JPH1045942A - Polymerization catalyst composition and method for producing liquid toner using the same - Google Patents
Polymerization catalyst composition and method for producing liquid toner using the sameInfo
- Publication number
- JPH1045942A JPH1045942A JP8224555A JP22455596A JPH1045942A JP H1045942 A JPH1045942 A JP H1045942A JP 8224555 A JP8224555 A JP 8224555A JP 22455596 A JP22455596 A JP 22455596A JP H1045942 A JPH1045942 A JP H1045942A
- Authority
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- Japan
- Prior art keywords
- polymerization catalyst
- catalyst composition
- polymerization
- olefin
- oligomer
- Prior art date
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Abstract
(57)【要約】
【課題】 有機過酸化物を用いて、不純物が混入しても
分解や爆発を起こしにくく、保存安定性に優れ、しかも
高い重合率が得られる重合触媒組成物を得る。
【解決手段】 有機過酸化物と少なくともα−オレフィ
ンのオリゴマーから形成する。該組成物を重合触媒と
し、重合溶媒として該α−オレフィンオリゴマーを用い
るとシャープな粒径分布を持つ液体重合トナーが得られ
る。(57) [Problem] To provide a polymerization catalyst composition using an organic peroxide, which is hardly decomposed or exploded even when impurities are mixed therein, has excellent storage stability, and can obtain a high polymerization rate. SOLUTION: It is formed from an oligomer of an organic peroxide and at least an α-olefin. When the composition is used as a polymerization catalyst and the α-olefin oligomer is used as a polymerization solvent, a liquid polymerization toner having a sharp particle size distribution can be obtained.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、有機過酸化物を含
む安全性の高い重合触媒組成物に関する。The present invention relates to a highly safe polymerization catalyst composition containing an organic peroxide.
【0002】[0002]
【従来の技術】有機過酸化物は分子中に−O−O−結合
を持ち、比較的低い温度で熱分解し、容易に遊離ラジカ
ルを発生するので、ラジカル重合におけるラジカル源、
即ち重合開始剤として使用されていることは周知であ
る。一般にこの化合物は常温で安定であり、オレフィン
やビニル系モノマーの重合及び共重合の他、不飽和ポリ
エステルの硬化にも利用されているが、火花、加熱、摩
擦、衝撃、不純物(酸又はアルカリ)の混入等により分解
又は爆発するという欠点があり、しかもこの爆発に対す
る感度はピクリン酸、TNT火薬等よりはるかに鋭敏で
ある。2. Description of the Related Art An organic peroxide has an --O--O-- bond in a molecule, and is thermally decomposed at a relatively low temperature to easily generate free radicals.
That is, it is well known that it is used as a polymerization initiator. In general, this compound is stable at room temperature, and is used for curing of unsaturated polyester in addition to polymerization and copolymerization of olefins and vinyl monomers, but sparks, heating, friction, impact, impurities (acid or alkali) Has the disadvantage that it decomposes or explodes due to the incorporation of it, and the sensitivity to this explosion is much more sensitive than that of picric acid, TNT or the like.
【0003】このように有機過酸化物は取り扱いが危険
なため、ジオクチルフタレート、ジブチルフタレート等
で希釈し、硫酸カルシウム、炭酸カルシウム、第2リン
酸カルシウム、水等の純品で希釈して使用されている。
しかし、こうして得られる重合触媒組成物においては経
時と共に過酸化物が次第に分解し、良好な重合率が得ら
れないばかりでなく、希釈剤が重合製品に残存するた
め、高純度の製品を得る場合はさらに重合製品の精製又
は乾燥を必要とした。Since the handling of organic peroxide is dangerous, it is diluted with dioctyl phthalate, dibutyl phthalate and the like, and diluted with pure products such as calcium sulfate, calcium carbonate, dibasic calcium phosphate and water. .
However, in the polymerization catalyst composition thus obtained, peroxides gradually decompose over time, and not only a good polymerization rate cannot be obtained, but also a diluent remains in the polymerization product, so that a high-purity product is obtained. Required further purification or drying of the polymerized product.
【0004】また希釈剤として、トルエン、アルコー
ル、その他溶剤などの溶解性や揮発性の良いものに過酸
化物を混合する方法も提案されているが、保存時に重合
開始剤が分解しやすく、重合率が上がらない問題や酸、
アルカリ等の不純物が混合した場合に重合開始剤が一気
に分解するなどの問題があった。As a diluent, a method has been proposed in which a peroxide is mixed with a solvent having good solubility and volatility such as toluene, alcohol, and other solvents. Problems, acidity,
When impurities such as alkalis were mixed, there was a problem that the polymerization initiator was decomposed at a stretch.
【0005】また特開平8−48710、特開平8−4
8713号公報に記載されているようなオレフィン重合
触媒は金属粉末であるために危険性が大きい。その他特
公平8−26082、特公平8−26083号公報には
過酸化ベンゾイルを希釈剤もなく使用する例が示されて
いるが、爆発、不純物、酸、アルカリの混入による引火
性など問題点は多い。Also, Japanese Patent Application Laid-Open Nos. 8-48710 and 8-4
The olefin polymerization catalyst described in JP-A-8713 is dangerous because it is a metal powder. Japanese Patent Publication Nos. Hei 8-26082 and Hei 8-26083 disclose examples in which benzoyl peroxide is used without a diluent. However, there are problems such as explosion, flammability due to mixing of impurities, acids and alkalis. Many.
【0006】[0006]
【発明が解決しようとする課題】本発明は上記のような
現状の問題点に鑑み、分解性や危険性の高い有機過酸化
物を用いて、不純物が混入しても分解や爆発を起こしに
くく、保存安定性に優れ、しかも高い重合率が得られる
重合触媒組成物を得ることを目的とする。SUMMARY OF THE INVENTION In view of the above-mentioned problems, the present invention uses an organic peroxide having a high decomposability and a high risk, and is hardly decomposed or exploded even if impurities are mixed therein. It is an object of the present invention to obtain a polymerization catalyst composition having excellent storage stability and a high conversion.
【0007】[0007]
【課題を解決するための手段】本発明によれば、第一
に、少なくとも有機過酸化物とα−オレフィンのオリゴ
マーを含有することを特徴とする重合触媒組成物が提供
される。第二に、上記第一に記載した重合触媒組成物に
おいて、α−オレフィンのオリゴマーが、炭素数5〜1
8のα−オレフィンの2〜1000量体であることを特
徴とする重合触媒組成物が提供される。第三に、上記第
一又は第二に記載した重合触媒組成物において、有機過
酸化物とα−オレフィンのオリゴマーが20〜80/8
0〜20の重量比で混合されていることを特徴とする重
合触媒組成物が提供される。第四に、上記第一〜第三の
いずれかに記載の重合触媒組成物を用い、かつ重合溶媒
としてα−オレフィンのオリゴマーを用いて、少なくと
も着色剤の存在下、ビニル系モノマーを重合又は共重合
することを特徴とする液体トナーの製造方法が提供され
る。第五に、上記第一〜第三のいずれかに記載の重合触
媒組成物を用いビニル系モノマーを重合又は共重合して
ポリマー粒子を作製し、得られたポリマー粒子を着色剤
とα−オレフィンのオリゴマーに分散することを特徴と
する液体トナーの製造方法が提供される。According to the present invention, first, there is provided a polymerization catalyst composition characterized by containing at least an oligomer of an organic peroxide and an α-olefin. Second, in the polymerization catalyst composition described in the first aspect, the α-olefin oligomer has 5 to 1 carbon atoms.
8. A polymerization catalyst composition is provided which is a 2- to 1000-mer of the α-olefin of No. 8. Third, in the polymerization catalyst composition according to the first or second aspect, the oligomer of the organic peroxide and the α-olefin is 20 to 80/8.
A polymerization catalyst composition is provided which is mixed in a weight ratio of 0 to 20. Fourth, using the polymerization catalyst composition according to any one of the above first to third, and using an α-olefin oligomer as a polymerization solvent, a vinyl monomer is polymerized or copolymerized in the presence of at least a colorant. A method for producing a liquid toner characterized by polymerizing is provided. Fifth, a polymer particle is produced by polymerizing or copolymerizing a vinyl monomer using the polymerization catalyst composition according to any of the above first to third, and the obtained polymer particle is subjected to a coloring agent and an α-olefin. A method for producing a liquid toner, characterized by being dispersed in an oligomer of
【0008】以下に本発明を詳細に説明する。上記のよ
うに本発明の重合触媒組成物は、有機過酸化物とα−オ
レフィンのオリゴマーから構成されるものであり、有機
過酸化物をα−オレフィンのオリゴマーに混合希釈する
ものである。本発明において使用されるα−オレフィン
のオリゴマーとしては、炭素数5〜18のα−オレフィ
ンで、2量体〜1000量体のものが好ましく、炭素数
9〜13で3〜100量体のものがさらに好ましい。こ
のように本発明の重合触媒組成物は、有機過酸化物を、
引火性がなく、かつ不揮発性、無臭の不活性物質である
α−オレフィンのオリゴマーに分散しているので、保存
時においても、長期間、過酸化物が分解せず、酸、アル
カリ、その他不純物の混入によっても過酸化物が分解す
ることはなく、取り扱い上も保存性を向上することがで
きる。かかる本発明の重合触媒組成物によれば、平均粒
径の小さい、シャープな粒度分布を持つ樹脂粒子やトナ
ー粒子を作ることができる。さらに、モノマーの重合率
やグラフト化率を向上することができることも分かっ
た。さらにまた、希釈剤のα−オレフィンのオリゴマー
は重合ポリマー中にも良く相溶するため、ポリマー中に
微量残っても電気抵抗の低下や強度低下を起すことはな
い。また、発泡性も少ない。Hereinafter, the present invention will be described in detail. As described above, the polymerization catalyst composition of the present invention is composed of an oligomer of an organic peroxide and an α-olefin, and the organic peroxide is mixed and diluted with the oligomer of the α-olefin. The α-olefin oligomer used in the present invention is preferably an α-olefin having 5 to 18 carbon atoms, preferably a dimer to 1000 mer, and a 3 to 100 mer having 9 to 13 carbon atoms. Is more preferred. Thus, the polymerization catalyst composition of the present invention comprises an organic peroxide,
Non-flammable, non-volatile, odorless, inert substance is dispersed in an α-olefin oligomer, so even during storage, peroxides do not decompose for a long time, and acids, alkalis, and other impurities The peroxide is not decomposed even by the incorporation of, and storage stability can be improved in handling. According to the polymerization catalyst composition of the present invention, resin particles and toner particles having a small average particle size and a sharp particle size distribution can be produced. Furthermore, it was found that the polymerization rate and the grafting rate of the monomer could be improved. Furthermore, since the α-olefin oligomer as the diluent is well compatible in the polymer, even if a small amount of the oligomer remains in the polymer, the decrease in electric resistance and the strength does not occur. In addition, the foaming properties are low.
【0009】[0009]
【発明の実施の形態】以下に本発明の実施の形態につい
て説明する。まず有機過酸化物としては、ベンゾイルパ
ーオキサイド、クメンパーオキサイド、ハイドロパーオ
キサイド、ジアシルパーオキサイド、ジアルキルパーオ
キサイド、パーオキシケタール、アルキルパーエステル
類などが挙げられる。Embodiments of the present invention will be described below. First, examples of the organic peroxide include benzoyl peroxide, cumene peroxide, hydroperoxide, diacyl peroxide, dialkyl peroxide, peroxyketal, and alkyl peresters.
【0010】α−オレフィンのオリゴマーの例として
は、以下のものが挙げられる。 (1) 1−ペンテンの10量体 (2) 2−メチル−1−ブテンの20量体 (3) 2−メチル−2−ブテンの5量体 (4) 1−ヘキセン9の100量体 (5) 2,3−ジメチル−2−ブテンの500量体 (6) 1−ヘプテンの15量体 (7) 1−オクテンの85量体 (8) 1−ノネンの1000量体 (9) 1−デセンの3量体 (10) 1−ドデシレンの5量体 (12) 1−ステアリレンの2量体Examples of the α-olefin oligomer include the following. (1) 1-pentene 10-mer (2) 2-methyl-1-butene 20-mer (3) 2-methyl-2-butene pentamer (4) 1-hexene 9 100-mer ( 5) 500-mers of 2,3-dimethyl-2-butene (6) 15-mers of 1-heptene (7) 85-mers of 1-octene (8) 1000-mers of 1-nonene (9) 1- Decene trimer (10) 1-Dodecylene pentamer (12) 1-Stearylene dimer
【0011】本発明の組成物において、有機過酸化物と
α−オレフィンのオリゴマーの混合比は、重量比で20
〜80/80〜20、好ましくは30〜70/70〜3
0が適切である。α−オレフィンのオリゴマーが20重
量部未満では有機過酸化物と均一に混合できないため保
存安定性に劣る。また酸、アルカリや不純物の混入によ
り分解が起きやすい。本発明の組成物は、乳化重合、塊
状重合、溶液重合などに適用できるが、この場合、使用
量は通常モノマーに対して0.01〜5重量部が好まし
い。。In the composition of the present invention, the mixing ratio of the organic peroxide and the α-olefin oligomer is 20% by weight.
~ 80/80 ~ 20, preferably 30 ~ 70/70 ~ 3
0 is appropriate. If the amount of the α-olefin oligomer is less than 20 parts by weight, it cannot be uniformly mixed with the organic peroxide, resulting in poor storage stability. Decomposition is likely to occur due to mixing of acids, alkalis and impurities. The composition of the present invention can be applied to emulsion polymerization, bulk polymerization, solution polymerization, and the like. In this case, the amount used is usually preferably 0.01 to 5 parts by weight based on the monomer. .
【0012】本発明の組成物を重合触媒としてトナー用
の重合粒子を作ることができるが、用いるモノマーとし
ては下記するようなトナー用として一般に用いられるも
のなら好ましく使用できる。スチレン、p−クロロスチ
レン、ビニルトルエン等のスチレン及びその置換体、ス
チレン/p−クロロスチレン、スチレン/ビニルトルエ
ン、スチレン/ビニルナフタレン、スチレン/アクリル
酸メチル、スチレン/アクリル酸エチル、スチレン/ア
クリル酸ブチル、スチレン/アクリル酸オクチル、スチ
レン/メタクリル酸メチル、スチレン/メタクリル酸エ
チル、スチレン/メタクリル酸ブチル、スチレン/α−
クロルメタクリル酸メチルなど、スチレンとその置換体
あるいはスチレンとアクリル系モノマーなどの共重合モ
ノマー。Polymerized particles for toner can be prepared by using the composition of the present invention as a polymerization catalyst. As monomers to be used, those generally used for toner as described below can be preferably used. Styrene such as styrene, p-chlorostyrene, vinyltoluene and its substituted products, styrene / p-chlorostyrene, styrene / vinyltoluene, styrene / vinylnaphthalene, styrene / methyl acrylate, styrene / ethyl acrylate, styrene / acrylic acid Butyl, styrene / octyl acrylate, styrene / methyl methacrylate, styrene / ethyl methacrylate, styrene / butyl methacrylate, styrene / α-
Copolymerized monomers such as styrene and substituted products thereof such as methyl chloromethacrylate or styrene and acrylic monomers.
【0013】殊に本発明の組成物を重合触媒とし、重合
溶媒として該α−オレフィンのオリゴマーを用い、カー
ボンボンブラックなどの着色剤の存在下で、上記したよ
うなビニル系モノマーを重合又は共重合するか、あるい
は本発明の組成物を重合触媒としてビニル系モノマーを
重合又は共重合してポリマー粒子を作製し、得られたポ
リマー粒子を着色剤と該α−オレフィンのオリゴマーに
分散することにより均一な粒径を有する液体トナーを作
製することができる。Particularly, the composition of the present invention is used as a polymerization catalyst, the α-olefin oligomer is used as a polymerization solvent, and the above-mentioned vinyl monomer is polymerized or copolymerized in the presence of a colorant such as carbon bon black. By polymerizing or polymerizing or copolymerizing a vinyl monomer using the composition of the present invention as a polymerization catalyst to prepare polymer particles, and dispersing the obtained polymer particles in a colorant and an oligomer of the α-olefin. A liquid toner having a uniform particle size can be manufactured.
【0014】[0014]
【実施例】以下に実施例により本発明をさらに具体的に
説明する。なお部はすべて重量基準である。The present invention will be described more specifically with reference to the following examples. All parts are based on weight.
【0015】〔実施例1〕下記成分を均一に混合し重合
触媒組成物Aを作製した。 〈重合触媒組成物A〉 BPO過酸化ベンゾイル 50部 15量体1−ヘプテン 50部 〈ポリマー粒子の作製〉次に1000mlの四つ口フラ
スコにイソドデカン500gをとり、80℃に加温した
中に、スチレン100g、ラウリルメタクリレート15
g、メタクリル酸5g、上記重合触媒組成物A10gを
混合し、2時間撹拌しながら滴下した。モノマー滴下
後、さらに6時間、80℃で撹拌しながら重合を行なっ
た。得られたポリマー粒子の重合率は98.9%、粒子
の平均粒径は0.50μmと小さく、粒径分布は0.1
μm以下5%、1.0μm以上10%とシャープな分布
を示した。なお撹拌による発泡は生じなかった。Example 1 A polymerization catalyst composition A was prepared by uniformly mixing the following components. <Polymerization catalyst composition A> BPO benzoyl peroxide 50 parts 15-mer 1-heptene 50 parts <Preparation of polymer particles> Next, 500 g of isododecane was placed in a 1000 ml four-necked flask and heated to 80 ° C. 100 g of styrene, lauryl methacrylate 15
g, 5 g of methacrylic acid, and 10 g of the polymerization catalyst composition A, and added dropwise with stirring for 2 hours. After the dropping of the monomer, polymerization was carried out for a further 6 hours while stirring at 80 ° C. The polymerization rate of the obtained polymer particles was 98.9%, the average particle size of the particles was as small as 0.50 μm, and the particle size distribution was 0.1%.
The distribution was sharp, 5 μm or less and 10 μm or more and 10% or less. No foaming was caused by stirring.
【0016】〔比較例1〕実施例1において、15量体
1−ヘプテンの代りにトルエンを用いた以外は実施例1
と同様にしてポリマー粒子を得た。重合率は86.2
%、粒子の平均粒径は5.4μmと大きく、沈降しやす
いものであった。Comparative Example 1 The procedure of Example 1 was repeated except that toluene was used instead of 15-mer 1-heptene.
In the same manner as in the above, polymer particles were obtained. The polymerization rate is 86.2.
%, The average particle size of the particles was as large as 5.4 μm, and the particles were easy to settle.
【0017】〔実施例2〕下記成分を均一に混合し重合
触媒組成物Bを作製した。 〈重合触媒組成物B〉 メチルエチルケトンパーオキサイド 85部 85量体1−オクテン 15部 〈ポリマー粒子の作製〉重合触媒組成物Aの代りにBを
用いた以外は実施例1と同様にして重合を行なった。得
られたポリマー粒子の重合率は92.5%、粒子の平均
粒径は1.25μm、粒径分布は0.1μm以下2%、
1.0μm以上21%であり、比較的均一な粒径分布で
あった。Example 2 A polymerization catalyst composition B was prepared by uniformly mixing the following components. <Polymerization catalyst composition B> Methyl ethyl ketone peroxide 85 parts 85mer 1-octene 15 parts <Preparation of polymer particles> Polymerization was carried out in the same manner as in Example 1 except that B was used instead of polymerization catalyst composition A. Was. The polymerization rate of the obtained polymer particles is 92.5%, the average particle size of the particles is 1.25 μm, the particle size distribution is 0.1 μm or less 2%,
It was 1.0 μm or more and 21%, and the particle size distribution was relatively uniform.
【0018】〔実施例3〕下記成分を均一に混合し重合
触媒組成物Cを作製した。 〈重合触媒組成物C〉 コハク酸パーオキサイド 15部 3量体1−デセン 85部 〈ポリマー粒子及び液体トナーの作製〉重合触媒組成物
Aの代りにCを用いた以外は実施例1と同様にして重合
を行なった。得られたポリマー粒子の重合率は95.2
%、粒子の平均粒径は0.82μm、粒径分布は0.1
μm以下8%、1.0μm以上10.5%であり、均一
な粒径分布であった。次に、このポリマー粒子をカーボ
ンブラックと5量体ドデシレンに分散し、液体トナーを
作製した。この液体トナーを用いてリコピーSP−35
(リコー製複写機)で複写を行なったところ、画像濃度
1.30、定着性85%が得られた。Example 3 A polymerization catalyst composition C was prepared by uniformly mixing the following components. <Polymerization catalyst composition C> 15 parts of succinic acid peroxide 85 parts of trimer 1-decene <Preparation of polymer particles and liquid toner> The same procedure as in Example 1 was carried out except that C was used in place of polymerization catalyst composition A. To carry out polymerization. The polymerization rate of the obtained polymer particles is 95.2.
%, The average particle size of the particles is 0.82 μm, and the particle size distribution is 0.1
The average particle size distribution was 8% or less and 1.0 μm or more and 10.5% or less. Next, the polymer particles were dispersed in carbon black and pentamer dodecylene to prepare a liquid toner. Using this liquid toner, Recopy SP-35
(Ricoh copier), image density 1.30 and fixability 85% were obtained.
【0019】〔実施例4〕 〈液体トナーの作製〉1000mlの四つ口フラスコに
4量体α−デカン500gをとり、85℃に加温した中
に、カーボンブラック50g、スチレン20g、ビニル
トルエン20g、2−エチルヘキシルメタクリレート5
0g、アクリル酸2g、分散剤(ノニオン界面活性剤)5
g、重合触媒組成物C10gを加え、均一に混合し、2
時間で滴下した。さらに4時間撹拌しながら重合し、重
合液体トナーを作製した。重合中の発泡は少なかった。
また得られたトナー粒子の平均粒子径は0.90μm
で、粒径分布は0.5〜1.3μmであり、均一な粒径
分布を持つ負帯電の液体トナーであった。次にこのトナ
ーを用いてリコピーFT−400i(リコー製複写機)で
複写したところ、画像濃度1.38、解像度6.3本/
mm、階調性7段、定着性82%と高品質の画像が得ら
れた。Example 4 <Preparation of Liquid Toner> 500 g of tetramer α-decane was placed in a 1000 ml four-necked flask, and heated to 85 ° C., and 50 g of carbon black, 20 g of styrene, and 20 g of vinyl toluene were added. , 2-ethylhexyl methacrylate 5
0 g, acrylic acid 2 g, dispersant (nonionic surfactant) 5
g, 10 g of polymerization catalyst composition C, and mix uniformly.
Dropped in time. Polymerization was further performed with stirring for 4 hours to produce a polymerized liquid toner. Foaming during polymerization was small.
The average particle size of the obtained toner particles is 0.90 μm.
The particle size distribution was 0.5 to 1.3 μm, and the liquid toner was a negatively charged liquid toner having a uniform particle size distribution. Next, using this toner, a copy was made with a Ricopy FT-400i (copier made by Ricoh Co., Ltd.).
mm, gradation of 7 steps, and fixability of 82%, a high quality image was obtained.
【0020】〔比較例2〕4量体α−デカンの代りにイ
ソドデカンを用いた以外は実施例4と同様に重合液体ト
ナーを作製した。得られたトナー粒子の平均粒子径は
5.6μmで不均一な粒子となり凝集が発生した。Comparative Example 2 A polymerized liquid toner was prepared in the same manner as in Example 4 except that isododecane was used instead of tetramer α-decane. The average particle diameter of the obtained toner particles was 5.6 μm, and the particles became non-uniform and aggregation occurred.
【0021】〈重合触媒組成物の保存性〉上記実施例で
得られた重合触媒A、B、Cは、いずれも12か月経過
後も安定しており、実施例1〜4の全てが12ヶ月後に
おいてもそのまま再現することができた。<Preservation property of polymerization catalyst composition> The polymerization catalysts A, B, and C obtained in the above Examples are all stable even after 12 months, and Even after months, it could be reproduced as it is.
【0022】[0022]
【発明の効果】以上のように、有機過酸化物とα−オレ
フィンのオリゴマーからなる本発明の重合触媒組成物に
よれば、安全性及び保存性が高く、しかも高重合率で、
粒子径の均一で小さいポリマー粒子が得られる。また、
このものは液体重合トナーを作製するのに好適である。As described above, according to the polymerization catalyst composition of the present invention comprising an oligomer of an organic peroxide and an α-olefin, the safety and the storage stability are high, and the polymerization rate is high.
Polymer particles having a uniform and small particle size can be obtained. Also,
This is suitable for producing a liquid polymerized toner.
Claims (5)
ンのオリゴマーを含有することを特徴とする重合触媒組
成物。1. A polymerization catalyst composition comprising at least an oligomer of an organic peroxide and an α-olefin.
5〜18のα−オレフィンの2〜1000量体であるこ
とを特徴とする請求項1記載の重合触媒組成物。2. The polymerization catalyst composition according to claim 1, wherein the α-olefin oligomer is a 2- to 1000-mer of an α-olefin having 5 to 18 carbon atoms.
マーが20〜80/80〜20の重量比で混合されてい
ることを特徴とする請求項1又は2記載の重合触媒組成
物。3. The polymerization catalyst composition according to claim 1, wherein the organic peroxide and the α-olefin oligomer are mixed in a weight ratio of 20 to 80/80 to 20.
媒組成物を用い、かつ重合溶媒としてα−オレフィンの
オリゴマーを用いて、着色剤の存在下、ビニル系モノマ
ーを重合又は共重合することを特徴とする液体トナーの
製造方法。4. A polymerization or copolymerization of a vinyl monomer in the presence of a colorant, using the polymerization catalyst composition according to claim 1 and an α-olefin oligomer as a polymerization solvent. A method for producing a liquid toner.
媒組成物を用い、ビニル系モノマーを重合又は共重合し
てポリマー粒子を作製し、得られたポリマー粒子を着色
剤とα−オレフィンのオリゴマーに分散することを特徴
とする液体トナーの製造方法。5. A polymer particle is produced by polymerizing or copolymerizing a vinyl monomer using the polymerization catalyst composition according to claim 1, and the obtained polymer particle is mixed with a colorant and α- A method for producing a liquid toner, comprising dispersing in an olefin oligomer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8224555A JPH1045942A (en) | 1996-08-07 | 1996-08-07 | Polymerization catalyst composition and method for producing liquid toner using the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8224555A JPH1045942A (en) | 1996-08-07 | 1996-08-07 | Polymerization catalyst composition and method for producing liquid toner using the same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH1045942A true JPH1045942A (en) | 1998-02-17 |
Family
ID=16815625
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8224555A Pending JPH1045942A (en) | 1996-08-07 | 1996-08-07 | Polymerization catalyst composition and method for producing liquid toner using the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH1045942A (en) |
-
1996
- 1996-08-07 JP JP8224555A patent/JPH1045942A/en active Pending
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