JP2008174430A - Hydrophobic spherical silica fine particles, production method thereof, and toner external additive for developing electrostatic image using the same - Google Patents
Hydrophobic spherical silica fine particles, production method thereof, and toner external additive for developing electrostatic image using the same Download PDFInfo
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Abstract
【課題】トナーの流動性を改良することができる疎水性球状シリカ微粒子及びその製造方法を提供する。
【解決手段】一般式(1):
Si(OR1)4 (1)
[式中、R1は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示されるテトラヒドロカルビルオキシシラン化合物及びその部分加水分解縮合生成物からなる群から選ばれる少なくとも1種の化合物を加水分解及び縮合することによって得られたSiO2単位からなる親水性球状シリカ微粒子の表面にR4SiO3/2単位(式中、R4は置換又は非置換の炭素原子数1〜20の1価炭化水素基である)を導入する工程と、次いでR6 3SiO1/2単位(式中、R6は同一又は異なり、置換又は非置換の炭素原子数1〜20の1価炭化水素基である)を導入する工程とを含む疎水化処理をして得られた疎水性球状シリカ微粒子であって、ヒドロカルビルオキシ基含量が1000ppm以下であり、粒子径が0.01〜5μmである疎水性球状シリカ微粒子。
【選択図】なしThe present invention provides a hydrophobic spherical silica fine particle capable of improving the fluidity of a toner and a method for producing the same.
A general formula (1):
Si (OR 1 ) 4 (1)
[Wherein R 1 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
Surface of hydrophilic spherical silica fine particles comprising SiO 2 units obtained by hydrolyzing and condensing at least one compound selected from the group consisting of tetrahydrocarbyloxysilane compounds and partial hydrolysis-condensation products thereof A step of introducing R 4 SiO 3/2 units (wherein R 4 is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms), and then R 6 3 SiO 1/2 units (Wherein R 6 is the same or different and is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms) and a hydrophobic sphere obtained by hydrophobization treatment Hydrophobic spherical silica fine particles having a hydrocarbyloxy group content of 1000 ppm or less and a particle size of 0.01 to 5 μm, which are silica fine particles.
[Selection figure] None
Description
本発明は疎水性球状シリカ微粒子、特には高分散性、低凝集性を有する疎水性球状シリカ微粒子に関するものである。 The present invention relates to hydrophobic spherical silica fine particles, and in particular, to hydrophobic spherical silica fine particles having high dispersibility and low aggregation.
さらに、高画質化のために用いる小粒径トナー用の外添剤に関する。 Further, the present invention relates to an external additive for a small particle size toner used for improving image quality.
電子写真法等で使用する乾式現像剤は、結着樹脂中に着色剤を分散したトナーそのものを用いる一成分現像剤と、そのトナーにキャリアを混合した二成分現像剤とに大別できる。これらの現像剤を用いてコピー操作を行う場合、プロセス適合性を有するためには、現像剤が流動性、耐ケーキング性、定着性、帯電性、クリーニング性等に優れていることが必要である。特に、流動性、耐ケーキング性、定着性、クリーニング性を高めるために、無機微粒子をトナーに添加することがしばしば行われている。しかしながら、無機微粒子の分散性がトナー特性に大きな影響を与え、分散性が不均一な場合には、流動性、耐ケーキング性、定着性に所望の特性が得られなかったり、クリーニング性が不十分になって、感光体上にトナー固着等が発生し、黒点状の画像欠陥が生じたりする原因となることがあった。これらの問題点を改善する目的で、表面を疎水化処理した無機微粒子が種々提案されている。例えば、有機ケイ素化合物により表面処理されたコロイドシリカ粒子(特許文献1)、ケイ素原子に結合した炭化水素基と加水分解性基とを有する少なくとも1種の有機ケイ素化合物により表面処理されたコロイド状シリカ(特許文献2、特許文献3)が挙げられる。 Dry developers used in electrophotography and the like can be roughly classified into a one-component developer using a toner itself in which a colorant is dispersed in a binder resin and a two-component developer in which a carrier is mixed with the toner. When performing a copying operation using these developers, in order to have process compatibility, the developer needs to be excellent in fluidity, caking resistance, fixing properties, charging properties, cleaning properties, and the like. . In particular, inorganic fine particles are often added to the toner in order to improve fluidity, caking resistance, fixing properties, and cleaning properties. However, the dispersibility of the inorganic fine particles has a great influence on the toner characteristics, and when the dispersibility is not uniform, desired characteristics cannot be obtained in the fluidity, caking resistance, and fixability, or the cleaning properties are insufficient. As a result, toner sticking or the like may occur on the photoconductor, which may cause black spot image defects. In order to improve these problems, various inorganic fine particles having a hydrophobic surface have been proposed. For example, colloidal silica particles surface-treated with an organosilicon compound (Patent Document 1), colloidal silica surface-treated with at least one organosilicon compound having a hydrocarbon group bonded to a silicon atom and a hydrolyzable group (Patent Literature 2, Patent Literature 3).
しかしながら、より高画質化を図るために有機感光体を使用したり、より小粒径のトナーを使用したりする場合には、上記の無機微粒子を使用したのでは十分な性能が得られない。また、有機感光体は無機感光体に比べてその表面が柔らかく、反応性も高いので寿命が短くなりやすい。したがって、このような有機感光体を用いた場合には、トナーに添加された無機微粒子によって感光体の変質や削れが生じ易い。さらに、トナーを小粒径にした場合には、通常用いられる粒子径のトナーと比較して粉体流動性が悪いので、無機微粒子をより多量に添加しなければならなくなり、その結果、無機微粒子が感光体へのトナー付着の原因となることがあった。 However, when using an organic photoreceptor or a toner having a smaller particle diameter in order to achieve higher image quality, sufficient performance cannot be obtained by using the inorganic fine particles described above. In addition, organic photoreceptors have a softer surface and higher reactivity than inorganic photoreceptors, so their lifetime is likely to be shortened. Therefore, when such an organic photoreceptor is used, the photoreceptor is easily altered or scraped by the inorganic fine particles added to the toner. Furthermore, when the toner has a small particle size, the powder fluidity is poor as compared with a toner having a particle size that is usually used, so a larger amount of inorganic fine particles must be added. May cause toner adhesion to the photoreceptor.
そこで、アルコキシシランの加水分解で製造した親水性球状シリカ微粒子の表面を第1段階の疎水化処理をする工程と、得られる疎水性シリカ微粒子の表面をトリオルガノシリル化、即ち、第2段階の疎水化処理をする工程とによって、疎水化することが提案されている(特許文献4)。 Therefore, the step of hydrophobizing the surface of the hydrophilic spherical silica fine particles produced by hydrolysis of alkoxysilane, and the step of triorganosilylation of the surface of the resulting hydrophobic silica fine particles, that is, the second step. Hydrophobization has been proposed by the process of hydrophobizing (Patent Document 4).
しかし、上記のアルコキシシランの加水分解で製造した親水性球状シリカ微粒子をこの方法により疎水化処理して得られた疎水性球状シリカ微粒子は、流動性が不十分で、トナー外添剤として使用しても、トナーに必要な流動性を付与することができない場合があった。 However, the hydrophobic spherical silica fine particles obtained by hydrophobizing the hydrophilic spherical silica fine particles produced by hydrolysis of the alkoxysilane described above have insufficient fluidity and are used as an external toner additive. In some cases, however, the required fluidity cannot be imparted to the toner.
本発明の課題は、トナーの流動性を改良することができる疎水性球状シリカ微粒子及びその製造方法を提供することである。 An object of the present invention is to provide hydrophobic spherical silica fine particles capable of improving the fluidity of a toner and a method for producing the same.
また、本発明の別の課題は、該疎水性球状シリカ微粒子を用いるトナー外添剤を提供することである。 Another object of the present invention is to provide an external toner additive using the hydrophobic spherical silica fine particles.
本発明は、上記の課題を解決する手段として、第一に、
一般式(1):
Si(OR1)4 (1)
[式中、R1は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示されるテトラヒドロカルビルオキシシラン化合物及びその部分加水分解縮合生成物からなる群から選ばれる少なくとも1種の化合物を加水分解及び縮合することによって得られたSiO2単位からなる親水性球状シリカ微粒子の表面にR4SiO3/2単位(式中、R4は置換又は非置換の炭素原子数1〜20の1価炭化水素基である)を導入する工程と、次いでR6 3SiO1/2単位(式中、R6は同一又は異なり、置換又は非置換の炭素原子数1〜20の1価炭化水素基である)を導入する工程とを含む疎水化処理をして得られた疎水性球状シリカ微粒子であって、ヒドロカルビルオキシ基含量が1000ppm以下であり、粒子径が0.01〜5μmである疎水性球状シリカ微粒子を提供する。
As a means for solving the above problems, the present invention firstly
General formula (1):
Si (OR 1 ) 4 (1)
[Wherein R 1 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
Surface of hydrophilic spherical silica fine particles comprising SiO 2 units obtained by hydrolyzing and condensing at least one compound selected from the group consisting of tetrahydrocarbyloxysilane compounds and partial hydrolysis-condensation products thereof A step of introducing R 4 SiO 3/2 units (wherein R 4 is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms), and then R 6 3 SiO 1/2 units (Wherein R 6 is the same or different and is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms) and a hydrophobic sphere obtained by hydrophobization treatment Hydrophobic spherical silica fine particles having a hydrocarbyloxy group content of 1000 ppm or less and a particle diameter of 0.01 to 5 μm are provided.
本発明は、第二に、上記の疎水性球状シリカ微粒子の製造方法として、
(A)(a−1)一般式(1):
Si(OR1)4 (1)
[式中、R1は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示される4官能性シラン化合物及びその部分加水分解縮合生成物からなる群から選ばれる少なくとも1種の化合物を、塩基性物質の存在下で親水性有機溶媒と水との混合媒体中で加水分解、縮合して、親水性球状シリカ微粒子を生成させる工程と、
(a−2)溶媒として用いられた前記混合媒体から親水性有機溶媒を除去して媒体を水に置換して、水の含有量が90質量%以上である親水性球状シリカ微粒子の水分散液を得る工程と、
(B)前記親水性球状シリカ微粒子水分散液中の親水性球状シリカ微粒子の表面にR4SiO3/2単位[式中、R4は置換又は非置換の、炭素原子数1〜20の1価炭化水素基である]を導入し、第一次疎水性球状シリカ微粒子を得る工程と、
(C)得られた第一次疎水性球状シリカ微粒子の表面にR6 3SiO1/2単位[式中、R6は同一又は異なり、置換又は非置換の、炭素原子数1〜6の1価炭化水素基である]を導入して第二次疎水性シリカ微粒子を得る工程と、
を有する製造方法を提供する。
The present invention secondly, as a method for producing the above-mentioned hydrophobic spherical silica fine particles,
(A) (a-1) General formula (1):
Si (OR 1 ) 4 (1)
[Wherein R 1 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
Hydrolysis of at least one compound selected from the group consisting of a tetrafunctional silane compound and a partial hydrolysis-condensation product thereof in a mixed medium of a hydrophilic organic solvent and water in the presence of a basic substance Condensing to produce hydrophilic spherical silica fine particles;
(A-2) An aqueous dispersion of hydrophilic spherical silica fine particles having a water content of 90% by mass or more by removing the hydrophilic organic solvent from the mixed medium used as the solvent and replacing the medium with water. Obtaining
(B) R 4 SiO 3/2 unit on the surface of the hydrophilic spherical silica fine particles in the hydrophilic spherical silica fine particle aqueous dispersion [wherein R 4 is a substituted or unsubstituted 1 to 1 carbon atom having 1 to 20 carbon atoms. Is a monovalent hydrocarbon group] to obtain primary hydrophobic spherical silica fine particles,
(C) R 6 3 SiO 1/2 unit on the surface of the obtained primary hydrophobic spherical silica fine particles [wherein R 6 is the same or different and is substituted or unsubstituted, 1 to 6 carbon atoms. Is a valent hydrocarbon group] to obtain secondary hydrophobic silica fine particles,
A production method is provided.
さらに、本発明は、前記疎水性球状シリカ微粒子からなる静電荷像現像用トナー外添剤を提供する。 Furthermore, the present invention provides a toner external additive for developing an electrostatic image comprising the hydrophobic spherical silica fine particles.
本発明の疎水性球状シリカ微粒子はトナー外添剤として有用であり、トナーの流動性を改良することができる。更に、該トナー外添剤は、トナーに必要な帯電を与えることができ、さらに、有機感光体との反応や相互作用がないため感光体の変質や削れが生じにくい。分散性に優れており、流動性が良好であるため感光体へのトナー付着が生じず、環境状態に依存しない帯電性を有する。このトナー外添剤を用いることで、電子写真法、静電記録法等における静電荷像の現像に応用することにより、高画質化が期待できる。 The hydrophobic spherical silica fine particles of the present invention are useful as an external toner additive, and can improve the fluidity of the toner. Furthermore, the toner external additive can give the toner the necessary charge, and further, since there is no reaction or interaction with the organic photoreceptor, the photoreceptor is unlikely to be altered or scraped. Since it has excellent dispersibility and fluidity, toner adhesion to the photoreceptor does not occur, and it has a charging property that does not depend on environmental conditions. By using this toner external additive, high image quality can be expected by applying it to the development of electrostatic images in electrophotography, electrostatic recording, and the like.
以下、本発明について詳細に説明する。 Hereinafter, the present invention will be described in detail.
合成シリカ微粒子は、その製法によって、シラン化合物を燃焼させて得られる燃焼法シリカ(即ち、ヒュームドシリカ)、金属珪素粉を爆発的に燃焼させて得られる爆燃法シリカ、珪酸ナトリウムと鉱酸との中和反応によって得られる湿式シリカ(このうちアルカリ条件で合成したものを沈降法シリカ、酸性条件で合成したものをゲル法シリカという)、ヒドロカルビルオキシシランの加水分解によって得られるゾルゲル法シリカ(いわゆるStoeber法)に大別される。本発明は、このうち、ゾルゲル法シリカに関するものである。
<疎水性球状シリカ微粒子の特徴>
まず、本発明の疎水性球状シリカ微粒子の特徴について、詳細に説明する。 本発明の微粒子は、4官能性シラン化合物及び/又はその部分加水分解縮合生成物を加水分解及び縮合することによって得られたSiO2単位からなる親水性球状シリカ微粒子の表面にR4SiO3/2単位(式中、R4は置換又は非置換の炭素原子数1〜20の1価炭化水素基である)を導入する工程、次いでR6 3SiO1/2単位(式中、R6は同一又は異なり、置換又は非置換の炭素原子数1〜20の1価炭化水素基である)を導入する工程を含む二段階の疎水化処理をして得られた疎水性球状シリカ微粒子であって、ヒドロカルビルオキシ基含量が1000ppm以下であり、好ましくは500ppm以下、特に好ましくは10ppm以下である。ヒドロカルビルオキシ基含量が1000ppmを超えると、この極性基の影響でトナーの流動性が不十分となる。
Synthetic silica fine particles are produced by combustion method silica obtained by burning a silane compound (that is, fumed silica), deflagration silica obtained by explosively burning metal silicon powder, sodium silicate and mineral acid. Wet silica obtained by the neutralization reaction of the above (the one synthesized under alkaline conditions is precipitated silica, the one synthesized under acidic conditions is gel silica), the sol-gel silica obtained by hydrolysis of hydrocarbyloxysilane (so-called Stoeber method). Of these, the present invention relates to sol-gel silica.
<Characteristics of hydrophobic spherical silica fine particles>
First, the characteristics of the hydrophobic spherical silica fine particles of the present invention will be described in detail. The fine particles of the present invention have R 4 SiO 3 / on the surface of hydrophilic spherical silica fine particles composed of SiO 2 units obtained by hydrolysis and condensation of a tetrafunctional silane compound and / or a partially hydrolyzed condensation product thereof. A step of introducing 2 units (wherein R 4 is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms), then R 6 3 SiO 1/2 units (wherein R 6 is Hydrophobic spherical silica fine particles obtained by two-stage hydrophobizing treatment including a step of introducing the same or different, substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms) The hydrocarbyloxy group content is 1000 ppm or less, preferably 500 ppm or less, particularly preferably 10 ppm or less. When the hydrocarbyloxy group content exceeds 1000 ppm, the fluidity of the toner becomes insufficient due to the influence of this polar group.
本発明の疎水性球状シリカ微粒子について、「球状」とは、真球だけでなく、若干歪んだ球も含む。具体的には、「球状」であるとは粒子を二次元に投影したときの円形度が0.8〜1の範囲にあることを意味する。ここで円形度とは、(実際の粒子を二次元投影したときの図形の面積と等しい真円の周囲長)/(実際の粒子を二次元投影したときの図形の面積の周囲長)を意味する。
上記微粒子の粒子径は0.01〜5μmであり、好ましくは0.05〜0.5μm、特に好ましくは0.1〜0.2μmである。この粒子径が0.01μmより小さい場合には、上記微粒子が凝集することにより、現像剤の流動性、耐ケーキング性、定着性等が不十分なものとなり、5μmより大きい場合には、感光体の変質や削れ、上記微粒子のトナーへの付着性の低下等の不都合を生ずる。なお、ここで「粒子径」とは体積基準メジアン径を意味する。
With respect to the hydrophobic spherical silica fine particles of the present invention, “spherical” includes not only true spheres but also slightly distorted spheres. Specifically, “spherical” means that the circularity when particles are projected two-dimensionally is in the range of 0.8-1. Here, the circularity means (peripheral length of a perfect circle equal to the area of the figure when an actual particle is projected two-dimensionally) / (perimeter of the area of the figure when an actual particle is projected two-dimensionally) To do.
The particle diameter of the fine particles is 0.01 to 5 μm, preferably 0.05 to 0.5 μm, particularly preferably 0.1 to 0.2 μm. When the particle diameter is smaller than 0.01 μm, the fine particles aggregate to result in insufficient developer fluidity, caking resistance, fixability, and the like. Inconveniences such as alteration or shaving and a decrease in adhesion of the fine particles to the toner occur. Here, “particle diameter” means a volume-based median diameter.
<疎水性球状シリカ微粒子の合成>
次に、本発明の疎水性球状シリカ微粒子の製造方法について詳細に説明する。該疎水性球状シリカ微粒子は、例えば、ゾルゲル法によりヒドロカルビルオキシ基を低減した親水性球状シリカ微粒子を製造する工程((A)工程)と、該親水性球状シリカ微粒子の表面を第1段階の疎水化処理をする工程((B)工程)と、得られた第1次疎水性球状シリカ微粒子の表面をトリオルガノシリル化、即ち、第2段階の疎水化処理をする工程((C)工程)とを有する方法により得られる。以下、各工程を説明する。
<Synthesis of hydrophobic spherical silica fine particles>
Next, the method for producing the hydrophobic spherical silica fine particles of the present invention will be described in detail. The hydrophobic spherical silica fine particles may be produced, for example, by a step of producing hydrophilic spherical silica fine particles having reduced hydrocarbyloxy groups by a sol-gel method (step (A)), and the surface of the hydrophilic spherical silica fine particles is a first step hydrophobic particle. Step ((B)), and a step of triorganosilylation of the surface of the obtained primary hydrophobic spherical silica fine particles, that is, a second step hydrophobization (step (C)) It is obtained by the method which has these. Hereinafter, each process will be described.
−親水性球状シリカ微粒子の合成((A)工程)−
本工程では、(a−1)一般式(1):
Si(OR1)4 (1)
[式中、R1は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示される4官能性シラン化合物及び/又はその部分加水分解縮合生成物を加水分解及び縮合させ親水性球状シリカ微粒子を生成させ、次いで(a−2)該シリカ微粒子が有するヒドロカルビルオキシ基含量を低減する工程と有する。その結果、この方法により最終的に得られる疎水性球状シリカ微粒子のヒドロカルビルオキシ基含量を1000ppm以下とすることができ、この極性基による悪影響を排除できるため、トナー流動性が良好となる。
-Synthesis of hydrophilic spherical silica fine particles (step (A))-
In this step, (a-1) general formula (1):
Si (OR 1 ) 4 (1)
[Wherein R 1 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
Hydrophilic spherical silica fine particles are produced by hydrolyzing and condensing the tetrafunctional silane compound and / or its partial hydrolytic condensation product represented by the formula (a-2), and then the hydrocarbyloxy group content of the silica fine particles is reduced. And having a process. As a result, the hydrocarbyloxy group content of the hydrophobic spherical silica fine particles finally obtained by this method can be reduced to 1000 ppm or less, and adverse effects due to this polar group can be eliminated, so that the toner fluidity is improved.
前記加水分解性基としては、例えば、ヒドロカルビルオキシ基、アミノ基、アシルオキシ基、好ましくは、ヒドロカルビルオキシ基、アミノ基、特に好ましくは、ヒドロカルビルオキシ基が挙げられる。前記ヒドロカルビルオキシ基としては、例えば、メトキシ基、エトキシ基、プロポキシ基、ブトキシ基、ヘキシルオキシ基、フェノキシ基等が挙げられ、好ましくは、メトキシ基、エトキシ基が挙げられる。 Examples of the hydrolyzable group include a hydrocarbyloxy group, an amino group, and an acyloxy group, preferably a hydrocarbyloxy group and an amino group, and particularly preferably a hydrocarbyloxy group. Examples of the hydrocarbyloxy group include a methoxy group, an ethoxy group, a propoxy group, a butoxy group, a hexyloxy group, and a phenoxy group, and a methoxy group and an ethoxy group are preferable.
該(A)工程は、さらに具体的には、
(a−1)一般式(1):
Si(OR1)4 (1)
[式中、R1は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示される4官能性シラン化合物及びその部分加水分解縮合生成物からなる群から選ばれる少なくとも1種の化合物を、塩基性物質の存在下で親水性有機溶媒と水との混合媒体中で加水分解、縮合して、親水性球状シリカ微粒子を生成させる工程と、
(a−2)溶媒として用いられた前記混合媒体から親水性有機溶媒を除去して媒体を水に置換して、水の含有量が90質量%以上である親水性球状シリカ微粒子の水分散液を得る工程と、を有してなる。
上記の(a−2)工程において、水分散液中の水の含有量が90質量%未満であれば、分散液中の親水性有機溶媒の量が多いためヒドロカルビルオキシ基の加水分解が十分進行せず、シリカ微粒子中の残存ヒドロカルビルオキシ基含量が多くなってしまう。
The step (A) is more specifically,
(A-1) General formula (1):
Si (OR 1 ) 4 (1)
[Wherein R 1 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
Hydrolysis of at least one compound selected from the group consisting of a tetrafunctional silane compound and a partial hydrolysis-condensation product thereof in a mixed medium of a hydrophilic organic solvent and water in the presence of a basic substance Condensing to produce hydrophilic spherical silica fine particles;
(A-2) An aqueous dispersion of hydrophilic spherical silica fine particles having a water content of 90% by mass or more by removing the hydrophilic organic solvent from the mixed medium used as the solvent and replacing the medium with water. And obtaining a step.
In the step (a-2), if the water content in the aqueous dispersion is less than 90% by mass, the hydrocarbyloxy group is sufficiently hydrolyzed because the amount of the hydrophilic organic solvent in the dispersion is large. Otherwise, the residual hydrocarbyloxy group content in the silica fine particles is increased.
上記一般式(1)中、R1は、好ましくは炭素原子数1〜6、より好ましくは1〜4、さらに好ましくは1〜2の1価炭化水素基である。R1で表される1価炭化水素基としては、例えば、メチル基、エチル基、プロピル基、ブチル基、フェニル基等、好ましくは、メチル基、エチル基、プロピル基、ブチル基、特に好ましくは、メチル基、エチル基が挙げられる。 In the general formula (1), R 1 is preferably a monovalent hydrocarbon group having 1 to 6 carbon atoms, more preferably 1 to 4, and still more preferably 1 to 2. Examples of the monovalent hydrocarbon group represented by R 1 include a methyl group, an ethyl group, a propyl group, a butyl group, and a phenyl group, preferably a methyl group, an ethyl group, a propyl group, and a butyl group, and particularly preferably , Methyl group, and ethyl group.
上記一般式(1)で示される4官能性シラン化合物としては、例えば、テトラメトキシシラン、テトラエトキシシラン、テトラプロポキシシラン、テトラブトキシシラン等のテトラアルコキシシラン、テトラフェノキシシラン等、好ましくは、テトラメトキシシラン、テトラエトキシシラン、テトラプロポキシシラン、テトラブトキシシラン、特に好ましくは、テトラメトキシシラン、テトラエトキシシランが挙げられる。また、一般式(1)で示される4官能性シラン化合物の部分加水分解縮合生成物としては、例えば、メチルシリケート、エチルシリケート等が挙げられる。 Examples of the tetrafunctional silane compound represented by the general formula (1) include tetraalkoxysilanes such as tetramethoxysilane, tetraethoxysilane, tetrapropoxysilane, and tetrabutoxysilane, tetraphenoxysilane, and the like. Silane, tetraethoxysilane, tetrapropoxysilane, and tetrabutoxysilane, particularly preferably tetramethoxysilane and tetraethoxysilane. Examples of the partial hydrolysis-condensation product of the tetrafunctional silane compound represented by the general formula (1) include methyl silicate and ethyl silicate.
前記親水性有機溶媒としては、一般式(1)で示される4官能性シラン化合物と、この部分加水分解縮合生成物と、水とを溶解するものであれば特に制限されず、例えば、アルコール類、メチルセロソルブ、エチルセロソルブ、ブチルセロソルブ、酢酸セロソルブ等のセロソルブ類、アセトン、メチルエチルケトン等のケトン類、ジオキサン、テトラヒドロフラン等のエーテル類等、好ましくは、アルコール類、セロソルブ類、特に好ましくはアルコール類が挙げられる。アルコール類としては、一般式(2):
R3OH (2)
[式中、R3は炭素原子数1〜6の1価炭化水素基である]
で示されるアルコールが挙げられる。
The hydrophilic organic solvent is not particularly limited as long as it dissolves the tetrafunctional silane compound represented by the general formula (1), the partial hydrolysis-condensation product, and water. For example, alcohols Cellosolves such as methyl cellosolve, ethyl cellosolve, butyl cellosolve, and cellosolve acetate, ketones such as acetone and methyl ethyl ketone, ethers such as dioxane and tetrahydrofuran, preferably alcohols and cellosolves, particularly preferably alcohols . As alcohols, general formula (2):
R 3 OH (2)
[Wherein R 3 is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
The alcohol shown by is mentioned.
上記一般式(2)中、R3は、好ましくは炭素原子数1〜4、特に好ましくは1〜2の1価炭化水素基である。R3で表される1価炭化水素基としては、例えば、メチル基、エチル基、プロピル基、イソプロピル基、ブチル基等のアルキル基等、好ましくはメチル基、エチル基、プロピル基、イソプロピル基、より好ましくはメチル基、エチル基が挙げられる。一般式(2)で示されるアルコールとしては、例えば、メタノール、エタノール、プロパノール、イソプロパノール、ブタノール等、好ましくは、メタノール、エタノールが挙げられる。アルコールの炭素原子数が増えると、生成する球状シリカ微粒子の粒子径が大きくなる。従って、目的とする球状シリカ微粒子の粒子径によりアルコールの種類を選択することが望ましい。 In the general formula (2), R 3 is preferably a monovalent hydrocarbon group having 1 to 4 carbon atoms, particularly preferably 1 to 2 carbon atoms. Examples of the monovalent hydrocarbon group represented by R 3 include alkyl groups such as a methyl group, an ethyl group, a propyl group, an isopropyl group, and a butyl group, preferably a methyl group, an ethyl group, a propyl group, an isopropyl group, More preferably, a methyl group and an ethyl group are mentioned. Examples of the alcohol represented by the general formula (2) include methanol, ethanol, propanol, isopropanol, butanol and the like, preferably methanol and ethanol. As the number of carbon atoms in the alcohol increases, the particle size of the spherical silica fine particles to be generated increases. Therefore, it is desirable to select the type of alcohol according to the particle diameter of the target spherical silica fine particles.
また、上記塩基性物質としてはアンモニア、及びジメチルアミン、ジエチルアミン等のジ低級アルキルアミン、好ましくは、アンモニア及びジエチルアミン、特に好ましくはアンモニアが挙げられる。これらの塩基性物質は、所要量を水に溶解した後、得られた水溶液(塩基性)を前記親水性有機溶媒と混合すればよい。 Examples of the basic substance include ammonia and di-lower alkylamines such as dimethylamine and diethylamine, preferably ammonia and diethylamine, and particularly preferably ammonia. These basic substances may be dissolved in water in a required amount, and the obtained aqueous solution (basic) may be mixed with the hydrophilic organic solvent.
この加水分解反応において使用される水の合計量は、一般式(1)で示される4官能性シラン化合物及び/又はその部分加水分解縮合生成物のヒドロカルビルオキシ基の合計1モルに対して0.5〜5モルであることが好ましく、0.6〜2モルであることがより好ましく、0.7〜1モルであることが特に好ましい。水に対する親水性有機溶媒の比率は、質量比で0.5〜10であることが好ましく、1〜5であることがより好ましく、1.5〜2であることが特に好ましい。塩基性物質の量は、一般式(1)で示される4官能性シラン化合物及び/又はその部分加水分解縮合生成物、のヒドロカルビルオキシ基の合計1モルに対して0.01〜2モルであることが好ましく、0.5〜1.5モルであることがより好ましく、1.0〜1.2モルであることが特に好ましい。 The total amount of water used in this hydrolysis reaction is 0.5 to a total of 1 mol of hydrocarbyloxy groups of the tetrafunctional silane compound represented by the general formula (1) and / or the partial hydrolysis condensation product thereof. 5 mol is preferable, 0.6 to 2 mol is more preferable, and 0.7 to 1 mol is particularly preferable. The ratio of the hydrophilic organic solvent to water is preferably 0.5 to 10 in terms of mass ratio, more preferably 1 to 5, and particularly preferably 1.5 to 2. The amount of the basic substance is 0.01 to 2 mol with respect to a total of 1 mol of hydrocarbyloxy groups of the tetrafunctional silane compound represented by the general formula (1) and / or a partial hydrolysis condensation product thereof. Preferably, it is 0.5 to 1.5 mol, more preferably 1.0 to 1.2 mol.
一般式(1)で示される4官能性シラン化合物等の加水分解及び縮合は、周知の方法、即ち、塩基性物質を含む親水性有機溶媒と水との混合物中に、一般式(1)で示される4官能性シラン化合物等を添加することにより行われる。 Hydrolysis and condensation of the tetrafunctional silane compound or the like represented by the general formula (1) can be carried out by a well-known method, that is, in a mixture of a hydrophilic organic solvent containing a basic substance and water by the general formula (1). It is performed by adding a tetrafunctional silane compound or the like shown.
親水性球状シリカ微粒子混合溶液分散液の分散媒を水に変換する工程は、例えば、該分散液に水を添加し親水性有機溶媒を留去する操作(必要に応じてこの操作を繰り返す)により行うことができる。このときに添加される水の合計量は、使用した親水性有機溶媒及び生成したアルコールの量の合計に対して、質量基準で、好ましくは2倍量を超える量、より好ましくは2.5〜3.5倍量、特に好ましくは3倍量であり、最終的に分散液の水含有量が90質量%以上、好ましくは98質量%以上となるようにする。こうして分散液中の水の含有量が90質量%以上である水分散液に変換すると、残存している一般式(1)で示される4官能性シラン化合物に由来するヒドロカルビルオキシ基(OR1)が加水分解され、ヒドロカルビルオキシ基量が減少した親水性球状シリカ微粒子とすることができる。 The step of converting the dispersion medium of the hydrophilic spherical silica fine particle mixed solution into water is performed by, for example, an operation of adding water to the dispersion and distilling off the hydrophilic organic solvent (repeat this operation as necessary). It can be carried out. The total amount of water added at this time is preferably more than twice the amount of the total amount of the hydrophilic organic solvent used and the amount of alcohol produced, more preferably 2.5 to The amount is 3.5 times, particularly preferably 3 times, so that the water content of the dispersion is finally 90% by mass or more, preferably 98% by mass or more. When the water content in the dispersion liquid is converted to an aqueous dispersion liquid of 90% by mass or more in this way, the remaining hydrocarbyloxy group (OR 1 ) derived from the tetrafunctional silane compound represented by the general formula ( 1 ) Is hydrolyzed to form hydrophilic spherical silica fine particles in which the amount of hydrocarbyloxy groups is reduced.
このようにして得られる親水性球状シリカ微粒子は、(B)工程で第1段階の疎水化処理に供される。 The hydrophilic spherical silica fine particles obtained in this way are subjected to a first hydrophobization treatment in the step (B).
−親水性球状シリカ微粒子の表面疎水化処理((B)工程)−
(B)工程は、上記親水性球状シリカ微粒子の表面にR4SiO3/2単位[式中、R4は置換又は非置換の、炭素原子数1〜20の1価炭化水素基である]を導入して第一次疎水性球状シリカ微粒子を得る工程、即ち、第1段階の疎水化処理を行う工程である。例えば、上記親水性球状シリカ微粒子を含み、分散液の水含有量が90質量%以上である水性分散液に、一般式(3):
-Surface hydrophobization treatment of hydrophilic spherical silica fine particles (step (B))-
In the step (B), R 4 SiO 3/2 units [wherein R 4 is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms] on the surface of the hydrophilic spherical silica fine particles. Is a step for obtaining primary hydrophobic spherical silica fine particles, that is, a step for performing a first-stage hydrophobic treatment. For example, an aqueous dispersion containing the hydrophilic spherical silica fine particles and having a water content of 90% by mass or more in the dispersion is represented by the general formula (3):
R4Si(OR5)3 (3)
[式中、R4は前記と同じであり、R5は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示される3官能性シラン化合物もしくはその部分加水分解縮合生成物又はこれらの混合物を添加し、親水性球状シリカ微粒子表面を処理して第1次疎水性球状シリカ微粒子の水性分散液を得る。
R 4 Si (OR 5 ) 3 (3)
[Wherein, R 4 is the same as defined above, and R 5 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
A trifunctional silane compound represented by the above, a partial hydrolysis-condensation product thereof, or a mixture thereof is added, and the surface of the hydrophilic spherical silica fine particles is treated to obtain an aqueous dispersion of primary hydrophobic spherical silica fine particles.
上記一般式(3)中、R4は、好ましくは炭素原子数1〜3、特に好ましくは1〜2の1価炭化水素基である。R4で表される1価炭化水素基としては、例えば、メチル基、エチル基、n−プロピル基、イソプロピル基、ブチル基、ヘキシル基等のアルキル基等、好ましくは、メチル基、エチル基、n−プロピル基、イソプロピル基、特に好ましくは、メチル基、エチル基が挙げられる。また、これらの1価炭化水素基の水素原子の一部又は全部が、フッ素原子、塩素原子、臭素原子等のハロゲン原子、好ましくはフッ素原子で置換されていてもよい。 In the general formula (3), R 4 is preferably a monovalent hydrocarbon group having 1 to 3 carbon atoms, particularly preferably 1 to 2 carbon atoms. Examples of the monovalent hydrocarbon group represented by R 4 include alkyl groups such as a methyl group, an ethyl group, an n-propyl group, an isopropyl group, a butyl group, and a hexyl group, preferably a methyl group, an ethyl group, An n-propyl group and an isopropyl group, particularly preferably a methyl group and an ethyl group are exemplified. Further, some or all of the hydrogen atoms of these monovalent hydrocarbon groups may be substituted with halogen atoms such as fluorine atom, chlorine atom, bromine atom, preferably fluorine atom.
上記一般式(3)中、R5は、好ましくは炭素原子数1〜3、特に好ましくは1〜2の1価炭化水素基である。R5で表される1価炭化水素基としては、例えば、メチル基、エチル基、プロピル基、ブチル基等のアルキル基等、好ましくは、メチル基、エチル基、プロピル基、特に好ましくは、メチル基、エチル基が挙げられる。 In the general formula (3), R 5 is preferably a monovalent hydrocarbon group having 1 to 3 carbon atoms, particularly preferably 1 to 2 carbon atoms. Examples of the monovalent hydrocarbon group represented by R 5 include an alkyl group such as a methyl group, an ethyl group, a propyl group, and a butyl group, preferably a methyl group, an ethyl group, and a propyl group, and particularly preferably a methyl group. Group and ethyl group.
一般式(3)で示される3官能性シラン化合物としては、例えば、メチルトリメトキシシラン、メチルトリエトキシシラン、エチルトリメトキシシラン、エチルトリエトキシシラン、n−プロピルトリメトキシシラン、n−プロピルトリエトキシシラン、イソプロピルトリメトキシシラン、イソプロピルトリエトキシシラン、ブチルトリメトキシシラン、ブチルトリエトキシシラン、ヘキシルトリメトキシシラン、トリフルオロプロピルトリメトキシシラン、ヘプタデカフルオロデシルトリメトキシシラン等のトリアルコキシシラン等、好ましくは、メチルトリメトキシシラン、メチルトリエトキシシラン、エチルトリメトキシシラン、エチルトリエトキシシラン、より好ましくは、メチルトリメトキシシラン、メチルトリエトキシシラン、又は、これらの部分加水分解縮合生成物が挙げられる。 Examples of the trifunctional silane compound represented by the general formula (3) include methyltrimethoxysilane, methyltriethoxysilane, ethyltrimethoxysilane, ethyltriethoxysilane, n-propyltrimethoxysilane, and n-propyltriethoxy. Trialkoxysilanes such as silane, isopropyltrimethoxysilane, isopropyltriethoxysilane, butyltrimethoxysilane, butyltriethoxysilane, hexyltrimethoxysilane, trifluoropropyltrimethoxysilane, heptadecafluorodecyltrimethoxysilane, etc., preferably , Methyltrimethoxysilane, methyltriethoxysilane, ethyltrimethoxysilane, ethyltriethoxysilane, more preferably methyltrimethoxysilane, methyltriethoxysilane, , These partial hydrolysis-condensation product thereof.
一般式(3)で示される3官能性シラン化合物の添加量は、使用された親水性球状シリカ微粒子のSiO2単位1モル当り0.001〜1モル、好ましくは0.01〜0.1モル、特に好ましくは0.01〜0.05モルである。 The addition amount of the trifunctional silane compound represented by the general formula (3) is 0.001 to 1 mol, preferably 0.01 to 0.1 mol, particularly preferably 0.01 to 0.1 mol per mol of SiO 2 unit of the used hydrophilic spherical silica fine particles. 0.05 mole.
−疎水性球状シリカ微粒子の表面トリオルガノシリル化処理((C)工程)−
(C)工程は、上記(B)工程で得られた第1次疎水性球状シリカ微粒子の表面にR6 3SiO1/2単位[式中、R6は同一又は異なり、置換又は非置換の、炭素原子数1〜6の1価炭化水素基である]を導入する工程、即ち、第2段階の疎水化処理を行う工程である。例えば、前記疎水性球状シリカ微粒子水分散液の分散媒を水からケトン系溶媒に変換し、疎水性球状シリカ微粒子ケトン系溶媒分散液を得ることと、該疎水性球状シリカ微粒子ケトン系溶媒分散液に一般式(4):
-Surface triorganosilylation treatment of hydrophobic spherical silica fine particles (step (C))-
In the step (C), R 6 3 SiO 1/2 unit [wherein R 6 is the same or different and substituted or unsubstituted on the surface of the primary hydrophobic spherical silica fine particles obtained in the step (B) , Which is a monovalent hydrocarbon group having 1 to 6 carbon atoms], that is, a step of performing a second-stage hydrophobization treatment. For example, the dispersion medium of the hydrophobic spherical silica fine particle aqueous dispersion is converted from water to a ketone solvent to obtain a hydrophobic spherical silica fine particle ketone solvent dispersion, and the hydrophobic spherical silica fine particle ketone solvent dispersion In general formula (4):
R6 3SiNHSiR6 3 (4)
[式中、R6は同一又は異なり、上記と同じである]
で示されるシラザン化合物、もしくは、一般式(5):
R6 3SiX (5)
[式中、R6は同一又は異なり、上記と同じであり、XはOH基又は加水分解性基である]
で示される1官能性シラン化合物、又は、これらの混合物を添加し、前記疎水性球状シリカ微粒子表面に残存する反応性基をトリオルガノシリル化することを有してなる工程である。
R 6 3 SiNHSiR 6 3 (4)
[Wherein R 6 is the same or different and is the same as above]
Or a silazane compound represented by the general formula (5):
R 6 3 SiX (5)
[Wherein R 6 is the same or different and is the same as above, and X is an OH group or a hydrolyzable group]
A monofunctional silane compound represented by the formula (1) or a mixture thereof is added, and the reactive group remaining on the surface of the hydrophobic spherical silica fine particles is triorganosilylated.
上記一般式(4)及び(5)中、R6は、好ましくは炭素原子数1〜4、特に好ましくは1〜2の1価炭化水素基である。R6で表される1価炭化水素基としては、例えば、メチル基、エチル基、プロピル基、イソプロピル基、ブチル基等のアルキル基等、好ましくは、メチル基、エチル基、プロピル基、特に好ましくは、メチル基、エチル基が挙げられる。また、これらの1価炭化水素基の水素原子の一部又は全部が、フッ素原子、塩素原子、臭素原子等のハロゲン原子、好ましくは、フッ素原子で置換されていてもよい。 In the general formulas (4) and (5), R 6 is preferably a monovalent hydrocarbon group having 1 to 4 carbon atoms, particularly preferably 1 to 2 carbon atoms. The monovalent hydrocarbon group represented by R 6 is, for example, an alkyl group such as a methyl group, an ethyl group, a propyl group, an isopropyl group, or a butyl group, preferably a methyl group, an ethyl group, or a propyl group. Includes a methyl group and an ethyl group. Further, some or all of the hydrogen atoms of these monovalent hydrocarbon groups may be substituted with halogen atoms such as fluorine atom, chlorine atom, bromine atom, preferably fluorine atom.
Xで表される加水分解性基としては、例えば、塩素原子、メトキシ基、エトキシ基等のアルコキシ基、アミノ基、アセトキシ基、プロピオニルオキシ基等のアシルオキシ基等、好ましくは、アルコキシ基、アミノ基、特に好ましくは、アルコキシ基が挙げられる。 Examples of the hydrolyzable group represented by X include an alkoxy group such as a chlorine atom, a methoxy group and an ethoxy group, an acyloxy group such as an amino group, an acetoxy group and a propionyloxy group, preferably an alkoxy group and an amino group. Particularly preferred is an alkoxy group.
球状シリカ微粒子水性分散液又は混合溶媒分散液の分散媒を、水又は混合溶媒からケトン系溶媒に変換するには、該分散液にケトン系溶媒を添加し、前記混合物から水又は混合溶媒を留去する操作(必要に応じてこの操作を繰り返す)により行うことができる。 In order to convert the dispersion medium of the spherical silica fine particle aqueous dispersion or the mixed solvent dispersion from water or a mixed solvent to a ketone solvent, a ketone solvent is added to the dispersion and water or the mixed solvent is distilled from the mixture. It can be performed by the operation to leave (repeat this operation as necessary).
このとき添加されるケトン系溶媒の量は、前記球状シリカ微粒子水性分散液中の親水性球状シリカ微粒子に対して質量比で0.5〜5倍量、好ましくは2〜5倍量、特に好ましくは3〜4倍量である。このケトン系溶媒としては、例えば、メチルエチルケトン、メチルイソブチルケトン、アセチルアセトン等、好ましくはメチルイソブチルケトンが挙げられる。 The amount of the ketone solvent added at this time is 0.5 to 5 times, preferably 2 to 5 times, particularly preferably 3 by mass ratio with respect to the hydrophilic spherical silica fine particles in the spherical silica fine particle aqueous dispersion. ~ 4 times the amount. Examples of the ketone solvent include methyl ethyl ketone, methyl isobutyl ketone, acetyl acetone, and preferably methyl isobutyl ketone.
一般式(4)で示されるシラザン化合物としては、例えば、ヘキサメチルジシラザン、ヘキサエチルジシラザン等、好ましくはヘキサメチルジシラザンが挙げられる。一般式(5)で示される1官能性シラン化合物としては、例えば、トリメチルシラノール、トリエチルシラノール等のモノシラノール化合物、トリメチルクロロシラン、トリエチルクロロシラン等のモノクロロシラン、トリメチルメトキシシラン、トリメチルエトキシシラン等のモノアルコキシシラン、トリメチルシリルジメチルアミン、トリメチルシリルジエチルアミン等のモノアミノシラン、トリメチルアセトキシシラン等のモノアシルオキシシラン、好ましくは、トリメチルシラノール、トリメチルメトキシシラン、トリメチルシリルジエチルアミン、特に好ましくは、トリメチルシラノール、トリメチルメトキシシランが挙げられる。 Examples of the silazane compound represented by the general formula (4) include hexamethyldisilazane and hexaethyldisilazane, preferably hexamethyldisilazane. Examples of the monofunctional silane compound represented by the general formula (5) include monosilanol compounds such as trimethylsilanol and triethylsilanol, monochlorosilanes such as trimethylchlorosilane and triethylchlorosilane, and monoalkoxy such as trimethylmethoxysilane and trimethylethoxysilane. Examples thereof include monoaminosilanes such as silane, trimethylsilyldimethylamine and trimethylsilyldiethylamine, and monoacyloxysilanes such as trimethylacetoxysilane, preferably trimethylsilanol, trimethylmethoxysilane and trimethylsilyldiethylamine, particularly preferably trimethylsilanol and trimethylmethoxysilane.
これらの使用量は、使用した親水性球状シリカ微粒子のSiO2単位1モルに対して0.05〜0.5モル、好ましくは0.1〜0.3モル、特に好ましくは0.15〜0.25モルである。 These are used in an amount of 0.05 to 0.5 mol, preferably 0.1 to 0.3 mol, particularly preferably 0.15 to 0.25 mol, based on 1 mol of SiO 2 units of the hydrophilic spherical silica fine particles used.
上記疎水性球状シリカ微粒子は、常法によって粉体として得てもよいし、シラザンとの反応後に有機化合物を添加して分散体として得てもよい。 The hydrophobic spherical silica fine particles may be obtained as a powder by a conventional method, or may be obtained as a dispersion by adding an organic compound after reaction with silazane.
<疎水性球状シリカ微粒子からなるトナー外添剤>
本発明の疎水性球状シリカ微粒子は、トナー外添剤等として有用である。該微粒子からなるトナー外添剤(以下、単に「微粒子」とも言う)のトナーに対する配合量は、トナー100質量部に対して、通常0.01〜20質量部であり、好ましくは0.1〜5質量部、特に好ましくは1〜2質量部である。この配合量が少なすぎると、トナーへの付着量が少なく十分な流動性が得られず、多すぎるとトナーの帯電性に悪影響を及ぼす。
<Toner external additive comprising hydrophobic spherical silica fine particles>
The hydrophobic spherical silica fine particles of the present invention are useful as an external toner additive. The amount of the toner external additive composed of the fine particles (hereinafter also simply referred to as “fine particles”) to the toner is usually 0.01 to 20 parts by mass, preferably 0.1 to 5 parts by mass with respect to 100 parts by mass of the toner. Especially preferably, it is 1-2 mass parts. If the blending amount is too small, the adhesion amount to the toner is small and sufficient fluidity cannot be obtained, and if it is too large, the chargeability of the toner is adversely affected.
該微粒子のトナー粒子表面への付着状態は、単に機械的に付着していても、ゆるく固着されていてもよい。また、この付着した微粒子は、トナー粒子の表面全体を覆っていても、一部だけを覆っていてもよい。さらに、該微粒子は、その一部が凝集体を形成してトナー粒子の表面を覆っていてもよいが、単層粒子の状態で覆っていることが好ましい。 The adhesion state of the fine particles to the toner particle surface may be merely mechanically adhered or may be loosely fixed. The adhered fine particles may cover the entire surface of the toner particles or only a part thereof. Further, the fine particles may partially form aggregates and cover the surface of the toner particles, but are preferably covered in the form of single-layer particles.
本発明の微粒子を適用可能なトナー粒子としては、結着樹脂と着色剤とを主成分として含有する公知のトナー粒子等が挙げられ、必要に応じて、さらに帯電制御剤等が添加されていてもよい。 Examples of toner particles to which the fine particles of the present invention can be applied include known toner particles containing a binder resin and a colorant as main components, and a charge control agent or the like is further added as necessary. Also good.
本発明の微粒子からなるトナー外添剤を添加されたトナーは、例えば、電子写真法、静電記録法等により、静電荷像を現像するために使用される静電荷像現像用等に使用される。前記トナーは、一成分現像剤として使用することができるが、それをキャリアと混合し、二成分現像剤として使用することもできる。二成分現像剤として使用する場合には、上記トナー外添剤を予めトナー粒子に添加せず、トナーとキャリアとの混合時に添加してトナーの表面被覆を行ってもよい。該キャリアとしては、公知のもの、例えば、フェライト、鉄粉等、又は、それらの表面に樹脂コーティングされたもの等が使用できる。 The toner to which the toner external additive comprising fine particles of the present invention is added is used, for example, for developing an electrostatic image used for developing an electrostatic image by electrophotography, electrostatic recording method or the like. The The toner can be used as a one-component developer, but it can also be used as a two-component developer by mixing it with a carrier. When used as a two-component developer, the toner external coating may not be added to the toner particles in advance, but may be added when the toner and the carrier are mixed to cover the surface of the toner. As the carrier, known ones, for example, ferrite, iron powder, etc., or those coated on the surface with resin can be used.
さらに、本発明者らは、本発明に係る疎水性球状シリカ微粒子からなるトナー外添剤は、所望の特性に加えて、トナーに対して環境に依存しない帯電性を付与するものとなることを見出した。 Furthermore, the present inventors have found that the toner external additive comprising the hydrophobic spherical silica fine particles according to the present invention imparts charging properties independent of the environment to the toner in addition to the desired characteristics. I found it.
以下、実施例及び比較例を用いて本発明を具体的に説明する。なお、下記の実施例は、本発明を何ら制限するものではない。 Hereinafter, the present invention will be specifically described with reference to Examples and Comparative Examples. The following examples do not limit the present invention.
<実施例1>
[疎水性球状シリカ微粒子の合成]
−(I)親水性球状シリカ微粒子の合成((A)工程)−
攪拌機と、滴下ロートと、温度計とを備えた3リットルのガラス製反応器にメタノール623.7gと、水41.4gと、28質量%アンモニア水49.8gとを入れて混合した。この溶液を35℃となるように調整し、攪拌しながらテトラメトキシシラン1163.7g(7.65モル)及び5.4質量%アンモニア水418.1gを同時に添加し始め、テトラメトキシシランは6時間かけて、アンモニア水は5時間かけて、それぞれを滴下した。それらの滴下が終了した後も、さらに0.5時間攪拌を継続して加水分解を行うことにより、親水性球状シリカ微粒子の懸濁液を得た。次いで、ガラス製反応器にエステルアダプターと冷却管とを取り付け、前記懸濁液を60〜70℃に加熱してメタノール1200gを留去し、その後、水1200gを添加した。次いで、懸濁液が100℃になるまでメタノール水300g留去、水300g添加を3回繰り返し、さらにメタノール水300gを留去し、親水性球状シリカ微粒子の水懸濁液を得た。このとき、ガスクロマトグラフ分析によると水懸濁液中の水含有量は99.9質量%であった。
<Example 1>
[Synthesis of hydrophobic spherical silica fine particles]
-(I) Synthesis of hydrophilic spherical silica fine particles (step (A))-
In a 3 liter glass reactor equipped with a stirrer, a dropping funnel, and a thermometer, 623.7 g of methanol, 41.4 g of water, and 49.8 g of 28% by mass ammonia water were mixed. The solution was adjusted to 35 ° C. and 1163.7 g (7.65 mol) of tetramethoxysilane and 418.1 g of 5.4 mass% ammonia water were begun to be added at the same time while stirring. Each was added dropwise over 5 hours. Even after the completion of the dropwise addition, the suspension was further stirred for 0.5 hour to carry out hydrolysis to obtain a suspension of hydrophilic spherical silica fine particles. Next, an ester adapter and a condenser tube were attached to a glass reactor, and the suspension was heated to 60 to 70 ° C. to distill off 1200 g of methanol, and then 1200 g of water was added. Then, 300 g of methanol water was distilled off and the addition of 300 g of water was repeated three times until the suspension reached 100 ° C., and 300 g of methanol water was further distilled off to obtain an aqueous suspension of hydrophilic spherical silica fine particles. At this time, according to gas chromatographic analysis, the water content in the water suspension was 99.9% by mass.
−(II)親水性球状シリカ微粒子表面の第1段階疎水化処理((B)工程)−
前記の工程(A)で得られた水懸濁液に室温でメチルトリメトキシシラン11.6g(0.085モル)を0.5時間かけて滴下し、滴下後も12時間攪拌を継続した。こうして、シリカ微粒子表面を第1段階の疎水化処理することにより、第1次疎水性球状シリカ微粒子水分散液を得た。
-(II) Hydrophobic spherical silica fine particle surface first-stage hydrophobization treatment (step (B))-
11.6 g (0.085 mol) of methyltrimethoxysilane was added dropwise to the aqueous suspension obtained in the above step (A) at room temperature over 0.5 hours, and stirring was continued for 12 hours after the addition. Thus, the first hydrophobic spherical silica fine particle aqueous dispersion was obtained by subjecting the surface of the silica fine particle to the first-stage hydrophobic treatment.
−(III)第1次疎水性球状シリカ微粒子表面の第2段階疎水化処理(トリオルガノシリル化処理)((C)工程)−
前記工程(B)により得られた分散液にメチルイソブチルケトン1440gを添加した後、この分散液を80〜110℃に加熱することにより、水1794gを10時間かけて留去した。得られた分散液に、室温において、ヘキサメチルジシラザン150g(0.93モル)を添加した後、この分散液を110℃に加熱し、3時間反応させることにより、分散液中のシリカ微粒子をトリメチルシリル化した。次いで、この分散液中の溶媒を80℃、減圧下(6650Pa)で留去することにより、疎水性球状シリカ微粒子475gを粉体として得た。
-(III) Second-stage hydrophobization treatment (triorganosilylation treatment) on the surface of primary hydrophobic spherical silica fine particles (step (C))-
After adding 1440 g of methyl isobutyl ketone to the dispersion obtained in the step (B), 1794 g of water was distilled off over 10 hours by heating the dispersion to 80 to 110 ° C. After adding 150 g (0.93 mol) of hexamethyldisilazane to the resulting dispersion at room temperature, this dispersion is heated to 110 ° C. and reacted for 3 hours to trimethylsilylate the silica fine particles in the dispersion. did. Subsequently, the solvent in this dispersion was distilled off at 80 ° C. under reduced pressure (6650 Pa) to obtain 475 g of hydrophobic spherical silica fine particles as a powder.
上記の工程(A)〜(C)により得られた最終的な疎水性球状シリカ微粒子について、下記の測定方法1〜3に従って、アルコキシ基含量、粒子径、及び形状の測定を行った。なお、得られた結果を表1に示す。 With respect to the final hydrophobic spherical silica fine particles obtained by the above steps (A) to (C), the alkoxy group content, particle diameter, and shape were measured according to the following measurement methods 1 to 3. The obtained results are shown in Table 1.
・測定方法1:疎水性球状シリカ微粒子のアルコキシ基含量
シリカ微粒子5gに1N水酸化カリウム−イソプロピルアルコール溶液10gを添加し、70℃で1時間加熱しシリカの分解を行い、その後、液体分を蒸留して取る。この留分をガスクロマトグラフ分析し含有されるメタノール量を定量することで、シリカ微粒子に含有されるアルコキシ基量を定量する。
Measurement method 1: Alkoxy group content of hydrophobic spherical silica fine particles 10 g of 1N potassium hydroxide-isopropyl alcohol solution is added to 5 g of silica fine particles and heated at 70 ° C. for 1 hour to decompose the silica, and then the liquid is distilled. Take it. The fraction of the alkoxy group contained in the silica fine particles is quantified by gas chromatographic analysis of this fraction and quantifying the amount of methanol contained.
・測定方法2:疎水性球状シリカ微粒子の粒子径測定
メタノールにシリカ微粒子を、0.5質量%となるように添加し、10分間超音波にかけることにより、該微粒子を分散させた。このように処理した微粒子の粒度分布を、レーザー回折散乱式粒度分布測定装置(堀場製作所製、商品名:LA910)により測定し、その体積基準メジアン径を粒子径とした。なお、メジアン径とは粒径分布を累積分布として表したときの累積50%に相当する粒子径である。
Measurement method 2: Measurement of particle diameter of hydrophobic spherical silica fine particles Silica fine particles were added to methanol so as to be 0.5 mass%, and the fine particles were dispersed by applying ultrasonic waves for 10 minutes. The particle size distribution of the fine particles treated in this way was measured by a laser diffraction / scattering particle size distribution analyzer (trade name: LA910, manufactured by Horiba, Ltd.), and the volume-based median diameter was defined as the particle size. The median diameter is a particle diameter corresponding to 50% cumulative when the particle size distribution is expressed as a cumulative distribution.
・測定方法3:疎水性球状シリカ微粒子の形状測定
電子顕微鏡(日立製作所製、商品名:S-4700型、倍率:10万倍)によって観察を行い、形状を確認した。「球状」であるとは、前述したように、粒子を二次元に投影したときの円形度が0.8〜1の範囲にあることを意味する。
Measurement method 3: Shape measurement of hydrophobic spherical silica fine particles The shape was confirmed by observation with an electron microscope (manufactured by Hitachi, trade name: S-4700 type, magnification: 100,000 times). “Spherical” means that the degree of circularity when the particles are projected two-dimensionally is in the range of 0.8 to 1, as described above.
[外添剤混合トナーの作製]
ガラス転移温度Tg60℃、軟化点110℃であるポリエステル樹脂96質量部と、着色剤(住友カラー(株)製、商品名:カーミン6BC)4質量部とを、溶融混練、粉砕及び分級することにより、平均粒径7μmのトナーを得た。このトナー40gに上記表面処理球状疎水性シリカ微粒子1gをサンプルミルにより混合し、外添剤混合トナーとした。これを用いて、下記の測定方法4に従って、トナー流動性を測定した。なお、得られた結果を表1に示す。
[Production of external additive mixed toner]
96 parts by mass of a polyester resin having a glass transition temperature T g of 60 ° C. and a softening point of 110 ° C. and 4 parts by mass of a colorant (manufactured by Sumitomo Color Co., Ltd., trade name: Carmine 6BC) are melt-kneaded, pulverized and classified. As a result, a toner having an average particle diameter of 7 μm was obtained. 40 g of this toner was mixed with 1 g of the above surface-treated spherical hydrophobic silica fine particles by a sample mill to obtain an external additive mixed toner. Using this, toner fluidity was measured according to the following measurement method 4. The obtained results are shown in Table 1.
・測定方法4:トナー流動性の測定
トナーの流動性は、粉体流動性分析装置FT−4(シスメックス(株)製)を用いて測定した。この装置の測定原理を説明する。垂直に置かれた筒状容器に粉体を充填し、該粉体中を垂直な軸棒の先端に設けられた二枚の回転翼(ブレード)を回転させながら一定の距離(高さH1からH2まで)下降させる。このときに粉体から受ける力をトルク成分と荷重成分とに分けてを測定することにより、ブレードがH1からH2まで下降するのに伴うそれぞれの仕事量(エネルギー)を求め、次いで両者のトータルエネルギー量を求める。こうして測定されたトータルエネルギー量が小さいほど粉体の流動性が良好であることを意味するので、粉体流動性の指標として使用する。
Measurement method 4: Measurement of toner fluidity The fluidity of the toner was measured using a powder fluidity analyzer FT-4 (manufactured by Sysmex Corporation). The measurement principle of this apparatus will be described. A cylindrical container placed vertically is filled with powder, and while rotating two rotating blades (blades) provided at the tip of a vertical shaft rod in the powder, a certain distance (from height H1) Down to H2. By measuring the force received from the powder separately for the torque component and the load component, the respective work (energy) associated with the blade descending from H1 to H2 is obtained, and then the total energy of both Find the amount. The smaller the total energy measured in this way, the better the fluidity of the powder, so it is used as an index of powder fluidity.
安定性試験、流速試験、通気試験、及び圧縮試験を行なった。
・・条件:
容器:安定性、流速及び通気の試験では、容積120ml、内径80mm、長さ60mmのガラス製円筒型容器を使用した。圧縮試験では容積25ml、内径25mm、長さ52.5mmのガラス製円筒型容器を使用した。容器の下部から空気を導入することができるように構成されている。
ブレード:円筒型容器内の中央に鉛直に装入されるステンレス製の軸棒の先端に水平に対向する形で二枚取り付けられている。ブレードは、容積120mlの容器の場合は直径48mmのものを使用し、容積25mlの容器の場合には直径23.5mlのものを使用する。
H1からH2までの長さ:容積120mlの容器の場合は50mmであり、容積25mlの容器の場合には47.5mmである。
A stability test, a flow rate test, an aeration test, and a compression test were performed.
··conditions:
Container: In the stability, flow rate, and ventilation tests, a glass cylindrical container having a volume of 120 ml, an inner diameter of 80 mm, and a length of 60 mm was used. In the compression test, a glass cylindrical container having a volume of 25 ml, an inner diameter of 25 mm, and a length of 52.5 mm was used. It is comprised so that air can be introduce | transduced from the lower part of a container.
Blades: Two blades are mounted horizontally facing the tip of a stainless steel shaft rod inserted vertically into the center of the cylindrical container. A blade with a diameter of 48 mm is used for a container with a volume of 120 ml, and a blade with a diameter of 23.5 ml is used for a container with a volume of 25 ml.
Length from H1 to H2: 50 mm for a container with a volume of 120 ml and 47.5 mm for a container with a volume of 25 ml.
・・安定性試験:上記のようにして、測定容器に充填した粉体を静置した状態から流動させた場合の粉体流動特性をみる。ブレード先端の回転速度を100mm/secの条件とし、トータルエネルギー量を7回連続して測定する。7回目のトータルエネルギー量(最も安定した状態であるので基本流動性エネルギーと称される)を表1に示した。小さいほど安定性が高い。 .. Stability test: As described above, the powder flow characteristics when the powder filled in the measurement container is allowed to flow from a static state are observed. Measure the total energy amount 7 times continuously with the blade tip rotation speed as 100mm / sec. Table 7 shows the total energy amount for the seventh time (referred to as basic fluidity energy because it is the most stable state). The smaller the value, the higher the stability.
・・流速試験:流速の変化に対する粉体流動特性をみる。ブレード先端の回転速度を10mm/secで測定した際のトータルエネルギー量を表1に示した。小さいほど流動性が高い。 ・ ・ Velocity test: The powder flow characteristics with respect to the change of the flow velocity are observed. Table 1 shows the total energy when the rotational speed of the blade tip was measured at 10 mm / sec. The smaller the value, the higher the fluidity.
・・通気試験:通気量に応じた粉体流動特性をみる。ブレード先端の回転速度を100mm/secとし、容器下部から導入する空気の通気量を0mm/secから0.1mm/secづつ増加させ0.5mm/secまでの6段階で別々に順序に測定し、最小の通気量(0mm/sec)及び最大の通気量(0.5mm/sec)でのトータルエネルギー量を表1に示した。小さいほど空気が関与する状態での粉体流動性が高い。 ・ ・ Aeration test: Check the powder flow characteristics according to the aeration rate. The rotation speed of the blade tip is set to 100 mm / sec, the air flow rate introduced from the bottom of the container is increased from 0 mm / sec in increments of 0.1 mm / sec, and measured separately in six steps from 0.5 mm / sec to the smallest Table 1 shows the total energy amount at the air flow rate (0 mm / sec) and the maximum air flow rate (0.5 mm / sec). The smaller the value, the higher the powder fluidity when air is involved.
・・圧縮試験は、圧縮に対する粉体流動特性をみるものである。粉体にピストンを介して加重を加えて10Nにて加圧して圧縮した後、ブレード先端の回転速度を100mm/secとして測定しトータルエネルギー量を求めた。結果を表1に示した。小さいほど粉体が圧縮を受けた場合の粉体流動性が高い。 ・ ・ The compression test examines the powder flow characteristics with respect to compression. After applying a weight to the powder through a piston and pressurizing and compressing with 10 N, the rotational speed of the blade tip was measured at 100 mm / sec to determine the total energy amount. The results are shown in Table 1. The smaller the powder, the higher the powder fluidity when the powder is compressed.
[現像剤の調製]
上で調製した外添剤混合トナー5質量部と、平均粒径85μmのフェライトコアにパーフルオロアルキルアクリレート樹脂及びアクリル樹脂をポリブレンドしたポリマーでコーティングしたキャリア95質量部とを混合して、現像剤を調製した。この現像剤を用いて、下記の測定方法5及び6に従って、トナー帯電量及び感光体へのトナー付着について測定した。なお、得られた結果を表1に示す。
[Preparation of developer]
5 parts by weight of the external additive mixed toner prepared above and 95 parts by weight of a carrier coated with a polymer obtained by polyblending a perfluoroalkyl acrylate resin and an acrylic resin on a ferrite core having an average particle diameter of 85 μm are mixed together to prepare a developer. Was prepared. Using this developer, the toner charge amount and toner adhesion to the photoreceptor were measured according to the following measurement methods 5 and 6. The obtained results are shown in Table 1.
・測定方法5:トナー帯電量の測定
上記現像剤を高温高湿(30℃、90%RH)又は低温低湿(10℃、15%RH)の条件下に1日放置した後、振とう機により30秒間混合して、摩擦帯電を行った。それぞれの試料の帯電量を、同一条件下で、ブローオフ粉体帯電量測定装置(東芝ケミカル(株)製、商品名:TB-200型)を用いて測定した。上記2つの条件におけるトナー帯電量の差を求めることにより、該トナーの環境依存性について評価した。
・ Measurement method 5: Measurement of toner charge amount The developer is left in a high temperature and high humidity (30 ° C, 90% RH) or low temperature and low humidity (10 ° C, 15% RH) condition for 1 day, and then shaken. Mixing for 30 seconds, triboelectric charging was performed. The charge amount of each sample was measured using a blow-off powder charge amount measuring device (trade name: TB-200, manufactured by Toshiba Chemical Corporation) under the same conditions. By determining the difference in toner charge amount under the above two conditions, the environmental dependency of the toner was evaluated.
・測定方法5:感光体へのトナー付着測定
上記現像剤を有機感光体が備えられた二成分改造現像機に入れ、30000枚のプリントテストを行った。該感光体へのトナーの付着は、全ベタ画像での白抜けとして感知できる。 白抜けの程度を次の基準で評価した。
白抜け10個以上/cm2:多い
白抜け1〜9個/cm2:少ない
白抜け0個/cm2:なし
Measurement method 5: Measurement of toner adhesion to the photoconductor The above developer was put into a two-component modified developer equipped with an organic photoconductor, and a print test of 30,000 sheets was performed. The adhesion of toner to the photoreceptor can be detected as white spots in all solid images. The degree of white spots was evaluated according to the following criteria.
White spots more than 10 / cm 2: many white spots 1 to 9 / cm 2: little white spots 0 / cm 2: None
<実施例2>
実施例1において、工程(A)で親水性球状シリカ微粒子の懸濁液を60〜90℃に加熱してメタノール水420g留去、水250g添加を4回繰り返し、さらに90〜98℃に加熱しメタノール351gを留去し、親水性球状シリカ微粒子の水懸濁液(水含有量は98.8質量%)を得たこと以外は同様にして、疎水性球状シリカ微粒子479gを乾燥粉体として得た。この疎水性球状シリカ微粒子を用いて実施例1と同様に測定した。この結果を表1に示す。
<Example 2>
In Example 1, in step (A), the suspension of hydrophilic spherical silica fine particles was heated to 60 to 90 ° C., 420 g of methanol water was distilled off, and 250 g of water was added four times, and further heated to 90 to 98 ° C. In the same manner as above except that 351 g of methanol was distilled off to obtain an aqueous suspension of hydrophilic spherical silica fine particles (water content was 98.8% by mass), 479 g of hydrophobic spherical silica fine particles were obtained as a dry powder. Measurement was performed in the same manner as in Example 1 using the hydrophobic spherical silica fine particles. The results are shown in Table 1.
<比較例1>
実施例1において、工程(A)で親水性球状シリカ微粒子の懸濁液を60〜70℃に加熱してメタノール1132gを留去し、その後、水1200gを添加して、次いでさらに70〜90℃に加熱しメタノール273gを留去し、親水性球状シリカ微粒子の水性懸濁液(水含有量は87.2質量%)を得たこと以外は同様にして、疎水性球状シリカ微粒子479gを乾燥粉体として得た。この疎水性球状シリカ微粒子を用いて、実施例1と同様に評価した。この結果を表1に示す。
<Comparative Example 1>
In Example 1, in step (A), the suspension of hydrophilic spherical silica fine particles was heated to 60 to 70 ° C. to distill off 1132 g of methanol, then 1200 g of water was added, and then 70 to 90 ° C. In the same manner except that 273 g of methanol was distilled off to obtain an aqueous suspension of hydrophilic spherical silica fine particles (water content was 87.2% by mass), 479 g of hydrophobic spherical silica fine particles were used as a dry powder. Obtained. Evaluation was performed in the same manner as in Example 1 using the hydrophobic spherical silica fine particles. The results are shown in Table 1.
<比較例2>
実施例1において、工程(A)で得られた親水性球状シリカ微粒子の水懸濁液に、室温でヘキサメチルジシラザン240gを添加し、120℃に加熱し、3時間反応させることにより、シリカ微粒子をトリメチルシリル化した。次いで、水を120℃、減圧下(6650Pa)で留去して、疎水性球状シリカ微粒子465gを乾燥粉体として得た。この疎水性球状シリカ微粒子を用いて、実施例1と同様に評価した。この結果を表1に示す。
<Comparative example 2>
In Example 1, 240 g of hexamethyldisilazane was added to the aqueous suspension of the hydrophilic spherical silica fine particles obtained in the step (A) at room temperature, heated to 120 ° C., and reacted for 3 hours. The fine particles were trimethylsilylated. Subsequently, water was distilled off at 120 ° C. under reduced pressure (6650 Pa) to obtain 465 g of hydrophobic spherical silica fine particles as a dry powder. Evaluation was performed in the same manner as in Example 1 using the hydrophobic spherical silica fine particles. The results are shown in Table 1.
<比較例3>
比較例1における工程(A)で得られた親水性球状シリカ微粒子の水性懸濁液に、室温でヘキサメチルジシラザン240gを添加し、120℃に加熱し、3時間反応させることにより、シリカ微粒子をトリメチルシリル化した。次いで、メタノールと水との混合物を80℃、減圧下(6650Pa)で留去して、疎水性球状シリカ微粒子463gを乾燥粉体として得た。この疎水性球状シリカ微粒子を用いて、実施例1と同様に評価した。この結果を表1に示す。
<Comparative Example 3>
By adding 240 g of hexamethyldisilazane at room temperature to the aqueous suspension of the hydrophilic spherical silica fine particles obtained in the step (A) in Comparative Example 1, the silica fine particles are heated at 120 ° C. and reacted for 3 hours. Was trimethylsilylated. Next, the mixture of methanol and water was distilled off at 80 ° C. under reduced pressure (6650 Pa) to obtain 463 g of hydrophobic spherical silica fine particles as a dry powder. Evaluation was performed in the same manner as in Example 1 using the hydrophobic spherical silica fine particles. The results are shown in Table 1.
<比較例4>
実施例1において、工程(B)であるメチルトリメトキシシランを用いたシリカ微粒子の表面疎水処理工程を省略し、工程(A)で得られた親水性球状シリカ微粒子の水懸濁液を直接工程(C)に供し、メチルイソブチルケトン1440gを添加した後に、80〜110℃に加熱し、メタノールと水との混合物820gとを6時間かけて留去したところ、親水性球状シリカ微粒子の分散体が凝固した。
<Comparative Example 4>
In Example 1, the surface hydrophobic treatment step of silica fine particles using methyltrimethoxysilane as the step (B) is omitted, and the aqueous suspension of hydrophilic spherical silica fine particles obtained in the step (A) is directly processed. In (C), after adding 1440 g of methyl isobutyl ketone, heating to 80-110 ° C. and distilling off 820 g of a mixture of methanol and water over 6 hours, a dispersion of hydrophilic spherical silica fine particles was obtained. It solidified.
<比較例5>
実施例1において、工程(B)であるメチルトリメトキシシランを用いたシリカ微粒子の表面疎水処理工程を省略し、比較例1における工程(A)で得られた親水性球状シリカ微粒子の水性懸濁液を直接工程(C)に供し、メチルイソブチルケトン1440gを添加した後に、80〜110℃に加熱し、メタノールと水との混合物820gとを6時間かけて留去したところ、親水性球状シリカ微粒子の分散体が凝固した。
<Comparative Example 5>
In Example 1, the surface hydrophobic treatment step of silica fine particles using methyltrimethoxysilane as the step (B) was omitted, and the aqueous suspension of hydrophilic spherical silica fine particles obtained in the step (A) in Comparative Example 1 was omitted. The solution was directly subjected to step (C), 1440 g of methyl isobutyl ketone was added, heated to 80 to 110 ° C., and 820 g of a mixture of methanol and water was distilled off over 6 hours. Hydrophilic spherical silica fine particles The dispersion was solidified.
<比較例6>
攪拌機と温度計とを備えた0.3リットルのガラス製反応器に爆燃法シリカ(商品名:SO-C1、アドマテクス社製)100gを仕込み、純水1gを攪拌下で添加し、密閉後、さらに60℃で10時間攪拌した。次いで、室温まで冷却した後、ヘキサメチルジシラザン2gを攪拌下で添加し、密閉後、さらに24時間攪拌した。120℃に昇温し、窒素ガスを通気しながら残存原料及び生成したアンモニアを除去し、疎水性球状シリカ微粒子100gを得た。この疎水性球状シリカ微粒子を用いて、実施例1と同様に評価した。この結果を表2に示す。
<Comparative Example 6>
A 0.3 liter glass reactor equipped with a stirrer and a thermometer was charged with 100 g of deflagration silica (trade name: SO-C1, manufactured by Admatechs), 1 g of pure water was added with stirring, and after sealing, another 60 Stir at 0 ° C. for 10 hours. Subsequently, after cooling to room temperature, 2 g of hexamethyldisilazane was added with stirring, and after sealing, the mixture was further stirred for 24 hours. The temperature was raised to 120 ° C., and the remaining raw material and generated ammonia were removed while ventilating nitrogen gas to obtain 100 g of hydrophobic spherical silica fine particles. Evaluation was performed in the same manner as in Example 1 using the hydrophobic spherical silica fine particles. The results are shown in Table 2.
<比較例7>
実施例1で調製した疎水性球状シリカ微粒子の代わりに、ヒュームドシリカを疎水化処理した疎水性シリカ(商品名:アエロジルR972、日本アエロジル(株)製、1次粒子の凝集体、ジメチルジクロロシラン処理品)を用いて、実施例1と同様に評価した。この結果を表2に示す。
<Comparative Example 7>
Hydrophobic silica obtained by hydrophobizing fumed silica instead of the hydrophobic spherical silica particles prepared in Example 1 (trade name: Aerosil R972, manufactured by Nippon Aerosil Co., Ltd., primary particle aggregate, dimethyldichlorosilane Evaluation was performed in the same manner as in Example 1 using the processed product. The results are shown in Table 2.
<比較例8>
実施例1で調製した疎水性球状シリカ微粒子の代わりに、沈降法シリカ表面を疎水化処理した疎水性シリカ(商品名:ニプシルSS50F、日本シリカ(株)製、1次粒子の凝集体)を用いて、実施例1と同様に評価した。この結果を表2に示す。
<Comparative Example 8>
Instead of the hydrophobic spherical silica fine particles prepared in Example 1, hydrophobic silica (trade name: Nipsil SS50F, manufactured by Nippon Silica Co., Ltd., primary particle aggregate) whose surface was subjected to a hydrophobization treatment was used. Then, evaluation was made in the same manner as in Example 1. The results are shown in Table 2.
(注)
(1)親水性球状シリカ微粒子の水懸濁液中((A)工程)
(2)7回目
(3)ブレードスピード 10mm/s
(4)通気量 0mm/s
(5)通気量 0.5mm/s
(6)加圧 10N
(note)
(1) In aqueous suspension of hydrophilic spherical silica fine particles (step (A))
(2) 7th time
(3) Blade speed 10mm / s
(4) Ventilation rate 0mm / s
(5) Ventilation rate 0.5mm / s
(6) Pressure 10N
(注)
(1)親水性球状シリカ微粒子の水懸濁液中((A)工程)
(2)7回目
(3)ブレードスピード 10mm/s
(4)通気量 0mm/s
(5)通気量 0.5mm/s
(6)加圧 10N
<評価>
実施例1及び実施例2では、本発明の条件を満たす疎水性球状シリカ微粒子が得られたため、目的とする諸特性を有するトナー外添剤が得られた。
(note)
(1) In aqueous suspension of hydrophilic spherical silica fine particles (step (A))
(2) 7th time
(3) Blade speed 10mm / s
(4) Ventilation rate 0mm / s
(5) Ventilation rate 0.5mm / s
(6) Pressure 10N
<Evaluation>
In Examples 1 and 2, hydrophobic spherical silica fine particles satisfying the conditions of the present invention were obtained, and thus a toner external additive having desired characteristics was obtained.
比較例1では、工程(A)において、親水性球状シリカ微粒子の水性懸濁液中の水含有量が90質量%未満であるために、得られる疎水性球状シリカ微粒子は、アルコキシ基含量の点で本発明の条件を満たさず、その結果、該微粒子からなるトナー外添剤は、良好な流動性をトナーに付与することができなかった。 In Comparative Example 1, since the water content in the aqueous suspension of hydrophilic spherical silica fine particles in the step (A) is less than 90% by mass, the obtained hydrophobic spherical silica fine particles have an alkoxy group content. Thus, the toner external additive composed of the fine particles could not give good fluidity to the toner.
比較例2では、工程(A)で得られた親水性球状シリカ微粒子を本発明の方法で必須である第一段階の疎水化処理を行わず、高い水含有量の水懸濁液中でトリメチルシリル化したものである。得られ処理シリカ微粒子は、疎水化処理が不完全で凝集したため不定形となった。該微粒子からなるトナー外添剤は、良好な流動性及び環境状態に依存しない帯電性をトナーに付与することができず、さらに、感光体へのトナー付着等が生じるものであった。 In Comparative Example 2, the hydrophilic spherical silica fine particles obtained in the step (A) were not subjected to the first-stage hydrophobization treatment essential in the method of the present invention, and trimethylsilyl in an aqueous suspension having a high water content. It has become. The resulting treated silica fine particles became amorphous due to incomplete hydrophobization treatment and aggregation. The toner external additive composed of the fine particles cannot impart good fluidity and chargeability independent of environmental conditions to the toner, and further causes toner adhesion to the photoreceptor.
比較例3では、工程(A)で得られた親水性球状シリカ微粒子を水含有量90質量%未満の水懸濁液中で、本発明の方法で必須である第一段階の疎水化処理に該当しないトリメチルシリル化処理をしたものである。得られた疎水性球状シリカ微粒子は、アルコキシ基含量の点で本発明の条件を満たさなかった。その結果、該微粒子からなるトナー外添剤は、良好な流動性をトナーに付与することができず、さらに、感光体へのトナー付着等が生じるものであった。 In Comparative Example 3, the hydrophilic spherical silica fine particles obtained in the step (A) were subjected to a first-stage hydrophobization treatment essential in the method of the present invention in an aqueous suspension having a water content of less than 90% by mass. A trimethylsilylation treatment not applicable. The obtained hydrophobic spherical silica fine particles did not satisfy the conditions of the present invention in terms of alkoxy group content. As a result, the toner external additive composed of the fine particles cannot impart good fluidity to the toner, and further causes toner adhesion to the photoreceptor.
比較例4では、本発明の方法で必須である第一段階の疎水化処理を行わず、第二段階の疎水化処理を直接行った例である。親水性球状シリカ微粒子の分散体が該疎水化処理中に凝固した。 Comparative Example 4 is an example in which the first-stage hydrophobic treatment, which is essential in the method of the present invention, is not performed, and the second-stage hydrophobic treatment is directly performed. A dispersion of hydrophilic spherical silica fine particles coagulated during the hydrophobic treatment.
比較例5では、工程(B)であるメチルトリメトキシシランを用いたシリカ微粒子の表面疎水化処理工程を省略し、比較例1における工程(A)で得られた親水性球状シリカ微粒子の水性懸濁液(低い含水量)を直接工程(C)に供しものであるが、親水性球状シリカ微粒子の分散体が工程(C)中に凝固した。 In Comparative Example 5, the surface hydrophobization treatment step of silica fine particles using methyltrimethoxysilane as the step (B) is omitted, and the aqueous suspension of hydrophilic spherical silica fine particles obtained in the step (A) in Comparative Example 1 is omitted. The suspension (low water content) was directly subjected to step (C), but the dispersion of hydrophilic spherical silica fine particles coagulated during step (C).
比較例6では、爆燃法のシリカをトリメチルシリル化したものであるが、得られる疎水性球状シリカ微粒子は、ゾルゲル法シリカでない点及びR4SiO3/2単位で疎水化処理されていない点で本発明の条件を満たさず、その結果、該微粒子からなるトナー外添剤は、良好な流動性及び環境状態に依存しない帯電性をトナーに付与することができず、さらに、感光体へのトナー付着等が生じるものであった。 In Comparative Example 6, deflagration method silica was trimethylsilylated, but the obtained hydrophobic spherical silica fine particles were not sol-gel method silica and were not hydrophobized with R 4 SiO 3/2 units. The toner external additive composed of the fine particles does not satisfy the conditions of the invention, and as a result, it cannot impart good fluidity and chargeability independent of the environmental state to the toner, and furthermore, the toner adheres to the photoreceptor. Etc. occurred.
比較例7及び8では、それぞれ、ヒュームドシリカ、沈降法シリカを疎水化処理したものであるが、これらの疎水性シリカ微粒子は、凝集したため不定形となった点、ゾルゲル法シリカでない点及びR4SiO3/2単位で疎水化処理されていない点で本発明の条件を満たさず、その結果、該微粒子からなるトナー外添剤は、良好な流動性及び環境状態に依存しない帯電性をトナーに付与することができず、さらに、感光体へのトナー付着等が生じるものであった。 In Comparative Examples 7 and 8, respectively, fumed silica and precipitated silica were hydrophobized, but these hydrophobic silica fine particles were agglomerated due to aggregation, were not sol-gel silica, and R 4 The toner external additive comprising fine particles does not satisfy the conditions of the present invention in that it is not hydrophobized with SiO 3/2 units. As a result, the toner external additive comprising the fine particles has good fluidity and chargeability independent of environmental conditions. In addition, toner adheres to the photosensitive member.
Claims (8)
Si(OR1)4 (1)
[式中、R1は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示されるテトラヒドロカルビルオキシシラン化合物及びその部分加水分解縮合生成物からなる群から選ばれる少なくとも1種の化合物を加水分解及び縮合することによって得られたSiO2単位からなる親水性球状シリカ微粒子の表面にR4SiO3/2単位(式中、R4は置換又は非置換の炭素原子数1〜20の1価炭化水素基である)を導入する工程と、次いでR6 3SiO1/2単位(式中、R6は同一又は異なり、置換又は非置換の炭素原子数1〜20の1価炭化水素基である)を導入する工程とを含む疎水化処理をして得られた疎水性球状シリカ微粒子であって、ヒドロカルビルオキシ基含量が1000ppm以下であり、粒子径が0.01〜5μmである疎水性球状シリカ微粒子。 General formula (1):
Si (OR 1 ) 4 (1)
[Wherein R 1 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
Surface of hydrophilic spherical silica fine particles comprising SiO 2 units obtained by hydrolyzing and condensing at least one compound selected from the group consisting of tetrahydrocarbyloxysilane compounds and partial hydrolysis-condensation products thereof A step of introducing R 4 SiO 3/2 units (wherein R 4 is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms), and then R 6 3 SiO 1/2 units (Wherein R 6 is the same or different and is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 20 carbon atoms) and a hydrophobic sphere obtained by hydrophobization treatment Hydrophobic spherical silica fine particles having a hydrocarbyloxy group content of 1000 ppm or less and a particle size of 0.01 to 5 μm, which are silica fine particles.
Si(OR1)4 (1)
[式中、R1は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示される4官能性シラン化合物及びその部分加水分解縮合生成物からなる群から選ばれる少なくとも1種の化合物を、塩基性物質の存在下で親水性有機溶媒と水との混合媒体中で加水分解、縮合して、親水性球状シリカ微粒子を生成させる工程と、
(a−2)溶媒として用いられた前記混合媒体から親水性有機溶媒を除去して媒体を水に置換して、水の含有量が90質量%以上である親水性球状シリカ微粒子の水分散液を得る工程と、
(B)前記親水性球状シリカ微粒子水分散液中の親水性球状シリカ微粒子の表面にR4SiO3/2単位[式中、R4は置換又は非置換の、炭素原子数1〜20の1価炭化水素基である]を導入し、第一次疎水性球状シリカ微粒子を得る工程と、
(C)得られた第一次疎水性球状シリカ微粒子の表面にR6 3SiO1/2単位[式中、R6は同一又は異なり、置換又は非置換の、炭素原子数1〜6の1価炭化水素基である]を導入して第二次疎水性シリカ微粒子を得る工程と、
を有する請求項1に記載の疎水性球状シリカ微粒子の製造方法。 (A) (a-1) General formula (1):
Si (OR 1 ) 4 (1)
[Wherein R 1 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
Hydrolysis of at least one compound selected from the group consisting of a tetrafunctional silane compound and a partial hydrolysis-condensation product thereof in a mixed medium of a hydrophilic organic solvent and water in the presence of a basic substance Condensing to produce hydrophilic spherical silica fine particles;
(A-2) An aqueous dispersion of hydrophilic spherical silica fine particles having a water content of 90% by mass or more by removing the hydrophilic organic solvent from the mixed medium used as the solvent and replacing the medium with water. Obtaining
(B) R 4 SiO 3/2 unit on the surface of the hydrophilic spherical silica fine particles in the hydrophilic spherical silica fine particle aqueous dispersion [wherein R 4 is a substituted or unsubstituted 1 to 1 carbon atom having 1 to 20 carbon atoms. Is a monovalent hydrocarbon group] to obtain primary hydrophobic spherical silica fine particles,
(C) R 6 3 SiO 1/2 unit on the surface of the obtained primary hydrophobic spherical silica fine particles [wherein R 6 is the same or different and is substituted or unsubstituted, 1 to 6 carbon atoms. Is a valent hydrocarbon group] to obtain secondary hydrophobic silica fine particles,
The manufacturing method of the hydrophobic spherical silica fine particle of Claim 1 which has these.
R3OH (2)
[式中、R3は炭素原子数1〜6の1価炭化水素基である]
で示されるアルコール溶媒である請求項2に係る製造方法。 The hydrophilic organic solvent has the general formula (2):
R 3 OH (2)
[Wherein R 3 is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
The production method according to claim 2, which is an alcohol solvent represented by the formula:
R4Si(OR5)3 (3)
[式中、R4は上記と同じであり、R5は同一又は異なり、炭素原子数1〜6の1価炭化水素基である]
で示される3官能性シラン化合物もしくはその部分加水分解縮合生成物又はこれらの混合物を添加して、前記親水性球状シリカ微粒子の表面を処理し、第1次疎水性球状シリカ微粒子の水分散液を得ることを含む請求項2〜4のいずれか1項に係る製造方法。 In the step (B), an aqueous dispersion of the hydrophilic spherical silica fine particles is added to the general formula (3):
R 4 Si (OR 5 ) 3 (3)
[Wherein, R 4 is the same as above, and R 5 is the same or different and is a monovalent hydrocarbon group having 1 to 6 carbon atoms]
The surface of the hydrophilic spherical silica fine particles is treated by adding a trifunctional silane compound represented by the formula (1) or a partially hydrolyzed condensation product thereof, or a mixture thereof, and an aqueous dispersion of primary hydrophobic spherical silica fine particles is obtained. The manufacturing method which concerns on any one of Claims 2-4 including obtaining.
R6 3SiNHSiR6 3 (4)
[式中、R6は同一又は異なり、置換又は非置換の、炭素原子数1〜6の1価炭化水素基である]
で示されるシラザン化合物、もしくは、一般式(5):
R6 3SiX (5)
[式中、R6は上記と同じであり、XはOH基又は加水分解性基である]
で示される1官能性シラン化合物、又は、これらの混合物を添加し、前記第一次疎水性球状シリカ微粒子の表面に残存する反応性基をトリオルガノシリル化することと、を含む請求項2〜5のいずれか1項に係る製造方法。 The step (C) converts the dispersion medium of the aqueous dispersion of the primary hydrophobic spherical silica fine particles into a ketone solvent to obtain a ketone solvent dispersion of the primary hydrophobic spherical silica fine particles; In the ketone solvent dispersion of the primary hydrophobic spherical silica fine particles, the general formula (4):
R 6 3 SiNHSiR 6 3 (4)
[Wherein R 6 is the same or different and is a substituted or unsubstituted monovalent hydrocarbon group having 1 to 6 carbon atoms]
Or a silazane compound represented by the general formula (5):
R 6 3 SiX (5)
[Wherein R 6 is the same as above, and X is an OH group or a hydrolyzable group]
Adding a monofunctional silane compound represented by the formula (1) or a mixture thereof to triorganosilylate reactive groups remaining on the surface of the primary hydrophobic spherical silica fine particles. The manufacturing method according to any one of 5.
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