JP2008077012A - Method for manufacturing electrophotographic toner - Google Patents

Method for manufacturing electrophotographic toner Download PDF

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JP2008077012A
JP2008077012A JP2006259431A JP2006259431A JP2008077012A JP 2008077012 A JP2008077012 A JP 2008077012A JP 2006259431 A JP2006259431 A JP 2006259431A JP 2006259431 A JP2006259431 A JP 2006259431A JP 2008077012 A JP2008077012 A JP 2008077012A
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water
mass
parts
mixing
pulverized product
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JP5040233B2 (en
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Tadahiro Tsubaki
忠洋 椿
Masahiro Maeda
正博 前田
Hideki Ikeda
英樹 池田
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Casio Computer Co Ltd
Casio Electronics Co Ltd
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Casio Computer Co Ltd
Casio Electronics Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for an electrophotographic toner which is excellent in fog characteristics by preventing aggregation of pulverized particles to improve classification yield in a production process. <P>SOLUTION: The method includes steps of: mixing a source material containing a binder resin and a colorant; melting and kneading the source material mixture; cooling and solidifying the kneaded material and then coarsely pulverizing the material; mixing water of 1 to 10 parts by mass or an alkaline electrolytic water of 0.5 to 10 parts by mass based on 100 parts by mass of the coarse pulverized product; pulverizing the mixture; and classifying the pulverized material. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、電子写真用トナーの製造方法に係り、特に、カブリ特性の良好な電子写真用トナーを高い分級収率で製造する方法に関する。   The present invention relates to a method for producing an electrophotographic toner, and more particularly, to a method for producing an electrophotographic toner having good fog characteristics with a high classification yield.

電子写真方式による画像形成は、一般に、帯電させたトナーにより静電荷像を現像して可視化し、現像により得られたトナー像を用紙に転写し、定着することにより行われる。このような画像形成に用いられるトナーの製造方法としては、粉砕法、重合法等があるが、一般には粉砕法が主流を占めている。   In general, image formation by electrophotography is performed by developing and visualizing an electrostatic image with charged toner, and transferring and fixing the toner image obtained by development onto a sheet. As a method for producing such a toner used for image formation, there are a pulverization method, a polymerization method, and the like. In general, the pulverization method dominates.

粉砕法の一般的な製造方法は、結着樹脂、着色剤、離型剤、及び帯電制御剤等の原料を乾式で混合した後、2軸押出機などで溶融混練し、冷却固化した後に粗粉砕を行い、混練粗砕物を得る。その後、ジェットミルなどで微粉砕を行い、適切な粒度分布になるように分級機で粒度調整を行う。更にシリカなどと一緒に混合機で混合することで表面処理を行い、トナーを得るものである。   A general production method of the pulverization method is to mix raw materials such as a binder resin, a colorant, a release agent, and a charge control agent in a dry manner, then melt and knead with a twin-screw extruder or the like, and after cooling and solidifying, Crushing is performed to obtain a kneaded crushed material. Thereafter, fine pulverization is performed with a jet mill or the like, and the particle size is adjusted with a classifier so as to obtain an appropriate particle size distribution. Further, the toner is obtained by performing surface treatment by mixing with silica etc. in a mixer.

近年の電子写真用トナーにおける要求性能は益々高度になっている。小粒径化、オイルレス化、低温定着化、高転写効率、高画質化がトナーに対する主な要求である。これらに共通するトナーの要素技術としては、顔料、帯電制御剤、離型剤等のトナー内添剤を微細に均一に結着樹脂中に分散させることが必要である。   The required performance of electrophotographic toners in recent years has become increasingly sophisticated. The main requirements for toners are to reduce the particle size, reduce oil, fix at low temperature, increase transfer efficiency, and improve image quality. As an elemental technology common to these toners, it is necessary to disperse a toner internal additive such as a pigment, a charge control agent, and a release agent finely and uniformly in the binder resin.

特に、トナーを小粒径化すると、粒子同士の静電気力やファンデルワールス力による凝集力が増大し、かつ微粉の量が増大するため、粉砕後の分級工程における分級収率が低下するという問題があり、この問題の解決が望まれている。   In particular, when the toner particle size is reduced, the cohesive force due to electrostatic force and van der Waals force between particles increases, and the amount of fine powder increases, so the classification yield in the classification process after pulverization decreases. There is a need to solve this problem.

一方、原料混合物に水を添加して混練し、帯電制御剤の均一な分散を図る方法が提案されている(例えば、特許文献1参照)。   On the other hand, a method has been proposed in which water is added to a raw material mixture and kneaded to achieve uniform dispersion of the charge control agent (see, for example, Patent Document 1).

しかし、この方法によると、確かに帯電制御剤の分散性を向上させることはできるが、粉砕後の粒子の凝集力を低減することはできず、分級収率を向上させることはできない。
特開平4−313762号公報
However, according to this method, it is possible to improve the dispersibility of the charge control agent, but it is not possible to reduce the cohesive force of the particles after pulverization and to improve the classification yield.
JP-A-4-313762

本発明は、以上のような事情の下になされ、製造工程において、粉砕粒子の凝集を防止して分級収率を向上させ、かぶり特性の良好な電子写真用トナーを製造する方法を提供することを目的とする。   The present invention has been made under the circumstances as described above, and provides a method for producing an electrophotographic toner having good fog characteristics by preventing aggregation of pulverized particles and improving classification yield in the production process. With the goal.

上記課題を解決するため、本発明の第1の態様は、結着樹脂及び着色剤を含む原料を混合する工程、原料混合物を溶融混練する工程、混練物を冷却固化した後、粗粉砕する工程、粗粉砕物100質量部に対し、1〜10質量部の水を混合する工程、混合物を粉砕する工程、及び粉砕物を分級する工程を具備する電子写真用トナーの製造方法を提供する。   In order to solve the above problems, the first aspect of the present invention includes a step of mixing a raw material containing a binder resin and a colorant, a step of melting and kneading the raw material mixture, and a step of coarsely pulverizing the kneaded product after cooling and solidifying. An electrophotographic toner manufacturing method comprising a step of mixing 1 to 10 parts by mass of water, a step of pulverizing the mixture, and a step of classifying the pulverized product with respect to 100 parts by mass of the coarsely pulverized product.

本発明の第2の態様は、結着樹脂及び着色剤を含む原料を混合する工程、原料混合物を溶融混練する工程、混練物を冷却固化した後、粗粉砕する工程、粗粉砕物100質量部に対し、0.5〜10質量部のアルカリ電解水を混合する工程、混合物を粉砕する工程、及び粉砕物を分級する工程を具備する電子写真用トナーの製造方法を提供する。   The second aspect of the present invention includes a step of mixing a raw material containing a binder resin and a colorant, a step of melt kneading the raw material mixture, a step of coarsely pulverizing the kneaded product after cooling and solidifying, and 100 parts by mass of the coarsely pulverized product. In contrast, the present invention provides a method for producing an electrophotographic toner comprising a step of mixing 0.5 to 10 parts by mass of alkaline electrolyzed water, a step of pulverizing the mixture, and a step of classifying the pulverized product.

本発明によると、混練物を冷却固化し、粗粉砕した後に、粗粉砕物に水又はアルカリ電解水を添加することで、粒子の凝集を妨げ、分級収率を向上させることができ、かつトナーのカブリ特性の良好な電子写真用トナーを得ることができる。   According to the present invention, the kneaded product is cooled and solidified, coarsely pulverized, and then water or alkaline electrolyzed water is added to the coarsely pulverized product to prevent particle aggregation and improve the classification yield. Thus, an electrophotographic toner having good fog characteristics can be obtained.

以下、本発明の実施の形態について説明する。   Embodiments of the present invention will be described below.

本発明の第1の実施形態に係る電子写真用トナーの製造方法は、結着樹脂及び着色剤を含む混練物を冷却固化し、粗粉砕した後に、粗粉砕物に所定量の水を添加し、これを更に粉砕し、分級することを特徴とする。   In the method for producing an electrophotographic toner according to the first embodiment of the present invention, a kneaded product containing a binder resin and a colorant is cooled and solidified, coarsely pulverized, and then a predetermined amount of water is added to the coarsely pulverized product. This is further pulverized and classified.

このように、粗粉砕物に水を添加し、粉砕及び分級することにより、分級の際の粉砕粒子の凝集を低減することができ、その結果、分級収率が向上する。このように分級の際の粉砕粒子の凝集を低減することができるのは、水は静電気を除電する作用を有するため、分級の際に、粉砕粒子が静電気により凝集することが妨げられるからである。粉砕粒子が凝集すると、超微粉量も増加するため分級収率も低下するが、水の存在により粉砕粒子の静電凝集が解離されるため、分級収率が向上する。また、分級機の機壁への静電付着も低減される。   Thus, by adding water to the coarsely pulverized product, pulverization and classification, aggregation of the pulverized particles during classification can be reduced, and as a result, the classification yield is improved. The reason why the agglomeration of the pulverized particles during classification can be reduced in this way is that water has a function of eliminating static electricity, and therefore, during classification, the pulverized particles are prevented from aggregating due to static electricity. . When the pulverized particles agglomerate, the amount of ultrafine powder increases and the classification yield also decreases. However, since the electrostatic aggregation of the pulverized particles is dissociated by the presence of water, the classification yield is improved. In addition, electrostatic adhesion to the wall of the classifier is also reduced.

本発明の第1の実施形態に係る電子写真用トナーの製造方法において、粗粉砕物に添加される水の量は、粗粉砕物100質量部に対し、1〜10質量部である。水の量が1質量部未満では、水の添加による効果を得ることができず、即ち、超微粉量が多く、分級収率が低く、一方、10質量部を超えても、超微粉量が多く、分級収率の向上が得られない。   In the method for producing an electrophotographic toner according to the first embodiment of the present invention, the amount of water added to the coarsely pulverized product is 1 to 10 parts by mass with respect to 100 parts by mass of the coarsely pulverized product. If the amount of water is less than 1 part by mass, the effect due to the addition of water cannot be obtained, that is, the amount of ultrafine powder is large and the classification yield is low. In many cases, the classification yield cannot be improved.

本発明の第2の実施形態に係る電子写真用トナーの製造方法は、結着樹脂及び着色剤を含む混練物を冷却固化し、粗粉砕した後に、粗粉砕物に所定量のアルカリ電解水を添加し、これを更に粉砕し、分級することを特徴とする。即ち、上述した第1の実施形態に係る電子写真用トナーの製造方法において、水の代わりにアルカリ電解水を添加するものである。   In the method for producing an electrophotographic toner according to the second embodiment of the present invention, a kneaded product containing a binder resin and a colorant is cooled and solidified, coarsely pulverized, and then a predetermined amount of alkaline electrolyzed water is added to the coarsely pulverized product. It is characterized by being added, further pulverized and classified. That is, in the electrophotographic toner manufacturing method according to the first embodiment described above, alkaline electrolyzed water is added instead of water.

このように、水の代わりにアルカリ電解水を用いた場合には、上記除電効果とともに、洗浄効果等の界面活性効果が発揮され、アルカリ電解水が微粉砕した後の微粒子に良く馴染むため、より高い凝集防止効果が発揮される。   In this way, when alkaline electrolyzed water is used instead of water, in addition to the above-mentioned static elimination effect, a surface active effect such as a cleaning effect is exhibited, and the alkaline electrolyzed water is well adapted to fine particles after being finely pulverized. High anti-aggregation effect is demonstrated.

なお、粗粉砕物に添加されるアルカリ電解水の量は、水の場合より少なくてもよく、粗粉砕物100質量部に対し、0.5〜10質量部である。アルカリ電解水の量が0.5質量部未満では、アルカリ電解水の添加による効果を得ることができず、即ち、超微粉量が多く、分級収率が低く、一方、10質量部を超えても、超微粉量が多く、分級収率の向上が得られない。   The amount of alkaline electrolyzed water added to the coarsely pulverized product may be less than that of water, and is 0.5 to 10 parts by mass with respect to 100 parts by mass of the coarsely pulverized product. If the amount of alkaline electrolyzed water is less than 0.5 parts by mass, the effect due to the addition of alkaline electrolyzed water cannot be obtained, that is, the amount of ultrafine powder is large and the classification yield is low, whereas it exceeds 10 parts by mass. However, the amount of ultrafine powder is large, and the improvement of the classification yield cannot be obtained.

アルカリ電解水は、水を電気分解することにより、陰極側に形成されるものである。なお、陽極側からは、酸性電解水が得られる。一般に、酸及びアルカリは、中和して塩を形成するが、酸性水及びアルカリ水は、中和しても塩を形成しないという特徴を有する。従って、酸性電解水及びアルカリ電解水は、酸、アルカリではない。   Alkaline electrolyzed water is formed on the cathode side by electrolyzing water. In addition, acidic electrolyzed water is obtained from the anode side. In general, acids and alkalis are neutralized to form a salt, but acidic water and alkaline water have a characteristic that they do not form a salt even when neutralized. Therefore, acidic electrolyzed water and alkaline electrolyzed water are not acids or alkalis.

即ち、電解水は、水分子が電気分解して相対的に水素イオンに偏りができるために、pHでは酸性及びアルカリ性を示している。そのため、電解水を中和しても塩を形成せず、中性の水に戻ってしまうので、塩により悪影響を受けることはない。   That is, electrolyzed water is acidic and alkaline at pH because water molecules are electrolyzed and can be relatively biased to hydrogen ions. Therefore, even if the electrolyzed water is neutralized, no salt is formed and the water is returned to neutral water, so that it is not adversely affected by the salt.

電気分解に供される水は、通常は、水道水、井戸水、食塩水等が使用される。水道水や井戸水には、カルシウム、マグネシウム、ナトリウム、カリウム等のイオンが含まれており、食塩水には、ナトリウムイオンが含まれているため、電気分解が可能である。   As water used for electrolysis, tap water, well water, salt water, etc. are usually used. Tap water and well water contain ions such as calcium, magnesium, sodium, and potassium, and salt water contains sodium ions, so electrolysis is possible.

濃度2%以下の食塩水を電気分解した場合、陽極からpH2.7以下の強酸性次亜塩素酸水が酸性電解水として得られ、陰極からはpH11〜12の強アルカリ電解水が得られる。   When electrolyzing a salt solution having a concentration of 2% or less, strong acidic hypochlorous acid water having a pH of 2.7 or less is obtained as acidic electrolyzed water from the anode, and strong alkaline electrolyzed water having a pH of 11 to 12 is obtained from the cathode.

以上の本発明の第1及び第2の実施形態において、結着樹脂としては、例えば、ポリエステル樹脂、スチレンアクリル樹脂、エポキシ樹脂等が挙げられる。これらの中では、ポリエステル樹脂が好ましい。   In the first and second embodiments of the present invention described above, examples of the binder resin include a polyester resin, a styrene acrylic resin, and an epoxy resin. In these, a polyester resin is preferable.

着色剤としては、従来公知のものを使用することができる。   A conventionally well-known thing can be used as a coloring agent.

トナーには、更に離型剤、帯電制御剤等を添加することができる。帯電制御剤及び離型剤としては、従来公知の離型剤を用いることができる。そのような離型剤として、低分子量ポリエチレン、低分子量ポリプロピレン、パラフィン等の極性の低いもの或いはカルナバワックス、エステル系等の極性の高いものを挙げることが出来る。また、エマルジョンタイプのカルボキシル基変性ポリオレフィンとして、エチレン、プロピレン、ブテン−1、ペンテン−1等のオレフィン単位を骨格としてカルボキシル基を有するように変性され、かつアンモニアまたはアミンでカルボキシル基の少なくとも一部が中和されたポリエチレンワックス、ポリプロピレンワックス等を使用することも可能である。これらのワックスのうち、カルナバワックスが好ましい。
本発明の第1及び第2の実施形態に係るトナーの製造方法は、次のようにして行われる。
A release agent, a charge control agent, and the like can be further added to the toner. Conventionally known release agents can be used as the charge control agent and the release agent. Examples of such a release agent include those having low polarity such as low molecular weight polyethylene, low molecular weight polypropylene and paraffin, and those having high polarity such as carnauba wax and ester. In addition, the emulsion type carboxyl group-modified polyolefin is modified so as to have a carboxyl group with an olefin unit such as ethylene, propylene, butene-1, and pentene-1 as a skeleton, and at least a part of the carboxyl group is formed with ammonia or amine. It is also possible to use neutralized polyethylene wax, polypropylene wax or the like. Of these waxes, carnauba wax is preferred.
The toner manufacturing methods according to the first and second embodiments of the present invention are performed as follows.

まず、結着樹脂、着色剤、離型剤、及び帯電制御剤等の材料の計量を行い、計量された材料を混合機により混合する。混合機としては、ヘンシェルミキサー、スーパーミキサー、V型ブレンダー、ナウターミキサー等、任意のものを用いることが出来る。
原料混合物は、次いで混練機に供給され、そこで溶融混練される。混練機としては、二軸押出し混練機及び単軸押出し混練機等の押出し混練機、連続式2本ロールミル、連続式3本ロールミル及びバッチ式ロールミル等のオープンロール型混練機等、任意の型のものを用いることができる。
First, materials such as a binder resin, a colorant, a release agent, and a charge control agent are measured, and the measured materials are mixed by a mixer. As a mixing machine, arbitrary things, such as a Henschel mixer, a super mixer, a V-type blender, and a Nauta mixer, can be used.
The raw material mixture is then fed to a kneader where it is melt kneaded. As the kneading machine, any type of extrusion kneading machine such as a twin-screw extrusion kneading machine and a single-screw extrusion kneading machine, an open roll type kneading machine such as a continuous two-roll mill, a continuous three-roll mill, and a batch roll mill can be used. Things can be used.

混練機から排出された溶融混練物は、通常、トナーの製造に用いられる方法に従って、冷却され、粗粉砕される。これによって得た粗粉砕物に対し、水又はアルカリ電解水を添加し、混合する。混合には、上述したヘンシェルミキサー、スーパーミキサー、V型ブレンダー、ナウターミキサー等、任意のものを用いることが出来る。   The melt-kneaded product discharged from the kneader is usually cooled and coarsely pulverized according to the method used for the production of toner. Water or alkaline electrolyzed water is added to the coarsely pulverized product thus obtained and mixed. For mixing, any of the above-described Henschel mixer, super mixer, V-type blender, nauter mixer, and the like can be used.

次に、水又はアルカリ電解水を混合した混合物を微粉砕し、次いで所定の粒度に分級して、トナー粒子母体が得られる。なお、粗粉砕及び微粉砕には、衝突板式粉砕機等の気流粉砕機を用いることができ、分級には、様々な気流分級機を用いることができる。   Next, the mixture obtained by mixing water or alkaline electrolyzed water is finely pulverized, and then classified to a predetermined particle size to obtain a toner particle matrix. For coarse pulverization and fine pulverization, an airflow pulverizer such as a collision plate pulverizer can be used, and various airflow classifiers can be used for classification.

この場合、微粉砕された粒子は、水又はアルカリ電解水の存在のため凝集せず、超微粉量も少ない。そのため分級収率が大幅に向上する。また、超微粉量が少ないため分級機の機壁への付着が低減でき、かつかぶりも低減できる。   In this case, the finely pulverized particles do not aggregate due to the presence of water or alkaline electrolyzed water, and the amount of ultrafine powder is small. Therefore, the classification yield is greatly improved. In addition, since the amount of ultrafine powder is small, adhesion to the wall of the classifier can be reduced, and fogging can be reduced.

このようにして得たトナー粒子母体に、シリカ等の外添剤を加え、混合・攪拌することにより、電子写真用トナーが得られる。   An electrophotographic toner can be obtained by adding an external additive such as silica to the toner particle matrix thus obtained, followed by mixing and stirring.

実施例
以下、本発明の実施例及び比較例を示し、本発明について更に具体的に説明する。
Examples Hereinafter, examples and comparative examples of the present invention will be shown to describe the present invention more specifically.

まず、下記に示す配合の原材料をヘンシェルミキサー(三井鉱山(株)製)にて混合し、二軸押出混練機により溶融混練した。   First, raw materials having the following composition were mixed with a Henschel mixer (manufactured by Mitsui Mining Co., Ltd.) and melt-kneaded with a twin-screw extrusion kneader.

架橋ポリエステル樹脂(軟化点141℃、ガラス転移点62℃) 93質量%
着色剤 (C.Iピグメントレッド 57:1) 3質量%
離型剤 (三洋化成(株)製 ビスコール660P) 3質量%
帯電制御剤 (オリエント化学(株)製 E−84) 1質量%
得られた混練物を空気中で冷却した後、ロートプレックス(三井鉱山(株)製)にて粗粉砕し、目開き2mmの篩いに通し、最大径2mm以下の粗粉砕品を得た。
Cross-linked polyester resin (softening point 141 ° C., glass transition point 62 ° C.) 93% by mass
Colorant (C.I Pigment Red 57: 1) 3% by mass
Mold release agent (Sanyo Chemical Co., Ltd., Biscol 660P) 3% by mass
Charge control agent (E-84, manufactured by Orient Chemical Co., Ltd.) 1% by mass
The obtained kneaded product was cooled in the air, and then coarsely pulverized with a Rotoplex (manufactured by Mitsui Mining Co., Ltd.), and passed through a sieve having an opening of 2 mm to obtain a coarsely pulverized product having a maximum diameter of 2 mm or less.

得られた粗粉砕物100質量部に対し、下記表1に示すように、種々の量の水又はアルカリ電解水を添加し、ヘンシェルミキサーで1分間混合した。次いで、水又はアルカリ電解水が添加された粗砕物を粉砕圧0.5MPaに調整した衝突板式粉砕機(日本ニューマチック工業社製「IDS−10」)にて質量平均粒径5.8μmに微粉砕し、さらに分級機(日本ニューマチック工業社製「DSX−10」で分級して、6.0μmの着色微粒子を得た。   As shown in Table 1 below, various amounts of water or alkaline electrolyzed water were added to 100 parts by mass of the coarsely pulverized product, and mixed for 1 minute with a Henschel mixer. Next, the mass average particle size was reduced to 5.8 μm with a collision plate type pulverizer (“IDS-10” manufactured by Nippon Pneumatic Industry Co., Ltd.) in which the crushed material to which water or alkaline electrolyzed water was added was adjusted to a pulverization pressure of 0.5 MPa. The resultant was pulverized and further classified with a classifier (“DSX-10” manufactured by Nippon Pneumatic Industry Co., Ltd.) to obtain 6.0 μm colored fine particles.

次に、この着色微粒子100質量部、疎水性シリカ(日本アエロジル社製「R972」)1質量部および疎水性シリカ(日本アエロジル社製「RX50」)0.5%を、ヘンシェルミキサーで混合し、トナーを得た。   Next, 100 parts by mass of the colored fine particles, 1 part by mass of hydrophobic silica (“R972” manufactured by Nippon Aerosil Co., Ltd.) and 0.5% of hydrophobic silica (“RX50” manufactured by Nippon Aerosil Co., Ltd.) are mixed with a Henschel mixer. A toner was obtained.

以上の実施例及び比較例で得たトナー試料について、下記の特性の測定及び試験を行い、特性を評価した。   The toner samples obtained in the above examples and comparative examples were measured and tested for the following characteristics to evaluate the characteristics.

1.粒径及び超微粉量の測定
ビーカーに試料少量と精製水、界面活性剤を入れ、超音波洗浄器にて分散したものを試料として用い、マルチサイザーII(コールター(株)製)により測定した。アパーチャーは100μmで行い、カウントは50,000個で行い、体積、個数分布をそれぞれ得て、体積分布のメジアン径を平均粒径とし、個数分布の2μm以下の割合(%)を超微粉量とした。
1. Measurement of particle size and amount of ultrafine powder A small sample, purified water, and a surfactant were placed in a beaker and dispersed with an ultrasonic cleaner, and the sample was measured with Multisizer II (manufactured by Coulter Co., Ltd.). The aperture is 100 μm, the count is 50,000, the volume and number distributions are obtained, the median diameter of the volume distribution is the average particle diameter, and the ratio (%) of the number distribution of 2 μm or less is the amount of ultrafine powder. did.

2.分級収率(%)
下記の式により、分級収率(%)を求めた。
2. Classification yield (%)
The classification yield (%) was determined by the following formula.

分級収率=((得られた分級品総量)÷(投入した微粉砕物総量))×100
3.かぶり
非磁性一成分現像装置「カシオページプレストN−5」(カシオ計算機(株)製:カラープリンタ毎分29枚機(A4横)、プロセススピード129mm/sec)にトナーを実装し、通常環境(25℃、50%RH)において、普通紙(XEROX−P紙A4サイズ)を用いて5%印字画像を10,000枚連続印字した後、白紙印字を行い、印字している途中でフロント扉を開けることにより、印字を強制終了させ、その時のOPCドラム上のカブリトナーをメンディングテープに写しとり、目視にて比較した。
Classification yield = ((Total amount of classified product obtained) ÷ (Total amount of finely pulverized product charged)) × 100
3. Fog A non-magnetic one-component developing device “Casio Page Presto N-5” (manufactured by Casio Computer Co., Ltd .: 29 printers per minute (A4 horizontal), process speed 129 mm / sec) with toner mounted in a normal environment ( After printing 10,000 sheets of 5% print images continuously on plain paper (XEROX-P paper A4 size) at 25 ° C. and 50% RH), perform blank paper printing and open the front door while printing. By opening, the printing was forcibly terminated, and the fog toner on the OPC drum at that time was copied onto a mending tape, and compared visually.

比較例2と比較し、比較例2よりカブリが少ない場合は○、比較例2とカブリ量が同等の場合は△、比較例2よりカブリが多い場合は×とした。   In comparison with Comparative Example 2, the case where there was less fog than in Comparative Example 2 was marked as ◯, the case where the amount of fog was equivalent to that in Comparative Example 2 was Δ, and the case where there was more fog than Comparative Example 2 was marked as x.

以上の試験結果を下記表1に示す。

Figure 2008077012
The above test results are shown in Table 1 below.
Figure 2008077012

上記表1から、以下のことが明らかである。即ち、粗粉砕物100質量部に対し、0.5〜10質量のアルカリ電解水を添加した実施例1、3、及び7、粗粉砕物100質量部に対し、1〜10質量の水を添加した実施例2、4〜6は、いずれも超微粉量が25%以下と少なく、分級収率が66%以上と高く、かつかぶりが少ないという優れた結果を得た。   From Table 1 above, the following is clear. That is, Examples 1, 3, and 7 in which 0.5 to 10 mass of alkaline electrolyzed water was added to 100 parts by mass of the coarsely pulverized product, and 1 to 10 masses of water were added to 100 parts by mass of the coarsely pulverized product. In Examples 2 and 4 to 6, excellent results were obtained in which the amount of ultrafine powder was as low as 25% or less, the classification yield was as high as 66% or more, and the fog was small.

これに対し、粗粉砕物に対し水またはアルカリ電解水を添加していない比較例1、水の添加量が0.5質量%と少ない比較例2、水の添加量が12質量%と多い比較例3は、超微粉量が27%以上と多く、分級収率は64%以下と低かった。また、比較例1及び比較例3は、かぶりが比較例2より多かった。   In contrast, Comparative Example 1 in which water or alkaline electrolyzed water is not added to the coarsely pulverized product, Comparative Example 2 in which the amount of water added is as small as 0.5% by mass, and Comparative Example 2 in which the amount of water added is as large as 12% by mass. In Example 3, the amount of ultrafine powder was as high as 27% or more, and the classification yield was as low as 64% or less. Further, Comparative Example 1 and Comparative Example 3 had more fog than Comparative Example 2.

Claims (2)

結着樹脂及び着色剤を含む原料を混合する工程、
原料混合物を溶融混練する工程、
混練物を冷却固化した後、粗粉砕する工程、
粗粉砕物100質量部に対し、1〜10質量部の水を混合する工程、
混合物を粉砕する工程、及び
粉砕物を分級する工程
を具備することを特徴とする電子写真用トナーの製造方法。
Mixing a raw material containing a binder resin and a colorant;
A step of melt-kneading the raw material mixture,
A step of coarsely pulverizing the kneaded product after cooling and solidifying,
A step of mixing 1 to 10 parts by mass of water with respect to 100 parts by mass of the coarsely pulverized product,
A method for producing an electrophotographic toner, comprising: a step of pulverizing a mixture; and a step of classifying the pulverized product.
結着樹脂及び着色剤を含む原料を混合する工程、
原料混合物を溶融混練する工程、
混練物を冷却固化した後、粗粉砕する工程、
粗粉砕物100質量部に対し、0.5〜10質量部のアルカリ電解水を混合する工程、
混合物を粉砕する工程、及び
粉砕物を分級する工程
を具備することを特徴とする電子写真用トナーの製造方法。
Mixing a raw material containing a binder resin and a colorant;
A step of melt-kneading the raw material mixture,
A step of coarsely pulverizing the kneaded product after cooling and solidifying,
A step of mixing 0.5 to 10 parts by mass of alkaline electrolyzed water with respect to 100 parts by mass of the coarsely pulverized product,
A method for producing an electrophotographic toner, comprising: a step of pulverizing a mixture; and a step of classifying the pulverized product.
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004013049A (en) * 2002-06-11 2004-01-15 Matsushita Electric Ind Co Ltd Toner and image forming apparatus
JP2004198570A (en) * 2002-12-17 2004-07-15 Canon Inc Black magnetic toner

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004013049A (en) * 2002-06-11 2004-01-15 Matsushita Electric Ind Co Ltd Toner and image forming apparatus
JP2004198570A (en) * 2002-12-17 2004-07-15 Canon Inc Black magnetic toner

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