JPH0891821A - Production of spherical hollow porous silica particles - Google Patents
Production of spherical hollow porous silica particlesInfo
- Publication number
- JPH0891821A JPH0891821A JP5328794A JP5328794A JPH0891821A JP H0891821 A JPH0891821 A JP H0891821A JP 5328794 A JP5328794 A JP 5328794A JP 5328794 A JP5328794 A JP 5328794A JP H0891821 A JPH0891821 A JP H0891821A
- Authority
- JP
- Japan
- Prior art keywords
- silica particles
- spherical hollow
- hollow porous
- porous silica
- added
- 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.)
- Granted
Links
Landscapes
- Manufacturing Of Micro-Capsules (AREA)
- Silicon Compounds (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、徐放性粒子、化粧品等
無機物充填剤として使用される球状中空シリカの製造法
に関するものであり、特に、ゾル・ゲル法による球状中
空多孔質シリカ粒子の製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing spherical hollow silica used as an inorganic filler for sustained release particles, cosmetics, etc., and particularly to a method for producing spherical hollow porous silica particles by the sol-gel method. The present invention relates to a manufacturing method.
【0002】[0002]
【従来の技術】中空多孔質粒子の製造法には水ガラスと
界面活性剤のベンゼン溶液からなるw/oエマルジョン
とアルカリ土類金属水溶液からw/o/wエマルジョン
を形成した後、ケイ酸塩の反応によるものがある。しか
しながら、この方法では不純物の除去が難しく、高純度
の中空多孔質粒子の製造は困難であった。2. Description of the Related Art A method for producing hollow porous particles is as follows. A w / o emulsion consisting of water glass and a benzene solution of a surfactant and a w / o / w emulsion from an alkaline earth metal aqueous solution are prepared, and then a silicate is prepared. Due to the reaction of. However, it was difficult to remove impurities by this method, and it was difficult to produce high-purity hollow porous particles.
【0003】[0003]
【発明が解決しようとする課題】従来の球状中空シリカ
粒子およびその製造方法は水ガラスを用いてw/o/w
エマルジョンを調整する方法であり、安定性、生成時間
および生成粒子の純度において問題があった。本発明は
ゾル・ゲル法を用いて部分加水分解後、乳化するという
手法で、これらの技術課題を解決しようとするものであ
る。The conventional spherical hollow silica particles and a method for producing the same are w / o / w using water glass.
It is a method of preparing an emulsion and has problems in stability, production time, and purity of produced particles. The present invention is intended to solve these technical problems by a method of emulsifying after partial hydrolysis using the sol-gel method.
【0004】[0004]
【課題を解決するための手段】本発明は、オルトケイ酸
テトラエチルに、アルコール、水および酸触媒を加えて
部分加水分解を行わせた後、フタル酸ジブチルを添加
し、この溶液を界面活性剤を含んだアンモニア水溶液中
で混合攪拌・乳化し、重縮合反応によって球状中空多孔
質シリカ粒子を製造する方法である。According to the present invention, tetraethyl orthosilicate is subjected to partial hydrolysis by adding alcohol, water and an acid catalyst, and then dibutyl phthalate is added, and this solution is treated with a surfactant. This is a method for producing spherical hollow porous silica particles by a polycondensation reaction by mixing and stirring and emulsifying in an aqueous ammonia solution containing.
【0005】本発明をさらに、詳細に説明する。オルト
ケイ酸テトラエチル(TEOS)を塩酸等の酸触媒で加
水分解すると求電子反応で反応が進行するためアルコキ
シドのアルコール基の一つが水酸基に置換すると、アル
コール基の負電荷部分の減少のため引き続く加水分解速
度は遅く、完全に加水分解することはない。その作用の
ためシリカアルコキシドには疎水性のアルコール基と親
水性の水酸基とが存在することになる。このような部分
加水分解反応を確実に進行させるためには酸触媒を用い
ることおよびTEOS1モルに対してアルコール6モ
ル、水4モル以下で反応を行わせることである。また、
1モル程度のアルコールがないと部分加水分解中に固体
が生成するために抑制剤として必要となる。最適な反応
条件としては、TEOS1モルに対してアルコール1〜
5モル、水1〜2モル程度が適当であった。The present invention will be described in more detail. When tetraethyl orthosilicate (TEOS) is hydrolyzed with an acid catalyst such as hydrochloric acid, the reaction proceeds by an electrophilic reaction, so if one of the alcohol groups of the alkoxide is replaced with a hydroxyl group, the subsequent hydrolysis will occur due to the reduction of the negatively charged portion of the alcohol group. It is slow and does not completely hydrolyze. Due to this action, the silica alkoxide has a hydrophobic alcohol group and a hydrophilic hydroxyl group. In order to surely proceed such a partial hydrolysis reaction, it is necessary to use an acid catalyst and carry out the reaction with 6 mol of alcohol and 4 mol or less of water per 1 mol of TEOS. Also,
Without about 1 mole of alcohol, a solid is produced during partial hydrolysis and is required as an inhibitor. The optimum reaction conditions are as follows: 1 mol of TEOS to 1 to 1 alcohol
About 5 mol and 1-2 mol of water were suitable.
【0006】この部分加水分解したアルコキシド溶液に
フタル酸ジブチルを添加し、アンモニア水溶液中に加え
るとともに乳化機等を用いて強く攪拌するとアルコキシ
ドの疎水基は有機溶媒側に親水基は水溶液側に向いたo
/wエマルジョンを形成する。アンモニアの塩基触媒で
部分加水分解したアルコキシドの加水分解・重縮合反応
は主にo/wエマルジョンの界面より進行する。エマル
ジョンの油滴中には添加した反応不活性なフタル酸ジブ
チルが存在するため油滴中の中心部分はシリカ粒子には
なり難い。反応終了後、これら有機溶媒は中空多孔質の
壁により簡単に洗浄除去できるため、球状中空多孔質シ
リカ粒子が製造できる。また、水溶液の攪拌速度を変え
ることで、生成粒子の平均粒径を調整でき、このように
して平均粒径2〜8μmの球状中空多孔質シリカ粒子が
製造できる。When dibutyl phthalate was added to this partially hydrolyzed alkoxide solution, and the mixture was added to an aqueous ammonia solution and stirred strongly using an emulsifier or the like, the hydrophobic groups of the alkoxide faced to the organic solvent side and the hydrophilic groups to the aqueous solution side. o
/ W form an emulsion. The hydrolysis / polycondensation reaction of the alkoxide partially hydrolyzed by the base catalyst of ammonia proceeds mainly from the interface of the o / w emulsion. Since the reaction-inactive dibutyl phthalate added is present in the oil droplets of the emulsion, the central portion of the oil droplets is unlikely to be silica particles. After the completion of the reaction, these organic solvents can be easily washed and removed by the hollow porous wall, and thus spherical hollow porous silica particles can be produced. Further, the average particle diameter of the produced particles can be adjusted by changing the stirring speed of the aqueous solution, and thus the spherical hollow porous silica particles having the average particle diameter of 2 to 8 μm can be produced.
【0007】[0007]
【実施例】オルトケイ酸テトラエチル(TEOS)20
mlを用い、部分加水分解反応はTEOS:エタノール:
水:塩酸で1:2:1:0.03のモル比で添加し、9
0分の反応時間で行ったものを用意した。これにフタル
酸ジブチル5ml加えて、0.003%の界面活性剤(Twe
en-80)を含んだ1.75%のアンモニア水溶液300ml
中に乳化機で攪拌(4000回転/分)しながら粒子生
成させる。その後、約1日静置し、メンブランフイルタ
ーで加圧濾過し、アルコール洗浄でシリカ粒子を得た。
その粒子を50℃で真空乾燥した特性を表1に示す。比
較として、通常のゾル・ゲル法により調整したシリカ粒
子(平均粒径約0.5μm)の嵩比重は0.77g/m
l、比表面積は20m2/gであり、本法のシリカ粒子
は多孔質粒子であることが分かる。また、研磨した粒子
断面を電子顕微鏡で観察した結果、このものはシリカの
球状中空粒子であることを確認した。Examples Tetraethyl orthosilicate (TEOS) 20
ml is used, and the partial hydrolysis reaction is TEOS: ethanol:
Add water: hydrochloric acid in a molar ratio of 1: 2: 1: 0.03, and
What was performed with a reaction time of 0 minutes was prepared. Add 5 ml of dibutyl phthalate and add 0.003% surfactant (Twe
300 ml of 1.75% aqueous ammonia solution containing en-80)
Particles are generated while stirring (4000 rpm) with an emulsifier. Then, the mixture was left standing for about 1 day, filtered under pressure with a membrane filter, and washed with alcohol to obtain silica particles.
The characteristics of the particles dried under vacuum at 50 ° C. are shown in Table 1. For comparison, the bulk specific gravity of silica particles (average particle size of about 0.5 μm) prepared by the usual sol-gel method is 0.77 g / m 2.
1, the specific surface area is 20 m 2 / g, and it can be seen that the silica particles of this method are porous particles. As a result of observing the cross section of the polished particles with an electron microscope, it was confirmed that these were spherical hollow silica particles.
【0008】[0008]
【表1】 [Table 1]
【0009】[0009]
【発明の効果】本発明によれば、高純度の球状中空多孔
質シリカ粒子を工業的に有利に得ることができる。Industrial Applicability According to the present invention, highly pure spherical hollow porous silica particles can be industrially advantageously obtained.
Claims (1)
ル、水および酸触媒を加えて部分加水分解を行わせた
後、フタル酸ジブチルを添加し、この溶液を界面活性剤
を含んだアンモニア水溶液中で混合攪拌し、乳化し、重
縮合反応させることにより球状中空多孔質シリカ粒子を
製造する方法。1. Tetraethyl orthosilicate is subjected to partial hydrolysis by adding alcohol, water and an acid catalyst, and then dibutyl phthalate is added, and this solution is mixed and stirred in an aqueous ammonia solution containing a surfactant. A method of producing spherical hollow porous silica particles by emulsification, polycondensation reaction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5328794A JP2590428B2 (en) | 1994-02-25 | 1994-02-25 | Method for producing spherical hollow porous silica particles |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5328794A JP2590428B2 (en) | 1994-02-25 | 1994-02-25 | Method for producing spherical hollow porous silica particles |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0891821A true JPH0891821A (en) | 1996-04-09 |
JP2590428B2 JP2590428B2 (en) | 1997-03-12 |
Family
ID=12938518
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5328794A Expired - Lifetime JP2590428B2 (en) | 1994-02-25 | 1994-02-25 | Method for producing spherical hollow porous silica particles |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2590428B2 (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR19990073271A (en) * | 1999-06-29 | 1999-10-05 | 정상옥 | Hollowness silica and manufacturing method thereof |
US6004525A (en) * | 1997-10-06 | 1999-12-21 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Hollow oxide particle and process for producing the same |
JP2000226453A (en) * | 1999-02-05 | 2000-08-15 | Jsr Corp | Hollow particle and preparation thereof |
JP2003095637A (en) * | 2001-09-25 | 2003-04-03 | Kubota Corp | Manufacturing method for spherical oxide particle |
KR100392194B1 (en) * | 2000-07-19 | 2003-07-22 | 이종협 | Preparation of Ceramic Hollow Sphere |
JP2006176343A (en) * | 2004-12-21 | 2006-07-06 | Catalysts & Chem Ind Co Ltd | Method for producing porous silica-based particle and porous silica-based particle obtained by the same |
KR100679356B1 (en) * | 2005-11-01 | 2007-02-05 | 한국화학연구원 | Hollow silica particles with controllable holes in their surfaces and manufacturing method thereof |
JP2007075660A (en) * | 2005-09-09 | 2007-03-29 | Nagoya Institute Of Technology | Method for producing hollow particle |
CN101823719A (en) * | 2010-05-18 | 2010-09-08 | 南京大学 | Two-step preparation method of hollow silica particles |
JP2013544743A (en) * | 2010-10-11 | 2013-12-19 | サントル ナスィオナル ド ラ ルシェルシュ スィアンティフィク | Method for producing foamy inorganic monolithic material and use of the material |
CN104093667A (en) * | 2012-02-13 | 2014-10-08 | 德山硅技术株式会社 | Silica balloon material having novel characteristic profiles |
JP2015506816A (en) * | 2011-12-01 | 2015-03-05 | レ イノベーションズ マタレアムLes Innovations Materium | Silica microcapsules, their manufacturing process and their use |
CN108221367A (en) * | 2018-03-21 | 2018-06-29 | 青岛纳博科环保科技有限公司 | Hydrophobic modifier for activated carbon fibre and preparation method thereof, hydrophobic active Carbon fibe and preparation method thereof |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5243881B2 (en) * | 2008-08-05 | 2013-07-24 | 花王株式会社 | Method for producing hollow silica particles |
-
1994
- 1994-02-25 JP JP5328794A patent/JP2590428B2/en not_active Expired - Lifetime
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6004525A (en) * | 1997-10-06 | 1999-12-21 | Kabushiki Kaisha Toyota Chuo Kenkyusho | Hollow oxide particle and process for producing the same |
JP2000226453A (en) * | 1999-02-05 | 2000-08-15 | Jsr Corp | Hollow particle and preparation thereof |
KR19990073271A (en) * | 1999-06-29 | 1999-10-05 | 정상옥 | Hollowness silica and manufacturing method thereof |
KR100392194B1 (en) * | 2000-07-19 | 2003-07-22 | 이종협 | Preparation of Ceramic Hollow Sphere |
JP2003095637A (en) * | 2001-09-25 | 2003-04-03 | Kubota Corp | Manufacturing method for spherical oxide particle |
US7901652B2 (en) | 2004-12-21 | 2011-03-08 | Jgc Catalysts And Chemicals Ltd. | Method of producing porous silica-based particles |
JP2006176343A (en) * | 2004-12-21 | 2006-07-06 | Catalysts & Chem Ind Co Ltd | Method for producing porous silica-based particle and porous silica-based particle obtained by the same |
JP2007075660A (en) * | 2005-09-09 | 2007-03-29 | Nagoya Institute Of Technology | Method for producing hollow particle |
KR100679356B1 (en) * | 2005-11-01 | 2007-02-05 | 한국화학연구원 | Hollow silica particles with controllable holes in their surfaces and manufacturing method thereof |
CN101823719A (en) * | 2010-05-18 | 2010-09-08 | 南京大学 | Two-step preparation method of hollow silica particles |
JP2013544743A (en) * | 2010-10-11 | 2013-12-19 | サントル ナスィオナル ド ラ ルシェルシュ スィアンティフィク | Method for producing foamy inorganic monolithic material and use of the material |
JP2015506816A (en) * | 2011-12-01 | 2015-03-05 | レ イノベーションズ マタレアムLes Innovations Materium | Silica microcapsules, their manufacturing process and their use |
CN104093667A (en) * | 2012-02-13 | 2014-10-08 | 德山硅技术株式会社 | Silica balloon material having novel characteristic profiles |
CN108221367A (en) * | 2018-03-21 | 2018-06-29 | 青岛纳博科环保科技有限公司 | Hydrophobic modifier for activated carbon fibre and preparation method thereof, hydrophobic active Carbon fibe and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
JP2590428B2 (en) | 1997-03-12 |
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Legal Events
Date | Code | Title | Description |
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EXPY | Cancellation because of completion of term |