JP2005126324A - Magnetite particle powder and its manufacturing method - Google Patents
Magnetite particle powder and its manufacturing method Download PDFInfo
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- JP2005126324A JP2005126324A JP2004344106A JP2004344106A JP2005126324A JP 2005126324 A JP2005126324 A JP 2005126324A JP 2004344106 A JP2004344106 A JP 2004344106A JP 2004344106 A JP2004344106 A JP 2004344106A JP 2005126324 A JP2005126324 A JP 2005126324A
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本発明は、黒色度、分散性、耐熱性、環境性にすぐれた塗料用黒色顔料、電子写真用磁性トナー用に適した微細なマグネタイト粒子粉末及びその製造方法に関するものである。 The present invention relates to a black pigment for paint excellent in blackness, dispersibility, heat resistance and environmental properties, fine magnetite particle powder suitable for magnetic toner for electrophotography, and a method for producing the same.
従来よりマグネタイト粒子粉末は黒色顔料として広く使用されているが、低コスト化のためにはマグネタイトの黒色度を高め分散性を向上させる必要があり耐熱性も230℃程度必要である。黒色度については粒径を細かくする必要があるが、微細にすればするほど耐熱性や分散性が低下し、平均粒径が0.3μ程度以下になると耐熱性の上限が180℃程度になり、180℃を超えるとマグネタイトの表面が酸化されて赤味を帯びてくる。 Conventionally, magnetite particle powder has been widely used as a black pigment. However, in order to reduce the cost, it is necessary to increase the blackness of the magnetite to improve dispersibility, and heat resistance is required to be about 230 ° C. As for the blackness, it is necessary to make the particle size finer, but as it becomes finer, the heat resistance and dispersibility decrease. When the average particle size is about 0.3 μm or less, the upper limit of heat resistance is about 180 ° C. When the temperature exceeds 180 ° C., the surface of the magnetite is oxidized and becomes reddish.
一方、マグネタイト粒子粉末は電子写真用の磁性トナーとしても使用されるが、周知の通りマグネタイト粒子粉末をトナー化するに当たっては、マグネタイトが高い分散性及び流動性を有し、且つ、黒色度が高く均一な帯電性を有することが必要になる。更に、トナー化時にマグネタイト粒子粉末の分散性が悪いと、トナー中のマグネタイト粒子の含有量が一定にならず、黒色のむらや磁気特性のバラツキを生じ現像性が不安定になり、カブリやトナー飛散が生ずることになる。 On the other hand, although the magnetite particle powder is also used as a magnetic toner for electrophotography, as is well known, when magnetite particle powder is converted into a toner, magnetite has high dispersibility and fluidity, and has high blackness. It is necessary to have uniform chargeability. In addition, if the dispersibility of the magnetite particle powder at the time of toner formation is poor, the content of magnetite particles in the toner will not be constant, resulting in uneven blackness and variations in magnetic properties, resulting in unstable developability, fog and toner scattering. Will occur.
マグネタイト自体の分散性については、微小な粒子は程度の差はあるが常に凝集した状態で、各粒子がそれぞれ一次粒子として単独に存在することはない。比表面積が大きくなれば、即ち、微粒子になるほど凝集作用は強くなる。しかし、良いトナーを作るためには、マグネタイト粒子を微細化させ、更に高分散化させる必要がある。又、マグネタイト粒子は程度の差こそあるが微細化するほど黒味は高くなり黒色度が向上するので、画像濃度を高めるためには、粒子を微細化させ出来る限り同一粒径でしかも粒度分布の狭いより均一な粒子に調整することが必要である。 Regarding the dispersibility of the magnetite itself, fine particles are always in an aggregated state to some extent, but each particle does not exist independently as a primary particle. As the specific surface area increases, that is, as the particles become finer, the aggregation action becomes stronger. However, in order to make a good toner, it is necessary to make magnetite particles finer and further highly dispersed. In addition, although the magnetite particles are different in degree, the blackness becomes higher and the blackness improves as the particle size is reduced. Therefore, in order to increase the image density, the particles can be made the same particle size as much as possible and the particle size distribution can be reduced. It is necessary to adjust to narrower and more uniform particles.
本発明の目的は、塗料用黒色顔料及び磁性トナー用に適した、微細で黒色度、分散性、耐熱性、環境性にすぐれたるマグネタイト粒子粉末及びその製造方法を提供することにある。 An object of the present invention is to provide a magnetite particle powder that is suitable for black pigments for paints and magnetic toners and has excellent blackness, dispersibility, heat resistance, and environmental properties, and a method for producing the same.
即ち、本発明は、塩化第一鉄水溶液に、塩化第一鉄1molに対して0.6〜1.0molの水酸化アルカリ及び0.1〜0.5molの炭酸アルカリを添加し;空気を吹き込みマグネタイトを生成させ;マグネタイトが生成したスラリーのpHを10〜13の範囲に調節し;Si化合物と塩化第ニ鉄水溶液とをスラリーに添加して、マグネタイト粒子の表面にSiとFeとを共沈させる;ことにより製造される、Si化合物の添加量がSi換算でFeに対し0.60〜2.39%であるマグネタイト粒子粉末、及びその製造方法に関する。本発明のマグネタイト粒子粉末は、以下に記載する方法によって製造される。 That is, the present invention adds 0.6 to 1.0 mol of alkali hydroxide and 0.1 to 0.5 mol of alkali carbonate to 1 mol of ferrous chloride in an aqueous ferrous chloride solution; Generate magnetite; adjust the pH of the slurry in which magnetite is generated to a range of 10 to 13; add Si compound and aqueous ferric chloride solution to the slurry, and co-precipitate Si and Fe on the surface of magnetite particles It is related with the magnetite particle powder which is manufactured by this, and the addition amount of Si compound is 0.60-2.39% with respect to Fe in Si conversion, and its manufacturing method. The magnetite particle powder of the present invention is produced by the method described below.
まず第一鉄塩水溶液に、アルカリ金属炭酸塩とアルカリ金属水酸化物の水溶液を添加し、反応温度を70〜100℃に保ちながら、酸化性ガスを通気させ多面体を呈する微細なマグネタイトを生成させ、二次反応としてアルカリ水溶液を加えてPHを10〜13の領域にしたあと水溶性Si及び/又はAl化合物と塩化第二鉄水溶液を滴下させながらマグネタイト粒子の表面にSi及び/又はAlの混合物をマグネタイト粒子表面に共沈させることによって製造する方法である。 First, an aqueous solution of alkali metal carbonate and alkali metal hydroxide is added to the ferrous salt aqueous solution, and while maintaining the reaction temperature at 70 to 100 ° C., an oxidizing gas is passed through to produce fine magnetite that exhibits a polyhedron. As a secondary reaction, an alkaline aqueous solution is added to make the pH in the range of 10 to 13, and then a mixture of Si and / or Al is added to the surface of the magnetite particles while dropping water-soluble Si and / or Al compound and ferric chloride aqueous solution. Is produced by co-precipitation on the surface of magnetite particles.
通常のマグネタイトの製造方法は、塩化第一鉄水溶液に当量の2倍以上の水酸化アルカリ水溶液を添加した後、反応温度を70〜100℃に保ちながら酸化性ガスを吹き込むことによってマグネタイトを生成させるが、この方法で得られるマグネタイト粒子粉末の粒径は0.5μ〜1.0μ程度であり、また粒度分布幅も広くなってしまう。そのために本発明は仕込み時の塩化第一鉄水溶液の仕込時の量を、通常の反応スラリー中の3mol程度と比較して、2.5mol以下、好ましくは2mol以下の低水準にまで減少させ、添加する水酸化アルカリ及び炭酸アルカリの量を塩化第一鉄1molに対して各々0.6〜1.0mol及び0.1〜0.5molとすることによって反応スラリー濃度を低くし、その結果酸素溶解量が増加して、反応バランスが良くなり、多面体を呈する微細なマグネタイトを製造することができる。このときの平均粒径は0.05μ〜0.2μ程度である。反応終了後のスラリーにアルカリを滴下させてPHを10〜13の領域とした中に、可溶性のSi化合物及び塩化第二鉄水溶液を添加することによりSiの混合物を共沈させる方法である。 The usual magnetite production method is to generate magnetite by adding an aqueous alkali hydroxide solution at least twice the equivalent to ferrous chloride aqueous solution and then blowing an oxidizing gas while maintaining the reaction temperature at 70 to 100 ° C. However, the particle size of the magnetite particle powder obtained by this method is about 0.5 to 1.0 μm, and the particle size distribution width is widened. Therefore, the present invention reduces the charged amount of the ferrous chloride aqueous solution at the time of charging to a low level of 2.5 mol or less, preferably 2 mol or less, compared with about 3 mol in the usual reaction slurry, The concentration of the alkali hydroxide and alkali carbonate to be added is 0.6 to 1.0 mol and 0.1 to 0.5 mol, respectively, with respect to 1 mol of ferrous chloride. The amount is increased, the reaction balance is improved, and a fine magnetite exhibiting a polyhedron can be produced. The average particle size at this time is about 0.05 to 0.2 μm. In this method, alkali is added dropwise to the slurry after the reaction to adjust the pH to a range of 10 to 13, and a Si mixture is coprecipitated by adding a soluble Si compound and a ferric chloride aqueous solution.
このときの平均粒径が0.15〜0.24μmであり、比表面積が14.1〜14.9m2/gであり、カサ密度が0.41〜0.43g/cm3となる。更にマグネタイト中のSi化合物の添加量はSi換算でFeに対し0.60〜2.39%であり、Si化合物の添加量が少なすぎると分散性や耐熱性に効果が少なく、多すぎるとSiの単独の沈澱物ができてしまう。耐熱性は、200℃で3時間加熱した場合の色の変化で評価される。 At this time, the average particle size is 0.15 to 0.24 μm, the specific surface area is 14.1 to 14.9 m 2 / g, and the bulk density is 0.41 to 0.43 g / cm 3 . Furthermore, the addition amount of Si compound in magnetite is 0.60 to 2.39% with respect to Fe in terms of Si. If the addition amount of Si compound is too small, the effect on dispersibility and heat resistance is small, and if too much, Si content is too large. A single precipitate is formed. The heat resistance is evaluated by a change in color when heated at 200 ° C. for 3 hours.
本発明で使用するSi化合物としては、可溶性のものもしくはコロイド状のものであれば良く、Na2SiO3,Na2SiO5等のケイ酸塩、水酸化物「例えばSi(OH)4」「例えばSiO2」が挙げられるが、特にケイ酸塩が好ましい。 The Si compound used in the present invention may be soluble or colloidal, such as silicates such as Na 2 SiO 3 and Na 2 SiO 5 , hydroxides such as “Si (OH) 4 ”, “ For example, “SiO 2 ” can be mentioned, and silicate is particularly preferable.
微細なマグネタイト粒子粉末の表面に、Si化合物の添加時のPHを10〜13の範囲とする理由はSi化合物の溶解を確実にするためである。
Si化合物及び塩化第二鉄の添加速度は1〜5mol/lに希釈した水溶液を100ml/分程度の速度で添加し、終了後30分〜60分撹拌しながら熟成をさせる事が必要である。滴下時間が短すぎると、被着状態が悪く微細な単独の結晶が析出し、遅すぎると反応時間が長くなり作業効率が悪くなる。
The reason for setting the pH at the time of addition of the Si compound to the range of 10 to 13 on the surface of the fine magnetite particle powder is to ensure the dissolution of the Si compound.
The addition rate of the Si compound and ferric chloride needs to be aged while adding an aqueous solution diluted to 1 to 5 mol / l at a rate of about 100 ml / min and stirring for 30 to 60 minutes after completion. If the dropping time is too short, the attached state is poor and fine single crystals are precipitated. If the dropping time is too slow, the reaction time becomes longer and the working efficiency becomes worse.
以下に実施例及び比較例により、本発明をさらに具体的に説明する。
(実施例1〜5)容量4lの反応器に所定量の塩化第一鉄水溶液(濃度328g/l)を仕込み、撹拌しながら水酸化ナトリウム(濃度328g/l)及び炭酸ナトリウム(濃度328g/l)を所定量添加し次いで90℃に昇温させた後、空気を3l/minの速度で吹き込み黒色の微細粒子を生成させた。この懸濁液に水酸化ナトリウム液を添加してPHを13に調節した後、水ガラスを添加し、良く撹拌した後、塩化第二鉄水溶液(濃度328g/l)を添加し、Si化合物を黒色の微粒子上に鉄と共に共沈させ、濾過、乾燥してSi化合物を含むマグネタイト粒子粉末を得た。[表1]にその詳細及び結果を示す。
Hereinafter, the present invention will be described more specifically with reference to examples and comparative examples.
(Examples 1 to 5) A predetermined amount of ferrous chloride aqueous solution (concentration 328 g / l) was charged into a reactor having a capacity of 4 l, and sodium hydroxide (concentration 328 g / l) and sodium carbonate (concentration 328 g / l) while stirring. ) Was added, and the temperature was raised to 90 ° C., and air was blown at a rate of 3 l / min to produce black fine particles. After adding sodium hydroxide solution to this suspension to adjust the pH to 13, water glass was added and stirred well, then an aqueous ferric chloride solution (concentration 328 g / l) was added, and the Si compound was added. It coprecipitated with iron on black fine particles, filtered and dried to obtain magnetite particle powder containing Si compound. The details and results are shown in [Table 1].
(比較例1〜4)実施例における反応条件の液量、撹拌速度、温度は変更せず、塩化第一鉄、水酸化ナトリウム、炭酸ナトリウム、塩化第二鉄の量を変化させ、またSi化合物の共沈を適宜省略した場合の詳細及び結果を[表1]に示す。 (Comparative Examples 1-4) The liquid amount, stirring speed, and temperature of the reaction conditions in the examples were not changed, and the amounts of ferrous chloride, sodium hydroxide, sodium carbonate, and ferric chloride were changed, and the Si compound The details and results when the coprecipitation is appropriately omitted are shown in [Table 1].
本発明による微細なマグネタイト粒子粉末は、黒色度、分散性、耐熱性、耐環境性にすぐれ、塗料用黒色顔料、及び電子写真用磁性トナーとしての良好な適性を有する。 The fine magnetite particle powder according to the present invention is excellent in blackness, dispersibility, heat resistance, and environmental resistance, and has good suitability as a black pigment for paint and a magnetic toner for electrophotography.
Claims (4)
平均粒径が0.15〜0.24μmであるマグネタイト粒子粉末の製造方法。 Adding 0.6 to 1.0 mol of alkali hydroxide and 0.1 to 0.5 mol of alkali carbonate to 1 mol of ferrous chloride to the ferrous chloride aqueous solution; blowing air to produce magnetite; The pH of the slurry in which the magnetite is generated is adjusted to a range of 10 to 13; the Si compound and the aqueous ferric chloride solution are adjusted so that the addition amount of the Si compound is 0.60 to 2.39% with respect to Fe in terms of Si. Including co-precipitation of Si and Fe on the surface of the magnetite;
The manufacturing method of the magnetite particle powder whose average particle diameter is 0.15-0.24 micrometer.
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Cited By (2)
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US7567872B2 (en) * | 2004-09-27 | 2009-07-28 | Horiba, Ltd. | Film forming condition determination method, film forming method, and film structure manufacturing method |
KR101305393B1 (en) | 2011-11-08 | 2013-09-06 | 한국과학기술연구원 | Amine functionalized mesoporous iron oxyhydroxide and method for fabricating the same |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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US7567872B2 (en) * | 2004-09-27 | 2009-07-28 | Horiba, Ltd. | Film forming condition determination method, film forming method, and film structure manufacturing method |
KR101305393B1 (en) | 2011-11-08 | 2013-09-06 | 한국과학기술연구원 | Amine functionalized mesoporous iron oxyhydroxide and method for fabricating the same |
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