JP5057552B2 - Binder resin for electrophotographic toner - Google Patents
Binder resin for electrophotographic toner Download PDFInfo
- Publication number
- JP5057552B2 JP5057552B2 JP2006180165A JP2006180165A JP5057552B2 JP 5057552 B2 JP5057552 B2 JP 5057552B2 JP 2006180165 A JP2006180165 A JP 2006180165A JP 2006180165 A JP2006180165 A JP 2006180165A JP 5057552 B2 JP5057552 B2 JP 5057552B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- raw material
- material monomer
- toner
- addition polymerization
- 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.)
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- 239000011347 resin Substances 0.000 title claims description 133
- 229920005989 resin Polymers 0.000 title claims description 133
- 239000011230 binding agent Substances 0.000 title claims description 46
- 239000000178 monomer Substances 0.000 claims description 75
- 239000002994 raw material Substances 0.000 claims description 58
- 238000012644 addition polymerization Methods 0.000 claims description 39
- 238000012643 polycondensation polymerization Methods 0.000 claims description 32
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 14
- 229920000728 polyester Polymers 0.000 claims description 11
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 9
- 238000006068 polycondensation reaction Methods 0.000 claims description 7
- 238000006116 polymerization reaction Methods 0.000 claims description 5
- 230000000379 polymerizing effect Effects 0.000 claims description 5
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 4
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- -1 carboxylic acid compound Chemical class 0.000 description 17
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- 238000004519 manufacturing process Methods 0.000 description 11
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- 125000002947 alkylene group Chemical group 0.000 description 7
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- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 6
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- SRPWOOOHEPICQU-UHFFFAOYSA-N trimellitic anhydride Chemical compound OC(=O)C1=CC=C2C(=O)OC(=O)C2=C1 SRPWOOOHEPICQU-UHFFFAOYSA-N 0.000 description 4
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- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
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- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
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- 239000006087 Silane Coupling Agent Substances 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
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- 230000000052 comparative effect Effects 0.000 description 2
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- 239000008151 electrolyte solution Substances 0.000 description 2
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- LATKICLYWYUXCN-UHFFFAOYSA-N naphthalene-1,3,6-tricarboxylic acid Chemical compound OC(=O)C1=CC(C(O)=O)=CC2=CC(C(=O)O)=CC=C21 LATKICLYWYUXCN-UHFFFAOYSA-N 0.000 description 1
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- FJKROLUGYXJWQN-UHFFFAOYSA-N papa-hydroxy-benzoic acid Natural products OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 239000001007 phthalocyanine dye Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920000259 polyoxyethylene lauryl ether Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000012763 reinforcing filler Substances 0.000 description 1
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 1
- 229960004889 salicylic acid Drugs 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000001507 sample dispersion Methods 0.000 description 1
- 125000000467 secondary amino group Chemical group [H]N([*:1])[*:2] 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 150000003440 styrenes Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012756 surface treatment agent Substances 0.000 description 1
- 150000003512 tertiary amines Chemical class 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- AAAQKTZKLRYKHR-UHFFFAOYSA-N triphenylmethane Chemical compound C1=CC=CC=C1C(C=1C=CC=CC=1)C1=CC=CC=C1 AAAQKTZKLRYKHR-UHFFFAOYSA-N 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Developing Agents For Electrophotography (AREA)
Description
本発明は、電子写真法、静電記録法、静電印刷法等において形成される潜像の現像に用いられる電子写真トナー用結着樹脂、及び該結着樹脂を含有した電子写真用トナーに関する。 The present invention relates to a binder resin for an electrophotographic toner used for developing a latent image formed in an electrophotographic method, an electrostatic recording method, an electrostatic printing method, and the like, and an electrophotographic toner containing the binder resin. .
近年、高画質化の追求から、定着性に優れた小粒径トナーの開発が望まれている。これに対して、トナー用結着樹脂としては、スチレンアクリル樹脂やポリエステル等が知られている。ポリエステルは、耐久性及び定着性に優れる一方、オフセットが発生しやすいという欠点を有している。そこで、耐オフセット性を改善する目的で、ポリエステル等の縮重合系樹脂の原料モノマー、並びにスチレン及びアクリルモノマー等の付加重合系樹脂の原料モノマーを重合させることにより得られた樹脂を含有するトナーが開示されている(特許文献1、2参照)。
しかし、従来の結着樹脂を用いて小粒径トナーを溶融混練粉砕法で製造する場合は、粉砕制御が困難である。また、粉砕性を高めるために結着樹脂の分子量を下げるとオフセットが問題となる。 However, when a small particle toner is manufactured by a melt kneading pulverization method using a conventional binder resin, it is difficult to control the pulverization. Further, if the molecular weight of the binder resin is lowered in order to improve the pulverization property, offset becomes a problem.
本発明の課題は、粉砕性が良好で、耐オフセット性に優れた電子写真トナー用結着樹脂、及びかかる結着樹脂を含有したトナーを提供することにある。 An object of the present invention is to provide a binder resin for an electrophotographic toner having good crushability and excellent offset resistance, and a toner containing such a binder resin.
本発明は、
〔1〕 少なくとも縮重合系樹脂の原料モノマー及び付加重合系樹脂の原料モノマーを重合させることにより得られる電子写真トナー用結着樹脂であって、前記付加重合系樹脂の原料モノマーが、スチレンを90重量%以上含有してなる、電子写真トナー用結着樹脂、及び
〔2〕 前記〔1〕記載の電子写真トナー用結着樹脂を含有してなる電子写真用トナー
に関する。
The present invention
[1] A binder resin for an electrophotographic toner obtained by polymerizing at least a raw material monomer of a condensation polymerization resin and a raw material monomer of an addition polymerization resin, wherein the raw material monomer of the addition polymerization resin is styrene. The present invention relates to a binder resin for electrophotographic toners containing at least wt%, and [2] an electrophotographic toner containing the binder resin for electrophotographic toners described in [1] above.
本発明の電子写真トナー用結着樹脂は、粉砕性が良好で、該結着樹脂を含有したトナーはオフセットの発生が抑制されるという優れた効果を奏することができる。 The binder resin for an electrophotographic toner of the present invention has an excellent effect that the pulverizability is good, and the toner containing the binder resin can suppress the occurrence of offset.
本発明の電子写真トナー用結着樹脂は、少なくとも縮重合系樹脂の原料モノマー及び付加重合系樹脂の原料モノマーを重合させることにより得られる電子写真トナー用結着樹脂であって、前記付加重合系樹脂が、スチレンを90重量%以上含有している点に大きな特徴を有する。即ち、付加重合系樹脂の原料モノマーとして、主成分としてスチレンを使用することで、耐オフセット性を維持したまま粉砕性を向上できるという驚くべき効果を奏することが判明した。 The binder resin for an electrophotographic toner of the present invention is a binder resin for an electrophotographic toner obtained by polymerizing at least a raw material monomer of a condensation polymerization resin and a raw material monomer of an addition polymerization resin, the addition polymerization system The resin has a great feature in that it contains 90% by weight or more of styrene. That is, it has been found that the use of styrene as the main component monomer of the addition polymerization resin has the surprising effect that the grindability can be improved while maintaining the offset resistance.
本発明の結着樹脂は、少なくとも縮重合系樹脂の原料モノマー及び付加重合系樹脂の原料モノマーを用いて、縮重合反応と付加重合反応を同一反応容器中で並行して行うことにより得られる樹脂が好ましい。縮重合反応と付加重合反応の進行及び完結は、時間的に同時である必要はなく、それぞれの反応機構に応じて反応温度及び時間を適当に選択し、反応を進行、完結させればよい。縮重合反応及び付加重合反応について、以下に詳述する。 The binder resin of the present invention is a resin obtained by performing a condensation polymerization reaction and an addition polymerization reaction in parallel in the same reaction vessel using at least a raw material monomer of a condensation polymerization resin and a raw material monomer of an addition polymerization resin. Is preferred. The progress and completion of the polycondensation reaction and the addition polymerization reaction do not need to be simultaneous in time, and the reaction temperature and time may be appropriately selected according to each reaction mechanism to advance and complete the reaction. The condensation polymerization reaction and the addition polymerization reaction will be described in detail below.
縮重合反応により得られる縮重合系樹脂成分としては、トナーの定着性の観点から、アルコール成分及びカルボン酸成分を縮重合させて得られるポリエステル、アルコール成分、カルボン酸成分及びアミド成分を形成するための原料モノマーを縮重合させて得られるポリエステル・ポリアミド、並びにカルボン酸成分及びアミド成分を形成するための原料モノマーを縮重合させて得られるポリアミドからなる群より選ばれた少なくとも1種であることが好ましく、これらの中ではポリエステルがより好ましい。 As the condensation polymerization resin component obtained by the condensation polymerization reaction, in order to form a polyester, an alcohol component, a carboxylic acid component, and an amide component obtained by condensation polymerization of an alcohol component and a carboxylic acid component from the viewpoint of toner fixing properties. It is at least one selected from the group consisting of a polyester / polyamide obtained by polycondensation of the raw material monomers and a polyamide obtained by polycondensation of the raw material monomers for forming the carboxylic acid component and the amide component. Among these, polyester is more preferable.
ポリエステルは、特に限定されないが、2価以上のアルコールからなるアルコール成分と、2価以上のカルボン酸化合物からなるカルボン酸成分を含む原料モノマーを縮重合させて得られる。 The polyester is not particularly limited, and can be obtained by polycondensing a raw material monomer containing an alcohol component composed of a divalent or higher alcohol and a carboxylic acid component composed of a divalent or higher carboxylic acid compound.
2価以上のアルコールとしては、トナーの保存安定性の観点から、式(I): As the dihydric or higher alcohol, from the viewpoint of storage stability of the toner, the formula (I):
(式中、ROはアルキレンオキサイドであり、Rは炭素数2又は3のアルキレン基、x及びyはアルキレンオキサイドの平均付加モル数を示す正の数であり、xとyの和は1〜16、好ましくは1〜10、より好ましくは1.5〜5である)
で表されるビスフェノールAのアルキレンオキサイド付加物が好ましい。かかるビスフェノールAのアルキレンオキサイド付加物の含有量は、アルコール成分中、50重量%以上が好ましく、60重量%以上がより好ましく、80重量%以上がさらに好ましい。
(In the formula, RO is an alkylene oxide, R is an alkylene group having 2 or 3 carbon atoms, x and y are positive numbers indicating the average added mole number of alkylene oxide, and the sum of x and y is 1 to 16) , Preferably 1-10, more preferably 1.5-5)
An alkylene oxide adduct of bisphenol A represented by The content of the alkylene oxide adduct of bisphenol A is preferably 50% by weight or more, more preferably 60% by weight or more, and still more preferably 80% by weight or more in the alcohol component.
式(I)で表されるビスフェノールAのアルキレンオキサイド付加物としては、ポリオキシエチレン-2,2-ビス(4-ヒドロキシフェニル)プロパン等のRが炭素数2のエチレンオキサイド付加物、ポリオキシプロピレン-2,2-ビス(4-ヒドロキシフェニル)プロパン等のRが炭素数3のプロピレンオキサイド付加物等が挙げられる。 Examples of the alkylene oxide adduct of bisphenol A represented by the formula (I) include polyoxyethylene-2,2-bis (4-hydroxyphenyl) propane and other ethylene oxide adducts having 2 carbon atoms, such as polyoxypropylene Examples thereof include propylene oxide adducts having 3 carbon atoms such as -2,2-bis (4-hydroxyphenyl) propane.
ビスフェノールAのアルキレンオキサイド付加物以外のアルコール成分としては、エチレングリコール、1,2-プロピレングリコール、1,4-ブタンジオール、ネオペンチルグリコール、ポリエチレングリコール、ポリプロピレングリコール、ビスフェノールA、水素添加ビスフェノールA、ソルビトール、ペンタエリスリトール、グリセロール、トリメチロールプロパン等が挙げられる。 The alcohol components other than the alkylene oxide adduct of bisphenol A include ethylene glycol, 1,2-propylene glycol, 1,4-butanediol, neopentyl glycol, polyethylene glycol, polypropylene glycol, bisphenol A, hydrogenated bisphenol A, and sorbitol. , Pentaerythritol, glycerol, trimethylolpropane and the like.
また、2価以上のカルボン酸化合物としては、例えば、アジピン酸、フマル酸、マレイン酸、コハク酸(例えば、n-ドデセニルコハク酸、イソドデセニルコハク酸、n-ドデシルコハク酸、イソオクテニルコハク酸、イソオクチルコハク酸等の炭素数1〜20のアルキル基または炭素数2〜20のアルケニル基で置換されたコハク酸)等の脂肪族カルボン酸、フタル酸、イソフタル酸、テレフタル酸、1,2,4-ベンゼントリカルボン酸(トリメリット酸)、2,5,7-ナフタレントリカルボン酸、ピロメリット酸等の芳香族カルボン酸、並びにこれらの酸の無水物及び低級アルキル(炭素数1〜3)エステル等が挙げられる。上記のような酸、これらの酸の無水物、及び酸のアルキルエステルを、本明細書では総称してカルボン酸化合物と呼ぶ。これらの中では、トナーの粉砕性と保存性の観点から、カルボン酸成分の50重量%以上がフタル酸、テレフタル酸であることが好ましく、テレフタル酸であることがより好ましい。 Examples of the divalent or higher carboxylic acid compound include adipic acid, fumaric acid, maleic acid, succinic acid (for example, n-dodecenyl succinic acid, isododecenyl succinic acid, n-dodecyl succinic acid, isooctenyl succinic acid, Aliphatic carboxylic acids such as isooctyl succinic acid and the like, succinic acid substituted with alkyl groups having 1 to 20 carbon atoms or alkenyl groups having 2 to 20 carbon atoms, phthalic acid, isophthalic acid, terephthalic acid, 1,2, 4-Benzenetricarboxylic acid (trimellitic acid), 2,5,7-naphthalenetricarboxylic acid, aromatic carboxylic acids such as pyromellitic acid, anhydrides of these acids and lower alkyl (C1-3) esters, etc. Is mentioned. Such acids, anhydrides of these acids, and alkyl esters of these acids are collectively referred to herein as carboxylic acid compounds. Among these, from the viewpoint of pulverization and storage stability of the toner, 50% by weight or more of the carboxylic acid component is preferably phthalic acid or terephthalic acid, and more preferably terephthalic acid.
また、ポリエステルは、軟化点と粉砕性の観点から、アルコール成分及び/又はカルボン酸成分として3価以上のモノマーを用いて得られた架橋ポリエステルであることが好ましい。3価以上のモノマーの含有量は、アルコール成分及びカルボン酸成分の総量中、2〜20モル%が好ましく、4〜18モル%がより好ましい。3価以上のモノマーとしては、1,2,4-ベンゼントリカルボン酸(トリメリット酸)及びその無水物が好ましい。 The polyester is preferably a crosslinked polyester obtained using a trivalent or higher monomer as the alcohol component and / or carboxylic acid component from the viewpoint of the softening point and grindability. The content of the trivalent or higher monomer is preferably 2 to 20 mol%, more preferably 4 to 18 mol% in the total amount of the alcohol component and the carboxylic acid component. As the trivalent or higher monomer, 1,2,4-benzenetricarboxylic acid (trimellitic acid) and its anhydride are preferable.
なお、アルコール成分には1価のアルコールが、カルボン酸成分には1価のカルボン酸化合物が、分子量調整や耐オフセット性向上の観点から、適宜含有されていてもよい。 The alcohol component may contain a monovalent alcohol, and the carboxylic acid component may contain a monovalent carboxylic acid compound as appropriate from the viewpoints of molecular weight adjustment and offset resistance improvement.
アルコール成分とカルボン酸成分との縮重合は、例えば、不活性ガス雰囲気中にて、要すればエステル化触媒を用いて、180〜250℃の温度で行うことができる。 The polycondensation of the alcohol component and the carboxylic acid component can be performed, for example, in an inert gas atmosphere at a temperature of 180 to 250 ° C. using an esterification catalyst if necessary.
また、ポリエステル・ポリアミドは、前記のアルコール成分及びカルボン酸成分に加えてアミド成分を形成するための原料モノマーを用い、これらの原料モノマーを縮重合させて得られ、ポリアミドは、前記のカルボン酸成分に加えてアミド成分を形成するための原料モノマーを用い、これらの原料モノマーを縮重合させて得られる。 The polyester / polyamide is obtained by using a raw material monomer for forming an amide component in addition to the alcohol component and the carboxylic acid component, and polycondensing these raw material monomers. The polyamide is obtained by using the carboxylic acid component described above. In addition to the above, a raw material monomer for forming an amide component is used, and these raw material monomers are subjected to condensation polymerization.
アミド成分を形成するために用いる原料モノマーとしては、公知の各種ポリアミン、アミノカルボン酸類、アミノアルコール等が挙げられ、好ましくはヘキサメチレンジアミン及びε-カプロラクタムである。 Examples of the raw material monomer used to form the amide component include various known polyamines, aminocarboxylic acids, aminoalcohols, etc., preferably hexamethylenediamine and ε-caprolactam.
なお、以上の原料モノマーには、通常開環重合モノマーに分類されるものも含まれているが、これらは、他のモノマーの縮重合反応で生成する水等の存在により加水分解して縮重合に供されるため、広義には縮重合系樹脂の原料モノマーに含まれると考えられる。 The above raw material monomers also include those normally classified as ring-opening polymerization monomers, but these are hydrolyzed by condensation due to the presence of water or the like produced by the condensation polymerization reaction of other monomers. Therefore, it is considered to be included in the raw material monomer of the condensation polymerization resin in a broad sense.
一方、付加重合反応に用いられる付加重合系樹脂の原料モノマーとしては、スチレン、α-メチルスチレン等のスチレン化合物;エチレン、プロピレン等のエチレン性不飽和モノオレフィン類;ブタジエン等のジオレフィン類;塩化ビニル等のハロビニル類;酢酸ビニル、プロピオン酸ビニル等のビニルエステル類;(メタ)アクリル酸のアルキル(炭素数1〜18)エステル、(メタ)アクリル酸ジメチルアミノエチル等のエチレン性モノカルボン酸のエステル;ビニルメチルエーテル等のビニルエーテル類;ビニリデンクロリド等のビニリデンハロゲン化物;N-ビニルピロリドン等のN-ビニル化合物類等が挙げられるが、これらの中では、本発明では、結着樹脂及びトナーの粉砕性の観点から、少なくともスチレンを用いる。スチレンの含有量は、付加重合系樹脂の原料モノマー中、90重量%以上であり、好ましくは95重量%以上であり、より好ましくは98重量%以上であり、さらに好ましくは実質的に100重量%である。 On the other hand, raw material monomers for addition polymerization resins used in addition polymerization reactions include styrene compounds such as styrene and α-methylstyrene; ethylenically unsaturated monoolefins such as ethylene and propylene; diolefins such as butadiene; Halovinyls such as vinyl; vinyl esters such as vinyl acetate and vinyl propionate; alkyl (carbon number 1 to 18) esters of (meth) acrylic acid, ethylenic monocarboxylic acids such as dimethylaminoethyl (meth) acrylate Examples include esters; vinyl ethers such as vinyl methyl ether; vinylidene halides such as vinylidene chloride; N-vinyl compounds such as N-vinylpyrrolidone. Among these, the present invention includes binder resins and toners. From the viewpoint of grindability, at least styrene is used. The content of styrene in the raw material monomer of the addition polymerization resin is 90% by weight or more, preferably 95% by weight or more, more preferably 98% by weight or more, and further preferably substantially 100% by weight. It is.
なお、付加重合系樹脂の原料モノマーの付加重合には、重合開始剤、架橋剤等を必要に応じて使用してもよい。 In addition, a polymerization initiator, a crosslinking agent, or the like may be used as necessary for the addition polymerization of the raw material monomer of the addition polymerization resin.
付加重合反応は、例えば、重合開始剤、架橋剤等の存在下、有機溶媒存在下又は無溶媒下で、常法により行うことができるが、例えば、温度条件は、好ましくは110〜200℃、より好ましくは140〜170℃である。 The addition polymerization reaction can be performed by a conventional method, for example, in the presence of a polymerization initiator, a crosslinking agent, or the like, in the presence of an organic solvent or in the absence of a solvent. For example, the temperature condition is preferably 110 to 200 ° C., More preferably, it is 140-170 degreeC.
付加重合反応の際に用いられる有機溶媒としては、キシレン、トルエン、メチルエチルケトン、アセトン等が挙げられる。有機溶媒の使用量は、付加重合系樹脂の原料モノマー100重量部に対して、10〜50重量部程度が好ましい。 Examples of the organic solvent used in the addition polymerization reaction include xylene, toluene, methyl ethyl ketone, and acetone. The amount of the organic solvent used is preferably about 10 to 50 parts by weight with respect to 100 parts by weight of the raw material monomer of the addition polymerization resin.
本発明の結着樹脂は、トナー中の離型剤等の添加剤の分散性を向上させる観点から、縮重合系樹脂の原料モノマーと付加重合系樹脂の原料モノマーに加えて、さらに縮重合系樹脂の原料モノマー及び付加重合系樹脂の原料モノマーのいずれとも反応し得る化合物(両反応性モノマー)を用いて得られる樹脂(ハイブリッド樹脂)であることが好ましい。従って、本発明において、縮重合反応と付加重合反応は、両反応性モノマーの存在下で行うことが好ましく、これにより、ハイブリッド樹脂は、縮重合系樹脂成分と付加重合系樹脂成分とが部分的に両反応性モノマーを介して結合し、縮重合系樹脂成分中に付加重合系樹脂成分がより微細に、かつ均一に分散している。 The binder resin of the present invention is a polycondensation system in addition to the condensation polymerization resin raw material monomer and the addition polymerization resin raw material monomer from the viewpoint of improving the dispersibility of additives such as a release agent in the toner. A resin (hybrid resin) obtained using a compound capable of reacting with both the raw material monomer of the resin and the raw material monomer of the addition polymerization resin (both reactive monomers) is preferable. Therefore, in the present invention, the condensation polymerization reaction and the addition polymerization reaction are preferably carried out in the presence of both reactive monomers. As a result, the hybrid resin has a partial condensation polymerization resin component and addition polymerization resin component. The addition polymerization resin component is more finely and uniformly dispersed in the condensation polymerization resin component.
両反応性モノマーとしては、分子内に、水酸基、カルボキシル基、エポキシ基、第1級アミノ基及び第2級アミノ基からなる群より選ばれた少なくとも1種の官能基、好ましくは水酸基及び/又はカルボキシル基、より好ましくはカルボキシル基と、エチレン性不飽和結合とを有する化合物が好ましく、このような両反応性モノマーを用いることにより、分散相となる樹脂の分散性をより一層向上させることができる。両反応性モノマーは、アクリル酸、メタクリル酸、フマル酸、マレイン酸及び無水マレイン酸からなる群より選ばれた少なくとも1種であることが好ましいが、反応性の観点から、アクリル酸、メタクリル酸及びフマル酸がより好ましい。 As the both reactive monomers, in the molecule, at least one functional group selected from the group consisting of a hydroxyl group, a carboxyl group, an epoxy group, a primary amino group and a secondary amino group, preferably a hydroxyl group and / or A compound having a carboxyl group, more preferably a carboxyl group, and an ethylenically unsaturated bond is preferred. By using such a bireactive monomer, the dispersibility of the resin that becomes the dispersed phase can be further improved. . Both reactive monomers are preferably at least one selected from the group consisting of acrylic acid, methacrylic acid, fumaric acid, maleic acid and maleic anhydride, but from the viewpoint of reactivity, acrylic acid, methacrylic acid and Fumaric acid is more preferred.
本発明において、両反応性モノマーは、縮重合系樹脂の原料モノマーとして扱う。両反応性モノマーの使用量は、縮重合系樹脂の原料モノマーであるカルボン酸成分中、1〜20重量%が好ましく、5〜15重量%がより好ましい。 In the present invention, the both reactive monomers are handled as raw material monomers for the condensation polymerization resin. The amount of the both reactive monomers used is preferably 1 to 20% by weight, more preferably 5 to 15% by weight in the carboxylic acid component which is a raw material monomer for the condensation polymerization resin.
本発明においては、縮重合系樹脂の付加重合系樹脂に対する重量比、即ち縮重合系樹脂の原料モノマーの付加重合系樹脂の原料モノマーに対する重量比(縮重合系樹脂の原料モノマー/付加重合系樹脂の原料モノマー)は、連続相が縮重合系樹脂であり、分散相が付加重合系樹脂であることが好ましいことから、55/45〜95/5が好ましく、60/40〜95/5がより好ましく、70/30〜90/10がさらに好ましい。 In the present invention, the weight ratio of the condensation polymerization resin to the addition polymerization resin, that is, the weight ratio of the condensation polymerization resin raw material monomer to the addition polymerization resin raw material monomer (condensation polymerization resin raw material monomer / addition polymerization resin). The raw material monomer) is preferably 55/45 to 95/5, more preferably 60/40 to 95/5, since the continuous phase is preferably a condensation polymerization resin and the dispersed phase is an addition polymerization resin. 70/30 to 90/10 is more preferable.
定着性を向上させる観点からは、本発明のトナーには離型剤を含有させることが好ましく、ワックスの分散性を向上させる観点からは、本発明の結着樹脂は、ワックスの存在下で縮重合系樹脂の原料モノマー及びスチレンを含む付加重合系樹脂の原料モノマーを重合させることにより得られる樹脂が好ましい。 From the viewpoint of improving the fixability, the toner of the present invention preferably contains a release agent. From the viewpoint of improving the dispersibility of the wax, the binder resin of the present invention is shrunk in the presence of the wax. A resin obtained by polymerizing a raw material monomer of a polymerization resin and a raw material monomer of an addition polymerization resin containing styrene is preferable.
ワックスとしては、低分子量ポリプロピレン、低分子量ポリエチレン、低分子量ポリプロピレンポリエチレン共重合体、マイクロクリスタリンワックス、パラフィンワックス、フィッシャートロプシュワックス等の脂肪族炭化水素系ワックス及びそれらの酸化物、カルナウバワックス、モンタンワックス、サゾールワックス及びそれらの脱酸ワックス等のエステル系ワックス、脂肪酸アミド類、脂肪酸類、高級アルコール類、脂肪酸金属塩等が挙げられ、これらのなかでは、離型性及び安定性の観点から、脂肪族炭化水素系ワックスが好ましい。 Examples of the wax include aliphatic hydrocarbon waxes such as low molecular weight polypropylene, low molecular weight polyethylene, low molecular weight polypropylene polyethylene copolymer, microcrystalline wax, paraffin wax, and Fischer-Tropsch wax, and oxides thereof, carnauba wax, and montan wax. , Ester waxes such as sazol wax and their deoxidized wax, fatty acid amides, fatty acids, higher alcohols, fatty acid metal salts, etc., among these, from the viewpoint of releasability and stability, Aliphatic hydrocarbon waxes are preferred.
ワックスの添加量は、結着樹脂の製造に用いられる原料モノマーの総量100重量部に対して、20重量部以下が好ましく、10重量部以下がより好ましい。 The amount of the wax added is preferably 20 parts by weight or less, and more preferably 10 parts by weight or less with respect to 100 parts by weight of the total amount of raw material monomers used in the production of the binder resin.
ワックスの添加時期は特に限定されず、重合開始当初であっても、重合反応途中であってもよい。 The addition timing of the wax is not particularly limited, and may be at the beginning of the polymerization or in the middle of the polymerization reaction.
本発明の結着樹脂の軟化点は、低温定着性、定着可能領域及び保存性の観点から、好ましくは70〜170℃、より好ましくは80〜150℃、さらに好ましくは80〜140℃、さらに好ましくは90〜130℃である。本明細書において、軟化点は、後述の実施例に記載の方法により測定される。 The softening point of the binder resin of the present invention is preferably from 70 to 170 ° C., more preferably from 80 to 150 ° C., further preferably from 80 to 140 ° C., more preferably from the viewpoints of low-temperature fixability, fixable area, and storage stability. Is 90-130 ° C. In the present specification, the softening point is measured by the method described in Examples described later.
本発明の結着樹脂は粉砕性に優れ、かかる結着樹脂を用いて耐オフセット性に優れたトナーが得られる。従って、本発明では、さらに、本発明の結着樹脂を含有したトナーを提供する。 The binder resin of the present invention is excellent in grindability, and a toner excellent in offset resistance can be obtained using such a binder resin. Therefore, the present invention further provides a toner containing the binder resin of the present invention.
本発明のトナーは2種類以上の結着樹脂を含有していても良い。その場合、少なくとも1種が本発明の結着樹脂であれば良いが、全てが、本発明の結着樹脂であることが好ましい。本発明の結着樹脂は、ワックスの分散性の観点から、結着樹脂中、40〜100重量%、好ましくは70〜100重量%、より好ましくは90〜100重量%、さらに好ましくは実質的に100%含有されることが望ましい。他の結着樹脂としては、エポキシ樹脂、ポリカーボネート、ポリウレタン、スチレン−アクリル樹脂等が挙げられ、本発明の効果を損なわない範囲で含有されていてもよい。 The toner of the present invention may contain two or more kinds of binder resins. In that case, at least one kind may be the binding resin of the present invention, but all are preferably the binding resin of the present invention. The binder resin of the present invention is 40 to 100% by weight, preferably 70 to 100% by weight, more preferably 90 to 100% by weight, and still more preferably substantially from the viewpoint of dispersibility of the wax. It is desirable to contain 100%. Examples of other binder resins include epoxy resins, polycarbonates, polyurethanes, styrene-acrylic resins, and the like, and they may be contained within a range that does not impair the effects of the present invention.
本発明のトナーは、結着樹脂以外に、着色剤、離型剤、荷電制御剤、磁性粉、導電性調整剤、体質顔料、繊維状物質等の補強充填剤、酸化防止剤、老化防止剤、流動性向上剤、クリーニング性向上剤等の添加剤が、適宜含有されていてもよい。 In addition to the binder resin, the toner of the present invention includes a colorant, a release agent, a charge control agent, a magnetic powder, a conductivity regulator, an extender pigment, a reinforcing filler such as a fibrous substance, an antioxidant, and an anti-aging agent. In addition, additives such as a fluidity improver and a cleaning property improver may be appropriately contained.
着色剤としては、トナー用着色剤として用いられている染料、顔料等を使用することができ、カーボンブラック、フタロシアニンブルー、パーマネントブラウンFG、ブリリアントファーストスカーレット、ピグメントグリーンB、ローダミン-Bベース、ソルベントレッド49、ソルベントレッド146、ソルベントブルー35、キナクリドン、カーミン6B、ジスアゾエロー等が挙げられ、これらは単独で又は2種以上を混合して用いることができ、本発明のトナーは、黒トナー、カラートナー、フルカラートナーのいずれであってもよい。着色剤の含有量は、結着樹脂100重量部に対して、1〜40重量部が好ましく、2〜10重量部がより好ましい。 As the colorant, dyes and pigments used as toner colorants can be used. Carbon black, phthalocyanine blue, permanent brown FG, brilliant first scarlet, pigment green B, rhodamine-B base, solvent red 49, Solvent Red 146, Solvent Blue 35, Quinacridone, Carmine 6B, Disazo Yellow, etc., and these can be used alone or in admixture of two or more. The toner of the present invention includes black toner, color toner, Any of full-color toners may be used. The content of the colorant is preferably 1 to 40 parts by weight and more preferably 2 to 10 parts by weight with respect to 100 parts by weight of the binder resin.
離型剤としては、前述したワックスが同様に挙げられる。これらのなかでは、離型性及び安定性の観点から、脂肪族炭化水素系ワックス及びエステル系ワックスが好ましく、これらは単独で又は2種以上を混合して含有されていても良い。離型剤の含有量は、結着樹脂100重量部に対して、0.5〜10重量部が好ましく、1〜5重量部がより好ましい。離型剤は分散性向上の観点から、結着樹脂製造時に樹脂の原料モノマーと共に用いられ、結着樹脂に内添されていてもよい。 As the mold release agent, the above-mentioned wax can be exemplified. Among these, aliphatic hydrocarbon waxes and ester waxes are preferable from the viewpoint of releasability and stability, and these may be contained alone or in admixture of two or more. The content of the release agent is preferably 0.5 to 10 parts by weight and more preferably 1 to 5 parts by weight with respect to 100 parts by weight of the binder resin. From the viewpoint of improving dispersibility, the release agent may be used together with the resin raw material monomer during the production of the binder resin, and may be internally added to the binder resin.
荷電制御剤としては、ニグロシン染料、3級アミンを側鎖として含有するトリフェニルメタン系染料、4級アンモニウム塩化合物、ポリアミン樹脂、イミダゾール誘導体等の正帯電性荷電制御剤及び含金属アゾ染料、銅フタロシアニン染料、サリチル酸のアルキル誘導体の金属錯体、ベンジル酸のホウ素錯体等の負帯電性荷電制御剤が挙げられる。 Charge control agents include nigrosine dyes, triphenylmethane dyes containing tertiary amines as side chains, quaternary ammonium salt compounds, polyamine resins, imidazole derivatives and other positively chargeable charge control agents and metal-containing azo dyes, copper Examples include negatively chargeable charge control agents such as phthalocyanine dyes, metal complexes of alkyl derivatives of salicylic acid, and boron complexes of benzylic acid.
荷電制御剤の含有量は、結着樹脂100重量部に対して、0.1〜5重量部が好ましく、0.5〜2重量部がより好ましい。 The content of the charge control agent is preferably 0.1 to 5 parts by weight and more preferably 0.5 to 2 parts by weight with respect to 100 parts by weight of the binder resin.
磁性粉としては、コバルト、鉄、ニッケル等の強磁性体、コバルト、鉄、ニッケル、アルミニウム、鉛、マグネシウム、亜鉛、マンガン等の金属の合金、Fe3O4、γ-Fe3O4、コバルト添加酸化鉄等の金属酸化物、Mn-Znフェライト、Ni-Znフェライト等の各種フェライト、マグネタイト、ヘマタイト等を1種又は2種以上を併せて使用することができる。さらに、これら磁性分の表面がシランカップリング剤、チタネートシランカップリング剤等の表面処理剤で処理されたもの、又はポリマーコーティングされたものであってもよい。 Magnetic powder includes ferromagnetic materials such as cobalt, iron and nickel, alloys of metals such as cobalt, iron, nickel, aluminum, lead, magnesium, zinc and manganese, Fe 3 O 4 , γ-Fe 3 O 4 and cobalt Metal oxides such as added iron oxide, various ferrites such as Mn—Zn ferrite and Ni—Zn ferrite, magnetite, hematite and the like can be used alone or in combination. Furthermore, the surface of these magnetic components may be treated with a surface treatment agent such as a silane coupling agent or a titanate silane coupling agent, or may be polymer-coated.
本発明のトナーが磁性トナーである場合には、磁性粉の含有量は、結着樹脂100重量部に対して、磁性粉の分散性及び帯電の環境性の観点から10〜90重量部が好ましく、20〜80重量部がより好ましく、30〜70重量部がさらに好ましい。また、色目や帯電量の調整のために、カーボンブラックやフタロシアニンブルー等公知の着色剤を併用してもよい。 When the toner of the present invention is a magnetic toner, the content of the magnetic powder is preferably 10 to 90 parts by weight with respect to 100 parts by weight of the binder resin from the viewpoint of the dispersibility of the magnetic powder and the charging environment. 20 to 80 parts by weight is more preferable, and 30 to 70 parts by weight is more preferable. Further, a known colorant such as carbon black or phthalocyanine blue may be used in combination for adjusting the color and the charge amount.
本発明のトナーは、混練粉砕法、スプレイドライ法、重合法等の公知の方法により製造することができるが、結着樹脂は粉砕性に優れるため、混練粉砕法により得られる粉砕トナーが好ましい。混練粉砕法の一般的な方法としては、例えば、結着樹脂、並びに、離型剤、荷電制御剤、磁性粉等の添加剤等をヘンシェルミキサー、ボールミル等の混合機で均一に混合した後、密閉式ニーダー又は1軸もしくは2軸の押出機等で溶融混練し、冷却、粉砕、分級する方法が挙げられる。さらに、製造過程における粗粉砕物や、得られたトナーの表面に、必要に応じて疎水性シリカ等の流動性向上剤等を添加してもよい。本発明のトナーの体積中位粒径(D50)は、3〜15μmが好ましく、4〜8μmがより好ましい。本発明において、体積中位粒径(D50)とは、体積分率で計算した累積体積頻度が粒径の小さい方から計算して50%になる粒径を意味する。 The toner of the present invention can be produced by a known method such as a kneading and pulverizing method, a spray drying method, or a polymerization method. However, since the binder resin is excellent in pulverizing properties, a pulverized toner obtained by a kneading and pulverizing method is preferable. As a general method of the kneading and pulverization method, for example, a binder resin, and a release agent, a charge control agent, an additive such as magnetic powder, and the like are uniformly mixed with a mixer such as a Henschel mixer and a ball mill, Examples of the method include melt kneading with a closed kneader or a single or twin screw extruder, cooling, pulverizing, and classification. Furthermore, a fluidity improver such as hydrophobic silica may be added to the coarsely pulverized product in the production process or the surface of the obtained toner, if necessary. The volume median particle size (D 50 ) of the toner of the present invention is preferably 3 to 15 μm, more preferably 4 to 8 μm. In the present invention, the volume-median particle size (D 50 ) means a particle size at which the cumulative volume frequency calculated by the volume fraction is 50% when calculated from the smaller particle size.
本発明のトナーは、単独で現像剤として、またはキャリアと混合して二成分系の現像剤として用いることができるが、トナーの添加剤の分散性が良好である観点から、磁性粉を含有する磁性一成分現像用トナーとして好適に用いることができる。また、本発明のトナーは、好ましくは線速200mm/sec(A4用紙40枚/分)以上の、より好ましくは250〜350mm/secの高速機に好適に使用することができる。 The toner of the present invention can be used alone as a developer or mixed with a carrier as a two-component developer, but contains magnetic powder from the viewpoint of good dispersibility of the toner additive. It can be suitably used as a magnetic one-component developing toner. Further, the toner of the present invention can be suitably used for a high-speed machine having a linear speed of 200 mm / sec (A4 paper 40 sheets / min) or more, more preferably 250 to 350 mm / sec.
〔樹脂の軟化点〕
フローテスター(島津製作所、CFT-500D)を用い、1gの試料を昇温速度6℃/分で加熱しながら、プランジャーにより1.96MPaの荷重を与え、直径1mm、長さ1mmのノズルから押出した。温度に対し、フローテスターのプランジャー降下量をプロットし、試料の半量が流出した温度を軟化点とする。
[Softening point of resin]
Using a flow tester (Shimadzu Corporation, CFT-500D), a 1 g sample was heated at a heating rate of 6 ° C / min, and a load of 1.96 MPa was applied by a plunger and extruded from a nozzle with a diameter of 1 mm and a length of 1 mm. . The amount of plunger drop of the flow tester is plotted against the temperature, and the temperature at which half of the sample flows out is taken as the softening point.
〔離型剤の融点〕
示差走査熱量計(セイコー電子工業社製、DSC210)を用いて200℃まで昇温し、その温度から降温速度10℃/分で0℃まで冷却したサンプルを昇温速度10℃/分で昇温し、融解熱の最大ピーク温度を融点とする。
[Melting point of release agent]
Using a differential scanning calorimeter (Seiko Denshi Kogyo Co., Ltd., DSC210), the temperature was raised to 200 ° C, and the sample was cooled to 0 ° C at a temperature drop rate of 10 ° C / min. The maximum peak temperature of heat of fusion is taken as the melting point.
〔トナーの体積中位粒径(D50)〕
測定機:コールターマルチサイザーII(ベックマンコールター社製)
アパチャー径:100μm
解析ソフト:コールターマルチサイザーアキュコンプ バージョン 1.19(ベックマンコールター社製)
電解液:アイソトンII(ベックマンコールター社製)
分散液:エマルゲン109P(花王社製、ポリオキシエチレンラウリルエーテル、HLB:13.6)を5重量%の濃度となるよう前記電解液に溶解させて分散液を得る。
分散条件:前記分散液5mLに測定試料10mgを添加し、超音波分散機にて1分間分散させ、その後、電解液25mLを添加し、さらに、超音波分散機にて1分間分散させて、試料分散液を調製する。
測定条件:前記試料分散液を前記電解液100mLに加えることにより、3万個の粒子の粒径を20秒で測定できる濃度に調整した後、3万個の粒子を測定し、その粒度分布から体積中位粒径(D50)を求める。
[Volume-median particle size of toner (D 50 )]
Measuring machine: Coulter Multisizer II (Beckman Coulter, Inc.)
Aperture diameter: 100μm
Analysis software: Coulter Multisizer AccuComp version 1.19 (Beckman Coulter)
Electrolyte: Isoton II (Beckman Coulter, Inc.)
Dispersion: Emulgen 109P (manufactured by Kao Corporation, polyoxyethylene lauryl ether, HLB: 13.6) is dissolved in the electrolytic solution to a concentration of 5% by weight to obtain a dispersion.
Dispersion conditions: 10 mg of a measurement sample is added to 5 mL of the above dispersion, and dispersed for 1 minute with an ultrasonic disperser, then 25 mL of electrolyte is added, and further dispersed for 1 minute with an ultrasonic disperser. Prepare a dispersion.
Measurement conditions: By adding the sample dispersion to 100 mL of the electrolytic solution, the particle size of 30,000 particles is adjusted to a concentration that can be measured in 20 seconds, and then 30,000 particles are measured, Determine the volume-median particle size (D 50 ).
樹脂製造例1〜4(実施例1〜4)
表1に示す無水トリメリット酸及びアクリル酸以外のポリエステルの原料モノマー及びエステル化触媒としてオクチル酸スズ10gを、窒素導入管、脱水管、攪拌器及び熱電対を装備した10リットル容の四つ口フラスコに入れ、230℃で8時間縮重合反応させた。さらに、8kPaで1時間反応させ、160℃まで冷却した後、表1に示すアクリル酸、ビニル系樹脂の原料モノマー及び重合開始剤の混合物を滴下ロートにより1時間かけて滴下した。滴下後、160℃に保持したまま、1時間付加重合反応を熟成させた後、200℃に昇温し、10kPaで1時間保持して、ビニル系樹脂の原料モノマーの除去をおこなった。その後、表1に示す無水トリメリット酸を加えて1時間反応させた後、40kPaで架橋反応を所定の軟化点に達するまで行い樹脂を得た。
Resin production examples 1 to 4 (Examples 1 to 4)
Four-necked 10 liters equipped with 10 g of tin octylate as a raw material monomer and esterification catalyst for polyesters other than trimellitic anhydride and acrylic acid shown in Table 1 and equipped with a nitrogen introduction tube, a dehydration tube, a stirrer and a thermocouple The flask was placed in a flask and subjected to a condensation polymerization reaction at 230 ° C. for 8 hours. Furthermore, after reacting at 8 kPa for 1 hour and cooling to 160 ° C., a mixture of acrylic acid, a raw material monomer of vinyl resin and a polymerization initiator shown in Table 1 was dropped over 1 hour with a dropping funnel. After dropping, the addition polymerization reaction was aged for 1 hour while maintaining the temperature at 160 ° C., and then the temperature was raised to 200 ° C. and maintained at 10 kPa for 1 hour to remove the vinyl-based resin raw material monomer. Thereafter, trimellitic anhydride shown in Table 1 was added and reacted for 1 hour, and then a crosslinking reaction was performed at 40 kPa until a predetermined softening point was reached to obtain a resin.
樹脂製造例5(実施例5)
表1に示す無水トリメリット酸及びアクリル酸以外のポリエステルの原料モノマー及びエステル化触媒としてオクチル酸スズ10gを、窒素導入管、脱水管、攪拌器及び熱電対を装備した10リットル容の四つ口フラスコに入れ、230℃で8時間縮重合反応させた。さらに、8kPaで1時間反応させ、表1に示すフィッシャートロプッシュワックス「サゾールH105」(サゾール社製)を添加し、160℃まで冷却した後、表1に示すアクリル酸、ビニル系樹脂の原料モノマー及び重合開始剤の混合物を滴下ロートにより1時間かけて滴下した。滴下後、160℃に保持したまま、1時間付加重合反応を熟成させた後、200℃に昇温し、10kPaで1時間保持して、ビニル系樹脂の原料モノマーの除去をおこなった。その後、表1に示す無水トリメリット酸を加えて1時間反応させた後、40kPaで架橋反応を所定の軟化点に達するまで行い樹脂を得た。
Resin Production Example 5 (Example 5)
Four-necked 10 liters equipped with 10 g of tin octylate as a raw material monomer and esterification catalyst for polyesters other than trimellitic anhydride and acrylic acid shown in Table 1 and equipped with a nitrogen introduction tube, a dehydration tube, a stirrer and a thermocouple The flask was placed in a flask and subjected to a condensation polymerization reaction at 230 ° C. for 8 hours. Further, the reaction is carried out at 8 kPa for 1 hour, Fischer-Tropsch wax “Sazol H105” (manufactured by Sazol) shown in Table 1 is added, and after cooling to 160 ° C., acrylic acid and vinyl resin raw material monomers shown in Table 1 And the mixture of the polymerization initiator was dripped over 1 hour with the dropping funnel. After dropping, the addition polymerization reaction was aged for 1 hour while maintaining the temperature at 160 ° C., and then the temperature was raised to 200 ° C. and maintained at 10 kPa for 1 hour to remove the vinyl-based resin raw material monomer. Thereafter, trimellitic anhydride shown in Table 1 was added and reacted for 1 hour, and then a crosslinking reaction was performed at 40 kPa until a predetermined softening point was reached to obtain a resin.
樹脂製造例6〜9(比較例1〜2及び実施例6〜7)
表1に示す原料を用いて、樹脂製造例1と同様にして反応を行ない、樹脂を得た。
Resin Production Examples 6-9 (Comparative Examples 1-2 and Examples 6-7)
Using the raw materials shown in Table 1, a reaction was carried out in the same manner as in Resin Production Example 1 to obtain a resin.
試験例1〔粉砕性〕
樹脂1〜9を「NEW ROTOPLEX」(HOSOKAWA/ALPINE社製)で粗粉砕後、篩いにかけ、16メッシュ(目開き:1mm)の篩いを通過し、22メッシュ(目開き:710μm)の篩いを通過しない樹脂粉体を得た。得られた樹脂粉体を10.00g精秤し、ミル&ミキサー MM-I型((株)日立リビングサプライ製)にて30秒間粉砕後、30メッシュ(目開き:500μm)の篩いにかけ、通過しない樹脂の重量(A)gを精秤し、式:
残存率=(A)/粉砕前の樹脂重量(10.00g)×100
により、残存率を求めた。この操作を3回行い、各回の残存率の平均値を算出した。得られた平均値を粉砕性指数とし、下記の評価基準に従って評価した。その結果、粉砕性は、樹脂1、4及び5が◎、樹脂2及び樹脂8と樹脂9の等量混合品が○、樹脂3と6が△、樹脂7が×であった。
Test Example 1 [Crushability]
Resins 1-9 are coarsely pulverized with “NEW ROTOPLEX” (HOSOKAWA / ALPINE), passed through a sieve of 16 mesh (opening: 1 mm), and passed through a sieve of 22 mesh (opening: 710 μm) Not obtained resin powder. 10.00g of the obtained resin powder is precisely weighed, pulverized for 30 seconds with a mill & mixer MM-I type (manufactured by Hitachi Living Supply Co., Ltd.), passed through a sieve of 30 mesh (opening: 500 μm), and does not pass The weight (A) g of the resin is precisely weighed and the formula:
Residual rate = (A) / resin weight before grinding (10.00 g) × 100
Thus, the residual rate was obtained. This operation was performed three times, and the average value of the residual rate at each time was calculated. The average value obtained was used as the grindability index, and evaluated according to the following evaluation criteria. As a result, the pulverizability was as follows: Resins 1, 4 and 5 were ◎, Resins 2 and 8 and an equivalent mixture of Resin 9 were ○, Resins 3 and 6 were Δ, and Resin 7 was ×.
〔粉砕性の評価基準〕
◎:粉砕性指数が5未満
○:粉砕性指数が5以上、10未満
△:粉砕性指数が10以上、15未満
×:粉砕性指数が15以上
[Evaluation criteria for grindability]
◎: Grindability index is less than 5 ○: Grindability index is 5 or more and less than 10 △: Grindability index is 10 or more, less than 15 ×: Grindability index is 15 or more
トナー製造例1〜8(実施例8〜13及び比較例3〜4)
表2に示すトナー原料をヘンシェルミキサーにて攪拌混合後、混練部分の全長1560mm、スクリュー径42mm、バレル内径43mmの同方向回転二軸押出機を用いて溶融混練した。ロールの回転速度は200r/min、ロール内の加熱温度は120℃であり、混合物の供給速度は10kg/時間、平均滞留時間は約18秒であった。得られた混練物を冷却ローラーで圧延冷却した後、ジェットミルで粉砕し、分級して、体積中位粒径(D50)6μmの粉体を得た。
Toner Production Examples 1-8 (Examples 8-13 and Comparative Examples 3-4)
The toner materials shown in Table 2 were stirred and mixed with a Henschel mixer, and then melt-kneaded using a co-rotating twin screw extruder having a total kneading part length of 1560 mm, a screw diameter of 42 mm, and a barrel inner diameter of 43 mm. The rotation speed of the roll was 200 r / min, the heating temperature in the roll was 120 ° C., the feed rate of the mixture was 10 kg / hour, and the average residence time was about 18 seconds. The obtained kneaded material was rolled and cooled with a cooling roller, then pulverized with a jet mill, and classified to obtain a powder having a volume-median particle size (D 50 ) of 6 μm.
得られた粉体100重量部と疎水性シリカ「アエロジル R-972」(日本アエロジル社製)1.5重量部及び疎水性酸化チタン「TiSr」(富士チタン社製)1.0重量部とをヘンシェルミキサーを用いて混合後、磁性トナーを得た。 Using a Henschel mixer, 100 parts by weight of the obtained powder, 1.5 parts by weight of hydrophobic silica “Aerosil R-972” (manufactured by Nippon Aerosil) and 1.0 part by weight of hydrophobic titanium oxide “TiSr” (manufactured by Fuji Titanium) After mixing, a magnetic toner was obtained.
試験例2〔耐オフセット性〕
「Laser Jet4200」(HP社製)に表2のトナー250gを実装し、未定着で2cm×12cm、0.6mg/cm2の画像出しを行った。得られた画像について、複写機「AR-505」(シャープ(株)製)の定着機をオフライン定着機の総定着圧が392Paになるように改良した定着機(定着速度250mm/sec:A4用紙50枚/分)を用いて、「CopyBond SF-70NA」(75g/m2、シャープ(株)製)に100℃から240℃へ10℃ずつ順次定着温度を上昇させながら定着試験を行った。オフセットを目視で観察し、オフセットが発生する温度を下記の評価基準に従って評価した。結果を表2に示す。
Test Example 2 [Offset resistance]
250 g of the toner shown in Table 2 was mounted on “Laser Jet 4200” (manufactured by HP), and an image of 2 cm × 12 cm and 0.6 mg / cm 2 was unfixed. For the obtained image, the fixing machine of the copier “AR-505” (manufactured by Sharp Corporation) is improved so that the total fixing pressure of the offline fixing machine is 392 Pa (fixing speed 250 mm / sec: A4 paper) 50 copies / minute) was used, and a fixing test was performed on “CopyBond SF-70NA” (75 g / m 2 , manufactured by Sharp Corporation) while gradually increasing the fixing temperature from 100 ° C. to 240 ° C. in 10 ° C. increments. The offset was visually observed, and the temperature at which the offset occurred was evaluated according to the following evaluation criteria. The results are shown in Table 2.
〔オフセットの評価基準〕
100〜240℃の間でオフセットの発生しない温度範囲
◎:90℃以上
○:70℃以上、90℃未満
△:50℃以上、70℃未満
×:50℃未満
[Evaluation criteria for offset]
Temperature range where offset does not occur between 100 and 240 ° C ◎: 90 ° C or more ○: 70 ° C or more, less than 90 ° C △: 50 ° C or more, less than 70 ° C ×: less than 50 ° C
以上の結果より、実施例の結着樹脂を含有したトナーは、オフセットの発生温度も高く、良好なものであることが分かる。 From the above results, it can be seen that the toner containing the binder resin of Example has a high offset occurrence temperature and is good.
トナー製造例9(実施例14)
トナー製造例1において、磁性粉の代わりに着色剤「ECB301」(大日精化社製)を結着樹脂100重量部に対して5重量部加えた以外は、トナー製造例1と同様にして、非磁性トナーを得た。得られたトナーについて、耐オフセット性を上記方法と同様にして試験した結果、良好な結果が得られた。なお、トナー評価の画像出しについては、「マイクロライン 5400」(沖データ社製)を用いた。本発明の結着樹脂は、非磁性トナーにおいても好適に使用することができることが分かる。
Toner Production Example 9 (Example 14)
In Toner Production Example 1, in the same manner as in Toner Production Example 1, except that 5 parts by weight of a colorant “ECB301” (manufactured by Dainichi Seika Co., Ltd.) is added to 100 parts by weight of the binder resin instead of magnetic powder. A non-magnetic toner was obtained. The obtained toner was tested for offset resistance in the same manner as described above, and as a result, good results were obtained. In addition, “Microline 5400” (manufactured by Oki Data Corporation) was used for image output for toner evaluation. It can be seen that the binder resin of the present invention can be suitably used in non-magnetic toners.
本発明のトナー用結着樹脂は、電子写真法、静電記録法、静電印刷法等において形成される潜像の現像等に用いられるトナーの結着樹脂として好適に用いられるものである。 The binder resin for toner of the present invention is suitably used as a binder resin for toner used for developing a latent image formed in electrophotography, electrostatic recording method, electrostatic printing method and the like.
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