JP3456010B2 - Manufacturing method of toner - Google Patents

Manufacturing method of toner

Info

Publication number
JP3456010B2
JP3456010B2 JP11497194A JP11497194A JP3456010B2 JP 3456010 B2 JP3456010 B2 JP 3456010B2 JP 11497194 A JP11497194 A JP 11497194A JP 11497194 A JP11497194 A JP 11497194A JP 3456010 B2 JP3456010 B2 JP 3456010B2
Authority
JP
Japan
Prior art keywords
toner
mixing
charge control
control agent
colorant
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
JP11497194A
Other languages
Japanese (ja)
Other versions
JPH07319203A (en
Inventor
幸弘 佐藤
信忠 藤武
隆 新卓
誠二 永島
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
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Priority to JP11497194A priority Critical patent/JP3456010B2/en
Publication of JPH07319203A publication Critical patent/JPH07319203A/en
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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、電子写真複写機やレー
ザビームプリンタ等の電子写真法を用いた画像形成装置
に用いられるトナーの製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a toner used in an image forming apparatus using an electrophotographic method such as an electrophotographic copying machine or a laser beam printer.

【0002】[0002]

【従来の技術】通常、トナーは、バインダ樹脂、着色
剤、帯電制御剤及び離型剤(ワックス)や磁性粉等のそ
の他の添加剤等からなるトナー材料を混合し、溶融混練
した後、粉砕、分級して製造される。
2. Description of the Related Art Usually, a toner is prepared by mixing a toner material including a binder resin, a colorant, a charge control agent, a release agent (wax) and other additives such as magnetic powder, melt-kneading, and then pulverizing. , Classified and manufactured.

【0003】[0003]

【発明が解決しようとする課題】この場合、トナー材料
を配合し混合する工程が極めて重要である。すなわち、
混合工程で各材料の混合が十分でないと、トナーとして
も性能的に振れのある不都合なものしか得られない。し
かしながら、各トナー材料はそれぞれ独自の物理特性
(粒度、見かけ比重、摩擦帯電性等)を有するため、一
度に仕込んで混合しても材料間の凝集が発生しやすく、
従って、得られるトナーには帯電量のばらつきや着色ム
ラ等の不具合が発生したり、また、長期あるいは連続使
用時の耐久性に難がある等、必ずしも常に満足すべき結
果は得られていなかった。また、上記の問題を解決すべ
く、混合での分散均一性を上げるために撹拌混合強度を
増す(混合回転数や混合時間等のアップ)試みもなされ
ているが、徒に生産性を悪化させるのみならず、帯電制
御剤や着色剤等の特定成分の過度の分散に起因するトナ
ーのチャージアップが発生して、画質劣化を招くという
問題が新たに発生する。特に小粒径のトナー(平均粒径
で10μm以下)の製造において、以上述べた問題が障
壁となっていた。本発明は上記した現状に鑑み、その課
題を解決すべくなされたものであって、その目的は小粒
径トナーとした場合でも、帯電量のばらつきや着色ムラ
が発生せず、また、チャージアップによる画質劣化がな
く、さらには、長期あるいは連続使用時の耐久性の高い
トナーの製造方法を提供することにある。
In this case, the step of blending and mixing the toner materials is extremely important. That is,
If the mixing of each material is not sufficient in the mixing step, only inconvenient toner having performance fluctuations can be obtained as a toner. However, since each toner material has its own unique physical characteristics (particle size, apparent specific gravity, triboelectrification property, etc.), coagulation between the materials is likely to occur even if they are charged at once and mixed.
Therefore, satisfactory results have not always been obtained, such that the obtained toner has defects such as variations in charge amount and uneven coloring, and has a problem in durability for long-term or continuous use. . In addition, in order to solve the above problems, attempts have been made to increase the stirring and mixing intensity (increase the mixing speed and mixing time) in order to improve the uniformity of dispersion in mixing, but this unnecessarily reduces productivity. Not only that, the toner is charged up due to excessive dispersion of the specific components such as the charge control agent and the colorant, which causes a new problem of image quality deterioration. In particular, in the production of toner having a small particle size (average particle size of 10 μm or less), the above-mentioned problems have been obstacles. SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances and has been made to solve the problem. The object is to prevent variations in charge amount and uneven coloring even when a toner having a small particle size is used, and to improve charge-up. Another object of the present invention is to provide a method for producing a toner that does not deteriorate in image quality due to the above and has high durability during long-term or continuous use.

【0004】[0004]

【課題を解決するための手段】本発明者らはかかる目的
を達成すべく鋭意検討した結果、混合工程においてトナ
ー材料を段階的に混合する方法、好適には着色剤及び/
または帯電制御剤を混合工程の途中段階もしくは最終段
階で混合するトナーの製造方法により、上記目的を満足
することを見い出し本発明に到達した。すなわち、本発
明の要旨は、少なくともバインダ樹脂並びに着色剤及び
/又は帯電制御剤から成るトナー材料の混合工程を有す
るトナーの製造方法において、着色剤及び帯電制御剤か
らなる群より選択される少なくとも1種のトナー材料の
少なくとも一部の混合を、混合工程の途中段階又は最終
段階で行うことを特徴とするトナーの製造方法に存す
る。
DISCLOSURE OF THE INVENTION As a result of intensive investigations by the present inventors in order to achieve such an object, a method of stepwise mixing toner materials in a mixing step, preferably a colorant and / or
Further, they have found that the above object is satisfied by a method for producing a toner in which a charge control agent is mixed at an intermediate stage or a final stage of the mixing process, and thus reached the present invention. That is, the gist of the present invention is to provide a method for producing a toner, which comprises a step of mixing a toner material comprising at least a binder resin and a colorant and / or a charge control agent.
Of at least one toner material selected from the group consisting of
At least part of the mixing, either in the middle of the mixing process or at the end
It exists in the manufacturing method of the toner characterized by performing in steps .

【0005】本発明のトナーの製造方法においては、混
合工程で各トナー材料が段階的に添加混合される。すな
わち、混合工程において、混合は2段階以上の操作を経
て実施される。特に、トナー性能に大きな影響を及ぼす
帯電制御剤及び/または着色剤が、混合工程の途中段階
もしくは最終段階で添加されることにより、始めから一
度に混合を行う場合に比べて各材料間の不必要な凝集及
び特定成分の過度の分散を同時に排除できる。従って、
本発明の製造方法によれば、前記した問題点を解消した
トナーをさしたる労力を必要としないで効率的に製造す
ることができる。以下、本発明のトナーの製造方法を詳
細に説明する。
In the toner manufacturing method of the present invention, each toner material is added and mixed stepwise in the mixing step. That is, in the mixing step, the mixing is carried out through two or more steps. In particular, since the charge control agent and / or the colorant, which has a great influence on the toner performance, is added in the middle stage or the final stage of the mixing process, the difference between the respective materials is increased as compared with the case where the mixing is performed all at once from the beginning. The required agglomeration and overdispersion of certain components can be eliminated at the same time. Therefore,
According to the manufacturing method of the present invention, it is possible to efficiently manufacture a toner that solves the above-mentioned problems, without requiring labor. Hereinafter, the method for producing the toner of the present invention will be described in detail.

【0006】まず、トナーの構成材料であるバインダ樹
脂、着色剤、帯電制御剤及びその他の添加物等を所定割
合で配合して混合する。この際の装置としては、Vブレ
ンダー、ボールミル等の重力落下式混合機やヘンシェル
ミキサー(三井三池加工機社製)、スーパーミキサー
(カワタ社製)等の高速流動式混合機が使用される。本
発明においては、この混合を段階的に実施し、好ましく
はトナー材料のうち帯電制御剤及び/または着色剤の少
なくとも一部を混合工程の途中段階又は最終段階で混合
することを特徴とする。帯電制御剤及び着色剤のうち混
合工程で添加する材料は、着色剤のみ、あるいは帯電制
御剤のみでもよく、着色剤及び帯電制御剤の両成分を加
えてもよい。両成分を加える場合、混合のある段階で着
色剤と帯電制御剤を同時に加えてもよいし、先に着色剤
を加えて混合して、更に、その後の段階で帯電制御剤を
加えてもよく、その添加順が逆の場合であってもよい。
またトナー材料の仕込み量の一部を混合した後、残量を
混合してもよい。更には一部のトナー材料の混合物とそ
の他のトナー材料の混合物を混合してもよい。また、混
合条件として、装置の撹拌回転数を最初から同じ条件の
まま行ってもよいし、途中もしくは最終での添加に合わ
せて変更してもよい。
First, a binder resin, a colorant, a charge control agent, and other additives, which are constituent materials of the toner, are mixed and mixed at a predetermined ratio. As a device in this case, a gravity dropping type mixer such as a V blender or a ball mill, a high speed fluid type mixer such as a Henschel mixer (manufactured by Mitsui Miike Machinery Co., Ltd.) or a super mixer (manufactured by Kawata Co., Ltd.) is used. The present invention is characterized in that this mixing is carried out stepwise, and preferably at least a part of the charge control agent and / or the colorant in the toner material is mixed in the middle step or the final step of the mixing step. Of the charge control agent and the colorant, the material added in the mixing step may be the colorant alone or the charge control agent alone, or both the colorant and the charge control agent components may be added. When both components are added, the colorant and the charge control agent may be added simultaneously at a certain stage of mixing, or the colorant may be added first and mixed, and then the charge control agent may be added at a subsequent stage. The order of addition may be reversed.
Further, the remaining amount may be mixed after mixing a part of the charged amount of the toner material. Further, a mixture of some toner materials and a mixture of other toner materials may be mixed. In addition, as the mixing condition, the number of rotations of stirring of the apparatus may be the same from the beginning, or may be changed according to the addition during or at the end.

【0007】混合時間は混合される構成材料及び混合装
置の特性に合わせて適宜設定される。必要に応じては、
途中段階もしくは最終段階での添加に合わせて混合装置
自体を変更してもよい。本発明において、特に望ましい
混合工程の実施の態様は、混合装置としてヘンシェル
ミキサー、スーパーミキサー等の高速流動式混合機を用
いること、途中もしくは最終で添加される着色剤及び
/または帯電制御剤の混合条件は、その前段階の条件よ
りも撹拌混合強度を弱めること(例えば、撹拌回転数を
下げること、混合時間を短時間化すること、あるいはそ
れらを組み合わせて行うこと等)である。
The mixing time is appropriately set according to the constituent materials to be mixed and the characteristics of the mixing apparatus. If necessary,
The mixing device itself may be changed according to the addition in the middle stage or the final stage. In the present invention, a particularly preferable embodiment of the mixing step is to use a high speed fluid mixer such as a Henschel mixer or a super mixer as a mixing device, and to mix a colorant and / or a charge control agent added during or at the end. The conditions are to lower the stirring and mixing strength as compared with the conditions of the preceding stage (for example, lowering the stirring rotation speed, shortening the mixing time, or performing them in combination).

【0008】ここで、高速流動型混合機とは、混合容器
底部に取り付けた羽根を高速で回転させて、羽根の強力
なせん断及び衝撃作用により粉粒体を流体のように分散
させて混合を行う形式の混合機をいう。この方式の混合
機は、重力落下方式の混合機に比べて撹拌強度が強く、
短時間で効率よく混合が行えるため、生産性の面で有利
である。しかし、逆に着色剤や帯電制御剤等の微粒子成
分の過度の分散を起こしやすい。そのため、これらの成
分を途中段階もしくは最終段階で添加し、しかもその時
の撹拌混合強度を弱めるとより好ましい結果を得られる
ことが見い出された。
[0008] Here, the high-speed fluid type mixer means that the blade attached to the bottom of the mixing container is rotated at a high speed to disperse the powdery particles like a fluid by the strong shearing and impact action of the blade for mixing. This is the type of mixer used. This type of mixer has stronger stirring strength than the gravity drop type mixer,
This is advantageous in terms of productivity because efficient mixing can be performed in a short time. However, on the contrary, the fine particles such as the colorant and the charge control agent are likely to be excessively dispersed. Therefore, it has been found that more preferable results can be obtained by adding these components at an intermediate stage or a final stage and weakening the stirring and mixing strength at that time.

【0009】また、これらの高速流動式混合機では、上
記したような強力な撹拌作用に伴う混合槽内温度上昇が
見られる。これらの発熱は、場合によっては、各トナー
材料に悪影響を及ぼし、特にバインダ樹脂が凝集固化す
る現象が発生すると、材料の分散混合性が悪化する原因
となる。従って、本発明においては、混合工程において
使用される混合装置の混合槽内の温度をバインダ樹脂の
ガラス転移温度以下で管理することが好ましい。中でも
特に下記の条件で行うのがよい。
Further, in these high-speed flow type mixers, the temperature rise in the mixing tank due to the strong stirring action as described above is observed. In some cases, these heat generations adversely affect each toner material, and in particular, when a phenomenon in which the binder resin coagulates and solidifies occurs, the dispersibility and mixing property of the material deteriorates. Therefore, in the present invention, it is preferable to control the temperature in the mixing tank of the mixing device used in the mixing step to be equal to or lower than the glass transition temperature of the binder resin. Above all, it is particularly preferable to carry out under the following conditions.

【0010】[0010]

【数1】混合槽内温度≦Tg−5(℃) (ただし、Tgは使用するバインダ樹脂のガラス転移温
度) 特に望ましくは、下記の条件がよい。
## EQU1 ## Temperature in mixing tank ≦ Tg−5 (° C.) (where Tg is the glass transition temperature of the binder resin used) Particularly desirably, the following conditions are preferable.

【0011】[0011]

【数2】混合槽内温度≦Tg−10(℃)[Equation 2] Temperature in mixing tank ≤ Tg-10 (° C)

【0012】上記の条件で混合を行うことにより、樹脂
の凝集固化の発生がなく、またその他の材料の分散混合
性の悪化も回避できる。なお、混合槽内温度を上記の条
件に抑えるためには、混合槽外部に水冷等の冷却装置を
設置する等の手段を講ずるのが望ましい。また混合工程
の全段階において温度管理することが好ましいが、混合
工程の一部のみ温度管理をしてもよい。混合の後、混合
物を溶融混練する。溶融混練工程で使用される装置とし
ては、2本あるいは3本ロール、バンバリーミキサー、
一軸あるいは二軸押し出し機等が挙げられる。この工程
において、バインダ樹脂と相溶性を有する成分は樹脂と
溶融し、また、バインダ樹脂と相溶性を有しない帯電制
御剤等の成分は、溶融した樹脂中に分散される。
By performing the mixing under the above conditions, the resin is not aggregated and solidified, and the deterioration of the dispersibility and mixing of other materials can be avoided. In order to keep the temperature inside the mixing tank within the above conditions, it is desirable to take measures such as installing a cooling device such as water cooling outside the mixing tank. It is preferable to control the temperature in all stages of the mixing process, but the temperature may be controlled only in a part of the mixing process. After mixing, the mixture is melt-kneaded. The apparatus used in the melt-kneading step is a two- or three-roll machine, a Banbury mixer,
Examples include a single-screw or twin-screw extruder. In this step, a component compatible with the binder resin is melted with the resin, and a component such as a charge control agent not compatible with the binder resin is dispersed in the melted resin.

【0013】次に上記溶融混練物を冷却固化させた後、
粗粉砕、微粉砕及び分級の各工程を経てトナーが製造さ
れる。粗粉砕にはハンマーミル、カッターミル等が、微
粉砕には高速回転式微粉砕機やジェット粉砕機等が用い
られ、分級には強制うず型遠心分級機や慣性分級機等が
用いられる。本発明のトナーの製造方法は、混合工程に
おいてトナー材料を段階的に混合するという要件さえ満
たせば、特に通常の単色画像形成用の非磁性の黒トナー
に限らず、磁性トナーやフルカラー画像形成用のカラー
トナー等、従来公知の種々の電子写真用のトナーの製造
に適用することができる。
Next, after the molten and kneaded product is cooled and solidified,
The toner is manufactured through the steps of coarse pulverization, fine pulverization and classification. A hammer mill, a cutter mill, or the like is used for coarse pulverization, a high-speed rotary fine pulverizer, a jet pulverizer, or the like is used for fine pulverization, and a forced spiral centrifugal classifier, an inertial classifier, or the like is used for classification. The method for producing a toner of the present invention is not limited to a non-magnetic black toner for normal monochromatic image formation, as long as the requirement that the toner materials are mixed stepwise in the mixing step is satisfied, and a magnetic toner or a full color image formation The present invention can be applied to the production of various conventionally known toners for electrophotography, such as the above color toner.

【0014】本発明に使用するトナー材料は従来公知の
もの全てが使用可能であるが、たとえば、下記の如くで
ある。 バインダ樹脂:スチレン/アクリル共重合樹脂、ポリエ
ステル樹脂、エポキシ樹脂など 着色剤 :カーボンブラック、モノアゾ顔料、ジス
アゾ顔料、キナクリドン顔料、銅フタロシアニン顔料、
アントラキノン染料、ローダミン染料など 帯電制御剤 :正帯電用としては、ニグロシン化合物
(変性物を含む)、第4アンモニウム化合物、スチレン
アミノ樹脂など、負帯電用としては、含金属錯体染料、
アルキルサリチル酸のクロムや亜鉛等との錯化合物など その他の添加剤:離型剤(ワックス)として、低分子量
のポリエチレンやポリプロピレンなど、磁性トナー作製
時の磁性粉として、マグネタイト微粒子やフェライト微
粒子など
As the toner material used in the present invention, all the conventionally known toner materials can be used, for example, as follows. Binder resin: Styrene / acrylic copolymer resin, polyester resin, epoxy resin, etc. Colorant: Carbon black, monoazo pigment, disazo pigment, quinacridone pigment, copper phthalocyanine pigment,
Charge control agents such as anthraquinone dyes and rhodamine dyes: Nigrosine compounds (including modified products), quaternary ammonium compounds, styrene amino resins, etc. for positive charging, metal-containing complex dyes for negative charging,
Other additives such as complex compounds of alkylsalicylic acid with chromium, zinc, etc .: As a releasing agent (wax), low-molecular-weight polyethylene or polypropylene, etc., as magnetic powder when producing magnetic toner, magnetite fine particles, ferrite fine particles, etc.

【0015】[0015]

【実施例】以下、本発明を実施例及び比較例により説明
する。実施例及び比較例中、「部」は「重量部」であ
る。 実施例1 トナー処方は下記にて行った。
EXAMPLES The present invention will be described below with reference to Examples and Comparative Examples. In the examples and comparative examples, “part” is “part by weight”. Example 1 The toner formulation was as follows.

【0016】[0016]

【表1】 ・バインダ樹脂成分 スチレン/n−ブチルアクリレート樹脂 100部 (軟化点約140℃、Tg約60℃) ・ワックス成分 低分子量ポリプロピレン 3部 (三洋化成製、ビスコール660P) ・着色剤成分 カーボンブラック 8部 (三菱化成製、三菱カーボンブラック#40) ・帯電制御剤成分 ニグロシン染料 3部 (オリエント化学製、ボントロンN09)[Table 1]   Binder resin component Styrene / n-butyl acrylate resin 100 parts                       (Softening point about 140 ° C, Tg about 60 ° C)   ・ Wax component Low molecular weight polypropylene 3 parts                       (Sanyo Kasei Co., Viscole 660P)   ・ Colorant component carbon black 8 parts                       (Mitsubishi Carbon, Mitsubishi Carbon Black # 40)   ・ Charge control agent component Nigrosine dye 3 parts                       (Bontron N09 manufactured by Orient Chemical Co., Ltd.)

【0017】製造に当たっては、まず、バインダ樹脂成
分とワックス成分とをヘンシェルミキサーで約30分間
混合した後、一旦装置を停止させ、着色剤成分と帯電制
御剤成分とをその中に加えて、さらに約3分間の混合を
行い、混合を終了した。なお、混合工程の全ての期間を
通じて、水冷を施すことにより混合槽内の温度は約50
℃以下とした。その後、二軸押し出し機にて、加熱溶融
混練した。得られた混練物を冷却固化させた後、フェザ
ーミルで粗粉砕し、ジェットミルで微粉砕した。さら
に、粒径が5μm以下のトナー微粉をローター回転型分
級機でカットして粒径を揃えた(平均粒径で約8μ
m)。ヘンシェルミキサーを用いて、この分級品に疎水
性シリカを添加し、トナーを作製した。このトナー6部
と、平均粒径約50μmのフェライトキャリア94部と
をVブレンダーで混合して現像剤を作製した。
In the production, first, the binder resin component and the wax component are mixed by a Henschel mixer for about 30 minutes, then the apparatus is stopped, the colorant component and the charge control agent component are added therein, and further, Mixing was performed for about 3 minutes, and the mixing was completed. It should be noted that the temperature in the mixing tank is kept at about 50 by water cooling throughout the entire mixing process.
The temperature was set to ℃ or below. Then, the mixture was melted and kneaded by heating with a twin-screw extruder. The obtained kneaded product was cooled and solidified, then roughly pulverized with a feather mill and finely pulverized with a jet mill. Further, toner fine powder having a particle size of 5 μm or less was cut by a rotor rotary classifier to make the particle size uniform (about 8 μm in average particle size).
m). Hydrophobic silica was added to this classified product using a Henschel mixer to prepare a toner. 6 parts of this toner and 94 parts of a ferrite carrier having an average particle size of about 50 μm were mixed with a V blender to prepare a developer.

【0018】これらのトナー及び現像剤に対する評価試
験として、有機光導電体ドラムを感光体とする市販の複
写機を用いた実写による画像品質確認及び耐久性確認
(5万枚連続実写試験)を行った。結果を表1に示す。
なお、画像濃度の測定は、画像のベタ部分をマクベス反
射濃度計を用いて行い、カブリの測定は、通紙前後の紙
の背景部の白度の差をハンター白度計で測定した。ま
た、ブローオフ法による現像剤の帯電量測定も併せて実
施し、Q/Mと表記した。
As an evaluation test for these toners and developers, image quality confirmation and durability confirmation (50,000 sheets continuous actual copying test) were carried out by actual copying using a commercially available copying machine using an organic photoconductor drum as a photoconductor. It was The results are shown in Table 1.
The image density was measured using a Macbeth reflection densitometer for the solid area of the image, and the fog was measured using a Hunter whiteness meter to measure the difference in whiteness of the background portion of the paper before and after passing the paper. The charge amount of the developer was also measured by the blow-off method, and the result was expressed as Q / M.

【0019】[0019]

【表2】 [Table 2]

【0020】表1によれば、画像品質として、十分な画
像濃度と低いカブリのレベルを有し、しかも5万枚を通
じてほぼ初期の画像品質を維持した。また、その間の現
像剤帯電量も極めて安定して推移することがわかった。
According to Table 1, the image quality has a sufficient image density and a low fog level, and moreover, the initial image quality was maintained over 50,000 sheets. Further, it was found that the charge amount of the developer during that time also changed extremely stably.

【0021】比較例1 実施例1と全く同様の配合処方を用い、ヘンシェルミキ
サーでの混合時に全ての材料を同時に仕込んで、約30
分間の混合を行うこと以外は、実施例1と全く同様な操
作でトナー及び現像剤を作製し、評価試験も同様に行っ
た。その結果を表2に示す。
Comparative Example 1 Using the same formulation as in Example 1, all the ingredients were charged at the same time when mixing with a Henschel mixer,
A toner and a developer were prepared in the same manner as in Example 1 except that mixing was carried out for 1 minute, and an evaluation test was also conducted in the same manner. The results are shown in Table 2.

【0022】[0022]

【表3】 [Table 3]

【0023】表2によれば、特に連続実写で画像濃度の
大幅な低下が見られ、画像品質の劣化が顕著であった。
また、その間の現像剤帯電量も大幅なチャージアップ傾
向が見られ、安定性に欠けることが確認された。これ
は、着色剤や帯電制御剤成分の混合工程での過度の分散
に起因するものと考えられる。 実施例2 トナー処方は下記にて行った。
According to Table 2, the image density is significantly reduced particularly in continuous shooting, and the image quality is significantly deteriorated.
Further, during that time, the developer charge amount also showed a significant charge-up tendency, and it was confirmed that the developer lacked stability. It is considered that this is due to excessive dispersion in the mixing step of the colorant and charge control agent components. Example 2 The toner formulation was as follows.

【0024】[0024]

【表4】 ・バインダ樹脂成分 ビスフェノールAのプロピレンオキシド 100部 付加物とテレフタル酸とを主成分に合成 されるポリエステル樹脂 (軟化点約140℃、Tg約65℃) ・ワックス成分 低分子量ポリプロピレン 3部 (三洋化成製、ビスコール550P) ・着色剤成分 カーボンブラック 10部 (三菱化成製、三菱カーボンブラックMA600) ・帯電制御剤成分 クロム含金属染料 3部 (オリエント化学製、ボントロンS34)[Table 4]   -Binder resin component Bisphenol A propylene oxide 100 parts                       Synthesis of adduct and terephthalic acid as main components                       Polyester resin                       (Softening point approx. 140 ° C, Tg approx. 65 ° C)   ・ Wax component Low molecular weight polypropylene 3 parts                       (Sanyo Kasei Co., Viscole 550P)   ・ Colorant component carbon black 10 parts                       (MITSUBISHI KASEI, MITSUBISHI CARBON BLACK MA600)   ・ Charge control agent component Chromium metal dye 3 parts                       (Bontron S34, manufactured by Orient Chemical Co., Ltd.)

【0025】製造に当たっては、まず、バインダ樹脂成
分とワックス成分とをスーパーミキサーで約40分間混
合した後、一旦装置を停止させ、着色剤成分と帯電制御
剤成分とをその中に加えて、さらに約5分間の混合を行
い、混合を終了した。なお、混合工程の全ての期間を通
じて、水冷を施すことにより混合槽内の温度は約50℃
以下とした。その後、二軸押し出し機にて、加熱溶融混
練した。得られた混練物を冷却固化させた後、フェザー
ミルで粗粉砕し、ジェットミルで微粉砕した。さらに、
粒径が5μm以下のトナー微粉をローター回転型分級機
でカットして粒径を揃えた(平均粒径で約7μm)。ヘ
ンシェルミキサーを用いて、この分級品に疎水性チタニ
アを添加し、トナーを作製した。このトナー7部と、平
均粒径約50μmのマグネタイトキャリア93部とをV
ブレンダーで混合して現像剤を作製した。これらのトナ
ー及び現像剤に対する評価試験として、有機光導電体ド
ラムを感光体とする市販のレーザービームプリンタを用
いた実写による画像品質確認及び耐久性確認(5千枚連
続実写試験)を行った。結果を表3に示す。なお、評価
方法は実施例1と同様に行った。
In the production, first, the binder resin component and the wax component are mixed with a super mixer for about 40 minutes, then the apparatus is temporarily stopped, the colorant component and the charge control agent component are added therein, and further, Mixing was performed for about 5 minutes, and the mixing was completed. It should be noted that the temperature in the mixing tank is about 50 ° C. by water cooling throughout the entire mixing process.
Below. Then, the mixture was melted and kneaded by heating with a twin-screw extruder. The obtained kneaded product was cooled and solidified, then roughly pulverized with a feather mill and finely pulverized with a jet mill. further,
The toner fine powder having a particle size of 5 μm or less was cut by a rotor rotary classifier to have a uniform particle size (average particle size of about 7 μm). Hydrophobic titania was added to this classified product using a Henschel mixer to prepare a toner. 7 parts of this toner and 93 parts of magnetite carrier having an average particle size of about 50 μm
A developer was prepared by mixing with a blender. As an evaluation test for these toners and developers, image quality confirmation and durability confirmation (5,000 sheets continuous copying test) were carried out by actual copying using a commercially available laser beam printer using an organic photoconductor drum as a photoconductor. The results are shown in Table 3. The evaluation method was the same as in Example 1.

【0026】[0026]

【表5】 [Table 5]

【0027】表3によれば、画像品質として、十分な画
像濃度と低いカブリのレベルを有し、しかも5千枚を通
じてほぼ初期の画像品質を維持した。また、その間の現
像剤帯電量も極めて安定して推移することがわかった。
According to Table 3, the image quality has a sufficient image density and a low fog level, and the almost initial image quality was maintained over 5,000 sheets. Further, it was found that the charge amount of the developer during that time also changed extremely stably.

【0028】実施例3 実施例2と全く同様の配合処方を用い、スーパーミキサ
ーでの混合時に、最初に樹脂成分、ワックス成分及び着
色剤成分を仕込んで約40分間の混合を行った後、一旦
装置を停止させ、帯電制御剤成分をその中に加えて、更
に約5分間の混合を行い、混合を終了した。なお、混合
工程の全てを通じて、水冷を施すことにより混合槽内の
温度は約50℃以下とした。以下、実施例2と全く同様
な操作でトナー及び現像剤を作製し、評価試験も同様に
行った。その結果を表4に示す。
Example 3 Using the same formulation as in Example 2, when mixing with a supermixer, the resin component, wax component and colorant component were first charged and mixed for about 40 minutes, and then once. The apparatus was stopped, the charge control agent component was added thereto, and the mixture was further mixed for about 5 minutes to complete the mixing. In addition, the temperature in the mixing tank was set to about 50 ° C. or lower by performing water cooling throughout the mixing process. Hereinafter, a toner and a developer were prepared in the same manner as in Example 2, and the evaluation test was also performed in the same manner. The results are shown in Table 4.

【0029】[0029]

【表6】 [Table 6]

【0030】表4によれば、画像品質として、十分な画
像濃度と低いカブリのレベルを有し、しかも5千枚を通
じてほぼ初期の画像品質を維持した。また、その間の現
像剤帯電量も極めて安定して推移することがわかった。
According to Table 4, the image quality has a sufficient image density and a low fog level, and the almost initial image quality was maintained over 5,000 sheets. Further, it was found that the charge amount of the developer during that time also changed extremely stably.

【0031】実施例4 実施例2と全く同様の配合処方を用い、スーパーミキサ
ーでの混合時に、最初に樹脂成分、ワックス成分及び帯
電制御剤成分を仕込んで約40分間の混合を行った後、
一旦装置を停止させ、着色剤成分をその中に加えて、更
に約5分間の混合を行い、混合を終了した。なお、混合
工程の全てを通じて、水冷を施すことにより混合槽内の
温度は約50℃以下とした。以下、実施例2と全く同様
な操作でトナー及び現像剤を作製し、評価試験も同様に
行った。その結果を表5に示す。
Example 4 Using the same formulation as in Example 2, when mixing with a supermixer, the resin component, the wax component and the charge control agent component were first charged and mixed for about 40 minutes.
The apparatus was once stopped, the colorant component was added thereto, and the mixture was further mixed for about 5 minutes, and the mixing was completed. In addition, the temperature in the mixing tank was set to about 50 ° C. or lower by performing water cooling throughout the mixing process. Hereinafter, a toner and a developer were prepared in the same manner as in Example 2, and the evaluation test was also performed in the same manner. The results are shown in Table 5.

【0032】[0032]

【表7】 [Table 7]

【0033】表5によれば、画像品質として、十分な画
像濃度と低いカブリのレベルを有し、しかも5千枚を通
じてほぼ初期の画像品質を維持した。また、その間の現
像剤帯電量も極めて安定して推移することがわかった。
According to Table 5, the image quality has a sufficient image density and a low fog level, and the almost initial image quality was maintained over 5,000 sheets. Further, it was found that the charge amount of the developer during that time also changed extremely stably.

【0034】比較例2 実施例2と全く同様の配合処方を用い、スーパーミキサ
ーでの混合時に全ての材料を同時に仕込んで、約40分
間の混合を行うこと以外は、実施例2と全く同様な操作
でトナー及び現像剤を作製し、評価試験も同様に行っ
た。その結果を表6に示す。
Comparative Example 2 Except that the same formulation as in Example 2 was used and all the ingredients were charged at the same time when mixing with a super mixer, and the mixture was mixed for about 40 minutes. A toner and a developer were prepared by the operation, and the evaluation test was conducted in the same manner. The results are shown in Table 6.

【0035】[0035]

【表8】 [Table 8]

【0036】表6によれば、特に連続実写で画像濃度の
大幅な低下が見られ、画像品質の劣化が顕著であった。
また、その間の現像剤帯電量も大幅なチャージアップ傾
向が見られ、安定性に欠けることが確認された。これ
は、着色剤や帯電制御剤成分の混合工程での過度の分散
に起因するものと考えられる。
According to Table 6, the image density was significantly reduced especially in continuous shooting, and the image quality was significantly deteriorated.
Further, during that time, the developer charge amount also showed a significant charge-up tendency, and it was confirmed that the developer lacked stability. It is considered that this is due to excessive dispersion in the mixing step of the colorant and charge control agent components.

【0037】[0037]

【発明の効果】以上述べたように、本発明のトナー製造
方法によれば、小粒径トナーの作製時においても帯電量
のばらつきや着色ムラが発生せず、また、チャージアッ
プによる画質劣化がなく、さらには、長期あるいは連続
使用時の耐久性に優れたトナーを効率的に製造すること
が可能となる。
As described above, according to the toner manufacturing method of the present invention, even when a small particle size toner is manufactured, variations in charge amount and coloring unevenness do not occur, and deterioration of image quality due to charge-up does not occur. Furthermore, it becomes possible to efficiently manufacture a toner having excellent durability even during long-term or continuous use.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 永島 誠二 新潟県上越市福田町1番地 三菱化成株 式会社直江津工場内 (56)参考文献 特開 平5−34976(JP,A) 特開 平5−61250(JP,A) 特開 平3−164750(JP,A) 特開 平6−95431(JP,A) (58)調査した分野(Int.Cl.7,DB名) G03G 9/08 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Seiji Nagashima 1 Fukuda-cho, Joetsu City, Niigata Prefecture Inside the Naoetsu Plant of Mitsubishi Kasei Co., Ltd. (56) References JP-A-5-34976 (JP, A) JP-A-5 -61250 (JP, A) JP-A-3-164750 (JP, A) JP-A-6-95431 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) G03G 9/08

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 少なくともバインダ樹脂並びに着色剤及
び/又は帯電制御剤から成るトナー材料の混合工程を有
するトナーの製造方法において、着色剤及び帯電制御剤
からなる群より選択される少なくとも1種のトナー材料
の少なくとも一部の混合を、混合工程の途中段階又は最
終段階で行うことを特徴とするトナーの製造方法。
1. A method for producing a toner, comprising a step of mixing a toner material comprising at least a binder resin and a colorant and / or a charge control agent, the colorant and the charge control agent
At least one toner material selected from the group consisting of
Of at least a part of the
A method for producing a toner, which is carried out at the final stage .
【請求項2】 着色剤及び帯電制御剤より選択される少
なくとも1種のトナー材料の少なくとも一部の混合を、
混合工程の最終段階で行うことを特徴とする請求項1に
記載のトナーの製造方法。
2. A small amount selected from colorants and charge control agents.
Mixing at least a portion of at least one toner material,
The method according to claim 1, which is performed in the final stage of the mixing process.
A method for producing the toner described above.
【請求項3】 着色剤及び帯電制御剤からなる群より選
択される少なくとも1種のトナー材料が帯電制御剤であ
ることを特徴とする請求項1又は2に記載のトナーの製
造方法。
3. A colorant and a charge control agent are selected from the group consisting of:
At least one toner material selected is a charge control agent
The toner according to claim 1 or 2, characterized in that
Build method.
【請求項4】 混合工程において使用される混合装置の
混合槽内温度がバインダ樹脂のガラス転移温度以下であ
ることを特徴とする請求項1乃至3のいずれかに記載の
トナーの製造方法。
4. The method for producing a toner according to claim 1, wherein the temperature in the mixing tank of the mixing device used in the mixing step is equal to or lower than the glass transition temperature of the binder resin.
JP11497194A 1994-05-27 1994-05-27 Manufacturing method of toner Expired - Lifetime JP3456010B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11497194A JP3456010B2 (en) 1994-05-27 1994-05-27 Manufacturing method of toner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11497194A JP3456010B2 (en) 1994-05-27 1994-05-27 Manufacturing method of toner

Publications (2)

Publication Number Publication Date
JPH07319203A JPH07319203A (en) 1995-12-08
JP3456010B2 true JP3456010B2 (en) 2003-10-14

Family

ID=14651165

Family Applications (1)

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

Country Link
JP (1) JP3456010B2 (en)

Also Published As

Publication number Publication date
JPH07319203A (en) 1995-12-08

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