JP3048255B2 - Inorganic composite particles and method for producing the same - Google Patents
Inorganic composite particles and method for producing the sameInfo
- Publication number
- JP3048255B2 JP3048255B2 JP3140723A JP14072391A JP3048255B2 JP 3048255 B2 JP3048255 B2 JP 3048255B2 JP 3140723 A JP3140723 A JP 3140723A JP 14072391 A JP14072391 A JP 14072391A JP 3048255 B2 JP3048255 B2 JP 3048255B2
- Authority
- JP
- Japan
- Prior art keywords
- particles
- inorganic
- fine particles
- pores
- porous inorganic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Landscapes
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
- Paper (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、新規な無機複合粒子に
関する。詳しくは、板状結晶の集合体よりなる多孔質無
機粒子の細孔に無機微粒子の凝集体が固定されてなる、
微細孔の容積が著しく大きい無機複合粒子である。The present invention relates to a novel inorganic composite particle. Specifically, an aggregate of inorganic fine particles is fixed to the pores of the porous inorganic particles formed of an aggregate of plate-like crystals,
It is an inorganic composite particle having a remarkably large micropore volume.
【0002】[0002]
【従来の技術】一般に、塩基性炭酸マグネシウム、珪酸
カルシウム等の板状結晶の集合体よりなる多孔質無機粒
子(以下、単に多孔質無機粒子ともいう)は、ある程度
の細孔容積を有しながらも液体の吸着速度が遅く、また
液体の保持力が弱いことにより、種々の用途において問
題を生じていた。例えば、該粒子を紙内填用の填料、コ
ート材用の填料等に使用した場合は、インクの吸収速度
が遅いため、印字に滲みが生じるという問題を有する。
この現象は、上記多孔質無機粒子の細孔直径200オン
グストローム以下の微細孔の細孔容積が少ないためであ
ると考えられる。2. Description of the Related Art Generally, porous inorganic particles (hereinafter simply referred to as "porous inorganic particles") composed of an aggregate of plate-like crystals such as basic magnesium carbonate and calcium silicate have a certain pore volume. However, the liquid adsorption speed is low and the liquid holding power is weak, causing problems in various applications. For example, when the particles are used as a filler for filling in paper, a filler for a coating material, or the like, there is a problem in that bleeding occurs in printing due to a low ink absorption speed.
This phenomenon is considered to be due to the small pore volume of the fine pores having a pore diameter of 200 Å or less of the porous inorganic particles.
【0003】従来、上記多孔質無機粒子の微細孔の容積
を増加させる方法として、粒子の製造条件を変える方法
が提案されているが、多孔質無機粒子の微細孔の容積を
製造条件のみで増大させるには限度があり、微細孔の容
積が十分に大きい多孔質無機粒子を得ることは困難であ
る。一方、多孔質無機粒子の一種である塩基性炭酸マグ
ネシウムの見かけ比重を上げる目的で、塩化マグネシウ
ムを炭酸化する塩基性炭酸マグネシウムの製造工程にお
いて原料の塩化マグネシウムと共に塩化カルシウムを添
加する方法も提案されている。しかしながら、かかる方
法によって製造された塩基性炭酸マグネシウムは、本発
明者らの実験によれば、その見かけ比重は増大するもの
の、細孔の内部に一次粒子径の大きい炭酸カルシウムの
結晶粒子が詰まった複合体となるために、該塩基性炭酸
マグネシウムが元来有する細孔容積が低下するばかりで
なく、目的とする微細孔の容積も殆ど増加しないものと
なる。Conventionally, as a method of increasing the volume of the fine pores of the porous inorganic particles, a method of changing the production conditions of the particles has been proposed, but the volume of the fine pores of the porous inorganic particles is increased only by the production conditions. However, it is difficult to obtain porous inorganic particles having a sufficiently large micropore volume. On the other hand, in order to increase the apparent specific gravity of basic magnesium carbonate, which is a kind of porous inorganic particles, a method of adding calcium chloride together with raw material magnesium chloride in a process of producing basic magnesium carbonate for carbonating magnesium chloride has also been proposed. ing. However, the basic magnesium carbonate produced by such a method, according to the experiments of the present inventors, although its apparent specific gravity is increased, the pores are filled with crystal particles of calcium carbonate having a large primary particle diameter inside the pores. In order to form a composite, not only the basic pore volume of the basic magnesium carbonate decreases, but also the volume of the target micropores hardly increases.
【0004】[0004]
【発明が解決しようとする課題】従って、本発明の目的
は、板状結晶の集合体よりなる多孔質無機粒子の元来有
する総細孔容積を低下させることなく、微細孔の容積が
大きい該無機粒子を提供することにある。SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a porous inorganic particle composed of an aggregate of plate-like crystals, which has a large pore volume without reducing the total pore volume inherent in the porous inorganic particle. It is to provide inorganic particles.
【0005】[0005]
【課題を達成するための手段】本発明者らは、かかる目
的を達成すべく鋭意研究を重ねた結果、多孔質無機粒子
の細孔に一次粒子径が小さい無機微粒子の凝集体を固定
することにより、該細孔が無機微粒子の凝集体の存在に
より微細化すると共に、細孔容積を低下することなく微
細孔の容積を著しく増大し得ることを見いだし、本発明
を解決するに至った。Means for Achieving the Object The present inventors have made intensive studies to achieve the above object and found that an aggregate of inorganic fine particles having a small primary particle diameter is fixed in the pores of the porous inorganic particles. As a result, the present inventors have found that the pores can be made finer due to the presence of aggregates of inorganic fine particles, and that the volume of the fine pores can be significantly increased without reducing the volume of the pores.
【0006】本発明は、板状結晶の集合体よりなる多孔
質無機粒子に、該多孔質無機粒子100重量部に対し
て、一次粒子径50〜5000オングストロームの無機
微粒子の凝集体0.5〜50重量部が固定されてなる無
機複合粒子である。According to the present invention, there is provided a porous inorganic particle composed of an aggregate of plate-like crystals, and an aggregate of inorganic fine particles having a primary particle diameter of 50 to 5000 angstroms with respect to 100 parts by weight of the porous inorganic particle. 50 parts by weight are fixed inorganic composite particles.
【0007】本発明の無機複合粒子の基本骨格となる多
孔質無機粒子は、板状結晶が集合体を形成することによ
って細孔を形成した粒子である。かかる板状結晶の集合
体よりなる多孔質無機粒子は特に限定されない。多孔質
無機粒子の種類を具体的に例示すれば、塩基性炭酸マグ
ネシウム、珪酸カルシウム、珪酸マグネシウム等よりな
る板状結晶の集合体が挙げられる。また、上記多孔質無
機粒子の形状も特に制限されるものではないが、球状が
最も好ましい。[0007] The porous inorganic particles serving as the basic skeleton of the inorganic composite particles of the present invention are particles in which plate-like crystals form aggregates to form pores. The porous inorganic particles formed of such an aggregate of plate-like crystals are not particularly limited. Specific examples of the types of the porous inorganic particles include an aggregate of plate-like crystals made of basic magnesium carbonate, calcium silicate, magnesium silicate, and the like. The shape of the porous inorganic particles is not particularly limited, but a spherical shape is most preferable.
【0008】本発明の無機複合粒子は、上記多孔質無機
粒子の細孔に無機微粒子の凝集体が固定されてなる。即
ち、一次粒子径が小さい無機微粒子の凝集体を多孔質無
機粒子の細孔径を制限するように該多孔質無機粒子の細
孔内或いは、その周辺に固定することにより、該凝集粒
子による微細孔の増加と共に、この凝集粒子によって制
限された多孔性粒子にも微細孔の増加が図れるため、多
孔性無機粒子の元来有する細孔容積を著しく低下させる
ことなく、得られる無機複合粒子の微細孔の容積を増大
させることが可能となる。かかる粒子構造は、本発明に
よって初めて提案されるものであり、従来、微細孔の容
積が少なくその用途が制限されていた板状結晶の集合体
よりなる多孔質無機粒子の用途を大きく拡大するもので
ある。The inorganic composite particles of the present invention are obtained by fixing aggregates of inorganic fine particles in the pores of the porous inorganic particles. That is, by fixing the aggregate of the inorganic fine particles having a small primary particle diameter in or around the pores of the porous inorganic particles so as to limit the pore diameter of the porous inorganic particles, the fine pores by the aggregated particles are fixed. With the increase of the pores, the pores of the porous particles restricted by the aggregated particles can be increased, so that the pores of the obtained inorganic composite particles can be obtained without significantly reducing the pore volume inherent in the porous inorganic particles. Can be increased. Such a particle structure is proposed for the first time by the present invention, and greatly expands the use of porous inorganic particles composed of an aggregate of plate-like crystals, which has conventionally had a small pore volume and limited its use. It is.
【0009】本発明において、無機複合粒子を構成する
無機微粒子は、一次粒子径が50〜5000オングスト
ロームであれば制限されないが、該粒子同士の凝集力、
多孔質無機粒子への固定力を考慮した場合、表面に官能
基、特に水酸基の量が多く存在し得るものが好適であ
る。好適な無機微粒子を例示すれば、シリカ、アルミ
ナ、チタニア等が挙げられる。そのうち特に、シリカが
特に好適である。かかる無機微粒子の凝集した状態、及
び一次粒子の大きさは走査電子顕微鏡によって確認する
ことができる。In the present invention, the inorganic fine particles constituting the inorganic composite particles are not limited as long as the primary particle diameter is 50 to 5000 angstroms.
In consideration of the fixing power to the porous inorganic particles, those having a large amount of functional groups, particularly hydroxyl groups, on the surface are preferable. Examples of suitable inorganic fine particles include silica, alumina, titania and the like. Among them, silica is particularly preferred. The state of aggregation of the inorganic fine particles and the size of the primary particles can be confirmed by a scanning electron microscope.
【0010】上記無機微粒子の凝集体を多孔質無機粒子
に固定する態様は、無機微粒子によって多孔質無機粒子
の細孔を制限する態様であれば特に制限されない。具体
的には、無機微粒子の凝集体は、該多孔質無機粒子の細
孔の周辺部、或いは細孔内部に固定されることが好まし
い。かかる固定状態は、走査電子顕微鏡写真によって観
察することができる。また、上記無機微粒子の凝集体の
固定力は、水中において50Wの超音波で3分間処理し
た後、70%以上、好ましくは90%以上の無機微粒子
が残存する程度が好ましい。即ち、残存する無機微粒子
の割合が上記範囲より少ない場合は、微細孔径の大幅な
減少をを招く他、無機微粒子の離脱により使用分野にお
いて、問題を生じる場合がある。例えば、紙用填料とし
てかかる無機複合粉体を使用した場合、無機微粒子の離
脱によりスラリー粘度の増大を招くことがある。無機微
粒子の残存率が上記範囲内にある本発明の無機複合粒子
は、例えば、多孔質無機粒子が塩基性炭酸マグネシウム
の場合、25g/100cc−水の粘度が一般に10c
ps以下の値を示す。[0010] The mode of fixing the aggregate of the inorganic fine particles to the porous inorganic particles is not particularly limited as long as the inorganic fine particles limit the pores of the porous inorganic particles. Specifically, it is preferable that the aggregate of the inorganic fine particles is fixed to the periphery of the pores of the porous inorganic particles or to the inside of the pores. Such a fixed state can be observed by a scanning electron micrograph. The fixing power of the aggregate of the inorganic fine particles is preferably such that 70% or more, preferably 90% or more of the inorganic fine particles remain after being treated with 50 W ultrasonic waves in water for 3 minutes. That is, when the proportion of the remaining inorganic fine particles is smaller than the above range, the fine pore diameter is significantly reduced, and in addition, the inorganic fine particles may be separated, which may cause a problem in the field of use. For example, when such an inorganic composite powder is used as a filler for paper, detachment of inorganic fine particles may cause an increase in slurry viscosity. The inorganic composite particles of the present invention in which the residual ratio of the inorganic fine particles is in the above range, for example, when the porous inorganic particles are basic magnesium carbonate, the viscosity of 25 g / 100 cc-water is generally 10 c.
Indicates a value of ps or less.
【0011】また、本発明において、多孔質無機粒子に
対する無機微粒子の割合は、多孔質無機粒子100重量
部に対して、無機微粒子0.5〜50重量部、好ましく
は、1〜40重量部が好ましい。かかる無機微粒子の割
合が、0.5重量部より少ない場合は、得られる無機複
合粒子の微細孔の増加の効果が乏しく、逆に上記割合が
50重量部より多い場合は、得られる無機複合粒子の微
細孔径の増加効果が頭打ちとなるばかりでなく、無機微
粒子が脱離し易くなるばかりでなく、製造においても該
無機微粒子の増粘効果により操作が困難となる。In the present invention, the ratio of the inorganic fine particles to the porous inorganic particles is 0.5 to 50 parts by weight, preferably 1 to 40 parts by weight, based on 100 parts by weight of the porous inorganic particles. preferable. When the proportion of the inorganic fine particles is less than 0.5 parts by weight, the effect of increasing the micropores of the obtained inorganic composite particles is poor. Conversely, when the proportion is more than 50 parts by weight, the obtained inorganic composite particles Not only does the effect of increasing the fine pore diameter reach a plateau, but also the inorganic fine particles are easily released, and the operation becomes difficult in production due to the thickening effect of the inorganic fine particles.
【0012】本発明の無機複合粒子は、基本骨格となる
多孔質無機粒子の元来有する細孔容積を維持しながら、
特に直径200オングストローム以下の細孔の容積が多
いという特徴を有する。本発明の無機複合粒子の直径2
00オングストローム以下の細孔の容積は、該多孔質無
機粒子の種類によって異なる。例えば、多孔質無機粒子
が塩基性炭酸マグネシウムである場合、上記範囲で無機
微粒子を固定した無機複合粒子は、直径200オングス
トローム以下の細孔の容積が2cc/100g以上であ
り、また、直径2000オングストローム以下の細孔の
容積が10cc/100g以上のものが好適である。更
に、上記無機複合粒子の直径20μm以下の細孔容積
は、50〜150cc/100gが好ましい。尚、上記
の細孔容積は、水銀ポロシメーターによる測定値より求
めた値である。The inorganic composite particles of the present invention maintain the original pore volume of the porous inorganic particles serving as the basic skeleton,
In particular, it has the feature that the volume of pores having a diameter of 200 Å or less is large. Diameter 2 of inorganic composite particles of the present invention
The volume of the pores of not more than 00 Å depends on the type of the porous inorganic particles. For example, when the porous inorganic particles are basic magnesium carbonate, the inorganic composite particles in which the inorganic fine particles are fixed in the above range have a pore volume of 200 angstrom or less in diameter of 2 cc / 100 g or more, and a diameter of 2000 angstrom. The following pores having a volume of 10 cc / 100 g or more are suitable. Further, the pore volume of the inorganic composite particles having a diameter of 20 μm or less is preferably 50 to 150 cc / 100 g. In addition, the above pore volume is a value obtained from a value measured by a mercury porosimeter.
【0013】本発明の無機複合粒子の製造方法は、特に
制限されない。代表的な方法を例示すれば、板状結晶の
集合体よりなる多孔質無機粒子と一次粒子径50〜50
00オングストロームの無機微粒子とを極性溶媒中で混
合した後、該粒子を乾燥することを特徴とする無機複合
粒子の製造方法が挙げられる。The method for producing the inorganic composite particles of the present invention is not particularly limited. To illustrate a typical method, for example, porous inorganic particles composed of an aggregate of plate-like crystals and a primary particle diameter of 50 to 50
A method for producing inorganic composite particles, which comprises mixing inorganic fine particles of 00 Å in a polar solvent and then drying the particles.
【0014】上記の製造方法に使用する多孔質無機粒子
は、板状結晶の集合体よりなる前記した公知の無機粒子
が特に制限なく使用されるが、一般に、平均粒子径が1
〜100μm、好ましくは3〜50μmの粒子が好適で
ある。また、無機微粒子の固定により直径200オング
ストローム以下の細孔容積の大きい無機複合粒子を得る
ために、直径20μm以下の細孔容積が、50cc/1
00g以上、更に、直径200オングストローム以下の
細孔の容積が0.5cc/100g以上、好ましくは、
1cc/100g以上の多孔質無機粒子を使用すること
が好ましい。As the porous inorganic particles used in the above-mentioned production method, the above-mentioned known inorganic particles composed of an aggregate of plate-like crystals are used without any particular limitation.
Particles of 100100 μm, preferably 3-50 μm, are suitable. Further, in order to obtain inorganic composite particles having a large pore volume of 200 Å or less in diameter by fixing the inorganic fine particles, the pore volume of 20 μm or less is reduced to 50 cc / 1.
The volume of pores having a diameter of 200 g or more and a diameter of 200 Å or less is preferably 0.5 cc / 100 g or more,
It is preferable to use porous inorganic particles of 1 cc / 100 g or more.
【0015】直径200オングストローム以下の細孔の
容積が0.5cc/100g以上の多孔質無機粒子の製
造方法は特に制限されないが、例えば、前記塩基性炭酸
マグネシウムについて好適な製造方法を例示すれば、水
溶性マグネシウム塩と水溶性炭酸塩とを40℃以上、沸
点未満の温度で反応速度を制御しながら反応させ、上記
温度範囲で静置熟成することによって得ることができ
る。上記水溶性マグネシウム塩と水溶性炭酸塩は公知の
ものが特に制限なく使用できる。また、反応速度の制御
は、反応温度において、両者を水溶液で供給する場合
は、一方の水溶液中に存在する塩1モルに対して、他方
の水溶液を0.03〜0.5モル/分の塩の添加量となる
ように調整して添加する方法、一方の塩を水溶液とし、
該水溶液中に他方の塩を固体で供給する方法、両者を共
に固体で水中に供給する方法等が挙げられる。また、上
記反応後の静置時間は、10分以上、好ましくは2時間
以上が好適である。The method for producing porous inorganic particles having a pore volume of 200 Å or less and a volume of 0.5 cc / 100 g or more is not particularly limited. For example, a preferred production method for the basic magnesium carbonate is as follows. It can be obtained by reacting a water-soluble magnesium salt and a water-soluble carbonate at a temperature of 40 ° C. or higher and lower than the boiling point while controlling the reaction rate, and allowing the mixture to stand and ripen in the above temperature range. Known water-soluble magnesium salts and water-soluble carbonates can be used without particular limitation. Further, the reaction rate is controlled at the reaction temperature when both are supplied as aqueous solutions, with respect to 1 mol of the salt present in one aqueous solution, the other aqueous solution is added in an amount of 0.03 to 0.5 mol / min. A method of adjusting the amount of salt to be added and adding one of the salts to an aqueous solution,
A method in which the other salt is supplied as a solid into the aqueous solution, a method in which both are supplied as solid in water, and the like can be mentioned. In addition, the standing time after the above reaction is suitably 10 minutes or more, preferably 2 hours or more.
【0016】このようにして得られる塩基性炭酸マグネ
シウムは、一般に球状で上記細孔を有するもの(以下、
上記塩基性炭酸マグネシウムを球状塩基性炭酸マグネシ
ウムともいう)である。The basic magnesium carbonate thus obtained is generally spherical and has the above-mentioned pores (hereinafter referred to as “basic magnesium carbonate”).
The basic magnesium carbonate is also referred to as spherical basic magnesium carbonate).
【0017】本発明において、無機微粒子は、前記した
種類のものが特に制限なく使用される。該無機微粒子の
粒径は、一次粒子径(直径)が50〜5000オングス
トロームの範囲内で該多孔性無機粒子の細孔径より小さ
いものであれば特に制限されないが、多孔性無機粒子と
の極性溶媒中での混合により、凝集体を形成し易い粒子
径、具体的には50〜1000オングストロームの一次
粒子径を有するものが好適である。In the present invention, the above-mentioned types of inorganic fine particles are used without any particular limitation. The particle diameter of the inorganic fine particles is not particularly limited as long as the primary particle diameter (diameter) is smaller than the pore diameter of the porous inorganic particles within the range of 50 to 5000 Å. Those having a particle diameter that easily forms an aggregate by mixing in the medium, specifically, a primary particle diameter of 50 to 1000 angstroms are preferable.
【0018】本発明において、無機複合粒子は、上記多
孔性無機粒子と無機微粒子とを、極性溶媒中で混合した
後、乾燥することによって得られる。即ち、上記手段に
よって、無機微粒子の凝集体が細孔内及び細孔周辺に固
定された無機複合粒子が得られる。上記無機微粒子の固
定機構は、明らかではないが、極性溶媒中での混合によ
って分散された無機微粒子が多孔性無機粒子の細孔内或
いは、細孔の周辺で凝集し、この状態で該多孔質無機粒
子に無機微粒子が付着したまま乾燥することにより、互
いの無機粒子の表面に存在する水酸基の脱水縮合等によ
り、無機微粒子の凝集体が多孔質無機粒子の細孔内或い
は、細孔の周辺に固定されるものと考えられる。In the present invention, the inorganic composite particles are obtained by mixing the porous inorganic particles and the inorganic fine particles in a polar solvent and then drying. That is, by the above-described means, an inorganic composite particle in which an aggregate of inorganic fine particles is fixed in and around the pore is obtained. Although the fixing mechanism of the inorganic fine particles is not clear, the inorganic fine particles dispersed by mixing in the polar solvent are aggregated in or around the pores of the porous inorganic particles, and in this state, the porous By drying while the inorganic fine particles are adhered to the inorganic particles, the aggregates of the inorganic fine particles are formed in the pores of the porous inorganic particles or in the vicinity of the pores due to dehydration condensation of hydroxyl groups present on the surfaces of the inorganic particles. It is thought that it is fixed to.
【0019】上記方法において、極性溶媒としては、
水、アルコール、水−アルコール混合溶媒等が挙げられ
る。そのうち、水又は水−アルコール混合溶媒が最も好
ましい。また、無機微粒子は、極性溶媒中で十分に分散
した状態で多孔質無機粒子と混合することが、該無機微
粒子の固定力を高めると共に、微細孔の形成を効果的に
行うために好ましい。例えば、無機微粒子として、シリ
カを使用する場合は、表面にシラノール基が少ない乾式
シリカを原料として使用することにより、該乾式シリカ
は、多孔質無機粒子と共に極性溶媒中に供給した直後は
表面のシラノール基が少ないために、該多孔性無機粒子
の細孔内に取り込まれ易く、取り込まれた後に、シラノ
ール基が増大して凝集を効率よく起こすことが可能であ
る。In the above method, the polar solvent includes
Examples thereof include water, alcohol, and a mixed solvent of water and alcohol. Among them, water or a mixed solvent of water and alcohol is most preferred. Further, it is preferable that the inorganic fine particles are sufficiently dispersed in a polar solvent and mixed with the porous inorganic particles in order to increase the fixing force of the inorganic fine particles and effectively form the fine pores. For example, when silica is used as the inorganic fine particles, by using dry silica having a small amount of silanol groups on the surface as a raw material, the dry silica is mixed with the porous inorganic particles into the polar solvent immediately after the supply of the silica to the polar solvent. Since the number of groups is small, it is easy to be taken into the pores of the porous inorganic particles, and after being taken in, the silanol groups increase and aggregation can be efficiently caused.
【0020】極性溶媒中における多孔質無機粒子及び無
機微粒子との濃度は特に制限されないが、一般に、得ら
れる無機複合粒子における多孔質無機粒子と無機微粒子
との割合となるように調整することが好ましい。また、
その極性溶媒中での濃度は、合計が、一般に10〜40
g/100ccとなるように調整することが好ましい。
また、多孔質無機粒子と無機微粒子との混合割合は、目
的とする無機複合粒子の組成、即ち、多孔質無機粒子1
00重量部に対して、無機微粒子0.5〜50重量部、
好ましくは、1〜40重量部の割合が好適である。The concentration of the porous inorganic particles and the inorganic fine particles in the polar solvent is not particularly limited, but it is generally preferable to adjust the ratio of the porous inorganic particles to the inorganic fine particles in the obtained inorganic composite particles. . Also,
The concentration in the polar solvent is generally from 10 to 40
g / 100 cc is preferably adjusted.
Further, the mixing ratio of the porous inorganic particles and the inorganic fine particles depends on the composition of the target inorganic composite particles, that is, the porous inorganic particles 1
With respect to 00 parts by weight, 0.5 to 50 parts by weight of inorganic fine particles,
Preferably, a ratio of 1 to 40 parts by weight is suitable.
【0021】上記の混合後、複合粒子の乾燥方法は特に
制限されない。例えば、静置乾燥、気流乾燥等の乾燥方
法が挙げられる。After the mixing, the method for drying the composite particles is not particularly limited. For example, drying methods such as standing drying and flash drying can be used.
【0022】また、本発明の無機複合粒子の他の製造方
法として、多孔質無機粒子と該多孔質無機粒子の細孔径
より小さい無機微粒子とを混合し、機械的摩擦力及び機
械的せん断力を粒子表面に加えることにより、該多孔質
無機粒子の細孔内に無定型無機粒子を固定することを特
徴とする無機複合粒子の製造方法が挙げられる。As another method for producing the inorganic composite particles of the present invention, a porous inorganic particle and an inorganic fine particle smaller than the pore diameter of the porous inorganic particle are mixed to reduce mechanical frictional force and mechanical shearing force. A method for producing inorganic composite particles, characterized in that amorphous inorganic particles are fixed in the pores of the porous inorganic particles by adding the particles to the surface of the particles.
【0023】上記方法において、機械的摩擦力及び機械
的せん断力を粒子表面に加える方法は、特に制限されな
いが、気流粉砕機等を使用し、粉砕が生じるエネルギー
量の10〜30%のエネルギー量で該気流粉砕機の運転
を行う方法が好適である。かかる方法において、無機微
粒子の凝集体は、多孔質無機粒子の細孔周辺或いは内部
にメカノケミカル的に固定されるものと推定される。In the above method, the method of applying the mechanical frictional force and the mechanical shearing force to the particle surface is not particularly limited. The method of operating the airflow pulverizer is preferable. In such a method, it is presumed that the aggregate of the inorganic fine particles is fixed mechanochemically around or inside the pores of the porous inorganic particles.
【0024】[0024]
【効果】本発明の無機複合粒子は、多孔質無機粒子が元
来有する総細孔容積と同程度の細孔容積を有しながら、
直径200オングストローム以下、特に直径2000オ
ングストローム以下の微細孔の容積が該多孔質無機粒子
より極めて多いものである。即ち、多孔質無機粒子と無
機微粒子がそれぞれ有する上記微細孔の容積より求めら
れる理論細孔容積に対して、1.5倍以上、場合によっ
ては2倍以上という驚くべき増加効果を示す。従って、
従来よりかかる微細孔容積の不足によって用途が制限さ
れていた該多孔質無機粒子の用途を飛躍的に拡大するも
のである。[Effect] The inorganic composite particles of the present invention have the same pore volume as the total pore volume that the porous inorganic particles originally have,
The volume of micropores having a diameter of 200 Å or less, particularly 2000 Å or less, is much larger than that of the porous inorganic particles. That is, a surprising increase effect of 1.5 times or more, and in some cases, 2 times or more, of the theoretical pore volume obtained from the volumes of the fine pores of the porous inorganic particles and the inorganic fine particles is exhibited. Therefore,
The purpose of the present invention is to dramatically expand the use of the porous inorganic particles, the use of which has been conventionally limited due to the shortage of the fine pore volume.
【0025】本発明の無機複合粒子は、微細孔の容積が
極めて多いため、液体の吸収速度、或いは担持力等が要
求される分野、具体的には、紙への内填用填料、感熱紙
等の紙のコート材用填料、化粧料等の用途に好適に使用
される。Since the inorganic composite particles of the present invention have a very large volume of micropores, they are required to have a liquid absorbing speed or a supporting force, specifically, a filler for filling in paper, a thermal paper, and the like. It is suitably used for applications such as fillers for paper coating materials and cosmetics.
【0026】また、本発明の無機複合粒子は、粒子の比
表面積も大きい。即ち、多孔質無機粒子と無機微粒子が
それぞれ有する比表面積より求められる理論細孔容積を
越える比表面積を有する。これは粒子の表面活性の増大
をもたらし、上記用途において更に好ましい効果を発揮
する。The inorganic composite particles of the present invention have a large specific surface area. That is, the specific surface area exceeds the theoretical pore volume obtained from the specific surface areas of the porous inorganic particles and the inorganic fine particles. This results in an increase in the surface activity of the particles, and exerts a more favorable effect in the above-mentioned application.
【0027】[0027]
【実施例】本発明を具体的に説明するために、以下、実
施例を示すが本発明はこれらの実施例に限定されるもの
ではない。なお、実施例、比較例において、下記の測定
及び試験は以下の方法によって行った。EXAMPLES The present invention will be described below in more detail with reference to Examples, but the present invention is not limited to these Examples. In the examples and comparative examples, the following measurements and tests were performed by the following methods.
【0028】細孔容積 ポロシメーター2000(商品名:カルロエルバインス
トルメント社製:Hgによる)Pore volume Porosimeter 2000 (trade name: manufactured by Carlo Elba Instruments Inc .: based on Hg)
【0029】無機微粒子の固定力 粉体3gに水50mlを加え、超音波(50W)にて3
分間分散させる。3分後上澄み液10mlをサンプリン
グして、脱離した無機微粒子の割合(重量%)を求め
た。Fixing force of inorganic fine particles 50 g of water was added to 3 g of the powder, and 3 g of ultrasonic waves (50 W) were applied.
Disperse for a minute. Three minutes later, 10 ml of the supernatant was sampled, and the ratio (% by weight) of the detached inorganic fine particles was determined.
【0030】無機微粒子の固定状態 走査電子顕微鏡(日本電子製:JSM−5400)を使
用して観察した。Fixed state of inorganic fine particles Observed using a scanning electron microscope (JSM-5400 manufactured by JEOL Ltd.).
【0031】吸油速度 粉体試料1を、径70mm、高さ40mmの上面が開口
した容器4の上面まで入れる。次いで径65mm、全重
量100gの時計皿を試料上に置き、自重で降下させて
試料を圧縮し、15秒後に、上記時計皿の周囲に取り付
けた紐により引き上げる。そして圧縮された試料の表面
にボイル油8を0.2ml滴下し、ボイル油と試料が接
触した時から、ボイル油が試料中に全て吸収されるまで
に要した時間を測定した。Oil Absorption Rate The powder sample 1 is introduced up to the upper surface of the container 4 having a diameter of 70 mm and a height of 40 mm and having an open upper surface. Next, a watch glass having a diameter of 65 mm and a total weight of 100 g is placed on the sample, lowered by its own weight to compress the sample, and after 15 seconds, pulled up by a string attached around the watch glass. Then, 0.2 ml of boil oil 8 was dropped on the surface of the compressed sample, and the time required from when the sample was brought into contact with the boil oil to when all the boil oil was absorbed into the sample was measured.
【0032】粒子径 コールターマルチサイザー(50μmアパチャー)を使
用して測定した。The particle size was measured using a Coulter Multisizer (50 μm aperture).
【0033】一次粒子径 走査電子顕微鏡(日本電子製 JSM−5400)を使
用して測定した。The primary particle size was measured using a scanning electron microscope (JSM-5400 manufactured by JEOL Ltd.).
【0034】インキの滲み試験 市販プリンター用黒インクを、コート紙のコート層上
に、ガラス製キャピラーより1滴ずつ間隔を置いて10
点落下させ、2分後、インクによって形成された円の最
大径の平均と、インクの滲みによって出る髭の最大長さ
の平均を示した。。Bleeding test of ink A black ink for a commercial printer was placed on a coated layer of coated paper at intervals of 10 drops from a glass capillar.
Two minutes after the drop, the average of the maximum diameter of the circle formed by the ink and the average of the maximum length of the beard generated by the bleeding of the ink were shown. .
【0035】尚、コート紙は、試料の無機複合粉体20
重量部に分散剤として0.2%ポリアクリル酸ソーダ水
溶液80重量部、バインダーとして10%ポリビニルア
ルコール水溶液40重量部よりなる塗布液を固形分の塗
布量が20g/m2となるようにバーコーターにより市
販の上質紙に公知の方法でコートし、乾燥することによ
って製造した。The coated paper is made of the inorganic composite powder 20 of the sample.
A bar coater was used in which a coating solution consisting of 80 parts by weight of a 0.2% aqueous solution of sodium polyacrylate as a dispersant and 40 parts by weight of a 10% aqueous solution of polyvinyl alcohol as a binder was applied so that the coating amount of solids was 20 g / m 2. By coating a commercially available high-quality paper with a known method, followed by drying.
【0036】スラリー粘度 無機複合粒子について25g/100cc−水の粘度
(cps)を測定した。Slurry viscosity The viscosity (cps) of 25 g / 100 cc-water of the inorganic composite particles was measured.
【0037】実施例1〜3 炭酸ナトリウムと塩化マグネシウムをそれぞれ等モルで
80℃の水中に、撹拌しながら添加した。添加開始より
60秒後に撹拌を停止し、同温度に保持したまま1時間
静置した。次いで沈澱物をろ過、洗浄し、更に乾燥して
平均粒径6.2μmの球状塩基性炭酸マグネシウムを得
た。得られた塩基性炭酸マグネシウムの粒子の構造を示
す顕微鏡写真を図2に示す。上記反応で得た球状塩基性
炭酸マグネシウム及び無機微粒子として、表1に示す平
均一次粒子径を有するレオロシールQS−102(商品
名:徳山曹達(株)社製)を表1の配合に従って500
mlの水に分散後、均一スラリーとしスプレードライに
より乾燥処理し、細孔に乾式シリカが固定された塩基性
炭酸マグネシウム(無機複合粒子)を得た。得られた無
機複合粒子をそれぞれ走査電子顕微鏡、X線マイクロア
ナライザーによって観察した結果、多孔質無機粒子表面
或いは細孔内に無機微粒子が固定されていることが確認
された。また、得られた無機複合粒子についての各種試
験結果を表2に示す。また、実施例1で得られた無機複
合粒子の構造を示す顕微鏡写真を図1に示す。Examples 1 to 3 Sodium carbonate and magnesium chloride were added in equimolar amounts to water at 80 ° C. with stirring. After 60 seconds from the start of the addition, the stirring was stopped, and the mixture was allowed to stand for 1 hour while maintaining the same temperature. Next, the precipitate was filtered, washed, and dried to obtain spherical basic magnesium carbonate having an average particle size of 6.2 μm. FIG. 2 shows a micrograph showing the structure of the obtained particles of basic magnesium carbonate. As the spherical basic magnesium carbonate and the inorganic fine particles obtained by the above reaction, Leolosil QS-102 (trade name: manufactured by Tokuyama Soda Co., Ltd.) having an average primary particle diameter shown in Table 1 was added according to the formulation in Table 1 for 500.
After dispersing in water (ml), a uniform slurry was formed and dried by spray drying to obtain basic magnesium carbonate (inorganic composite particles) having dry silica fixed in the pores. As a result of observing the obtained inorganic composite particles with a scanning electron microscope and an X-ray microanalyzer, it was confirmed that the inorganic fine particles were fixed on the surface of the porous inorganic particles or in the pores. Table 2 shows various test results on the obtained inorganic composite particles. FIG. 1 shows a micrograph showing the structure of the inorganic composite particles obtained in Example 1.
【0038】実施例4 実施例1において、無機微粒子として表1に示す合成シ
リカ(15m2/g)を、表1に示す配合比で使用した
以外は同様にして無機複合粒子を製造した。得られた無
機複合粒子についての各種試験結果を表2に示す。Example 4 Inorganic composite particles were produced in the same manner as in Example 1 except that the synthetic silica (15 m 2 / g) shown in Table 1 was used as the inorganic fine particles at the compounding ratio shown in Table 1. Table 2 shows the results of various tests on the obtained inorganic composite particles.
【0039】実施例5 実施例1において、無機微粒子として表1に示すフュー
ムドチタニア(商品名Titanium Dioxid
e P−25、50m2/g:日本アエロジル(株)社
製)を使用した以外は同様にして無機複合粒子を得た。
得られた無機複合粒子をそれぞれ走査電子顕微鏡、X線
マイクロアナライザーによって観察した結果、多孔質無
機粒子表面或いは細孔内に無機微粒子が固定されている
ことが確認された。また、得られた無機複合粒子につい
ての各種試験結果を表2に示す。Example 5 In Example 1, fumed titania (trade name: Titanium Dioxide) shown in Table 1 was used as inorganic fine particles.
eP-25, 50 m 2 / g: manufactured by Nippon Aerosil Co., Ltd.), except that inorganic composite particles were obtained.
As a result of observing the obtained inorganic composite particles with a scanning electron microscope and an X-ray microanalyzer, it was confirmed that the inorganic fine particles were fixed on the surface of the porous inorganic particles or in the pores. Table 2 shows various test results on the obtained inorganic composite particles.
【0040】実施例6 実施例1において、表1に示すように、多孔質無機粒子
をフローライト(珪酸カルシウム:商品名、徳山曹達
(株)社製)に代えた以外は、実施例1と同様にして無
機複合複合粒子を製造した。得られた無機複合粒子をそ
れぞれ走査電子顕微鏡、X線マイクロアナライザーによ
って観察した結果、多孔質無機粒子表面或いは細孔内に
無機微粒子が固定されていることが確認された。また、
得られた無機複合粒子についての各種試験結果を表2に
示す。Example 6 Example 1 was the same as Example 1 except that the porous inorganic particles were changed to Florite (calcium silicate: trade name, manufactured by Tokuyama Soda Co., Ltd.) as shown in Table 1. Similarly, inorganic composite composite particles were produced. As a result of observing the obtained inorganic composite particles with a scanning electron microscope and an X-ray microanalyzer, it was confirmed that the inorganic fine particles were fixed on the surface of the porous inorganic particles or in the pores. Also,
Table 2 shows the results of various tests on the obtained inorganic composite particles.
【0041】比較例1、2 実施例1及び実施例6で用いた多孔質無機粒子を表2に
示すように、単独でスラリー化した後、スプレードライ
ヤーで乾燥して粒子を得た。得られた粒子についての各
種試験結果を表1に示す。Comparative Examples 1 and 2 As shown in Table 2, the porous inorganic particles used in Examples 1 and 6 were individually slurried and then dried with a spray dryer to obtain particles. Table 1 shows the results of various tests on the obtained particles.
【0042】比較例3 塩基性炭酸マグネシウムの懸濁液に水酸化マグネシウム
と水酸化カルシウムの懸濁液を添加しながら炭酸ガスの
吹き込みを行い、塩基性炭酸マグネシウムの細孔に炭酸
カルシウムが充填された複合粒子を製造した。得られた
複合粒子についての各種試験結果を表2に示す。Comparative Example 3 Carbon dioxide gas was blown into the suspension of basic magnesium carbonate while adding the suspension of magnesium hydroxide and calcium hydroxide to fill the pores of the basic magnesium carbonate with calcium carbonate. Composite particles were produced. Table 2 shows the results of various tests on the obtained composite particles.
【0043】[0043]
【表1】 [Table 1]
【0044】[0044]
【表2】 [Table 2]
【図1】実施例1で得られた無機複合粒子の構造を示す
電子顕微鏡写真。FIG. 1 is an electron micrograph showing the structure of the inorganic composite particles obtained in Example 1.
【図2】比較例1で得られた無機複合粒子の構造を示す
電子顕微鏡写真。FIG. 2 is an electron micrograph showing the structure of the inorganic composite particles obtained in Comparative Example 1.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C09C 3/06 C09C 3/06 D21H 19/38 D21H 1/22 B (58)調査した分野(Int.Cl.7,DB名) B01J 19/00 C01B 33/24 C01F 5/24 C08K 7/16 C08K 9/02 C09C 3/06 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 identification code FI C09C 3/06 C09C 3/06 D21H 19/38 D21H 1/22 B (58) Fields surveyed (Int.Cl. 7 , DB name) ) B01J 19/00 C01B 33/24 C01F 5/24 C08K 7/16 C08K 9/02 C09C 3/06
Claims (2)
に、該多孔質無機粒子100重量部に対して、一次粒子
径50〜5000オングストロームの無機微粒子の凝集
体0.5〜50重量部が固定されてなる無機複合粒子。1. A porous inorganic particle composed of an aggregate of plate-like crystals, and an aggregate of inorganic fine particles having a primary particle diameter of 50 to 5,000 angstroms with respect to 100 parts by weight of the porous inorganic particle, 0.5 to 50 wt. Inorganic composite particles with fixed parts.
と一次粒子径50〜5000オングストロームの無機微
粒子とを極性溶媒中で混合した後、該粒子を乾燥するこ
とを特徴とする無機複合粒子の製造方法。2. An inorganic composite, comprising mixing porous inorganic particles composed of an aggregate of plate-like crystals and inorganic fine particles having a primary particle diameter of 50 to 5000 angstroms in a polar solvent, and drying the particles. Method for producing particles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3140723A JP3048255B2 (en) | 1991-05-17 | 1991-05-17 | Inorganic composite particles and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3140723A JP3048255B2 (en) | 1991-05-17 | 1991-05-17 | Inorganic composite particles and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04341342A JPH04341342A (en) | 1992-11-27 |
| JP3048255B2 true JP3048255B2 (en) | 2000-06-05 |
Family
ID=15275212
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3140723A Expired - Fee Related JP3048255B2 (en) | 1991-05-17 | 1991-05-17 | Inorganic composite particles and method for producing the same |
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| Country | Link |
|---|---|
| JP (1) | JP3048255B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008123566A1 (en) * | 2007-04-02 | 2008-10-16 | Kyowa Chemical Industry Co., Ltd. | Carbonic acid group-containing magnesium hydroxide particle and method for producing the same |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07276788A (en) * | 1994-04-02 | 1995-10-24 | Nagoya Pulp Kk | Recording paper |
| JP2004331417A (en) * | 2003-04-30 | 2004-11-25 | Nittetsu Mining Co Ltd | Basic magnesium carbonate-coated composite particles, method for producing the same, and composition containing the same |
| CA2685544C (en) * | 2007-04-27 | 2016-08-09 | Board Of Regents Of The University Of Texas System | Porous particles and methods of making thereof |
| JP2009137838A (en) * | 2008-12-22 | 2009-06-25 | Merck Ltd | Extender pigment and method for producing the same |
-
1991
- 1991-05-17 JP JP3140723A patent/JP3048255B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008123566A1 (en) * | 2007-04-02 | 2008-10-16 | Kyowa Chemical Industry Co., Ltd. | Carbonic acid group-containing magnesium hydroxide particle and method for producing the same |
| CN101652323B (en) * | 2007-04-02 | 2011-09-07 | 协和化学工业株式会社 | Carbonic acid group-containing magnesium hydroxide particle and method for producing the same |
| JP5202514B2 (en) * | 2007-04-02 | 2013-06-05 | 協和化学工業株式会社 | Carbonate group-containing magnesium hydroxide particles and method for producing the same |
| US9346683B2 (en) | 2007-04-02 | 2016-05-24 | Kyowa Chemical Industry Co., Ltd. | Carbonate radical-containing magnesium hydroxide particle and manufacturing method thereof |
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| JPH04341342A (en) | 1992-11-27 |
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