JP2007093882A - Method for manufacturing electrophotographic toner - Google Patents

Method for manufacturing electrophotographic toner Download PDF

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JP2007093882A
JP2007093882A JP2005281840A JP2005281840A JP2007093882A JP 2007093882 A JP2007093882 A JP 2007093882A JP 2005281840 A JP2005281840 A JP 2005281840A JP 2005281840 A JP2005281840 A JP 2005281840A JP 2007093882 A JP2007093882 A JP 2007093882A
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fine powder
toner
particles
electrophotographic toner
external additive
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JP4561566B2 (en
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Tadahiro Tsubaki
忠洋 椿
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Casio Computer Co Ltd
Casio Electronics Co Ltd
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Casio Electronics Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for manufacturing electrophotographic toner that can prevent white stripes or fog in an image by effectively decreasing ultrafine powder. <P>SOLUTION: The method includes steps of mixing and kneading a binder resin, a colorant and a charge control agent, pulverizing the kneaded material from the kneading step, classifying a fine powder material from the pulverizing step, intensively stirring a fine powder material from the classifying step to embed an ultrafine powder material included in the fine powder material into mother particles of the fine powder material, and adding an external additive to the fine particles from the intensive stirring step, wherein an ultrafine powder material in a size of 2 μm or less is decreased by 5% or more in the intensive stirring step. <P>COPYRIGHT: (C)2007,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、超微紛体の量を減少させた電子写真用トナーの製造方法に関する。   The present invention relates to a method for producing an electrophotographic toner, and more particularly, to a method for producing an electrophotographic toner in which the amount of ultrafine powder is reduced.

一般に、電子写真用トナーは、着色剤、結着樹脂、帯電制御剤、および離型剤を含む原料混合物を溶融混練し、粉砕し、分級することにより製造される。このような製造方法により得られる、いわゆる粉砕トナーは、極めて小粒径の超微紛体を含んでいる。   In general, an electrophotographic toner is produced by melt-kneading, pulverizing, and classifying a raw material mixture containing a colorant, a binder resin, a charge control agent, and a release agent. The so-called pulverized toner obtained by such a manufacturing method contains an ultrafine powder having a very small particle diameter.

一方、近年の高画質化、低消費量等の顧客要求に応じて、トナー開発においてはトナーの小粒径化が重要な要素である。トナーの小粒径化が進む中で、粉砕にジェット気流を用いて得た粉砕トナーにおいては、トナー母粒子に混在する、設計者の予期せぬ粒径2μm以下の超微粉体の制御が重要になる。超微粉体の割合が多いと、非磁性一成分トナーにおいては、トナーの凝集による薄層形成不良等が生じ、画像に白スジ、カブリの増大となって現われ易い。   On the other hand, in response to customer demands such as high image quality and low consumption in recent years, it is an important factor in toner development to reduce the toner particle size. In the pulverized toner obtained by using a jet stream for pulverization as the particle size of the toner advances, the control of the ultra fine powder having a particle diameter of 2 μm or less, which is not expected by the designer, is mixed in the toner base particles. Become important. When the ratio of the ultrafine powder is large, in the non-magnetic one-component toner, a thin layer formation failure or the like due to toner aggregation occurs, and the image is likely to appear as white streaks and fogging.

このような問題を解決するため、気流で分級することにより超微粉体を除去する方法が提案されている(例えば、特許文献1参照)が、この方法は、専用の装置を必要とし、しかも装置が複雑であるという問題がある。   In order to solve such a problem, a method of removing ultrafine powder by classifying with an air stream has been proposed (see, for example, Patent Document 1), but this method requires a dedicated device, and There is a problem that the apparatus is complicated.

また、外添剤添加用の混合機を用いてプレミキシングをしている方法もある(例えば、特許文献2参照)が、この方法は超微粉体の除去が目的ではなく、トナーの凝集体の解砕が目的でありまた、混合機の回転速度が低いため、超微粉体の除去には効果がない。
特開2000−267353号公報 特開平10−319629号公報
In addition, there is a method of premixing using a mixer for adding external additives (see, for example, Patent Document 2), but this method is not intended to remove ultrafine powder, and toner aggregates. In addition, since the rotational speed of the mixer is low, there is no effect in removing ultrafine powder.
JP 2000-267353 A Japanese Patent Laid-Open No. 10-319629

本発明は、以上の事情の下になされ、超微粉体を効果的に減少させることにより画像に白スジ、カブリが発生するのを防止することの可能な電子写真用トナーの製造方法を提供することを目的とする。   The present invention has been made under the above circumstances, and provides an electrophotographic toner manufacturing method capable of preventing white streaks and fogging in an image by effectively reducing ultrafine powder. The purpose is to do.

上記課題を解決するため、本発明は、結着樹脂、着色剤および帯電制御剤を混合および混練する工程、前記混練工程からの混練物を粉砕する工程、前記粉砕工程からの微粉体を分級する工程、前記分級工程からの微粉体を強攪拌し、微粉体中に含まれる超微粉体を微粉体母粒子に埋没させる工程、および前記強攪拌工程からの微粒子に外添剤を添加する工程を具備し、前記強攪拌工程において、2μm以下の超微粉体を5%以上減少させることを特徴と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 present invention classifies a binder resin, a colorant and a charge control agent by mixing and kneading, a step of pulverizing a kneaded product from the kneading step, and a fine powder from the pulverizing step. Step, strongly stirring the fine powder from the classification step, burying the ultrafine powder contained in the fine powder in the fine powder mother particles, and adding the external additive to the fine particles from the strong stirring step And a method of producing an electrophotographic toner, wherein ultrafine powder of 2 μm or less is reduced by 5% or more in the strong stirring step.

かかる電子写真用トナーの製造方法において、前記強攪拌工程を、前記外添剤添加工程で用いた混合機を用いて、前記外添剤添加工程における混合機の駆動時間および/または回転数を越える駆動時間および/または回転数で混合機を駆動することにより行うことができる。この場合、強攪拌工程において、粒径5〜15nmのシリカを0.1〜0.5質量%添加することができる。   In such a method for producing an electrophotographic toner, the strong stirring step exceeds the driving time and / or the rotational speed of the mixer in the external additive addition step using the mixer used in the external additive addition step. This can be done by driving the mixer with drive time and / or speed. In this case, 0.1 to 0.5% by mass of silica having a particle size of 5 to 15 nm can be added in the strong stirring step.

以上のような方法により、粒径5.0〜0〜9.0μmのトナーを製造することができる。
なお、外添剤としては、粒径5〜15nmのシリカを用いることができる。
By the method as described above, a toner having a particle size of 5.0 to 0 to 9.0 μm can be produced.
As an external additive, silica having a particle size of 5 to 15 nm can be used.

本発明によると、強攪拌工程において、分級工程からの超微粉体を含む微粉体を、高剪断力をもって混合することにより、超微粉体粒子が微粉体の母体粒子中へ埋め込まれ、それによって5%以上の減少率で超微粉体粒子の数を減少させたトナーを得ることができる。このようなトナーを用いることにより、白スジおよびカブリのない良好な画質の形成が可能である。   According to the present invention, in the strong stirring step, the fine powder including the ultra fine powder from the classification step is mixed with a high shearing force so that the ultra fine powder particles are embedded in the fine base material particles. Thus, it is possible to obtain a toner in which the number of ultrafine powder particles is reduced at a reduction rate of 5% or more. By using such a toner, it is possible to form a good image quality without white stripes and fog.

以下、発明を実施するための最良の形態について説明する。   The best mode for carrying out the invention will be described below.

本発明の一実施形態に係るトナーの製造方法は、結着樹脂、着色剤、および帯電制御剤を含む原料混合物を溶融混練し、混練物を粉砕し、分級し、強攪拌し、外添剤を添加することにより行われる。   A method for producing a toner according to an embodiment of the present invention includes melt-kneading a raw material mixture containing a binder resin, a colorant, and a charge control agent, pulverizing the kneaded material, classifying, vigorously stirring, and external additives. Is added.

結着樹脂、着色剤、および帯電制御剤を含むトナー原料は、最初に、混合機により混合される。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。   Toner raw materials including a binder resin, a colorant, and a charge control agent are first 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.

結着樹脂としては、公知のものを含む広い範囲から選択することができる。具体的には、ポリスチレン、スチレン−アクリル酸エステル共重合体、スチレン−メタクリル酸共重合体、およびスチレン−ブタジエン共重合体などのスチレン系樹脂をはじめ、飽和ポリエステル樹脂、不飽和ポリエステル樹脂、エポキシ樹脂、フェノール樹脂、クマロン樹脂、キシレン樹脂、塩化ビニル樹脂、ポリオレフィン樹脂などが例示でき、これらの樹脂を二種類以上組み合わせて用いてもよい。なお、これらの樹脂のうち、ポリエステル系樹脂、特に架橋ポリエステル樹脂が好ましい。   The binder resin can be selected from a wide range including known ones. Specific examples include styrene resins such as polystyrene, styrene-acrylic acid ester copolymers, styrene-methacrylic acid copolymers, and styrene-butadiene copolymers, saturated polyester resins, unsaturated polyester resins, and epoxy resins. Phenolic resin, coumarone resin, xylene resin, vinyl chloride resin, polyolefin resin and the like can be exemplified, and two or more of these resins may be used in combination. Of these resins, polyester resins, particularly crosslinked polyester resins are preferred.

着色剤および帯電制御剤としては、通常、電子写真用トナーに使用される任意のものを使用可能である。   As the colorant and charge control agent, any of those usually used for electrophotographic toners can be used.

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、二軸押出し混練機およ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本ロールミルおよ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。   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.

混練機からの混練物は、次いで冷却された後、粉砕される。この粉砕工程では、例えばハンマーミル等を用いて数mmの粒径に粗粉砕し、次いでジェットミル等を用いて5〜15μm程度の粒径に微粉砕してもよい。   The kneaded product from the kneader is then cooled and then pulverized. In this pulverization step, for example, coarse pulverization to a particle size of several mm using a hammer mill or the like may be performed, and then pulverized to a particle size of about 5 to 15 μm using a jet mill or the like.

次いで、粉砕により得た微粉体は、微小粒子と粗大粒子を除去して所定の平均粒子径を得るように分級される。分級には、風力分級機を用いることができる。   Next, the fine powder obtained by pulverization is classified so as to obtain a predetermined average particle diameter by removing fine particles and coarse particles. An air classifier can be used for classification.

なお、分級によっては2μm以下の超微粉体を除去することができないため、分級工程からの微粉体中には、なお2μm以下の超微粉体が含まれている。このような超微粉体の存在は、トナーの流動性を低下させたり、画像形成装置内のトナー飛散を生じたり、画像に白スジ、カブリを生じさせてしまうため、減少させる必要がある。   In addition, since ultrafine powder of 2 μm or less cannot be removed depending on classification, ultrafine powder of 2 μm or less is still included in the fine powder from the classification step. The presence of such ultra fine powders needs to be reduced because it reduces toner fluidity, causes toner scattering in the image forming apparatus, and causes white streaks and fog in the image.

本発明では、このような超微粉体をトナーから取り除くのではなく、母体粒子中に埋め込むことにより、その量を減少させている。この超微粉体の母体粒子中への埋め込みに、強攪拌工程が行われる。強攪拌工程は、分級工程からの超微粉体を含む微粉体を、高剪断力をもって混合することにより行われる。高剪断力による混合は、混合機を高速駆動することにより、混合機を長時間駆動することにより、或いはその双方により行うことができる。このような強攪拌により、超微粉体粒子は微粉体の母体粒子中へ埋め込まれ、その結果、超微粉体粒子の数が大幅に減少される。   In the present invention, such an ultra fine powder is not removed from the toner, but is embedded in the base particles to reduce the amount thereof. A strong stirring step is performed for embedding the ultrafine powder in the base particles. The strong stirring step is performed by mixing the fine powder including the ultra fine powder from the classification step with a high shearing force. Mixing with a high shear force can be performed by driving the mixer at high speed, driving the mixer for a long time, or both. By such strong stirring, the ultrafine powder particles are embedded in the base particles of the fine powder, and as a result, the number of ultrafine powder particles is greatly reduced.

強攪拌工程は、超微粉体粒子の数の減少率が5%以上になるように行われる。減少率が5%未満では、強攪拌工程の効果がなく、超微粉体粒子の存在から生ずる、白スジはカブリの発生といった問題を防止することができない。   The strong stirring step is performed so that the reduction rate of the number of ultrafine powder particles is 5% or more. If the reduction rate is less than 5%, there is no effect of the strong stirring step, and white streaks resulting from the presence of ultrafine powder particles cannot prevent the occurrence of fog.

強攪拌工程は、引き続き行われる外添剤添加工程で用いる混合機と同一の混合機を用いて行うことができる。この場合、外添剤添加工程における混合機の駆動時間および/または回転数を越える駆動時間および/または回転数で混合機を駆動することにより行うことができる。   The strong stirring step can be performed using the same mixer as that used in the subsequent external additive addition step. In this case, it can be carried out by driving the mixer at a driving time and / or rotational speed exceeding the driving time and / or rotational speed of the mixer in the external additive addition step.

この強攪拌工程において、トナーの流動性および均一性を改善するため、シリカ粒子を添加することが望ましい。添加されるシリカ粒子の粒径は5〜15nmであるのが好ましい。シリカ粒子の粒径が小さすぎる場合にはシリカ粒子添加の効果が得にくく、大きすぎる場合には強攪拌による超微粉体粒子の減少効果が得にくく、画像に白スジが生じ易くなる。また、シリカ粒子の添加量は、0.1〜0.5質量%であるのが好ましい。シリカ粒子の添加量が少なすぎる場合には、シリカ粒子添加の効果が得にくく、大きすぎる場合には、画像にカブリが生じ易くなる。   In this strong stirring step, it is desirable to add silica particles in order to improve the fluidity and uniformity of the toner. The particle diameter of the added silica particles is preferably 5 to 15 nm. When the particle size of the silica particles is too small, it is difficult to obtain the effect of adding silica particles, and when it is too large, it is difficult to obtain the effect of reducing the ultrafine powder particles by vigorous stirring, and white streaks are likely to occur in the image. Moreover, it is preferable that the addition amount of a silica particle is 0.1-0.5 mass%. When the addition amount of the silica particles is too small, it is difficult to obtain the effect of adding the silica particles, and when it is too large, the image is likely to be fogged.

強攪拌工程により超微粉体粒子が減少した微粉体は、外添剤添加工程に供される。外添剤の添加は、トナーの流動性の向上、摩擦帯電量の調整、クリーニング性の向上等を目的として行われ、外添剤としては、シリカ、酸化チタン、脂肪酸金属塩等が用いられ、特に疎水性シリカが好適に用いられる。   The fine powder in which the ultrafine powder particles are reduced by the strong stirring process is subjected to the external additive adding process. The external additive is added for the purpose of improving the fluidity of the toner, adjusting the triboelectric charge amount, improving the cleaning property, etc., and as the external additive, silica, titanium oxide, fatty acid metal salt, etc. are used. In particular, hydrophobic silica is preferably used.

以上のような方法により製造されたトナーの粒径は、5.0〜0〜9.0μmであるのが望ましい。トナーの粒径が小さすぎる場合には、画像に白スジおよびカブリが生じ易く、大きすぎる場合には、画像にカブリが生じ易くなる。   The particle size of the toner produced by the above method is desirably 5.0 to 0 to 9.0 μm. When the particle size of the toner is too small, white streaks and fog are likely to occur in the image, and when it is too large, fog is likely to occur in the image.

以下に、本発明の実施例および比較例について説明する。   Examples of the present invention and comparative examples will be described below.

実施例1
架橋ポリエステル樹脂(Tg:62℃、Tm:141℃)93.0質量部、着色剤(C.Iピグメントレッド 57.1)5質量部、離型剤(ビスコール660P:三洋化成社製)3.0質量%、帯電制御剤(E−84:オリエント化学社製)1.0質量部をヘンシェルミキサー(三井鉱山社製)にて予備混合した。
Example 1
2. 93.0 parts by mass of a crosslinked polyester resin (Tg: 62 ° C., Tm: 141 ° C.), 5 parts by mass of a colorant (CI Pigment Red 57.1), a release agent (Biscol 660P: manufactured by Sanyo Chemical Co., Ltd.) 0% by mass and 1.0 part by mass of a charge control agent (E-84: manufactured by Orient Chemical Co., Ltd.) were premixed with a Henschel mixer (manufactured by Mitsui Mining Co., Ltd.).

得られた原料混合物を二軸押出混練機により溶融混練を行い、混練物を得た。この混練物を冷却した後、カウンタージェット式粉砕機(AFG−2:ホソカワミクロン社製)にて質量平均粒径5.8μmに粉砕し、更に分級機(エルボージェット:マツボー社製)で分級し、平均粒径6.2μmの着色微粒子を得た。   The obtained raw material mixture was melt-kneaded with a twin-screw extrusion kneader to obtain a kneaded product. After cooling the kneaded product, it was pulverized to a mass average particle size of 5.8 μm with a counter jet pulverizer (AFG-2: manufactured by Hosokawa Micron), and further classified with a classifier (Elbow Jet: manufactured by Matsubo), Colored fine particles having an average particle diameter of 6.2 μm were obtained.

この着色微粒子は、4.3%(個数)の2μm以下の超微紛体を含んでいた。   The colored fine particles contained 4.3% (number) of ultrafine particles of 2 μm or less.

次いで、この着色微粒子に疎水性シリカ(R812:日本アエロジル社製)0.1質量部を加え、ヘンシェルミキサー(FM−10)により、羽の周速40m/sで5分間、強攪拌した。この疎水性シリカの粒径は7nmであった。   Next, 0.1 part by mass of hydrophobic silica (R812: manufactured by Nippon Aerosil Co., Ltd.) was added to the colored fine particles, and the mixture was vigorously stirred with a Henschel mixer (FM-10) at a peripheral speed of wings of 40 m / s for 5 minutes. The particle size of this hydrophobic silica was 7 nm.

この強攪拌工程により、2μm以下の超微紛体は4.0%(個数)に減少した。強攪拌工程による超微紛体の減少率は、5.6%であった。   By this strong stirring process, the ultrafine powder of 2 μm or less was reduced to 4.0% (number). The reduction rate of the ultrafine powder by the strong stirring process was 5.6%.

その後、強攪拌工程で用いたのと同一のミキサー(ヘンシェルミキサー、FM−10)により、疎水性シリカ(R812:日本アエロジル社製)0.5質量部を加え、羽の周速30m/sで5分間攪拌し、平均粒径6.1μmのマゼンタトナーを得た。   Then, 0.5 parts by mass of hydrophobic silica (R812: manufactured by Nippon Aerosil Co., Ltd.) was added by the same mixer (Henschel mixer, FM-10) used in the strong stirring step, and the peripheral speed of the wings was 30 m / s. The mixture was stirred for 5 minutes to obtain a magenta toner having an average particle size of 6.1 μm.

なお、2μm以下の超微紛体の個数、トナーの粒径は、下記の測定条件で測定した。   The number of ultrafine particles having a particle size of 2 μm or less and the toner particle size were measured under the following measurement conditions.

測定機器:マルチサイザーIII
測定粒子個数:50000個
アパーチャー径:50μm
実施例2〜4、比較例1,2
強攪拌工程におけるヘンシェルミキサーの羽の周速、強攪拌工程で加えたシリカの粒径、添加量を変化させたことを除いて実施例1と同様の手順で、6種のマゼンタトナーを得た。
Measuring equipment: Multisizer III
Number of particles measured: 50000 Aperture diameter: 50 μm
Examples 2 to 4, Comparative Examples 1 and 2
Six types of magenta toners were obtained in the same procedure as in Example 1 except that the peripheral speed of the Henschel mixer blade in the strong stirring step, the particle size of the silica added in the strong stirring step, and the amount added were changed. .

これらのトナーについて、カラープリンター「スピーディア:N5」(カシオ計算機製)により印刷試験を行い、白スジおよびカブリについて目視で評価した。その結果を下記表1及び表2に示す。   These toners were subjected to a printing test using a color printer “Speedia: N5” (manufactured by Casio Computer Co., Ltd.), and white stripes and fogging were visually evaluated. The results are shown in Tables 1 and 2 below.

白スジおよびカブリの評価基準は下記の通りである。   The evaluation criteria for white stripes and fog are as follows.

色スジ
○:白スジ発生なし
△:白スジを数本確認できる
×:白スジを瞬時に確認できる
カブリ
○:カブリが認められる。
△:ややカブリがある。
×:明らかにカブリがある。

Figure 2007093882
Color stripe
○: No white streak
Δ: Several white streaks can be confirmed
×: White streaks can be confirmed instantly
Fog
○: Fog is recognized.
Δ: Slightly fogged.
X: There is clearly fog.
Figure 2007093882

Figure 2007093882
Figure 2007093882

上記表1及び表2から、次のことが明らかである。即ち、強攪拌工程により、5%以上の減少率で超微紛体の個数を減少させたトナー(実施例1〜4)を用いた場合、いずれも白スジ、カブリが発生せず、良好な画質を示した。これに対し、強攪拌工程においてヘンシェルミキサーの羽の周速が30m/sと低いために超微紛体の減少率が4.7%と低いトナー(比較例1)では、カブリが発生し、強攪拌工程において添加されたシリカの粒径が40nmと大きすぎるために超微紛体の減少率が2.3%と低いトナー(比較例2)では、白スジおよびカブリが発生した。   From the above Tables 1 and 2, the following is clear. That is, in the case of using the toner (Examples 1 to 4) in which the number of ultrafine particles was reduced by a reduction rate of 5% or more by a strong stirring process, neither white streaks nor fog occurred, and good image quality was obtained. showed that. On the other hand, in the strong agitation process, the Henshell mixer's peripheral speed of the wing is as low as 30 m / s. Therefore, the toner (Comparative Example 1) having a low reduction rate of the ultrafine powder of 4.7% causes fogging and strong. In the toner (Comparative Example 2) in which the reduction rate of the ultrafine powder was as low as 2.3% because the particle size of the silica added in the stirring step was too large at 40 nm, white streaks and fogging occurred.

Claims (5)

結着樹脂、着色剤および帯電制御剤を混合および混練する工程、
前記混練工程からの混練物を粉砕する工程、
前記粉砕工程からの微粉体を分級する工程、
前記分級工程からの微粉体を強攪拌し、微粉体中に含まれる超微粉体を微粉体母粒子に埋没させる工程、および
前記強攪拌工程からの微粒子に外添剤を添加する工程
を具備し、前記強攪拌工程において、2μm以下の超微粉体を5%以上減少させることを特徴とする電子写真用トナーの製造方法。
Mixing and kneading a binder resin, a colorant and a charge control agent;
Pulverizing the kneaded product from the kneading step,
A step of classifying the fine powder from the pulverization step,
A step of strongly stirring the fine powder from the classification step, burying the ultrafine powder contained in the fine powder in the fine powder mother particles, and a step of adding an external additive to the fine particles from the strong stirring step. And a method for producing an electrophotographic toner, wherein ultrafine powder of 2 μm or less is reduced by 5% or more in the strong stirring step.
前記強攪拌工程を、前記外添剤添加工程で用いた混合機を用いて、前記外添剤添加工程における混合機の駆動時間および/または回転数を越える駆動時間および/または回転数で混合機を駆動することにより行うことを特徴とする請求項1に記載の電子写真用トナーの製造方法。   Using the mixer used in the external additive addition step, the strong agitation step is performed at a drive time and / or rotation speed exceeding the drive time and / or rotation speed of the mixer in the external additive addition step. The method for producing an electrophotographic toner according to claim 1, wherein the toner is driven by driving the toner. 前記強攪拌工程において、粒径5〜15nmのシリカを0.1〜0.5質量%添加することを特徴とする請求項1叉は2に記載の電子写真用トナーの製造方法。   3. The method for producing an electrophotographic toner according to claim 1, wherein 0.1 to 0.5% by mass of silica having a particle diameter of 5 to 15 nm is added in the strong stirring step. 粒径5.0〜0〜9.0μmのトナーを製造することを特徴とする請求項1〜3のいずれかに記載の電子写真用トナーの製造方法。   4. The method for producing an electrophotographic toner according to claim 1, wherein a toner having a particle size of 5.0 to 0 to 9.0 [mu] m is produced. 前記外添剤は、粒径5〜15nmのシリカであることを特徴とする請求項1〜4のいずれかに記載の電子写真用トナーの製造方法。 The method for producing an electrophotographic toner according to claim 1, wherein the external additive is silica having a particle size of 5 to 15 nm.
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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05281782A (en) * 1992-04-02 1993-10-29 Konica Corp Negatively charged toner and image forming method
JPH0869173A (en) * 1994-08-31 1996-03-12 Toshiba Corp Developing method and developing device using the method
JPH09288374A (en) * 1996-04-23 1997-11-04 Minolta Co Ltd Toner for two-component developer
JPH10104871A (en) * 1996-09-30 1998-04-24 Sharp Corp Toner and its production
JP2000105488A (en) * 1998-09-29 2000-04-11 Canon Inc Developing device and image forming device using the same
JP2002014488A (en) * 2000-06-29 2002-01-18 Matsushita Electric Ind Co Ltd Toner and electrophotographic device
JP2004333681A (en) * 2003-05-02 2004-11-25 Canon Inc Development method, development apparatus, and image forming apparatus

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05281782A (en) * 1992-04-02 1993-10-29 Konica Corp Negatively charged toner and image forming method
JPH0869173A (en) * 1994-08-31 1996-03-12 Toshiba Corp Developing method and developing device using the method
JPH09288374A (en) * 1996-04-23 1997-11-04 Minolta Co Ltd Toner for two-component developer
JPH10104871A (en) * 1996-09-30 1998-04-24 Sharp Corp Toner and its production
JP2000105488A (en) * 1998-09-29 2000-04-11 Canon Inc Developing device and image forming device using the same
JP2002014488A (en) * 2000-06-29 2002-01-18 Matsushita Electric Ind Co Ltd Toner and electrophotographic device
JP2004333681A (en) * 2003-05-02 2004-11-25 Canon Inc Development method, development apparatus, and image forming apparatus

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