of the impact type crusher used in the present invention is shown in FIG.

【0012】従来、衝撃式粉砕機のローター及びライナ
ーの形状としては種々のものが提案されており、例えば
ローターが平板の埋め込みによる水車羽根状のものでラ
イナーが凹凸の突起を有するもの、又はローター外側表
面及びライナー内側表面に凹凸状の突起を有するもの
(特開昭59−105853号公報)、ローター外側表
面及びライナー内側表面共に波形状のシャープな鋭角粉
砕刃を有するもの(特開昭59−127651号公報)
などが知られているが、本発明に用いる衝撃式粉砕機と
しては、特にローター外側表面及びライナー内側表面の
片方あるいは双方に波形状の鋭角粉砕刃を有するもの
が、好ましく用いられる。図2に一例として、双方が波
形状の鋭角粉砕刃を有する場合を示す。
Conventionally, various shapes of the rotor and liner of the impact type crusher have been proposed. For example, the rotor has a turbine blade shape by embedding a flat plate and the liner has irregular projections, or the rotor. Those having uneven projections on the outer surface and the inner surface of the liner (JP-A-59-105853), and those having a wavy, sharp, acute-angle crushing blade on both the outer surface of the rotor and the inner surface of the liner (JP-A-59-59). No. 127651)
However, as the impact type pulverizer used in the present invention, one having a corrugated acute-angle pulverizing blade on one or both of the outer surface of the rotor and the inner surface of the liner is preferably used. As an example, FIG. 2 shows a case where both have corrugated acute-angle crushing blades.

【0013】衝撃式粉砕機のローターとライナーとの間
に形成される粉砕領域の間隙は好ましくは0.1〜8m
mである。なお、この間隙とはローター粉砕刃の山部と
ライナー粉砕刃の山部との距離を意味する。衝撃式粉砕
機の運転条件は適宜選択されるが、ローターの回転周速
は50〜180m/s、中でも特に60〜160m/s
が好ましい。また前述した様な粗大粒子の発生、トナー
の性能低下を防止するために粉砕領域内の雰囲気温度
(T)はトナーに含まれる樹脂のガラス転移温度(T
g)より低いことが好ましく、Tg−Tの値が8℃以上
であるとより好ましい。粉砕領域内の温度を調節する方
法とは、粉砕機への流入空気の温度を制御する、粉砕ト
ナーのフィード量を制御する、粉砕領域周辺への壁面の
温度を制御する等が挙げられる。
The gap in the crushing area formed between the rotor and the liner of the impact crusher is preferably 0.1 to 8 m.
m. The gap means the distance between the crest of the rotor crushing blade and the crest of the liner crushing blade. The operating conditions of the impact type crusher are appropriately selected, but the rotational peripheral speed of the rotor is 50 to 180 m / s, and especially 60 to 160 m / s.
Is preferred. Further, in order to prevent the generation of coarse particles and the deterioration of toner performance as described above, the ambient temperature (T) in the crushing area is set to the glass transition temperature (T) of the resin contained in the toner.
It is preferably lower than g), and more preferably a Tg-T value of 8 ° C or higher. Examples of the method of adjusting the temperature in the crushing area include controlling the temperature of the air flowing into the crusher, controlling the feed amount of the crushing toner, and controlling the temperature of the wall surface around the crushing area.

【0014】また特に粉砕工程の最終工程に衝撃式粉砕
機を用いる場合には、一台の衝撃式粉砕機で粉砕と球形
化を連続的に行うことも本発明の一様態として挙げるこ
とが出来る。しかし体積粉砕を行う条件と、表面粉砕の
条件は異なるので、トナーの種類によって適宜条件調整
が必要である。また例えば体積粉砕が十分に行われた
後、更に粉砕トナーを滞留させることにより、粉砕トナ
ーの表面粉砕を行う方法が挙げられる。この際、回転軸
方向に十分に長いローターを用いるか、或いはトナーを
搬送する流入空気の風量を少なくするかして、粉砕領域
内での粉砕トナーの滞留時間を通常の粉砕に比べて十分
に長くすればよい。
Further, particularly when an impact type crusher is used in the final step of the crushing process, continuous crushing and spheroidizing with one impact type crusher can be mentioned as a mode of the present invention. . However, since the conditions for volume pulverization and the conditions for surface pulverization are different, it is necessary to appropriately adjust the conditions depending on the type of toner. Further, for example, there is a method in which after the volume pulverization is sufficiently performed, the pulverized toner is further retained to pulverize the surface of the pulverized toner. At this time, the residence time of the pulverized toner in the pulverization area is set to be sufficiently longer than that in normal pulverization by using a rotor that is sufficiently long in the rotation axis direction or by reducing the amount of inflowing air that conveys the toner. It should be long.

【0015】また一台の衝撃式粉砕機の粉砕領域が、体
積粉砕が行われる部分と表面粉砕が行われる部分を有す
る様に設定してもよい。このような場合には粉砕領域の
少なくとも一部分が表面粉砕が行われるような条件にな
っていればよく、その他の粉砕領域の部分の条件につい
ては特に限定されない。具体的な方法としては、ロータ
ーの回転周速を部分的に変える、段付ローター、傾斜ロ
ーター、段付ライナー、傾斜ライナー等を用いて粉砕領
域の間隙を部分的に変える等が挙げられる。
The crushing area of one impact crusher may be set so as to have a portion where volume crushing is performed and a portion where surface crushing is performed. In such a case, it is sufficient that at least a part of the crushing area is under the condition that the surface crushing is performed, and the condition of the other crushing area is not particularly limited. Specific methods include partially changing the rotational peripheral speed of the rotor, and partially changing the gap in the crushing region using a stepped rotor, a tilted rotor, a stepped liner, a tilted liner, or the like.

【0016】本発明に用いる衝撃式粉砕機は図1に示し
た様な横型でも、縦型でもよい。本発明のトナー製造方
法においては実質的にトナー材料をまず体積粉砕し、そ
の後表面粉砕すれば良く、従って粉砕トナーを衝撃式粉
砕機に供給する前に分級手段を設けて粗粉砕物、微粉砕
物を取り分ける工程を入れることもその一実施形態とし
て含まれる。又、前述したように一台の衝撃式粉砕機で
粉砕及び球形化を連続的に行う場合にも、その途中段階
で適宜分級工程を設けてもよい。
The impact type crusher used in the present invention may be a horizontal type as shown in FIG. 1 or a vertical type. In the toner manufacturing method of the present invention, substantially, the toner material is first subjected to volume pulverization and then surface pulverization. Therefore, before supplying the pulverized toner to the impact type pulverizer, a classifying means is provided to coarsely pulverize and finely pulverize. Including a step of separating the objects is also included as one embodiment. Further, as described above, even when crushing and spheroidizing are continuously performed by one impact crusher, a classifying step may be appropriately provided at an intermediate stage thereof.

【0017】前述の粉砕機により球形化され、排出口か
ら排出されたトナーは、その後通常分級処理を行って約
3〜20μm、好ましくは5〜15μmの所定粒径のト
ナーを回収する。分級装置としては、各種の分級機例え
ば気流式分級機(日本ニューマチック社製 DS分級
機)、コアンダ効果を利用した多産物同時分級機(日鉄
鉱業社製 エルボージェット)、ジグザグ分級機等を採
用することが出来る。そして、得られた所定粒径以外の
分級粗粉及び分級微粉は製造工程に循環して再利用する
ことができる。例えば分級粗粉は粉砕工程に循環して再
粉砕し、分級微粉は原料粉と一緒に混合工程や溶融混練
工程に循環して使用することが出来る。
The toner spheroidized by the above-mentioned pulverizer and discharged from the discharge port is then subjected to a normal classification treatment to recover a toner having a predetermined particle diameter of about 3 to 20 μm, preferably 5 to 15 μm. As the classifier, various classifiers such as an airflow classifier (DS classifier manufactured by Nippon Pneumatic Co., Ltd.), a multi-product simultaneous classifier utilizing the Coanda effect (Elbow Jet manufactured by Nippon Steel Mining Co., Ltd.), a zigzag classifier, etc. Can be adopted. Then, the obtained classified coarse powder and classified fine powder having a particle size other than the predetermined particle size can be recycled by being recycled to the manufacturing process. For example, the classified coarse powder can be recycled to the crushing step for re-crushing, and the classified fine powder can be recycled together with the raw material powder for use in the mixing step and the melt-kneading step.

【0018】上記のようにして得られたトナーは、更に
種々の公知の外添剤を外添する工程を経て、その後所定
の容器に充填されて製品化される。
The toner obtained as described above is further subjected to the step of externally adding various known external additives, and then filled in a predetermined container to be manufactured.

【0019】[0019]

【実施例】以下、実施例により本発明をさらに詳細に説
明するが、本発明はその要旨を超えないかぎり、以下の
実施例により何ら制限されるものではない。 (実施例1)
EXAMPLES The present invention will be described in more detail with reference to examples below, but the present invention is not limited to the following examples as long as the gist thereof is not exceeded. (Example 1)

【0020】[0020]

【表1】 スチレンアクリレート共重合樹脂 100部 (軟化点145℃、ガラス転移点64℃) 着色剤 カーボンブラック MA100 6部 (三菱化成(株)製) 低分子量ポリプロピレン ビスコール550P 1部 (三洋化成(株)製) 帯電制御剤 第4アンモニウム塩 ボントロンP−51 2部 (オリエント化学(株)製)[Table 1] Styrene acrylate copolymer resin 100 parts (softening point 145 ° C, glass transition point 64 ° C) Colorant carbon black MA100 6 parts (manufactured by Mitsubishi Kasei Co., Ltd.) Low molecular weight polypropylene viscol 550P 1 part (Sanyo Kasei Co., Ltd. )) Charge control agent quaternary ammonium salt Bontron P-51 2 parts (manufactured by Orient Chemical Co., Ltd.)

【0021】を配合し、混合・混練・粗粉砕し得られた
フレーク(平均粒径300μm前後)を10kg/hの
速度にて第1段目の衝撃式粉砕機(ターボ工業(株)製
ターボミルT−250RS型)で粉砕領域の雰囲気温
度50℃以下、ローター回転数13000rpm(周速
171m/s)、ローターとライナーの間隙2mmで粉
砕を行い、続いて2段目の衝撃式粉砕機(第1段目の粉
砕機と同機種)にて、ローター回転数を11000rp
m(周速144m/s)に変えた以外はすべて1段目と
同条件で球形化を行った。その後、得られたトナーをエ
ルボージェット分級機(EJ−LABO型)で分級し、
平均粒径9.0μmの製品トナー粒子群を得た。この時
次式で定義される実用球形度
Flakes (average particle size of about 300 μm) obtained by mixing, mixing, kneading and coarsely crushing are mixed with a first-stage impact crusher (turbo mill manufactured by Turbo Industry Co., Ltd.) at a speed of 10 kg / h. (T-250RS type), the temperature of the atmosphere in the crushing region is 50 ° C or less, the number of rotations of the rotor is 13000 rpm (peripheral speed is 171 m / s), the gap between the rotor and the liner is 2 mm, and then the second-stage impact crusher (No. Rotor speed is 11000 rp with the same model as the first crusher)
Sphericalization was performed under the same conditions as in the first step, except that the speed was changed to m (peripheral speed 144 m / s). Then, the obtained toner is classified by an elbow jet classifier (EJ-LABO type),
A product toner particle group having an average particle size of 9.0 μm was obtained. At this time, the practical sphericity defined by the following equation

【0022】[0022]

【数1】 [Equation 1]

【0023】を顕微鏡写真より算出すると0.88とい
う値が得られた。また、この製品トナー100重量部に
シリカ粉末(日本アエロジル(株)R972)0.2重
量部を混合して得られたトナーの流動性を開口法にて測
定した所、15mmφという良好な値を得た。上記のト
ナー4重量部とフェライト粉末をコア材とするキャリア
100重量部とを混合して現像剤となし、有機光導電体
を感光体とした複写機を使用して実写テストを行った。
なお、実写テストにおける補給用トナーには、上記の現
像剤に使用したのと同一のトナーを使用した。実写テス
トの結果はカブリが無く、高階調性の画像が得られ、実
写品質は良好であった。また、その他の使用上の不都合
も無かった。
A value of 0.88 was obtained by calculating from the micrograph. Further, the fluidity of a toner obtained by mixing 100 parts by weight of this product toner with 0.2 part by weight of silica powder (R972 of Nippon Aerosil Co., Ltd.) was measured by an opening method, and a good value of 15 mmφ was obtained. Obtained. 4 parts by weight of the above toner and 100 parts by weight of a carrier having a ferrite powder as a core material were mixed to form a developer, and an actual copying test was conducted using a copying machine having an organic photoconductor as a photoconductor.
As the replenishment toner in the actual copying test, the same toner as that used for the above developer was used. The result of the live-shooting test was that there was no fog, a high gradation image was obtained, and the live-shooting quality was good. In addition, there was no other inconvenience in use.

【0024】(比較例1)実施例1と同じトナー粗粉砕
物を用いて、ジェット式粉砕機(日本ニューマチック社
製 I−10)により平均粒径9.0μmのトナー産物
を得たところ、その実用球形度は0.82となり、実施
例1で得られたトナーの球形度より悪かった。また、そ
のシリカ0.2部添加品の流動性は17mmφであり、
流動性の面でも実施例1は向上していることが分かっ
た。また、実施例1と同じ流動性を示す迄シリカの添加
量を調整した場合、0.50重量部必要であり、実施例
1は少ないシリカ添加量で十分な流動性が得られること
が確認された。
Comparative Example 1 A toner product having an average particle size of 9.0 μm was obtained by using the same coarsely pulverized toner as in Example 1 and using a jet pulverizer (I-10 manufactured by Nippon Pneumatic Co., Ltd.). The practical sphericity was 0.82, which was worse than that of the toner obtained in Example 1. Further, the fluidity of the product added with 0.2 parts of silica is 17 mmφ,
It was found that Example 1 was also improved in terms of fluidity. Further, when the addition amount of silica was adjusted to show the same fluidity as in Example 1, 0.50 parts by weight was required, and it was confirmed that in Example 1, sufficient fluidity can be obtained with a small amount of silica added. It was

【0025】(比較例2)2段目の衝撃式粉砕機の粉砕
領域の雰囲気温度を64℃とした以外は実施例1と同様
にトナーを作製したところ、トナー中に0.5〜1mm
位の粗大粒子が発生し、次の分級工程の原料供給部で閉
塞するトラブルが発生した。また、その形状指数は0.
89、シリカ0.2重量部添加品の流動性は15mmφ
と実施例1と同様の球形化効果が得られたが、この方法
はトナー表面を軟化あるいは溶融させて球形化する方法
であり、実施例1とは本質的に球形化の方法が異なる。
また、前記粗大粒子の影響により実写時の画質において
階調性が劣り、トナーの熱履歴によるカブリの発生も見
られ、実施例1に劣る結果であった。
(Comparative Example 2) A toner was prepared in the same manner as in Example 1 except that the atmosphere temperature in the crushing area of the second-stage impact crusher was 64 ° C.
Coarse particles were generated, and there was a problem that the raw material supply part in the next classification step was clogged. The shape index is 0.
89, 0.2 parts by weight of silica has a fluidity of 15 mmφ
The same spheronization effect as in Example 1 was obtained, but this method is a method of spheroidizing by softening or melting the toner surface, and the spheroidizing method is essentially different from Example 1.
Further, due to the influence of the coarse particles, the gradation in the image quality at the time of actual copying is inferior, and fog is also generated due to the thermal history of the toner, which is inferior to that in Example 1.

【0026】[0026]

【発明の効果】以上説明した本発明によれば、カブリ現
象が少なく且つ良好な画質を与える静電荷像現像用トナ
ーの球形化方法であって、工程がシンプルであると共に
トナーへの熱的ダメージを与えない製産方法が提供さ
れ、本発明の工業価値は顕著である。
According to the present invention described above, there is provided a method of spheroidizing a toner for developing an electrostatic charge image, which has a low fog phenomenon and provides a good image quality. The process is simple and the toner is thermally damaged. The production value of the present invention is provided, and the industrial value of the present invention is remarkable.

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

【図1】本発明で使用する粉砕機の一例の断面図であ
る。
FIG. 1 is a sectional view of an example of a crusher used in the present invention.

【図2】図1におけるA−A線断面図である。FIG. 2 is a sectional view taken along line AA in FIG.

【符号の説明】[Explanation of symbols]

1 ローター 2 回転軸 3 ローター外側表面の粉砕刃 4 粉砕領域 5 ライナー内側表面の粉砕刃 6 ライナー 7 供給口 8 排出口 9 撹拌羽根 10 撹拌羽根 11 間隙 1 rotor 2 rotating shaft 3 crushing blade on outer surface of rotor 4 crushing area 5 crushing blade on inner surface of liner 6 liner 7 supply port 8 discharge port 9 stirring blade 10 stirring blade 11 gap

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 樹脂及び着色剤を含有するトナー材料の
粉砕工程を有する静電荷像現像用トナーの製造方法にお
いて、粉砕後、衝撃式粉砕機によって粉砕トナーを表面
粉砕し球形化することを特徴とする製造方法。
1. A method of producing a toner for developing an electrostatic charge image, which comprises a step of pulverizing a toner material containing a resin and a colorant, wherein after pulverizing, the pulverized toner is surface-pulverized by an impact type pulverizer to be spherical. And manufacturing method.
【請求項2】 衝撃式粉砕機の粉砕領域内の雰囲気温度
(T)が、トナーに含有される樹脂のガラス転移温度
(Tg)より低いことを特徴とする請求項1に記載の製
造方法。
2. The manufacturing method according to claim 1, wherein the atmospheric temperature (T) in the crushing region of the impact crusher is lower than the glass transition temperature (Tg) of the resin contained in the toner.
【請求項3】 Tg−Tが8℃以上であることを特徴と
する請求項2に記載の製造方法。
3. The manufacturing method according to claim 2, wherein Tg-T is 8 ° C. or higher.
【請求項4】 粉砕トナーの重量平均粒径が20μm以
下であることを特徴とする請求項1,2又は3に記載の
製造方法。
4. The manufacturing method according to claim 1, wherein the crushed toner has a weight average particle diameter of 20 μm or less.
【請求項5】 衝撃式粉砕機のローター外側表面及びラ
イナー内側表面の片方あるいは双方が波形状の鋭角粉砕
刃を有することを特徴とする請求項1,2,3又は4に
記載の製造方法。
5. The method according to claim 1, 2, 3 or 4, wherein one or both of the outer surface of the rotor and the inner surface of the liner of the impact type crusher has a corrugated sharp-angle crushing blade.
【請求項6】 ローターの回転周速が50〜180m/
sであることを特徴とする請求項1,2,3,4又は5
に記載の製造方法。
6. The rotating peripheral speed of the rotor is 50 to 180 m /
s, Claims 1, 2, 3, 4 or 5
The manufacturing method described in.
【請求項7】 衝撃式粉砕機の粉砕領域の間隙が、0.
1〜8mmであることを特徴とする請求項1,2,3,
4,5又は6に記載の製造方法。
7. The gap in the crushing area of the impact crusher is less than 0.
It is 1-8 mm, Claims 1, 2, 3,
The manufacturing method according to 4, 5, or 6.
JP6033739A 1994-03-03 1994-03-03 Production of electrostatic charge image developing toner Pending JPH07244399A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6033739A JPH07244399A (en) 1994-03-03 1994-03-03 Production of electrostatic charge image developing toner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6033739A JPH07244399A (en) 1994-03-03 1994-03-03 Production of electrostatic charge image developing toner

Publications (1)

Publication Number Publication Date
JPH07244399A true JPH07244399A (en) 1995-09-19

Family

ID=12394786

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6033739A Pending JPH07244399A (en) 1994-03-03 1994-03-03 Production of electrostatic charge image developing toner

Country Status (1)

Country Link
JP (1) JPH07244399A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5865381A (en) * 1996-07-30 1999-02-02 Canon Kabushiki Kaisha Surface treating apparatus for solid particles, surface treating method therefor and method for producing toner
JP2001129418A (en) * 1999-11-01 2001-05-15 Nisshin Flour Milling Co Ltd Mechanical pulverizer
JP2003088770A (en) * 2001-09-19 2003-03-25 Ricoh Co Ltd Grinder and method for producing toner by using the same
US7323283B2 (en) 2004-03-03 2008-01-29 Toyo Ink Mgf. Co., Ltd. Method of producing an electrostatic charge image developing toner

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5865381A (en) * 1996-07-30 1999-02-02 Canon Kabushiki Kaisha Surface treating apparatus for solid particles, surface treating method therefor and method for producing toner
JP2001129418A (en) * 1999-11-01 2001-05-15 Nisshin Flour Milling Co Ltd Mechanical pulverizer
JP2003088770A (en) * 2001-09-19 2003-03-25 Ricoh Co Ltd Grinder and method for producing toner by using the same
US7323283B2 (en) 2004-03-03 2008-01-29 Toyo Ink Mgf. Co., Ltd. Method of producing an electrostatic charge image developing toner

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