JP3409100B2 - Manufacturing method of toner - Google Patents

Manufacturing method of toner

Info

Publication number
JP3409100B2
JP3409100B2 JP20152495A JP20152495A JP3409100B2 JP 3409100 B2 JP3409100 B2 JP 3409100B2 JP 20152495 A JP20152495 A JP 20152495A JP 20152495 A JP20152495 A JP 20152495A JP 3409100 B2 JP3409100 B2 JP 3409100B2
Authority
JP
Japan
Prior art keywords
cooling
toner
kneaded product
temperature
kneaded
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.)
Expired - Lifetime
Application number
JP20152495A
Other languages
Japanese (ja)
Other versions
JPH0934173A (en
Inventor
浩司 佐野
昇 黒田
脩 神津
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 JP20152495A priority Critical patent/JP3409100B2/en
Publication of JPH0934173A publication Critical patent/JPH0934173A/en
Application granted granted Critical
Publication of JP3409100B2 publication Critical patent/JP3409100B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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】本発明は電子写真、静電記
録、静電印刷などにおける静電荷像を現像するための乾
式トナーの製造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 for producing a dry toner for developing an electrostatic image in electrophotography, electrostatic recording, electrostatic printing and the like.

【0002】[0002]

【従来の技術】静電荷像を現像する方法には、(1)大
別して絶縁性有機液体中に各種の着色剤及び結着樹脂を
主成分とした微細なトナーが粒子を分散させた現像液を
用いる液体現像方式と、(2)天然または合成樹脂に極
性制御剤、着色剤を分散含有させたトナーといわれる微
粉末現像剤を用いる乾式現像方式とが知られている。乾
式現像方式では、トナーを用いて静電荷像を現像し、必
要に応じて、転写シート上に転写した後、これを転写シ
ート上に融着させることによって行われる。その際、ト
ナー像の融着は溶液蒸気との接触、加圧または加熱によ
って行われる。この(2)の乾式現像方式によれば、コ
ピーが乾いた状態で得られ、またコピー速度が速いこと
から広く採用される。
2. Description of the Related Art A method of developing an electrostatic charge image is as follows. (1) A developing solution in which fine toner containing various colorants and a binder resin as main components is dispersed in an insulating organic liquid. And a dry developing method using (2) a fine powder developer called a toner in which a polar control agent and a colorant are dispersed and contained in a natural or synthetic resin. In the dry developing method, the electrostatic charge image is developed using toner, and if necessary, transferred onto a transfer sheet, and then fused onto the transfer sheet. At that time, the fusion of the toner image is performed by contact with the solution vapor, pressurization or heating. According to the dry developing method (2), a copy can be obtained in a dry state, and the copying speed is high, so that it is widely used.

【0003】しかしながら、乾式現像剤によって静電荷
像を現像する際、往々にして、非画像部にまでトナーが
付着し、いわゆる地汚れを発生させたり、また、画像部
にトナーが充分付着しないで画像濃度低下を起させたり
することがある。さらに、複写機によって多数枚コピー
を行うこと、現像剤の寿命より早く画像濃度低下や、地
汚れが発生する現象いわゆるフィルミングによる耐久性
低下が生じる。これらはいずれもトナー中に着色剤、極
性制御剤、離型剤の分散が悪いために生じるものであ
る。着色剤、極性制御剤、離型剤の分散が悪いと、帯電
能力の低い、或いは、帯電能力のばらつきの大きいトナ
ーになり、画像濃度が低下する。また、帯電能力低下の
ため非画像部にトナーが付着して、地汚れが発生し、離
型剤の分散が悪いと、離型剤がトナー表面に遊離し、キ
ャリア表面にフィルミングするため、耐久性が低下す
る。
However, when developing an electrostatic image with a dry developer, the toner often adheres to the non-image area to cause so-called scumming, and the toner does not adhere sufficiently to the image area. The image density may be reduced. Further, when a large number of copies are made by a copying machine, the image density is reduced earlier than the life of the developer, and the phenomenon of background smearing, which is so-called filming, causes deterioration in durability. These are all caused by poor dispersion of the colorant, the polarity control agent and the release agent in the toner. If the colorant, the polarity control agent, and the release agent are poorly dispersed, the toner has a low charging ability or a large variation in the charging ability, and the image density is lowered. In addition, the toner adheres to the non-image area due to a decrease in the charging ability, and scumming occurs, and if the release agent is poorly dispersed, the release agent is released on the toner surface and filming on the carrier surface occurs. Durability decreases.

【0004】こうした不都合を解消するために、地汚れ
を生じさせることなく、高濃度で高耐久性のあるトナー
を製造するために、トナー中の着色剤、極性制御剤、離
型剤の分散性を高める製造方法がとられてきた。混練に
より分散性を向上させる手段の一つとして、時間当たり
の混練処理量を少なくする方法がある。これは、混練処
理量を少なくすることにより、相対的に、混練機内での
滞留時間を増し、分散時間を増やすというものである。
また、最初に結着樹脂の一部と着色剤、極性制御剤の一
部、または全部を混練後、冷却・粉砕し、これを残りの
材料と再度混練する、いわゆるマスターバッチ法などが
ある(特開平3−164750号)。このようにして、
混練により分散された材料は、冷却され、粉砕、分級に
より製品とされる。
In order to eliminate such inconvenience, in order to produce a toner having a high concentration and a high durability without causing scumming, the dispersibility of the colorant, the polarity control agent and the release agent in the toner is improved. Manufacturing methods have been taken to increase the As one of means for improving the dispersibility by kneading, there is a method of reducing the kneading amount per unit time. This is to reduce the kneading amount, thereby relatively increasing the residence time in the kneader and increasing the dispersion time.
Further, there is a so-called masterbatch method in which a part of the binder resin and a colorant and a part or all of the polarity control agent are first kneaded, and then cooled and ground, and this is kneaded again with the rest of the materials ( JP-A-3-164750). In this way
The material dispersed by kneading is cooled, pulverized and classified to obtain a product.

【0005】ところで、ここでの「冷却」は粉末のトナ
ーを得るために固化する目的で行なわれるが、この冷却
において、できるだけ早く冷却することにより、混練で
分散した着色剤、極性制御剤、離型剤の混練物中での再
凝集を防止する効果を得られることが判明した。例え
ば、冷却を行わず放置し、空冷にて固化させたトナーを
粉砕、分級して作成したトナーの場合、冷却を行って作
成したトナーに比べ、地汚れ、現像濃度低下、キャリア
寿命の低下が多くみられる。また、混練物を冷却する時
に、粉砕を容易にするために、圧延ローラーなどによ
り、2〜5[mm]程度の板状に圧延する方法がある。
さらに、この圧延により材料の表面積が増え、冷却が促
進されることにより、冷却装置の小型化がはかれるとい
うメリットを持つ。圧延方法としては、ローラー内部に
冷却溶媒を充填または循環し、冷却速度を早め、着色
剤、極性制御剤、離型剤の再凝集を防止する冷却式圧延
方法もある。
By the way, the "cooling" here is carried out for the purpose of solidifying in order to obtain a powdery toner. In this cooling, the colorant dispersed in the kneading, the polarity control agent, and the releasing agent are separated by cooling as quickly as possible. It was found that the effect of preventing re-aggregation in the kneaded product of the molding agent can be obtained. For example, in the case of a toner prepared by crushing and classifying a toner solidified by air cooling after being left without cooling, scumming, a decrease in developing density, and a decrease in carrier life are caused as compared with a toner prepared by cooling. Many are seen. In addition, there is a method of rolling the kneaded product into a plate shape of about 2 to 5 [mm] with a rolling roller or the like in order to facilitate pulverization when cooling.
Further, this rolling has an advantage that the surface area of the material is increased and cooling is promoted, so that the cooling device can be downsized. As a rolling method, there is also a cooling type rolling method in which a cooling solvent is filled or circulated in the roller to accelerate the cooling rate and prevent reaggregation of the colorant, the polarity control agent and the release agent.

【0006】現在のところ、混練後の材料を最も効率良
く冷却する手段は、上記の冷却式圧延方法であり、一般
的に用いられている。しかし、この方法では材料の厚み
をせいぜい1[mm]程度にしかしていないため、材料
内部の冷却速度は遅く、表面と中心部との冷却速度に差
を生じる。このような場合、せっかく混練機により均一
な分散状態が得られたものでも、この冷却速度差によ
り、凝集の速度が異なり、不均一な分散状態となる。従
って、粉砕、分級後のトナーにおいても、結着樹脂中の
着色剤、極性制御剤、離型剤の分散が不均一となり、地
汚れ、濃度低下、更にはキャリア寿命低下などの原因と
なるおそれがある。
At present, the most efficient means for cooling the kneaded material is the above-mentioned cooling type rolling method, which is generally used. However, in this method, the thickness of the material is at most about 1 [mm], so that the cooling rate inside the material is slow and a difference occurs in the cooling rate between the surface and the central portion. In such a case, even if a uniform dispersion state is obtained by the kneading machine, the speed of aggregation is different due to the difference in the cooling rate, resulting in a non-uniform dispersion state. Therefore, even in the toner after pulverization and classification, the dispersion of the colorant, the polarity control agent, and the release agent in the binder resin becomes non-uniform, which may cause scumming, decrease in concentration, and further decrease in carrier life. There is.

【0007】これらの問題を解決するために、特開平2
−97969号には、混練物を急冷する方法が提案され
ている。この方法によると、混練物を冷却する時の冷却
速度を、混練機吐出口より吐出後、5[秒]以内、また
は、14[℃/s]以上で冷却することにより、粉砕後
のトナー中に遊離ポリエチレンの存在が少なくなり、オ
フセット、スリーブ汚染、反転カブリ現像などのない、
物理的および化学的特性の優れたトナーが得られるとし
ている。しかし、この条件を満足する方法でも、冷却条
件によっては十分な品質が得られないのが現状である。
In order to solve these problems, Japanese Unexamined Patent Application Publication No.
No. 97969 proposes a method of rapidly cooling a kneaded product. According to this method, the cooling speed when cooling the kneaded material is within 5 [seconds] after discharging from the discharge port of the kneading machine, or at 14 [° C./s] or higher, so that the toner in the crushed toner is cooled. Since there is less free polyethylene, there is no offset, sleeve contamination, reverse fog development, etc.
It is said that a toner having excellent physical and chemical properties can be obtained. However, even with the method that satisfies this condition, it is the current situation that sufficient quality cannot be obtained depending on the cooling condition.

【0008】[0008]

【発明が解決しようとする課題】本発明の目的は、混練
工程において着色剤、極性制御剤、離型剤などが再凝集
や遊離することなく分散状態であり、しかも冷却速度が
一定であり、トナーの品質として帯電量分布が狭分布で
あり、画像を形成したときに地汚れ、画像濃度低下がな
く、耐オフセット性に優れたトナーを得る方法を提供す
ることにある。
An object of the present invention is to keep a colorant, a polarity control agent, a release agent and the like in a dispersed state without re-aggregation or release in a kneading step, and to keep a constant cooling rate. It is an object of the present invention to provide a method of obtaining a toner having a narrow charge amount distribution as a quality of a toner, causing no background stain and a decrease in image density when an image is formed, and having excellent offset resistance.

【0009】[0009]

【課題を解決するための手段】本発明者らは、通常のト
ナーの製造工程において、所定の原材料を混合、溶融混
練した後の冷却条件を規定し、或いは、新規な冷却方式
を採用することによって良質のトナーが得られることを
見出した。本発明はそれに基づいてなされたものであ
る。
SUMMARY OF THE INVENTION The present inventors define cooling conditions after mixing and melting and kneading predetermined raw materials in a normal toner manufacturing process, or adopt a new cooling system. It has been found that high quality toner can be obtained. The present invention has been made on the basis thereof.

【0010】本発明によれば、(1)少なくとも結着樹
脂、着色剤及び帯電制御剤を主原料とし、それを混練機
で混練した後、冷却固化し、粉砕・分級して所定のトナ
ーを得るトナーの製造方法において、混練機外に吐出さ
れた混練物を直ちに冷却装置に移す間にその混練物に外
力を加え、かつ、該冷却装置での冷却速度を冷却開始時
点から20[℃/s]以上にすることを特徴とするトナ
ーの製造方法、(2)前記(1)において、混練物の冷
却後の温度を結着樹脂のガラス転移点以下にすることを
特徴とするトナーの製造方法、(3)前記(1)におい
て、さらに離型剤を加えた主原料を用い、その混練物の
冷却後の温度を該離型剤のガラス転移点以下にすること
を特徴とするトナーの製造方法、(4)前記(1)にお
いて、混練物の厚みを0.5[mm]以下の薄膜状にし
て冷却速度を速め、また冷却速度の混練物内でのばらつ
きを少なくしたことを特徴とするトナーの製造方法、
(5)前記(1)において、混練物の直径を1[mm]
以下の棒状にして冷却速度を速め、また冷却速度の混練
物内でのばらつきを少なくしたことを特徴とするトナー
の製造方法、が提供される。
According to the present invention, (1) at least a binder resin, a colorant and a charge control agent as main materials are kneaded in a kneader, cooled and solidified, crushed and classified to give a predetermined toner. In the method for producing a toner to be obtained, an external force is applied to the kneaded product discharged to the outside of the kneader immediately while it is transferred to a cooling device, and the cooling rate in the cooling device is 20 [° C. / s] or more, and (2) The method for producing a toner according to (1), wherein the temperature after cooling the kneaded material is equal to or lower than the glass transition point of the binder resin. Method, (3) The toner according to the above (1), characterized in that the main raw material to which a release agent is further added is used, and the temperature of the kneaded product after cooling is set to the glass transition point of the release agent or lower. Manufacturing method, (4) In the above (1), thickness of kneaded product The method of manufacturing a toner, wherein 0.5 [mm] in the following thin film faster the cooling rate, also it has less variation in the kneaded product of cooling rate,
(5) In the above (1), the kneaded product has a diameter of 1 [mm].
Provided is a method for producing a toner, characterized in that the cooling rate is increased and the variation in cooling rate in the kneaded material is reduced in the following rod shape.

【0011】また、本発明によれば、(6)前記(4)
において、混練物を薄膜状にする手段として、混練機と
冷却装置との間に所定の温度に加熱した圧延ローラーを
設け、これに混練物を通し、該混練物の温度を少なくと
も結着樹脂の流出開始温度以上の温度に保った状態で薄
膜状にし、その後、該冷却装置で冷却することにより、
薄膜化を容易にすることを特徴とするトナーの製造方
法、(7)前記(5)において、混練物を棒状にする手
段として、混練機と冷却装置との間に所定の温度に加熱
した中空パイプを設けこれに混練物を通し、該混練物の
温度を少なくとも結着樹脂の流出開始温度以上の温度に
保った状態で棒状にし、或いは混練物を延伸機によって
引き伸ばして棒状にし、その後、該冷却機で冷却するこ
とにより、棒状化を容易にすることを特徴とするトナー
の製造方法、が提供される。ここでいう「所定の温度」
とは結局、結着樹脂の流出開始温度以上の温度を意味す
る。
According to the present invention, (6) said (4)
In the above, as a means for forming the kneaded material into a thin film, a rolling roller heated to a predetermined temperature is provided between the kneading machine and the cooling device, and the kneaded material is passed through this, and the temperature of the kneaded material is at least that of the binder resin. By forming a thin film in a state of being kept at a temperature equal to or higher than the outflow starting temperature, and then cooling with the cooling device,
(7) A method for producing a toner, characterized in that a thin film is easily formed. (7) In (5), as a means for forming a kneaded product into a rod shape, a hollow heated to a predetermined temperature between a kneading machine and a cooling device. A pipe is provided through which the kneaded material is passed, and the kneaded material is formed into a rod shape while maintaining the temperature at least at the outflow starting temperature of the binder resin, or the kneaded material is stretched into a rod shape by a stretching machine, and then, Provided is a method for producing a toner, which is characterized by facilitating rod formation by cooling with a cooler. "Predetermined temperature" here
After all, means a temperature equal to or higher than the outflow start temperature of the binder resin.

【0012】[0012]

【発明の実施の形態】以下、本発明をさらに詳細に説明
する。本発明における冷却条件および冷却方法は、通常
の粉砕トナーの製造工程である、原材料の混合、溶融混
練の後の冷却工程についてであり、混合、溶融混練の方
法、条件は問わず、いずれの方法にも適用できる。従来
の冷却方式では、前述のように、せっかく溶融混練工程
において高分散、均一分散状態をつくったとしても、冷
却工程で着色剤、極性制御剤、離型剤が再凝集したり、
遊離したりして、トナーとして優れた品質を得ることは
難しかった。特に、最近の傾向として、高画質を得るた
めにトナーが小粒径化してくると、この傾向は、さらに
顕著に表れるようになったきた。本発明者らは、混練機
により高分散、均一分散となった混練物に、混練機より
吐出後、外力を加えながら冷却工程に搬送し、かつ、冷
却工程の冷却条件として、溶融混練物の冷却速度をある
一定値以上で急冷すると、従来の問題を解決できること
を見いだした。従って、具体的には、混練物に例えば圧
縮力などを与えつつ冷却装置まで移動させ、更に、その
冷却を冷却開始時から20[℃/s]より好ましくは5
0[℃/s]より速い速度で急冷することで達成され
る。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in more detail below. The cooling conditions and the cooling method in the present invention are the usual pulverized toner manufacturing steps, that is, the cooling step after the mixing of the raw materials and the melt-kneading, and any method regardless of the method and the conditions of the mixing and the melt-kneading. Can also be applied to. In the conventional cooling method, as described above, even if a high dispersion in the melt-kneading step, a uniform dispersion state is created, the colorant, the polarity control agent, and the release agent are reaggregated in the cooling step, or
It has been difficult to obtain excellent quality as a toner due to liberation. In particular, as a recent tendency, when the toner has a smaller particle size in order to obtain a high image quality, this tendency has become more remarkable. The inventors of the present invention, the highly kneaded material which is highly dispersed by the kneading machine, after being discharged from the kneading machine, the kneaded material is conveyed to the cooling step while applying an external force, and as the cooling condition of the cooling step, the molten kneaded material is used. It was found that conventional problems can be solved by rapidly cooling at a certain rate or more. Therefore, specifically, the kneaded product is moved to the cooling device while applying, for example, a compressive force to the kneaded product, and the cooling is more preferably 20 [° C./s] from the start of cooling, more preferably 5
It is achieved by quenching at a rate faster than 0 [° C / s].

【0013】ここで、冷却速度によりトナーの品質が変
化する理由としては、一般的に溶融混練によって、高分
散、均一分散状態になったものの、混練機から吐出され
たときの品質(混練物の温度)は、結着樹脂の軟化点以
上になっており、分子運動が活発に行われ易い状態にな
っている。さらに、混練による高分散状態では、高分子
物質(結着樹脂)と、着色剤、帯電制御剤、離型剤など
の粒子との全界面積が非常に大きく、従って、全界面自
由エネルギーも大きい。これをそのままの状態、温度に
放置しておくと、高分子物質である結着樹脂そのもの
や、結着樹脂中で着色剤、帯電制御剤、離型剤などは、
全界面エネルギーを減少させようとする、即ち、最も安
定な存在状態になろうとし、せっかく高分散、均一分散
したものが再凝集、再結合をするようになるためであ
る。この再凝集・再結着の程度は、温度と時間に関係
し、温度が高い程、時間が遅い程、品質は劣化する傾向
がある。
The reason why the quality of the toner changes depending on the cooling rate is that although it is generally in a highly dispersed and uniformly dispersed state by melt kneading, the quality when discharged from a kneader (kneaded product) The temperature is higher than the softening point of the binder resin, and the molecular motion is easily activated. Furthermore, in a highly dispersed state by kneading, the total interfacial area between the polymer substance (binder resin) and particles such as colorants, charge control agents and release agents is very large, so the total interfacial free energy is also large. . If this is left as it is at the temperature, the binder resin itself, which is a polymer substance, and the colorant, charge control agent, release agent, etc. in the binder resin,
This is because it is attempted to reduce the total interfacial energy, that is, the most stable existing state is attempted, and those with high dispersion and uniform dispersion will reaggregate and recombine. The degree of this re-aggregation / re-bonding is related to temperature and time, and the higher the temperature and the slower the time, the more the quality tends to deteriorate.

【0014】この現象をさらに詳しく検討したところ、
以下のようなことが新たにわかった。すなわち、溶融混
練により高分散となった混練物は、混練機から吐出され
たときの品温で保持しても、ある一定時間は前述したよ
うな再凝集、再結合はおこらない。この一定時間とは結
着樹脂や着色剤、帯電制御剤、離型剤の種類、組合わせ
などによっても幾分は異なるが、或る時間を過ぎると急
激に再凝集、再結合などの変化がおこる。しかし、混練
物になんらかの手段により外力が加わっていると、その
間は、高分子中での粒子の運動が抑制される。更に、こ
のような状態を維持した後、20[℃/s]以上という
急速な冷却条件を与えることで、着色剤、帯電制御剤、
離型剤などの再凝集、再結合を抑えられることがわかっ
た。また、特開平2−97969号で提案された方法で
も、冷却を開始した時点からの冷却速度が20[℃/
s]に達しないと、目標の品質トナーが得られなくなる
場合があった。
When this phenomenon was examined in more detail,
The following was newly found. That is, the kneaded material that has been highly dispersed by melt-kneading does not undergo the above-mentioned re-aggregation and re-bonding for a certain period of time even if it is held at the product temperature when it is discharged from the kneading machine. This fixed time will vary somewhat depending on the type and combination of binder resin, colorant, charge control agent, release agent, etc., but after a certain period of time, changes such as reaggregation and recombination will suddenly occur. Get off. However, when an external force is applied to the kneaded material by some means, the movement of particles in the polymer is suppressed during that time. Furthermore, after maintaining such a state, a rapid cooling condition of 20 [° C./s] or more is applied to obtain a colorant, a charge control agent,
It was found that re-aggregation and re-bonding of the release agent can be suppressed. In the method proposed in JP-A-2-97969, the cooling rate from the start of cooling is 20 [° C /
If [s] is not reached, the target quality toner may not be obtained.

【0015】さらに、混練物の冷却後の品質を原材料中
の最低ガラス転移点以下にすることで、その効果は顕著
となる。その理由は、前述から明らかなように、混練物
中の粘度が上がることで再凝集、再結合が抑制できるた
めであり、その管理温度としては、高分子物質の組成が
変化し始めるガラス転移点(Tg)が最も有効である。
具体的には、離型剤を含まない混練物においては、結着
樹脂のガラス転移点以下とし、オフセット防止のために
加える低分子ポリエチレンや、カルナウバワックス等の
離型剤を含んだ混練物では、この離型剤のガラス転移点
以下とすることが望ましい。
Further, by setting the quality of the kneaded product after cooling to be equal to or lower than the lowest glass transition point in the raw material, the effect becomes remarkable. The reason is that, as is clear from the above, re-aggregation and recombination can be suppressed by increasing the viscosity of the kneaded material, and the control temperature is such that the glass transition point at which the composition of the polymer substance begins to change. (Tg) is the most effective.
Specifically, in a kneaded product containing no mold release agent, a kneaded product containing a mold release agent such as low molecular weight polyethylene or carnauba wax at a temperature not higher than the glass transition point of the binder resin and added to prevent offset. Then, it is desirable that the temperature is not higher than the glass transition point of this release agent.

【0016】一方、この冷却条件を達成するための冷却
方法としては、熱交換量の大きい通常の冷却装置を使用
することも考えられるが、一般的に圧延式冷却機では冷
却固化後の厚みが1[mm]程度となってしまう。しか
し、1[mm]程度の厚さであると、トナーとしたと
き、1つ1つのトナー粒子を見てみると、冷却時に表面
に存在していたものと、中心部に存在していたものとで
は帯電特性やオフセット性の異なる粒子となってしま
う。この傾向は、トナー粒子が小さくなるほど顕著にな
る傾向がある。これを解決するためには、冷却速度が均
一なものとする必要があり、具体的には、冷却前の厚さ
が0.5[mm]以下の薄膜状とし、さらに望ましくは
0.1[mm]以下の薄膜状とする必要がある。混練物
を薄膜状にするには、所定の温度(結着樹脂の流出開始
温度以上の温度)に加熱した圧延ローラに混練物を通す
ことにより行なうことができる。また、同一の目的とし
て、混練物の冷却前の形状を1[mmφ]以下の棒状、
さらに望ましくは0.5[mmφ]以下の棒状とする方
法もある。混練物を棒状にするには、例えば混練物を所
定温度(結着樹脂の流出開始温度以上の温度)に加熱し
た中空パイプを通すことにより、あるいは延伸すること
により行うことができる。
On the other hand, as a cooling method for achieving this cooling condition, it is conceivable to use an ordinary cooling device having a large heat exchange amount, but generally, in a rolling type cooling machine, the thickness after cooling and solidification is It becomes about 1 [mm]. However, when the toner has a thickness of about 1 mm, looking at each of the toner particles, one that was present on the surface and one that was present at the center when cooled And, the particles have different charging characteristics and offset properties. This tendency tends to be more remarkable as the toner particles are smaller. In order to solve this, it is necessary to make the cooling rate uniform. Specifically, the thickness before cooling is a thin film having a thickness of 0.5 [mm] or less, more preferably 0.1 [mm]. mm] or less. The kneaded product can be formed into a thin film by passing the kneaded product through a rolling roller heated to a predetermined temperature (a temperature above the outflow starting temperature of the binder resin). For the same purpose, the kneaded product before cooling has a rod shape of 1 [mmφ] or less,
More preferably, there is a method of forming a rod shape of 0.5 [mmφ] or less. The kneaded product can be formed into a rod shape, for example, by passing the kneaded product through a hollow pipe heated to a predetermined temperature (a temperature above the outflow start temperature of the binder resin) or by stretching.

【0017】混練機外に吐出されたトナー混練物を、冷
却固化するのに先立って、一定以下の厚さ或いは太さの
薄膜状又は棒状にすることで、従来の方式に比べ、表面
積が飛躍的に増加して冷却効率が大幅に向上する。な
お、冷却装置は水冷式でも空冷式のいずれも使用でき
る。さらに、混練物を薄膜状、棒状にしたことで、通常
のハンマーミル等の粗粉砕を行なわなくても、工程間の
輸送中に1[mm]以下に小粒径化するため、トータル
的には設備投資額をひくくすることもできるというメリ
ットも合せ持つ。
The toner kneaded product discharged to the outside of the kneading machine is formed into a thin film or rod having a thickness or a certain thickness or less before being cooled and solidified, so that the surface area is greatly increased as compared with the conventional method. And the cooling efficiency is significantly improved. The cooling device can be either water-cooled or air-cooled. Furthermore, since the kneaded product is formed into a thin film or a rod, the particle size can be reduced to 1 [mm] or less during transportation between processes without the need for coarse crushing with a normal hammer mill, etc. Has the merit of being able to reduce the amount of capital investment.

【0018】[0018]

【実施例】次に実施例、比較例をあげて本発明を具体的
に説明する。ここでの部は重量基準である。
EXAMPLES Next, the present invention will be specifically described with reference to Examples and Comparative Examples. Parts herein are by weight.

【0019】実施例1〜10及び比較例1〜5 (イ)実施例1〜5及び比較例1においては、 スチレン−ブチルメタクリレート共重合体(Tg=71[℃])100部 カーボンブラック 10部 ニグロシン 2部 を混合し、混練機で溶融混練する。 (ロ)実施例6〜10においては、 スチレン−ブチルメタクリレート共重合体(Tg=71[℃])100部 カーボンブラック 5部 低分子ポリエチレン(Tg=59[℃]) ニグロシン 2部 を混合し、混練機で溶融混練する。 (ハ)上記の方法で得られた混練物を、それぞれ冷却ロ
ーラーに至る間、スチール製ベルト式圧延機にて挟みな
がら通過させ、更に、冷却ローラー(表面温度15
[℃])にて圧延冷却し、冷却コンベアにて常温まで冷
却し、ハンマーミルにて粗粉砕する。更に、ジェット粉
砕機にて粉砕し、風力式分級機にて分級して5〜20
[μm]の微粉体を得る。この微粉体100部に、コロ
イダルシリカ0.4部を添加し、トナーとした。評価項
目としては、電気抵抗、帯電量、帯電量分布、耐オフセ
ット性、地汚れ濃度、画像濃度、およびキャリア耐久性
について、表1に示す方法にて試験を行なった。
Examples 1 to 10 and Comparative Examples 1 to 5 (a) In Examples 1 to 5 and Comparative Example 1, 100 parts of styrene-butyl methacrylate copolymer (Tg = 71 [° C.]) carbon black 10 parts Nigrosine (2 parts) is mixed and melt-kneaded with a kneader. (B) In Examples 6 to 10, styrene-butyl methacrylate copolymer (Tg = 71 [° C.]) 100 parts Carbon black 5 parts Low molecular weight polyethylene (Tg = 59 [° C.]) Nigrosine 2 parts were mixed, Melt and knead with a kneader. (C) The kneaded product obtained by the above method is passed while being sandwiched by a steel belt type rolling mill while reaching the cooling rollers, and further, the cooling rollers (surface temperature 15
[° C.]), rolling and cooling, cooling to room temperature on a cooling conveyor, and coarse pulverization with a hammer mill. Further, crush with a jet crusher and classify with a wind-powered classifier for 5 to 20
A fine powder of [μm] is obtained. To 100 parts of this fine powder, 0.4 part of colloidal silica was added to obtain a toner. As the evaluation items, the electrical resistance, charge amount, charge amount distribution, offset resistance, background stain density, image density, and carrier durability were tested by the methods shown in Table 1.

【0020】(ニ)比較例2及び比較例3は実施例1〜
5と同一処方、同一条件で混合、溶融混練し、冷却コン
ベアに至る間は、圧延機は通過させず、冷却ローラー
(表面温度15[℃])に導入した。以降は実施例1〜
5と同様にトナー化し、表1に示す方法にて試験を行っ
た。
(D) Comparative Examples 2 and 3 are Examples 1 to 1.
In the same formulation and under the same conditions as in Example 5, the mixture was melted and kneaded, and was introduced into a cooling roller (surface temperature 15 [° C.]) without passing through a rolling mill while reaching a cooling conveyor. After that, Example 1
Toner was formed in the same manner as in No. 5, and the test was conducted by the method shown in Table 1.

【0021】(ホ)比較例4は実施例6〜10と同一処
方、同一条件で混合、溶融混練し、冷却コンベアに至る
間は、圧延機は通過させず、冷却ローラー(表面温度1
5[℃])に導入した。以降は実施例6〜10と同様に
トナー化し、表1に示す方法にて試験を行った。
(E) In Comparative Example 4, the rolling mill was not passed through while mixing, melting and kneading under the same formulation and under the same conditions as in Examples 6 to 10 and reaching the cooling conveyor.
5 [° C.]). Thereafter, the toner was formed in the same manner as in Examples 6 to 10, and the test was conducted by the method shown in Table 1.

【0022】(ヘ)比較例5は実施例6〜10、および
比較例3と同一処方、同一条件で溶融混練してできた混
練物を、圧延機、冷却ローラーを通過させず、放置し、
空冷にて常温まで徐冷し、続いて、上記の粉砕、分級工
程を経て、更に同一処方のコロイダルシリカを添加して
トナーとし、表1に示す方法にて試験を行なった。
(F) In Comparative Example 5, the kneaded product obtained by melt-kneading under the same formulation and under the same conditions as in Examples 6 to 10 and Comparative Example 3 was allowed to stand without passing through a rolling mill or a cooling roller,
The toner was gradually cooled to room temperature by air cooling, and subsequently, through the above-mentioned pulverization and classification steps, colloidal silica having the same formulation was further added to obtain a toner, and the toner was tested by the method shown in Table 1.

【0023】(ト)更に、実施例1〜10および比較例
1〜4では、上記の方法で得られた混練物を、冷却ロー
ラーにて圧延冷却するとき、混練機の吐出口の直後、冷
却ローラーの直前、および冷却ローラー直後の3ヶ所
に、非接触式赤外線照射温度測定器を設け、それぞれの
点での温度を混練機側よりt1、t2、t3とし、混練
物の温度変化Δt1=t1−t2、Δt2=t2−t3
を測定した。また、t1−t3=ΔTとした。更に、そ
れぞれの温度測定器の間の混練物の通過時間s1、およ
びs2を測定し、冷却速度V1およびV2を求めた。ま
た、s1+s2=Sとし、混練機吐出口から冷却ローラ
ー通過後までの冷却速度V=ΔT/Sを求めた。なお、
混練機から冷却ローラーまでの間の混練物の冷却速度V
1は、冷却ローラーの位置を移動することにより調整で
きる。また、冷却ローラーにおける冷却速度V2は、冷
却ローラーのギャップ調整、および冷却ローラーの回転
速度を調整することにより調整可能である。これらを調
整することにより、異なる冷却速度を得た実施例1〜1
0および比較例1〜5の冷却条件をまとめて表2に示
す。
(G) Further, in Examples 1 to 10 and Comparative Examples 1 to 4, when the kneaded product obtained by the above method is rolled and cooled by a cooling roller, it is cooled immediately after the discharge port of the kneader. Non-contact infrared irradiation temperature measuring devices are provided at three positions immediately before the roller and immediately after the cooling roller, and the temperature at each point is set to t1, t2, and t3 from the kneading machine side, and the temperature change of the kneaded product Δt1 = t1. -T2, Δt2 = t2-t3
Was measured. Further, t1−t3 = ΔT. Further, the passing times s1 and s2 of the kneaded material between the respective temperature measuring devices were measured to obtain the cooling rates V1 and V2. Further, s1 + s2 = S, and the cooling rate V = ΔT / S from the kneader discharge port to after passing through the cooling roller was obtained. In addition,
Cooling speed V of the kneaded material between the kneader and the cooling roller
1 can be adjusted by moving the position of the cooling roller. The cooling speed V2 of the cooling roller can be adjusted by adjusting the gap of the cooling roller and adjusting the rotation speed of the cooling roller. Examples 1 to 1 in which different cooling rates were obtained by adjusting these
The cooling conditions of 0 and Comparative Examples 1 to 5 are summarized in Table 2.

【0024】[0024]

【表1】 [Table 1]

【0025】[0025]

【表2】 [Table 2]

【0026】表1に基づく評価方法にて、実施例1〜1
0および比較例1〜5について評価した結果をまとめて
表3に示す。
According to the evaluation method based on Table 1, Examples 1 to 1
Table 3 summarizes the results of evaluation of 0 and Comparative Examples 1 to 5.

【表3】 [Table 3]

【0027】実施例11、12及び比較例6、7 ここで、実施例、比較例は実施例6〜10と同一処方、
同一条件で混練し得られた混練物を冷却するとき、混練
機吐出口後方に、混練物を圧延する圧延ローラーを設
け、その後方にテンションローラーを設け、該圧延物を
引き延ばして薄膜化し、自然放冷により冷却した。圧延
ローラーには、圧延を容易にするため、一般に複写機な
どで定着部に用いられる、ゴム製ヒートローラーを用
い、約140℃に加熱して使用した。また、固化後の混
練物の厚みを、ダイヤルゲージにて測定した。なお、こ
のときの室温は21℃、湿度40%であった。以上の方
法にて作成した混練物を、実施例1〜10と同様の方法
にて、粉砕、分級、およびコロイダルシリカを添加混合
して、トナーとした。表1に基づく評価方法にて、実施
例11、12および比較例6、7について評価した結果
をまとめて表4に示す。
Examples 11 and 12 and Comparative Examples 6 and 7 Here, Examples and Comparative Examples have the same formulation as Examples 6 to 10,
When cooling the kneaded product obtained by kneading under the same conditions, a rolling roller for rolling the kneaded product is provided at the rear of the kneading machine discharge port, a tension roller is provided at the rear of the kneading device, and the rolled product is stretched into a thin film to naturally It was cooled by cooling. For the rolling roller, a rubber heat roller, which is generally used for a fixing unit in a copying machine or the like, was used by heating to about 140 ° C. to facilitate rolling. The thickness of the kneaded product after solidification was measured with a dial gauge. The room temperature at this time was 21 ° C. and the humidity was 40%. The kneaded material prepared by the above method was pulverized, classified, and colloidal silica was added and mixed in the same manner as in Examples 1 to 10 to obtain a toner. Table 4 summarizes the evaluation results of Examples 11 and 12 and Comparative Examples 6 and 7 by the evaluation method based on Table 1.

【0028】[0028]

【表4】 [Table 4]

【0029】実施例13、14及び比較例8、9 ここでの実施例、比較例は、実施例6〜10と同一処
方、同一条件で混練し得られた混練物を冷却するとき、
混練機吐出口後方に、混練物を棒状に引き延ばす延伸機
を設けて棒状化し、自然放冷により冷却した。また、固
化後の混練物の直径を、ダイヤルゲージにて測定した。
なお、このときの室温は21℃、湿度40%であった。
以上の方法にて作成した混練物を、実施例1〜10と同
様の方法にて、粉砕、分級、およびコロイダルシリカを
添加混合して、トナーとした。表1に基づく評価方法に
て、実施例13、14および比較例8、9について評価
した結果をまとめて表5に示す。
Examples 13 and 14 and Comparative Examples 8 and 9 In these Examples and Comparative Examples, when the kneaded products obtained by kneading under the same formulation and under the same conditions as in Examples 6 to 10 were cooled,
A stretching machine for stretching the kneaded product into a rod shape was provided behind the discharge port of the kneading machine to form a rod shape, and cooled by spontaneous cooling. Further, the diameter of the kneaded product after solidification was measured with a dial gauge.
The room temperature at this time was 21 ° C. and the humidity was 40%.
The kneaded material prepared by the above method was pulverized, classified, and colloidal silica was added and mixed in the same manner as in Examples 1 to 10 to obtain a toner. Table 5 shows the evaluation results of Examples 13 and 14 and Comparative Examples 8 and 9 summarized by the evaluation method based on Table 1.

【0030】[0030]

【表5】 [Table 5]

【0031】[0031]

【発明の効果】請求項1の発明によれば、混練によって
結着樹脂中に分散した着色剤、極性制御剤の再凝集が発
生せず、低地汚れ、高濃度、高耐久のトナーを得ること
ができる。請求項2の発明によれば、混練によって結着
樹脂中に分散した着色剤、極性制御剤の再凝集が発生せ
ず、低地汚れ、高濃度、高耐久のトナーを得ることがで
きる。請求項3の発明によれば、混練によって結着樹脂
中に分散した着色剤、極性制御剤および離型剤の再凝集
が発生せず、更には、粉砕工程において離型剤がトナー
表面から遊離せず、低地汚れ、高濃度、高耐久のトナー
を得ることができる。請求項4の発明によれば、混練に
よって結着樹脂中に分散した着色剤、極性制御剤および
離型剤の再凝集が発生せず、更には、粉砕工程において
離型剤がトナー表面から遊離せず、低地汚れ、高濃度、
高耐久のトナーを得ることができることに加え、材料厚
が薄いことによって、粉砕に要するエネルギーの低減が
はかれる。請求項5の発明によれば、混練によって結着
樹脂中に分散した着色剤、極性制御剤および離型剤の再
凝集が発生せず、更には、粉砕工程において離型剤がト
ナー表面から遊離せず、低地汚れ、高濃度、高耐久のト
ナーを得ることができることに加え、材料径が細いこと
によって、粉砕に要するエネルギーの低減がはかれる。
請求項6又は7の発明によれば、混練物の薄膜化又は棒
状化を行なう際に、圧延部における材料の粘度変化を小
さく抑え、連続的に薄膜化又は棒状化する際に課題とな
る材料切れの発生を解消でき、低地汚れ、高濃度、高耐
久のトナーを安定して得ることができる。
According to the invention of claim 1, a colorant dispersed in a binder resin and a polarity control agent are not re-aggregated by kneading, and a toner with low background stain, high density and high durability is obtained. You can According to the invention of claim 2, the colorant and the polarity control agent dispersed in the binder resin by kneading do not re-aggregate, and a toner with low background stain, high concentration and high durability can be obtained. According to the invention of claim 3, re-aggregation of the colorant, the polarity control agent and the release agent dispersed in the binder resin by kneading does not occur, and the release agent is released from the toner surface in the pulverizing step. Without doing so, it is possible to obtain a toner with low background stain, high density and high durability. According to the invention of claim 4, re-aggregation of the colorant, the polarity control agent and the release agent dispersed in the binder resin by kneading does not occur, and the release agent is released from the toner surface in the pulverizing step. No, low soiling, high density,
In addition to being able to obtain a highly durable toner, the energy required for pulverization can be reduced due to the thin material thickness. According to the invention of claim 5, the reaggregation of the colorant, the polarity control agent and the release agent dispersed in the binder resin by kneading does not occur, and the release agent is released from the toner surface in the pulverizing step. In addition to being able to obtain low-contamination, high-concentration, high-durability toner without doing so, the energy required for pulverization can be reduced due to the small material diameter.
According to the invention of claim 6 or 7, when the kneaded product is made into a thin film or formed into a rod, the change in the viscosity of the material in the rolling section is suppressed to a small level, and the material becomes a problem when the film is continuously formed into a thin film or formed into a rod. It is possible to eliminate the occurrence of breakage, and it is possible to stably obtain toner with low background stain, high density, and high durability.

フロントページの続き (56)参考文献 特開 平2−97969(JP,A) 特開 平7−152205(JP,A) 特開 平6−138704(JP,A) (58)調査した分野(Int.Cl.7,DB名) G03G 9/08 Continuation of the front page (56) Reference JP-A-2-97969 (JP, A) JP-A-7-152205 (JP, A) JP-A-6-138704 (JP, A) (58) Fields investigated (Int .Cl. 7 , DB name) G03G 9/08

Claims (7)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 少なくとも結着樹脂、着色剤及び帯電制
御剤を主原料とし、それを混練機で混練した後、冷却固
化し、粉砕・分級して所定のトナーを得るトナーの製造
方法において、混練機外に吐出された混練物を直ちに冷
却装置に移す間にその混練物に外力を加え、かつ、該冷
却装置での冷却速度を冷却開始時点から20[℃/s]
以上にすることを特徴とするトナーの製造方法。
1. A method for producing a toner, comprising at least a binder resin, a colorant and a charge control agent as main raw materials, kneading the mixture with a kneader, cooling and solidifying, crushing and classifying to obtain a predetermined toner, While the kneaded product discharged to the outside of the kneading machine is immediately transferred to the cooling device, an external force is applied to the kneading product, and the cooling rate in the cooling device is 20 [° C / s] from the start of cooling.
A method for producing a toner characterized by the above.
【請求項2】 請求項1において、混練物の冷却後の温
度を結着樹脂のガラス転移点以下にすることを特徴とす
るトナーの製造方法。
2. The method for producing a toner according to claim 1, wherein the temperature of the kneaded material after cooling is set to be equal to or lower than the glass transition point of the binder resin.
【請求項3】 請求項1において、さらに離型剤を加え
た主原料を用い、その混練物の冷却後の温度を該離型剤
のガラス転移点以下にすることを特徴とするトナーの製
造方法。
3. The production of a toner according to claim 1, wherein the main raw material to which a release agent is further added is used, and the temperature of the kneaded product after cooling is set to be equal to or lower than the glass transition point of the release agent. Method.
【請求項4】 請求項1において、混練物の厚みを0.
5[mm]以下の薄膜状にして冷却速度を早め、また冷
却速度の混練物内でのばらつきを少なくしたことを特徴
とするトナーの製造方法。
4. The kneaded product according to claim 1, having a thickness of 0.
A method for producing a toner, characterized in that a thin film having a thickness of 5 [mm] or less is used to accelerate the cooling rate and to reduce variations in the cooling rate within the kneaded product.
【請求項5】 請求項1において、混練物の直径を1
[mm]以下の棒状にして冷却速度を速め、また冷却速
度の混練物内でのばらつきを少なくしたことを特徴とす
るトナーの製造方法。
5. The kneaded material according to claim 1, having a diameter of 1
A method for producing a toner, characterized in that the cooling rate is increased by forming a rod having a size of [mm] or less, and the variation in the cooling rate within the kneaded material is reduced.
【請求項6】 請求項4において、混練物を薄膜状にす
る手段として、混練機と冷却装置との間に所定の温度に
加熱した圧延ローラーを設け、これに混練物を通し、該
混練物の温度を少なくとも該混練機より吐出された時点
の温度に保った状態で薄膜状にし、その後、該冷却装置
で冷却することにより、薄膜化を容易にすることを特徴
とするトナーの製造方法。
6. The kneaded product according to claim 4, wherein a rolling roller heated to a predetermined temperature is provided between the kneader and the cooling device as a means for forming the kneaded product into a thin film, and the kneaded product is passed through the rolling roller. A method for producing a toner, wherein the temperature is maintained at least at a temperature at the time of being discharged from the kneader to form a thin film, and then the film is cooled by the cooling device to facilitate thinning.
【請求項7】 請求項5において、混練物を棒状にする
手段として、混練機と冷却装置との間に所定に加熱した
中空パイプを設けこれに混練物を通し、該混練物の温度
を少なくとも該混練機より吐出された時点の温度に保っ
た状態で棒状にし、或いは混練物を延伸機によって引き
伸ばして棒状にし、その後、該冷却機で冷却することに
より、棒状化を容易にすることを特徴とするトナーの製
造方法。
7. The method according to claim 5, wherein the kneaded product is rod-shaped and a predetermined heated hollow pipe is provided between the kneading machine and the cooling device, and the kneaded product is passed through the hollow pipe to keep the temperature of the kneaded product at least. Characterized by facilitating the bar-shape by making the bar-shape while keeping the temperature at the time of being discharged from the kneader, or stretching the kneaded product by a stretching machine to make a bar-shape, and then cooling it by the cooler. Toner manufacturing method.
JP20152495A 1995-07-14 1995-07-14 Manufacturing method of toner Expired - Lifetime JP3409100B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20152495A JP3409100B2 (en) 1995-07-14 1995-07-14 Manufacturing method of toner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20152495A JP3409100B2 (en) 1995-07-14 1995-07-14 Manufacturing method of toner

Publications (2)

Publication Number Publication Date
JPH0934173A JPH0934173A (en) 1997-02-07
JP3409100B2 true JP3409100B2 (en) 2003-05-19

Family

ID=16442479

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3409100B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1961783A2 (en) 2007-02-26 2008-08-27 Ricoh Company, Ltd. Method for producing resinous particles

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6352561B1 (en) * 1996-12-23 2002-03-05 W. L. Gore & Associates Implant deployment apparatus
US20040138734A1 (en) * 2001-04-11 2004-07-15 Trivascular, Inc. Delivery system and method for bifurcated graft
CA2573889C (en) * 2004-06-16 2014-02-04 Cook Incorporated Thoracic deployment device and stent graft

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1961783A2 (en) 2007-02-26 2008-08-27 Ricoh Company, Ltd. Method for producing resinous particles
US7927777B2 (en) 2007-02-26 2011-04-19 Ricoh Company, Ltd. Method for producing resinous particles

Also Published As

Publication number Publication date
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