JP3462552B2 - Powder surface modification method - Google Patents
Powder surface modification methodInfo
- Publication number
- JP3462552B2 JP3462552B2 JP01319694A JP1319694A JP3462552B2 JP 3462552 B2 JP3462552 B2 JP 3462552B2 JP 01319694 A JP01319694 A JP 01319694A JP 1319694 A JP1319694 A JP 1319694A JP 3462552 B2 JP3462552 B2 JP 3462552B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- plasma
- gas
- fluidized bed
- reduced pressure
- 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 - Fee Related
Links
Landscapes
- Developing Agents For Electrophotography (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、電子写真法、静電印刷
法、静電記録法などにおいて形成される静電現像をする
ための現像用トナーおよびキャリヤ、磁性用粉体、半導
体用粉体、蛍光用粉体、電池用粉体などのエレクトロニ
クス分野、クロマトグラフ用充填剤や触媒などを扱う化
学品分野、分散安定剤や粉体塗料、高機能塗料インキな
どを扱う塗料分野、耐酸化安定性向上を狙う金属分野、
化粧品、医薬品、臨床検査・診断、食品分野、その他カ
ーボンブラックなど広汎な産業上の利用分野を有する粉
体工業に利用される粉体の改質、表面処理に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a developing toner and carrier for electrostatic development formed in electrophotography, electrostatic printing, electrostatic recording, etc., magnetic powder, semiconductor powder. Body, fluorescent powder, battery powder and other electronics fields, chromatographic fillers and catalysts, chemical fields, dispersion stabilizers, powder coatings, high-performance coating inks and other coating fields, oxidation resistance Metal fields aiming to improve stability,
The present invention relates to the modification and surface treatment of powders used in the powder industry, which has a wide range of industrial fields such as cosmetics, pharmaceuticals, clinical tests / diagnosis, food fields, and carbon black.
【0002】[0002]
【従来の技術】従来、粉体の表面改質方法の一つとして
プラズマ重合・処理をする方法が例えば特願平4−31
5505号において提案されている。この方法の概要
は、減圧流動層を用いたプラズマ重合・処理の表面改質
方法であって、減圧流動層内の粉体を下部から上部への
ガスの気流による力、すなわち浮力によって空間に保
持、流動化させた後、プラズマ雰囲気下に粉体を曝し粉
体の表面をプラズマ重合・処理する方法であり、減圧流
動層本体に振動を加えない粉体の改質方法である。2. Description of the Related Art Conventionally, a method of plasma polymerization / treatment is one of the methods for modifying the surface of powder, for example, Japanese Patent Application No. 4-31.
No. 5505. The outline of this method is a surface modification method of plasma polymerization / treatment using a reduced pressure fluidized bed, in which the powder in the reduced pressure fluidized bed is retained in space by the force of gas flow from the lower part to the upper part, that is, buoyancy. After fluidizing, the powder is exposed to a plasma atmosphere to subject the surface of the powder to plasma polymerization / treatment, which is a method of modifying the powder without applying vibration to the reduced pressure fluidized bed body.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、上記従
来の改質方法を一般的な粉体の改質処理に応用する場
合、次のような問題を有していた。すなわち、10μm
以下の粉体の表面にプラズマ重合膜を生成するような場
合、粉体をガスの気流による浮力で流動化するだけでは
粉体間を解きほぐせず、粉体の一部が分散せずにブロッ
ク化して該粉体のブロック物中にチャネリングとよばれ
るガス気流の通路が形成され、全ての粉体にガスが接触
できる状態にならず、結果的に個々の粉体の表面に均一
な膜厚を有するプラズマ重合膜が生成できないという問
題を有していた。本発明は、前記したような減圧流動層
を用いた粉体表面の改質方法を改良し、付着性が強くチ
ャンネリングが起きやすい10μm以下という微小粉体
からなる粉体の表面にプラズマ重合膜を均一に生成する
か、またはプラズマ処理を均一に行う改質方法を提供す
ることを目的とする。However, when the above-mentioned conventional reforming method is applied to a general powder reforming treatment, there are the following problems. That is, 10 μm
When a plasma-polymerized film is formed on the surface of the powders below, the fluidization of the powders by the buoyancy of the gas stream does not unravel the powders, and some of the powders do not disperse. A gas flow path called channeling is formed in the block of the powder by blocking, and the gas cannot come into contact with all the powders, resulting in a uniform film on the surface of each powder. There is a problem that a plasma-polymerized film having a thickness cannot be produced. The present invention improves the method of modifying the surface of a powder using a reduced pressure fluidized bed as described above, and a plasma polymerized film is formed on the surface of a powder composed of fine powder having a size of 10 μm or less, which has strong adhesiveness and easily causes channeling. It is an object of the present invention to provide a reforming method for uniformly producing the above or performing the plasma treatment uniformly.
【0004】[0004]
【課題を解決するための手段】本発明の第1の発明は、
重合性モノマーガスで浮遊させてなる粉体を振動下にて
プラズマ雰囲気に曝し、該粉体の表面に重合性モノマー
ガスのプラズマ重合膜を生成せしめることを特徴とする
粉体表面の改質方法である。また、本発明の第2の発明
は、非重合性ガスで浮遊させてなる粉体を振動下にてプ
ラズマ雰囲気に曝し、該粉体の表面をプラズマ処理する
ことを特徴とする粉体表面の改質方法である。本発明に
おいては、粉体に振動を加えることにより、表面の改質
が困難とされた10μm以下という粒径領域の粉体でも
安定した良好な表面状態が得られ、しかも振動を与えて
いない従来の減圧流動層を使用した粉体表面の改質方法
よりも少量のガス量で良好な粉体の表面状態が得られ
る。The first invention of the present invention is as follows:
A method for modifying a powder surface, which comprises exposing a powder suspended in a polymerizable monomer gas to a plasma atmosphere under vibration to form a plasma-polymerized film of the polymerizable monomer gas on the surface of the powder. Is. A second aspect of the present invention is characterized in that the powder suspended in a non-polymerizable gas is exposed to a plasma atmosphere under vibration, and the surface of the powder is plasma-treated. This is a reforming method. In the present invention, by applying vibration to the powder, it is possible to obtain a stable and good surface condition even in the case of powder having a particle size range of 10 μm or less, which is difficult to modify the surface. It is possible to obtain a good powder surface condition with a smaller amount of gas than in the powder surface modification method using the reduced pressure fluidized bed.
【0005】本発明の第1の発明で使用される粉体とし
ては、平均粒径が0.5μm〜10μmの現像用トナー
およびキャリヤ、フェライトおよびマグネタイトなどの
磁性材料、各種の顔料粉体、炭化珪素および窒化珪素な
どの耐熱性粉体、化粧品などの粒状および針状粉体やプ
ラスチックファイバー、セルロース繊維ファイバー、ガ
ラス繊維、金属繊維などの短繊維状の粉体が適用され
る。また、本発明の第2の発明で使用される粉体として
は、少なくとも粉体の表面に高分子材料の一部が露出し
ているものが適用され、例えば前記現像用トナー、樹脂
被覆したキャリヤ、プラスチックファイバー、セルロー
ス繊維ファイバー、ガラス繊維、金属繊維の他に各種の
樹脂の粉体が適用される。なお、粉体に振動を効率よく
伝え、流動化を促進し良好な粉体の表面状態を得るため
に、表面改質を目的とする粉体以外に媒体とする粉体
(50μm〜5mm程度)を前記粉体に混在させて処理
してもよい。The powder used in the first invention of the present invention includes developing toner and carrier having an average particle diameter of 0.5 μm to 10 μm, magnetic materials such as ferrite and magnetite, various pigment powders, carbonization. Heat-resistant powders such as silicon and silicon nitride, granular and acicular powders such as cosmetics, and short fiber powders such as plastic fibers, cellulose fiber fibers, glass fibers and metal fibers are applied. Further, as the powder used in the second invention of the present invention, one in which at least a part of the polymer material is exposed on the surface of the powder is applied, and for example, the above-mentioned developing toner, resin-coated carrier In addition to plastic fiber, cellulose fiber, glass fiber, metal fiber, various resin powders are applied. In addition, in order to efficiently transmit vibration to the powder, promote fluidization, and obtain a good powder surface state, a powder (about 50 μm to 5 mm) as a medium other than the powder for the purpose of surface modification May be mixed with the powder for processing.
【0006】本発明の第1の発明でいうプラズマ重合お
よび第2のプラズマ処理はグロー放電とも呼ばれる通常
数Torr以下の低圧力の気体中における放電現象の低
温プラズマを利用するものである。プラズマ重合を利用
した第1の発明による表面改質によれば、重合性モノマ
ーガスを有機化合物とし、粉体材料自体の性質を変える
ことなく、粉体の表面に元の粉体材料にはない新しい物
理的、化学的性質を有した有機重合体薄膜が生成でき
る。この特徴を活かし、単一の重合性モノマーの重合膜
を生成する以外に、複数の重合性モノマーガスを用いて
粉体表面の機能レベルをコントロールしたものも製造す
ることが可能である。例えば電子写真用複写機現像剤に
おいて高精細用微小トナーの表面改質に本発明の技術を
利用すれば、低温度定着用トナー、臭気対策用トナーに
対応して表面物性のバランスがとれた良好なトナーも製
造が可能である。The plasma polymerization and the second plasma treatment referred to in the first aspect of the present invention utilize low temperature plasma, which is also called glow discharge, which is a discharge phenomenon in a gas at a low pressure of usually several Torr or less. According to the surface modification according to the first invention utilizing plasma polymerization, the polymerizable monomer gas is made to be an organic compound, the property of the powder material itself is not changed, and the original powder material does not exist on the surface of the powder. An organic polymer thin film having new physical and chemical properties can be produced. Taking advantage of this feature, it is possible to produce not only a polymerized film of a single polymerizable monomer but also one in which the functional level of the powder surface is controlled by using a plurality of polymerizable monomer gases. For example, in the electrophotographic copying machine developer, when the technique of the present invention is used for surface modification of high-definition fine toner, the surface properties are well balanced in correspondence with low-temperature fixing toner and odor countermeasure toner. Various toners can be manufactured.
【0007】本発明で用いられる重合性モノマーガスと
しては、テトラフルオロエチレン、ヘキサフルオロベン
ゼン、パーフルオロベンゼン、ペンタフルオロベンゼ
ン、パーフルオロピリジン、パーフルオロメチルシクロ
ヘキサン、ヘキサフルオロプロペン、ヘキサメチルジシ
ロキサン、トリエトキシビニルシラン、ビニルメトキシ
シラン、1,1,3,3−テトラメチルジシロキサン、
テトラエチルオルソシリケート、ジアリルジメチルシラ
ン、メタン、エタン、プロパン、n−ブタン、i−ブタ
ン、プロピレン、アクリロニトリル、プロピオニトリ
ル、プロピルアミン、アリールアミン、エチレン、アレ
ン、アセチレン、エチレンオキシド、ベンゼン、トルエ
ン、キシレン、ヘキサン、シクロヘキサン、アクリル酸
およびアクリル酸エステル、メタクリル酸およびメタク
リル酸エステル、クロルベンゼン、ニトロトルエン、ス
チレンおよびスチレン誘導体などが挙げられるがこれに
限定されるものではない。また重合性モノマーガスを供
給する場合に同伴ガスを利用しようとするときは、この
同伴ガスとしてヘリウム、アルゴン、ネオン、窒素など
の不活性ガスを用いることができる。また第2の発明に
よるプラズマ処理は、ヘリウム、アルゴン、ネオン、空
気、酸素、窒素、水素、四フッ化メタン、一酸化炭素、
アンモニアなどの気体を少なくとも1種含む非重合性ガ
スをプラズマ化させ、このプラズマ雰囲気に粉体を曝し
表面処理改質を行うもので、プラズマ処理することによ
って、例えば高分子材料の粉体では表面官能基、表面橋
架け、枝分かれ、酸化などの導入、ラジカルの発生、表
面の分解およびエッチングなどの表面改質が起こり、よ
って例えば現像用トナーの場合は、摩擦帯電の極性と量
を任意に変化させることができたり、トナーの保存性改
良、定着時の臭気発生を防止することができる。Examples of the polymerizable monomer gas used in the present invention include tetrafluoroethylene, hexafluorobenzene, perfluorobenzene, pentafluorobenzene, perfluoropyridine, perfluoromethylcyclohexane, hexafluoropropene, hexamethyldisiloxane and trifluoroethylene. Ethoxyvinylsilane, vinylmethoxysilane, 1,1,3,3-tetramethyldisiloxane,
Tetraethylorthosilicate, diallyldimethylsilane, methane, ethane, propane, n-butane, i-butane, propylene, acrylonitrile, propionitrile, propylamine, arylamine, ethylene, arene, acetylene, ethylene oxide, benzene, toluene, xylene, Examples thereof include, but are not limited to, hexane, cyclohexane, acrylic acid and acrylic acid ester, methacrylic acid and methacrylic acid ester, chlorobenzene, nitrotoluene, styrene, and styrene derivative. When an entrained gas is to be used when supplying the polymerizable monomer gas, an inert gas such as helium, argon, neon or nitrogen can be used as the entrained gas. Further, the plasma treatment according to the second invention is performed by helium, argon, neon, air, oxygen, nitrogen, hydrogen, tetrafluoromethane, carbon monoxide,
A non-polymerizable gas containing at least one gas such as ammonia is made into plasma, and the powder is exposed to this plasma atmosphere for surface treatment modification. Introducing functional groups, surface bridging, branching, oxidation, etc., surface generation such as radical generation, surface decomposition and etching occurs, so in the case of developing toner, for example, the polarity and amount of triboelectrification can be changed arbitrarily. It is possible to improve the storage stability of the toner and prevent the generation of odor during fixing.
【0008】次に本発明の改質方法を適用できる装置に
ついて説明する。第1の発明のプラズマ重合や、第2の
発明のプラズマ処理に用いる装置としては、例えば内部
電極方式のベルジャー型、クロス型、外部電極方式の円
筒型などの各種混合装置を適用して行うことが可能であ
るが、特に後者の円筒型の外部電極方式の減圧流動層を
用いたプラズマ装置が好適であり、振動モーターを備え
た振動台に減圧流動層を固定したものが好ましい。図1
は本発明の改質方法を適用できる装置の一例の説明図
で、振動台10に設置、固定されたガラス製の減圧流動
層5の下部には外部の高周波電源9と接続された電極8
があり、その下部にはガラスビーズ焼結体からなる多孔
性の分散板7(該分散板7は直径1〜20μmの孔を複
数有する)が設けられている。また、減圧流動層5の上
下の間の圧力差を測定するマノメーター4および減圧流
動層5内の圧力を計測するピラニー真空計6が付されて
おり、減圧流動層5を経たガスは、微粉回収フラスコ3
内に噴出し、真空ポンプ1に接続して減圧されるように
なっている。なお各部分を接続するバルブはそれぞれ2
で示している。振動台10には底部に角度が45゜に配
置した2つの振動モーター11を有し、該振動モーター
11により減圧流動層5に周波数が10〜2000Hz
および振幅が0.1〜2mmの振動を与え、粉体に適度
な空間を与えてプラズマ雰囲気内の粉体の流動を促進さ
せ、粉体表面で改質が満遍なく進み、プラズマ重合・処
理が均一になされる。このように振動台10は減圧流動
層5全体に振動を加えて、効率のよい粉体の流動化を促
す役目を果たす。なお、分散板7の上部の2箇所には、
ガラス板を隔てた外部に電極8が巻き付けられており、
一方はマッチングボックスを経て高周波電源9に、他の
一方はアースに接続されて、減圧流動層5内にプラズマ
が発生するようになっている。プラズマ重合またはプラ
ズマ処理を行う場合は、多孔性の分散板7の上に改質す
べき粉体の適量を載置し、重合性モノマーガスまたは非
重合性ガスを供給しながら該粉体を浮遊させてプラズマ
雰囲気にする。Next, an apparatus to which the reforming method of the present invention can be applied will be described. As an apparatus used for the plasma polymerization of the first invention and the plasma treatment of the second invention, various mixing apparatuses such as a bell jar type of internal electrode type, a cross type, and a cylindrical type of external electrode type are applied. However, the latter plasma apparatus using a reduced pressure fluidized bed of the cylindrical external electrode system is particularly preferable, and a vibrating table equipped with a vibration motor having the reduced pressure fluidized bed fixed thereto is preferable. Figure 1
3 is an explanatory view of an example of an apparatus to which the reforming method of the present invention can be applied, in which the electrode 8 connected to an external high-frequency power source 9 is provided below the vacuum decompression fluidized bed 5 made of glass, which is installed and fixed on the vibrating table 10.
And a porous dispersion plate 7 made of a glass bead sintered body (the dispersion plate 7 has a plurality of holes having a diameter of 1 to 20 μm) is provided in the lower part thereof. Further, a manometer 4 for measuring the pressure difference between the upper and lower sides of the reduced pressure fluidized bed 5 and a Pirani vacuum gauge 6 for measuring the pressure inside the reduced pressure fluidized bed 5 are attached, and the gas that has passed through the reduced pressure fluidized bed 5 is recovered as fine powder. Flask 3
It is spouted into the inside and connected to the vacuum pump 1 to reduce the pressure. There are 2 valves for each part.
It shows with. The vibrating table 10 has two vibrating motors 11 arranged at an angle of 45 ° on the bottom, and the vibrating motors 11 cause the depressurized fluidized bed 5 to have a frequency of 10 to 2000 Hz.
And vibration with an amplitude of 0.1 to 2 mm gives an appropriate space to the powder to promote the flow of the powder in the plasma atmosphere, the reforming progresses evenly on the powder surface, and the plasma polymerization / treatment is uniform. Done As described above, the vibrating table 10 applies a vibration to the entire reduced pressure fluidized bed 5 to promote efficient fluidization of the powder. In addition, at the two places on the upper part of the dispersion plate 7,
The electrode 8 is wrapped around the outside of the glass plate,
One is connected to the high-frequency power source 9 via the matching box and the other is connected to the ground so that plasma is generated in the reduced pressure fluidized bed 5. When performing plasma polymerization or plasma treatment, an appropriate amount of the powder to be modified is placed on the porous dispersion plate 7, and the powder is suspended while supplying the polymerizable monomer gas or the non-polymerizable gas. To create a plasma atmosphere.
【0009】本発明の第1の発明を実施するためには、
重合性モノマーガスを供給して粉体表面にプラズマ重合
膜を生成する。すなわち、重合性モノマーガスボンベ1
5から重合性モノマーガスをフローメーター13を経て
振動台10により振動させた減圧流動層5内に供給し粉
体を浮遊させた後、プラズマを発生させ粉体表面に重合
膜を生成させる。ただし、重合性モノマーガスとして、
スチレンなどの揮発し易い液状モノマーを用いる場合
は、液状モノマーを液状モノマー容器12内に入れ、液
状モノマーを非重合性ガスボンベ14からフローメータ
ー13を経て該液状モノマー容器内に通過させた同伴ガ
ス(非重合性ガス)とともに気化させて減圧流動層5内
に供給し粉体を浮遊させた後、プラズマを発生させ粉体
表面に重合膜を生成させる。一方、本発明の第2の発明
を実施するためには、非重合性ガスのみを用いて粉体表
面をプラズマ処理する。すなわち、非重合性ガスボンベ
14よりフローメーター13を経て非重合性ガスを、振
動させた減圧流動層5内に供給し粉体を浮遊させた後、
プラズマを発生させ粉体表面をプラズマ処理して、粉体
表面を改質する。なお、上記において、重合性モノマー
ガスを使用してプラズマ重合する場合に、同時に非重合
性ガスボンベ14からの非重合性ガスを液状モノマー容
器12を経由することなく直接重合性モノマーガスと共
に減圧流動層に供給することもできる。これにより重合
反応を抑制することもできるし、粉体に浮力を付与する
ための気流の確保が可能となる。さらに図1には、重合
性モノマーガスボンベ15は1本しか示されていない
が、複数の種類の異なる重合性モノマーガスボンベを用
意して、希望する比率で重合体の種類の異なるプラズマ
重合膜を生成させることもできる。また、減圧流動層5
内に重合性モノマーガスあるいは非重合性ガス以外のガ
スを供給し粉体を浮遊させてから重合性モノマーガスあ
るいは非重合性ガスを供給させてもよい。本発明におい
ては、重合膜の生成の程度および粉体表面の改質程度
は、真空度、印加電圧、電極間の距離、基板温度、さら
に気体の種類、流量および装置内の流れのパターンなど
のプラズマ操作条件で変わるので最適なプラズマ条件は
各種粉体に応じて適時見いだすことが必要である。ま
た、粉体の体積平均粒径が0.5〜10μmの場合は、
該粉体として真密度が0.9〜22kg/cm3 のもの
を使用し、減圧流動層5内における粉体の浮遊状態が空
間率0.45〜0.85とすることが良好な表面状態を
得るうえで好ましい。In order to carry out the first invention of the present invention,
A polymerizable monomer gas is supplied to form a plasma polymerized film on the surface of the powder. That is, the polymerizable monomer gas cylinder 1
The polymerizable monomer gas from No. 5 is supplied to the reduced pressure fluidized bed 5 vibrated by the vibrating table 10 through the flow meter 13 to suspend the powder, and then plasma is generated to form a polymerized film on the surface of the powder. However, as the polymerizable monomer gas,
When volatile liquid monomer such as styrene is used, the liquid monomer is put in the liquid monomer container 12, and the liquid monomer is passed from the non-polymerizable gas cylinder 14 into the liquid monomer container through the flow meter 13 ( After being vaporized together with the (non-polymerizable gas) and supplied into the reduced pressure fluidized bed 5 to suspend the powder, plasma is generated to generate a polymerized film on the surface of the powder. On the other hand, in order to carry out the second aspect of the present invention, the powder surface is plasma-treated using only the non-polymerizable gas. That is, after the non-polymerizable gas is supplied from the non-polymerizable gas cylinder 14 through the flow meter 13 into the vibrating reduced pressure fluidized bed 5 to suspend the powder,
Plasma is generated and the powder surface is plasma-treated to modify the powder surface. In the above, when performing the plasma polymerization using the polymerizable monomer gas, the non-polymerizable gas from the non-polymerizable gas cylinder 14 is directly flown together with the polymerizable monomer gas without passing through the liquid monomer container 12 under reduced pressure fluidized bed. Can also be supplied to. As a result, the polymerization reaction can be suppressed, and an air flow for imparting buoyancy to the powder can be secured. Further, although only one polymerizable monomer gas cylinder 15 is shown in FIG. 1, a plurality of different kinds of polymerizable monomer gas cylinders are prepared to produce a plasma polymerized film having different kinds of polymers at a desired ratio. You can also let it. Also, the reduced pressure fluidized bed 5
A gas other than the polymerizable monomer gas or the non-polymerizable gas may be supplied to suspend the powder, and then the polymerizable monomer gas or the non-polymerizable gas may be supplied. In the present invention, the degree of formation of the polymerized film and the degree of modification of the powder surface include the degree of vacuum, the applied voltage, the distance between the electrodes, the substrate temperature, the type of gas, the flow rate and the flow pattern in the apparatus. It is necessary to find the optimum plasma condition in a timely manner according to various powders, because it depends on the plasma operation condition. When the volume average particle diameter of the powder is 0.5 to 10 μm,
A surface state in which the powder has a true density of 0.9 to 22 kg / cm 3 and the floating state of the powder in the reduced pressure fluidized bed 5 has a porosity of 0.45 to 0.85 is preferable. To obtain
【0010】[0010]
【実施例】次に実施例によって本発明を説明する。
実施例1
図1に示した装置において、減圧流動層がパイレックス
ガラス製で高さ1000mmおよび内径30mmであ
り、振動台(中央化工機社製、VUA−10型)が該減
圧流動層に固定された装置を使用して次のプラズマ重合
を行った。減圧流動層の内部には、孔径が3μmの多数
の孔を有する分散板を設け、該分散板のすぐ上部と、そ
の100mm上部に銅板からなる電極を前記減圧流動層
の円筒部に巻き付け、一方の電極はマッチングボックス
を経て13.56MHzの高周波電源に接続し、他方の
電極はアースと接続してある。プラズマ重合は、まず平
均粒径6μmのトナー粉体10gを減圧流動層内の分散
板に載置し、振動台内部の振動モーターを稼動させて減
圧流動層を振動させ、次に重合性モノマーガスとしてヘ
キサメチルジシロキサンを30cc/minおよび同伴
ガスとしてアルゴンガスを90cc/minを減圧流動
層内に供給し、層内圧力を0.1Torrに調整してト
ナー粉体を浮遊させた後、電極間に50Wの電力を加え
て減圧流動層内をプラズマ雰囲気にしてトナー粉体をプ
ラズマ雰囲気に10分間曝し、該トナー粉体の表面にヘ
キサメチルジシロキサンをプラズマ重合し重合膜を生成
した。なお、減圧流動層の外部に取り付けた振動計によ
り該減圧流動層の振動を測定したところ振動は50H
z、振幅は1.0mmであり、振動化時の平均空間率は
0.75であった。なお、用いたトナー粉体は次のよう
にして製造したものである。
・スチレンーブチルアクリレート共重合体樹脂 100重量部
・カーボンブラック 7重量部
(三菱化成工業社製、商品名:MA−100)
・ポリプロピレン 4重量部
(三菱化成工業社製、商品名:ビスコール660P)
・含金属染料 2重量部
(保土谷化学工業社製、商品名:T−77)
本実施例では上記組成からなる配合物を混練粉砕法によ
り処理して、平均粒径6μmのトナー粉体を作製した。
ついでシリカ微粉体(日本アエロジル社製、商品名:R
−972)0.2重量%を得られたトナー粉体の表面に
付着させた。なお、得られたトナー粉体のガラス転移温
度は55.3℃であり、溶融開始温度は75.6℃であ
った。EXAMPLES The present invention will now be described with reference to examples. Example 1 In the apparatus shown in FIG. 1, the reduced pressure fluidized bed was made of Pyrex glass and had a height of 1000 mm and an inner diameter of 30 mm, and a vibrating table (VUA-10 manufactured by Chuo Kakoki Co., Ltd.) was fixed to the reduced pressure fluidized bed. The following plasma polymerization was carried out using the above apparatus. Inside the reduced-pressure fluidized bed, a dispersion plate having a large number of holes with a diameter of 3 μm was provided, and an electrode made of a copper plate was wrapped around the cylindrical portion of the reduced-pressure fluidized bed just above the dispersion plate and 100 mm above it. The electrode of is connected to a high frequency power source of 13.56 MHz via a matching box, and the other electrode is connected to the ground. In plasma polymerization, 10 g of toner powder having an average particle size of 6 μm is first placed on a dispersion plate in a reduced pressure fluidized bed, a vibration motor inside a vibrating table is operated to vibrate the reduced pressure fluidized bed, and then a polymerizable monomer gas is added. Hexamethyldisiloxane is supplied as 30 cc / min and argon gas as entrainment gas is supplied as 90 cc / min into the depressurized fluidized bed, and the in-layer pressure is adjusted to 0.1 Torr to suspend the toner powder. A power of 50 W was applied to the inside of the vacuum fluidized bed to form a plasma atmosphere, and the toner powder was exposed to the plasma atmosphere for 10 minutes. Hexamethyldisiloxane was plasma-polymerized on the surface of the toner powder to form a polymer film. The vibration of the reduced pressure fluidized bed was measured by a vibrometer attached to the outside of the reduced pressure fluidized bed.
The z and the amplitude were 1.0 mm, and the average porosity when vibrating was 0.75. The toner powder used is manufactured as follows.・ Styrene-butyl acrylate copolymer resin 100 parts by weight ・ Carbon black 7 parts by weight (Mitsubishi Chemical Co., Ltd., trade name: MA-100) ・ Polypropylene 4 parts by weight (Mitsubishi Kasei Co., Ltd., trade name: Viscole 660P) 2 parts by weight of metal-containing dye (Hodogaya Chemical Co., Ltd., trade name: T-77) In this example, the compound having the above composition was treated by a kneading pulverization method to obtain a toner powder having an average particle size of 6 μm. It was made.
Then silica fine powder (product name: R, manufactured by Nippon Aerosil Co., Ltd.)
-972) 0.2% by weight was adhered to the surface of the obtained toner powder. The glass transition temperature of the obtained toner powder was 55.3 ° C, and the melting start temperature was 75.6 ° C.
【0011】実施例2
ヘキサメチルジシロキサンを15cc/minにアルゴ
ンガスを45cc/minを同伴させて減圧流動層内に
供給し、層内圧力を0.1Torrに調整し、振動条件
は30Hz、振幅0.5mmであり、流動化時の平均空
間率は0.54にした以外は実施例1と同様にしてトナ
ー粉体の表面に該ヘキサメチルジシロキサンをプラズマ
重合し重合膜を生成した。Example 2 Hexamethyldisiloxane was supplied in a reduced pressure fluidized bed with 15 cc / min of argon gas and 45 cc / min of argon gas, the pressure in the layer was adjusted to 0.1 Torr, and the vibration condition was 30 Hz and amplitude. It was 0.5 mm, and the hexamethyldisiloxane was plasma-polymerized on the surface of the toner powder to form a polymerized film in the same manner as in Example 1 except that the average porosity during fluidization was 0.54.
【0012】実施例3
実施例1と同様にして混練粉砕法によってトナー粉体を
作製し、ガスとしてはアルゴンガスのみを100cc/
min減圧流動層に供給し、その他の条件はすべて実施
例1と同様にしてトナー粉体の表面処理を行った。Example 3 A toner powder was prepared by a kneading and pulverizing method in the same manner as in Example 1, and only argon gas was used as a gas at 100 cc /
The toner powder was surface-treated in the same manner as in Example 1 under the same conditions as in Example 1.
【0013】比較例1
プラズマ重合膜を生成する場合に振動を加えず、他は実
施例1と同様にして比較用のトナーを得た。Comparative Example 1 A toner for comparison was obtained in the same manner as in Example 1 except that vibration was not applied when forming the plasma polymerized film.
【0014】比較例2
プラズマ重合およびプラズマ処理していない実施例1で
得たトナー粉体をそのまま比較用のトナーとした。Comparative Example 2 The toner powder obtained in Example 1 which was not subjected to plasma polymerization and plasma treatment was used as it was for comparison.
【0015】比較例3
プラズマ処理をする場合に振動を加えず、他は実施例3
と同様にして比較用のトナーを得た。Comparative Example 3 No vibration was applied when plasma treatment was performed, and the other examples were used.
A comparative toner was obtained in the same manner as in.
【0016】上記実施例1、実施例2および比較例1、
比較例2で得られたトナー粉体を用いて下記特性を評価
した。
(1)ガラス転移温度(Tg)
示差走査熱量測定装置(SEIKO社製)を用いて測定
した。
(2)溶融開始温度
フローテスター(島津製作所社製、CFT−500型)
を用いて、等速昇温法(5℃/min)により測定し
た。
(3)保存安定性(ブロッキングテスト)
実施例および比較例で得られたトナー粉体20gを、2
00ccのガラス製ビーカーに入れ、それを50℃の温
度にコントロールしたオーブン内に入れた。その条件で
8時間保った後、オーブンから取り出し、25℃、60
%RHの条件下に24時間放置した。その後、ビーカー
を逆さまにして中のトナーを紙の上に移し、円錐状に載
置されたトナー粉体の様子を目視および指触で評価し
た。評価は次に示す評価基準に従って行った。
1:パウダー状でブロッキングがなく、さらさらしてい
る。
2:指で触れてつぶれる直径3mm以下の塊がある。
3:指でふれてつぶれる直径10mm以下の塊がある。
4:基準3以上の塊あるいはビーカー内で固定してい
る。The above-mentioned Examples 1 and 2 and Comparative Example 1,
The following characteristics were evaluated using the toner powder obtained in Comparative Example 2. (1) Glass transition temperature (Tg) It was measured using a differential scanning calorimeter (manufactured by SEIKO). (2) Melting start temperature flow tester (CFT-500 type manufactured by Shimadzu Corporation)
Was measured by the constant velocity heating method (5 ° C./min). (3) Storage stability (blocking test) 20 g of the toner powder obtained in Examples and Comparative Examples
It was placed in a 00 cc glass beaker and placed in an oven controlled at a temperature of 50 ° C. After keeping the conditions for 8 hours, remove from the oven,
It was left under the condition of% RH for 24 hours. Then, the beaker was turned upside down, the toner inside was transferred onto the paper, and the appearance of the toner powder placed in a conical shape was evaluated visually and by touch. The evaluation was performed according to the following evaluation criteria. 1: Powdery, non-blocking, free-flowing. 2: There is a lump with a diameter of 3 mm or less that can be touched and crushed by a finger. 3: There is a lump with a diameter of 10 mm or less that can be crushed by touching with a finger. 4: Fixed in a lump or beaker of standard 3 or more.
【0017】(4)非オフセット温度領域
まず、前記実施例および比較例で得たトナー粉体4重量
部と、樹脂被覆を施してないフェライトキャリヤ(パウ
ダーテック社製、商品名:FL−1020)96重量部
とを混合して二成分系現像剤を作製した。次に該現像剤
を使用して市販の複写機(シャープ社製、商品名:SF
−9800)にてA4の転写紙に縦2cm、横5cmの
帯状の未定着画像を複数作製した。ついで、表層がテフ
ロンで形成された熱定着ロールと、表層がシリコーンゴ
ムで形成された圧力定着ロールとが対になって回転する
定着機を、ロール圧力が1kg/cm2 であり、ロール
スピードが100mm/secになるように調整し、該
定着ロールの表面温度を階段的に変化させて、各表面温
度において上記未定着画像を有した転写紙のトナー像の
定着を行った。この時、余白部分にトナー汚れが生じる
か否かの観測を行い、汚れが生じない温度領域を非オフ
セット温度領域とした。
(5)定着強度
前記定着機において、熱定着ロールの表面温度を70℃
および100℃に設定し、前記未定着画像が形成された
転写紙のトナー像の定着を行った。ついで定着画像の画
像濃度を測定した後、定着画像を綿パッドで摺擦して再
び画像濃度を測定した。得られた測定値を下記式に当て
はめて定着強度を算出した。画像濃度はマクベス社製の
反射濃度計RD−914を使用して測定した。
定着強度(%)=(摺擦後の定着画像の画像濃度/摺擦
前の定着画像の画像濃度)×100
上記項目の試験結果を表1に示す。(4) Non-Offset Temperature Region First, 4 parts by weight of the toner powder obtained in the above Examples and Comparative Examples and a ferrite carrier not coated with a resin (Powder Tech Co., trade name: FL-1020). 96 parts by weight were mixed to prepare a two-component developer. Next, a commercially available copying machine (manufactured by Sharp Corporation, trade name: SF
-9800), a plurality of belt-shaped unfixed images having a length of 2 cm and a width of 5 cm were prepared on an A4 transfer paper. Then, a fixing machine in which a heat fixing roll having a surface layer made of Teflon and a pressure fixing roll having a surface layer made of silicone rubber are paired and rotated, a roll pressure is 1 kg / cm 2 and a roll speed is The surface temperature of the fixing roll was changed stepwise so that the toner image on the transfer paper having the unfixed image was fixed at each surface temperature. At this time, it was observed whether or not the toner was smeared in the blank area, and the temperature range in which the smear did not occur was taken as the non-offset temperature range. (5) Fixing strength In the fixing machine, the surface temperature of the heat fixing roll is 70 ° C.
Then, the temperature was set to 100 ° C., and the toner image on the transfer paper on which the unfixed image was formed was fixed. Then, after measuring the image density of the fixed image, the fixed image was rubbed with a cotton pad to measure the image density again. The obtained measured value was applied to the following formula to calculate the fixing strength. The image density was measured using a reflection densitometer RD-914 manufactured by Macbeth. Fixing strength (%) = (image density of fixed image after rubbing / image density of fixed image before rubbing) × 100 Table 1 shows the test results of the above items.
【0018】[0018]
【表1】 [Table 1]
【0019】表1から明らかなように実施例1および実
施例2で得られたトナー粉体は、表面にプラズマ重合膜
を生成したので、十分な定着画像と非オフセット温度領
域を得た上で比較例と比べて保存安定性に経時変化がな
くプラズマ重合による効果が十分に維持されていること
が確認された。このトナー粉体は、実用上十分な低温定
着特性を維持しながら、保存性が十分に改善されている
ことが確認された。これに対して、比較例1および比較
例2のトナー粉体は、表面にプラズマ重合膜が十分に均
一に形成されていないので、保存安定性が悪く、実用上
問題があることが確認された。As is clear from Table 1, the toner powders obtained in Examples 1 and 2 formed a plasma polymerized film on the surface thereof, and therefore, after obtaining a sufficient fixed image and a non-offset temperature region. It was confirmed that the storage stability did not change with time as compared with the comparative example, and the effect of plasma polymerization was sufficiently maintained. It was confirmed that this toner powder had a sufficiently improved storage stability while maintaining a practically sufficient low temperature fixing property. On the other hand, in the toner powders of Comparative Examples 1 and 2, the plasma polymerized film was not formed sufficiently uniformly on the surface, so it was confirmed that the storage stability was poor and there was a practical problem. .
【0020】また、前記実施例3、比較例2および比較
例3で得られたトナー粉体を用いて下記特性を評価し
た。
(6)ガスクロマトグラフ質量分析計(GC−MS)に
よる測定
本測定では残留モノマーが多いと見られるスチレン、ト
ルエンを着目成分として選んだ。測定条件はサンプル量
2mg、加熱条件は120℃および170℃で10分間
の2通りである。結果は表2中に示す通り、本発明のプ
ラズマ処理の表面改質によって、比較例2および比較例
3に比べて実施例3のトナー粉体中のスチレンおよびト
ルエンの残留モノマー量が少なくなっていることが確認
された。Further, the following characteristics were evaluated using the toner powders obtained in Example 3, Comparative Example 2 and Comparative Example 3. (6) Measurement by Gas Chromatograph Mass Spectrometer (GC-MS) Styrene and toluene, which are considered to have a large amount of residual monomers in this measurement, were selected as the components of interest. The measurement condition is a sample amount of 2 mg, and the heating condition is two ways of 120 ° C. and 170 ° C. for 10 minutes. As shown in Table 2, the surface modification of the plasma treatment of the present invention reduces the residual monomer amounts of styrene and toluene in the toner powder of Example 3 as compared with Comparative Examples 2 and 3. Was confirmed.
【0021】(7)臭気の官能テスト
容量150ccのポリスチレン製ボトルに試料を20g
入れ、キャップを閉じた後、50℃の温度雰囲気のオー
ブンに入れた。その条件で8時間保った後、オーブンか
ら取り出し、その直後にキャップを開け嗅覚により臭気
を評価した。さらにキャップを閉じて室温にて24時間
放置後にキャップを開け嗅覚により同一試料の臭気を評
価した。評価として5段階の序列を付けて行った。ま
た、個人差を除くために官能テストを3人で行い3人の
合議によって評価値を決定した。評価基準は、5が無臭
で、1になるほど臭気が多いことを示す。以上の結果を
表2に示す。(7) Sensory test for odor 20 g of a sample in a polystyrene bottle having a capacity of 150 cc
After putting it in and closing the cap, it was placed in an oven at a temperature of 50 ° C. After keeping the condition for 8 hours, the container was taken out from the oven, and immediately after that, the cap was opened and the odor was evaluated by the sense of smell. Further, after closing the cap and leaving it at room temperature for 24 hours, the cap was opened and the odor of the same sample was evaluated by the sense of smell. The evaluation was carried out with a rank of 5 levels. In addition, in order to eliminate individual differences, a sensory test was conducted by three people, and the evaluation value was determined by a consultation of the three people. The evaluation criteria show that 5 is odorless, and the more it is 1, the more odor. The above results are shown in Table 2.
【0022】[0022]
【表2】 [Table 2]
【0023】表2に示す通り、本発明の改質方法による
実施例3のトナー粉体の場合、臭気が十分に改善され、
プラズマの表面処理による効果が十分にあることを確認
した。As shown in Table 2, in the case of the toner powder of Example 3 according to the modifying method of the present invention, the odor was sufficiently improved,
It was confirmed that the effect of the plasma surface treatment was sufficient.
【0024】(8)連続コピー試験
前記(4)で得られた実施例1〜実施例3の現像剤を使
用して市販の複写機(シャープ社製、商品名:SF−9
800)で5000枚までの連続コピー試験を行った。
初期の摩擦帯電量とコピー後の摩擦帯電量とを測定し
た。また、初期の画像濃度と、連続コピー後の画像濃度
も測定した。コピー原稿はA4サイズであり、その10
%に当たる部分が黒色部である。なお、画像濃度測定に
はマクベス社製の反射濃度計RD−914を使用した。
実施例1〜実施例3で得られたトナー粉体の摩擦帯電量
は、初期値から5000枚コピー後の値は、−20μc
/gから−25μc/gの値で推移した。画像濃度は、
1.31から1.35までの値を推移した。この測定結
果から、実施例1〜実施例3で得られたトナー粉体は、
十分連続コピーに耐えられ、実用上問題のないことが確
認された。(8) Continuous Copy Test A commercially available copying machine (manufactured by Sharp Corporation, trade name: SF-9) using the developers of Examples 1 to 3 obtained in (4) above.
800), a continuous copy test up to 5000 sheets was conducted.
The initial triboelectric charge amount and the triboelectric charge amount after copying were measured. The initial image density and the image density after continuous copying were also measured. The copy manuscript is A4 size, 10
The portion corresponding to% is the black portion. A reflection densitometer RD-914 manufactured by Macbeth was used for image density measurement.
The triboelectric charge amounts of the toner powders obtained in Examples 1 to 3 are −20 μc after the initial value after copying 5000 sheets.
/ G to −25 μc / g. The image density is
The value changed from 1.31 to 1.35. From the measurement results, the toner powders obtained in Examples 1 to 3 are
It was confirmed that it could withstand continuous copying satisfactorily and had no practical problems.
【0025】[0025]
【発明の効果】本発明は、粉体に浮遊と振動を施しなが
らプラズマ重合・処理をおこない粉体の表面改質、表面
処理を行い得るので、種々の特性の粉体を容易に提供す
ることができる。また方法の実施に当たっては、振動台
付き減圧流動層内における粉体の混合割合を任意に選択
できることや、処理温度の均一性、処理装置の制御が自
由にコントロールできるので、微小粒径の粉体に各種の
機能を付与することができる。INDUSTRIAL APPLICABILITY According to the present invention, plasma polymerization and treatment can be carried out while subjecting the powder to floating and vibration, and the surface modification and surface treatment of the powder can be performed, so that powder having various characteristics can be easily provided. You can Further, in carrying out the method, since it is possible to arbitrarily select the mixing ratio of the powder in the reduced pressure fluidized bed with a vibrating table, the uniformity of the processing temperature, and the control of the processing apparatus can be freely controlled, the powder having a fine particle diameter Various functions can be added to.
【図1】図1は振動台付き減圧流動層型プラズマ装置の
概略図である。FIG. 1 is a schematic diagram of a reduced pressure fluidized bed type plasma device with a vibrating table.
1 真空ポンプ 2 バルブ 3 微粉回収フラスコ 4 マノメーター 5 減圧流動層 6 ピラニー真空計 7 分散板 8 電極 9 高周波電源 10 振動台 11 振動モーター 12 液状モノマー容器 13 フローメーター 14 非重合性ガスボンベ 15 重合性モノマーガスボンベ 1 vacuum pump 2 valves 3 Fine powder recovery flask 4 Manometer 5 Reduced pressure fluidized bed 6 Pirani vacuum gauge 7 Dispersion plate 8 electrodes 9 High frequency power supply 10 shaking table 11 Vibration motor 12 Liquid monomer container 13 Flow meter 14 Non-polymerizable gas cylinder 15 Polymerizable monomer gas cylinder
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平3−267301(JP,A) 特開 平6−145212(JP,A) 特開 平3−44649(JP,A) 特開 昭63−269168(JP,A) 特開 昭60−47004(JP,A) 特開 昭62−257175(JP,A) 特開 昭58−222503(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01J 19/08 G03G 9/087 G03G 9/10 ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-3-267301 (JP, A) JP-A-6-145212 (JP, A) JP-A-3-44649 (JP, A) JP-A-63- 269168 (JP, A) JP 60-47004 (JP, A) JP 62-257175 (JP, A) JP 58-222503 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) B01J 19/08 G03G 9/087 G03G 9/10
Claims (4)
体を振動下にてプラズマ雰囲気に曝し、該粉体の表面に
重合性モノマーガスのプラズマ重合膜を生成せしめるこ
とを特徴とする粉体表面の改質方法。1. A powder characterized in that a powder suspended in a polymerizable monomer gas is exposed to a plasma atmosphere under vibration to form a plasma-polymerized film of the polymerizable monomer gas on the surface of the powder. Surface modification method.
動下にてプラズマ雰囲気に曝し、該粉体の表面をプラズ
マ処理することを特徴とする粉体表面の改質方法。2. A modified powder surface characterized by exposing a powder suspended in a non-polymerizable gas to a plasma atmosphere under vibration to subject the surface of the powder to plasma treatment. Quality method.
に振動を与える手段が減圧流動層に接触された振動台に
よりなされることを特徴とする請求項1および請求項2
記載の粉体表面の改質方法。3. The powder is suspended in a reduced pressure fluidized bed, and means for vibrating the powder is provided by a vibrating table in contact with the reduced pressure fluidized bed.
A method for modifying the surface of a powder as described.
Hzおよび振幅が0.1〜2mmの振動を減圧流動層に
与えることを特徴とする請求項3記載の粉体表面の改質
方法。4. The frequency is 10 to 2000 depending on the vibrating table.
4. The method for modifying the surface of a powder according to claim 3, wherein the reduced pressure fluidized bed is subjected to vibrations of Hz and amplitude of 0.1 to 2 mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP01319694A JP3462552B2 (en) | 1994-01-10 | 1994-01-10 | Powder surface modification method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP01319694A JP3462552B2 (en) | 1994-01-10 | 1994-01-10 | Powder surface modification method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07194968A JPH07194968A (en) | 1995-08-01 |
JP3462552B2 true JP3462552B2 (en) | 2003-11-05 |
Family
ID=11826410
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP01319694A Expired - Fee Related JP3462552B2 (en) | 1994-01-10 | 1994-01-10 | Powder surface modification method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3462552B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2649136B1 (en) * | 2010-12-08 | 2015-11-04 | Haydale Graphene Industries plc | Particulate materials, composites comprising them, preparation and uses thereof |
JP5854817B2 (en) * | 2011-12-21 | 2016-02-09 | キユーピー株式会社 | Boiled egg shell cracking device |
JP6328537B2 (en) * | 2014-10-31 | 2018-05-23 | エア・ウォーター・マッハ株式会社 | Plasma processing method and plasma processing apparatus |
-
1994
- 1994-01-10 JP JP01319694A patent/JP3462552B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH07194968A (en) | 1995-08-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4340660A (en) | Toner for development having crosslinked polymers | |
US3669885A (en) | Electrically insulating carrier particles | |
US4824753A (en) | Carrier coated with plasma-polymerized film and apparatus for preparing same | |
JP3462552B2 (en) | Powder surface modification method | |
JP2000310884A (en) | Toner, image forming method and apparatus unit | |
JPH0344649A (en) | Developer for electrophotography | |
JP3459734B2 (en) | Toner for developing electrostatic images | |
JPH06145212A (en) | Method for improving surface of powder | |
JP2536519B2 (en) | Electrophotographic developing carrier | |
US5153616A (en) | Method for recording images | |
JPH04166864A (en) | Developing device | |
JP2536518B2 (en) | Electrophotographic developing carrier | |
JPH0772655A (en) | Production of electrophotographic toner | |
JPH0458029B2 (en) | ||
JPS6114645A (en) | Forming of image | |
JPH03152552A (en) | Image forming method | |
JPH05323669A (en) | Production of electrophotographic toner | |
JPH09304974A (en) | Carrier for developing electrostatic charge image, developer and developing method | |
JPH0359563A (en) | Developer and image forming method | |
JP3582020B2 (en) | Carrier for negatively charged developer | |
JP2671251B2 (en) | Method for manufacturing electrophotographic carrier | |
JPS62257175A (en) | Coated carrier for plasma-polymerized film | |
JPS641017B2 (en) | ||
JPH05323666A (en) | Production of electrophotographic toner | |
JPH0772656A (en) | Production of electrophotograaphic toner |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20030805 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080815 Year of fee payment: 5 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090815 Year of fee payment: 6 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100815 Year of fee payment: 7 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110815 Year of fee payment: 8 |
|
LAPS | Cancellation because of no payment of annual fees |