JPH0645452B2 - Method for producing silica gel - Google Patents

Method for producing silica gel

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Publication number
JPH0645452B2
JPH0645452B2 JP61276666A JP27666686A JPH0645452B2 JP H0645452 B2 JPH0645452 B2 JP H0645452B2 JP 61276666 A JP61276666 A JP 61276666A JP 27666686 A JP27666686 A JP 27666686A JP H0645452 B2 JPH0645452 B2 JP H0645452B2
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JP
Japan
Prior art keywords
gel
reaction
silica gel
weight
parts
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 - Lifetime
Application number
JP61276666A
Other languages
Japanese (ja)
Other versions
JPS63134511A (en
Inventor
保治 山田
邦治 中吉
洋次郎 今
誠治 佐藤
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Nippon Steel Chemical and Materials Co Ltd
Original Assignee
Nippon Steel Chemical Co Ltd
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Publication date
Application filed by Nippon Steel Chemical Co Ltd filed Critical Nippon Steel Chemical Co Ltd
Priority to JP61276666A priority Critical patent/JPH0645452B2/en
Publication of JPS63134511A publication Critical patent/JPS63134511A/en
Publication of JPH0645452B2 publication Critical patent/JPH0645452B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Silicon Polymers (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、シリカゲルを製造する方法に係り、特にテト
ラアルコキシシランを原料としてシリカゲルを製造する
方法に関する。
TECHNICAL FIELD The present invention relates to a method for producing silica gel, and more particularly to a method for producing silica gel using tetraalkoxysilane as a raw material.

[従来の技術] 従来、シリカゲルを製造する方法としては、テトラメト
キシシラン、テトラエトキシシラン等のテトラアルコキ
シシランを酸の存在下に水/アルコキシシランのモル比
5以上の反応条件で加水分解することによりシラノール
を経てゾル状シリカとし、次いで静置状態に保持しなが
らゲル状物にした後、室温で数日保持乾燥してシリカゲ
ルを得る方法等が知られている。
[Prior Art] Conventionally, as a method for producing silica gel, a tetraalkoxysilane such as tetramethoxysilane or tetraethoxysilane is hydrolyzed in the presence of an acid under a reaction condition of a water / alkoxysilane molar ratio of 5 or more. There is known a method in which silica gel is obtained by passing through silanol to give a sol-like silica, which is then kept in a standing state to give a gel-like substance, which is then dried at room temperature for several days to obtain silica gel.

[発明が解決しようとする問題点] しかしながら、この従来の方法では、加水分解及び重合
によってゲル構造が完結するのに長い日数がかかり、も
しこのゲル熟成時間を省略すると、製造されたシリカゲ
ル中に未反応のアルコキシ基が残留し、このゲルを乾
燥、焼結した際に有機残基が炭化されて黒色の粒子がシ
リカゲルに混入するという問題が生じる。
[Problems to be Solved by the Invention] However, in this conventional method, it takes a long time for the gel structure to be completed by hydrolysis and polymerization, and if the gel aging time is omitted, the produced silica gel is Unreacted alkoxy groups remain, and when this gel is dried and sintered, the organic residue is carbonized and black particles are mixed into silica gel.

[問題点を解決するための手段] 本発明は、かかる観点に鑑みて創案されたもので、テト
ラアルコキシシランを加水分解してシリカゲルを製造す
る方法において、水/テトラアルコキシシランの反応モ
ル比が3以上で、かつ、還流条件下に加水分解反応及び
ゾル・ゲル反応を行うシリカゲルの製造方法である。
[Means for Solving Problems] The present invention has been conceived in view of such a viewpoint, and in a method for producing silica gel by hydrolyzing tetraalkoxysilane, the reaction molar ratio of water / tetraalkoxysilane is It is a method for producing silica gel in which the hydrolysis reaction and the sol-gel reaction are carried out under reflux conditions of 3 or more.

本発明方法で使用するテトラアルコキシシランは、一般
式Si(OR)(但し、式中Rはアルキル基を示す)
で示される化合物であり、例えばテトラメトキシシラ
ン、テトラエトキシシラン、テトライソプロポキシシラ
ン等が挙げられる。このテトラアルコキシシランは、塩
化水銀やナトリウムアルコラート等を触媒として硅素と
アルコールとを直接接触させて合成する方法、硅素の塩
化物とアルコールとの反応によって合成する方法等、如
何なる方法で製造されたものであってもよい。
The tetraalkoxysilane used in the method of the present invention is represented by the general formula Si (OR) 4 (wherein R represents an alkyl group).
And examples thereof include tetramethoxysilane, tetraethoxysilane, and tetraisopropoxysilane. This tetraalkoxysilane is produced by any method such as a method of directly contacting silicon and alcohol with mercury chloride or sodium alcoholate as a catalyst, a method of synthesizing by reaction of silicon chloride and alcohol, and the like. May be

また、テトラアルコキシシランの加水分解を促進するた
め、加水分解触媒を使用することが望ましく、このよう
な触媒としては塩酸、硫酸、炭酸ガス、アンモニア等が
挙げられる。
Further, in order to accelerate the hydrolysis of the tetraalkoxysilane, it is desirable to use a hydrolysis catalyst, and examples of such a catalyst include hydrochloric acid, sulfuric acid, carbon dioxide gas, ammonia and the like.

次に、本発明におけるテトラアルコキシシランの加水分
解反応について説明する。テトラアルコキシシランの加
水分解反応はゾル・ゲル反応として古くから知られてい
る。その反応工程は加水分解と脱水縮合とを繰返しなが
ら高分子化することにより進行するため非常に複雑にな
り、これを反応式で完全に記述することは困難である。
そこで、以下に示すような反応式を基に必要水分量を求
めるのが妥当である。
Next, the hydrolysis reaction of tetraalkoxysilane in the present invention will be described. The hydrolysis reaction of tetraalkoxysilane has long been known as a sol-gel reaction. The reaction process is extremely complicated because it proceeds by polymerizing while repeating hydrolysis and dehydration condensation, which makes it very complicated and it is difficult to describe it completely by a reaction formula.
Therefore, it is appropriate to calculate the required water content based on the reaction formula shown below.

Si(OR)+4HO →Si(OH)+4ROH (1) Si(OH)→SiO+2HO (2) Si(OR)+2HO →SiO+4ROH (3) すなわち、テトラアルコキシシランの加水分解を定量的
に進めるには、上記反応式(1)に基づき、テトラアル
コキシシラン1モルに対して4モルの水を添加する必要
があるが、反応式(2)に基づき脱水縮合で生成する水
分量を考慮すると、反応式(33)に示されるようにテ
トラアルコキシシランに対して2倍モルの水を添加すれ
ばよいことになる。
Si (OR) 4 + 4H 2 O → Si (OH) 4 + 4ROH (1) Si (OH) 4 → SiO 2 + 2H 2 O (2) Si (OR) 4 + 2H 2 O → SiO 2 + 4ROH (3) That is, tetra In order to promote the hydrolysis of alkoxysilane quantitatively, it is necessary to add 4 mol of water to 1 mol of tetraalkoxysilane based on the above reaction formula (1), but dehydration is performed based on the reaction formula (2). Considering the amount of water produced by the condensation, it is sufficient to add twice the molar amount of water to the tetraalkoxysilane as shown in the reaction formula (33).

加水分解反応は、一般には室温若しくは若干の加温下で
行われるが、本発明は良好なシリカゲルを効率的に製造
するため還流条件下に行うものである。このため、加水
分解反応及びゲル構造の完結が極めて速やかに進行す
る。
The hydrolysis reaction is generally carried out at room temperature or under slight heating, but the present invention is carried out under reflux conditions in order to efficiently produce good silica gel. Therefore, the hydrolysis reaction and the completion of the gel structure proceed extremely quickly.

水の添加量は、理論的には上記反応式(3)から明らか
なように、テトラアルコキシシラン1モルに対して2モ
ル必要であるが、添加量が少ないと加水分解反応が不十
分となり、ゲル焼成後シリカ中に炭化物を生成する。ま
た、添加量が多いと加水分解反応はうまく進行するが、
ゲル焼成時に多量の水を除去せねばならず、工業的には
有利とは言えない。従って、水の添加量は加水分解反応
を十分に行なわしめるに足る量であって、可及的に少量
であることが望ましいが、本発明においてはテトラアル
コキシシラン1モルに対し3モル以上あれば十分であ
る。3モルより少ないと非常に長い反応時間を必要とす
る。
The amount of water added is theoretically required to be 2 mol per 1 mol of tetraalkoxysilane, as is clear from the above reaction formula (3), but if the added amount is too small, the hydrolysis reaction becomes insufficient, After the gel is fired, carbide is formed in silica. Also, if the addition amount is large, the hydrolysis reaction proceeds well,
A large amount of water has to be removed during gel firing, which is not industrially advantageous. Therefore, the amount of water added is an amount sufficient to carry out the hydrolysis reaction, and it is desirable that the amount is as small as possible. It is enough. If it is less than 3 mol, a very long reaction time is required.

水の添加方法は、加水分解反応を行なうときに一括添加
する方法、所定量を幾つかに分割して適当な時間毎に添
加する方法、あるいは定量ポンプで連続的に添加する方
法等のいずれでも差支えないが、ゲル状物を効率的に得
るためには一括添加する方法が優れている。
The water may be added all at once when performing the hydrolysis reaction, by dividing a predetermined amount into several portions and adding them at appropriate intervals, or by continuously adding them with a metering pump. Although there is no problem, the method of adding all at once is superior in order to efficiently obtain the gel-like material.

加水分解反応を還流条件下で行なうことによりゲル状物
を得るまでの時間が短縮され、また、テトラアルコキシ
シラン1モルに対し3モル以上の水を添加すれば、焼成
後炭化物等のない良好なシリカが得られる。また、水の
添加量の増加に伴いゲル状物を得るまでの時間が短縮さ
れる。さらに、この加水分解反応には溶媒としてアルコ
ールを添加することが有利で、この場合アルコールの添
加量は、通常テトラアルコキシシラン1モルに対して
0.5〜1モルであるが、特にこの量である必要はな
い。アルコールの使用量を多くすればゲル状物を得るま
での時間が長くなり、逆に、アルコールの使用量を少く
すれば、加水分解反応中白濁するが、ゲル状物を得るま
での時間は短縮され、生成するシリカの物性にも特に影
響はない。従って、アルコールは全く添加しなくてもよ
いが、反応を効率的に行なわしめるために適当量加える
ことが望ましい。
By carrying out the hydrolysis reaction under reflux conditions, the time required to obtain a gel-like substance is shortened, and if 3 mol or more of water is added to 1 mol of tetraalkoxysilane, it is possible to obtain good charcoal-free materials after firing. Silica is obtained. In addition, the time required to obtain a gel-like substance is shortened as the amount of water added increases. Further, it is advantageous to add an alcohol as a solvent to the hydrolysis reaction. In this case, the amount of the alcohol to be added is usually 0.5 to 1 mol with respect to 1 mol of the tetraalkoxysilane. It doesn't have to be. If the amount of alcohol used is increased, the time until a gel is obtained becomes longer, and conversely, if the amount of alcohol used is decreased, it becomes cloudy during the hydrolysis reaction, but the time to obtain a gel is shortened. Therefore, there is no particular influence on the physical properties of the produced silica. Therefore, alcohol may not be added at all, but it is desirable to add an appropriate amount in order to carry out the reaction efficiently.

加水分解反応によりゾルが生成し、続いてゲル化が進行
するが、本発明においてはこのゾル・ゲル反応も還流条
件下に行い反応を速やかに完結させる。ゾル又はゲル状
物をそのまま還流条件下に保持することにより加水分解
が促進され、アルコールが放出される。これによりアル
コキシ基の残留分の少ないシリカゲルを短時間で得るこ
とができる。また、還流を行なうことにより加水分解工
程に必要な水を有効に確保できるので、水/テトラアル
コキシシランのモル比3以上で乾燥・焼結工程後に炭化
物が全く混っていないシリカゲルを得ることができる。
A sol is produced by the hydrolysis reaction and then gelation proceeds. In the present invention, this sol-gel reaction is also carried out under reflux conditions to complete the reaction promptly. By keeping the sol or gel as it is under reflux conditions, hydrolysis is promoted and alcohol is released. As a result, silica gel having a small amount of residual alkoxy groups can be obtained in a short time. Further, since the water required for the hydrolysis step can be effectively secured by carrying out the reflux, it is possible to obtain silica gel having no carbide after the drying / sintering step at a water / tetraalkoxysilane molar ratio of 3 or more. it can.

[実施例] 以下、実施例及び比較例に基いて、本発明方法を具体的
に説明する。
[Examples] Hereinafter, the method of the present invention will be specifically described based on Examples and Comparative Examples.

実施例1 ガラス製反応容器にテトラメトキシシラン100重量部
とメタノール16.7重量部とを仕込み、これに純水3
5.7重量部を一括添加し、次いで炭酸ガスを吹込ん
だ。その後200r.p.m.で攪拌しながら加熱し、還流条
件下で加水分解反応を行い、約100分でゲル状物を得
た。さらに還流条件下で3時間保持しゲル構造の完結を
行なった。得られたゲル状物を乾燥し、さらに1,10
0℃で焼結したところ、炭化物の混じらない白色の良好
なシリカが得られた。
Example 1 A glass reaction vessel was charged with 100 parts by weight of tetramethoxysilane and 16.7 parts by weight of methanol, and pure water 3
5.7 parts by weight were added all at once, and then carbon dioxide gas was blown in. Then, the mixture was heated at 200 rpm while stirring, and a hydrolysis reaction was performed under reflux conditions to obtain a gel-like product in about 100 minutes. Further, the gel structure was completed by maintaining it under reflux conditions for 3 hours. The obtained gel-like substance is dried and further 1,10
Upon sintering at 0 ° C., good white silica free of carbides was obtained.

実施例2 実施例1と同様の反応容器を使用し、テトラメトキシシ
ラン100重量部とメタノール17重量部とを仕込み、
さらに純水47.3重量部を一括添加し、次いで炭酸ガ
スを吹込んだ。実施例1と同様に加水分解反応を行なっ
たところ、約30分でゲル状物が得られた。さらに還流
条件下で約1時間保持し、実施例1と同様にして白色の
良好なシリカを得た。
Example 2 Using a reaction vessel similar to that of Example 1, 100 parts by weight of tetramethoxysilane and 17 parts by weight of methanol were charged,
Further, 47.3 parts by weight of pure water was added all at once, and then carbon dioxide gas was blown in. When the hydrolysis reaction was carried out in the same manner as in Example 1, a gel-like substance was obtained in about 30 minutes. Further, the mixture was maintained under reflux conditions for about 1 hour, and white favorable silica was obtained in the same manner as in Example 1.

実施例3 テトラメトキシシラン100重量部とメタノール66.
7重量部とを仕込み、さらに純水58.7重量部を一括
添加し、次いで炭酸ガスを吹込んだ。実施例1と同様に
加水分解反応を行ない、約90分でゲル状物を得た。さ
らに還流条件下で1時間保持し、実施例1と同様にして
白色の良好なシリカを得た。
Example 3 100 parts by weight of tetramethoxysilane and 66.
7 parts by weight were charged, 58.7 parts by weight of pure water was further added all at once, and then carbon dioxide gas was blown in. A hydrolysis reaction was carried out in the same manner as in Example 1 to obtain a gel-like product in about 90 minutes. Further, the mixture was maintained under reflux conditions for 1 hour, and white favorable silica was obtained in the same manner as in Example 1.

実施例4 テトラメトキシシラン100重量部とメメタノール8.
3重量部とを仕込み、さらに純水58.7重量部を一括
添加し、次いで炭酸ガスを吹込んだ。実施例1と同様に
加水分解反応を行ない、約20分で白濁したゲル状物を
得た。さらに還流条件下で1時間保持し、実施例1と同
様にして白色の良好なシリカを得た。
Example 4 100 parts by weight of tetramethoxysilane and memethanol 8.
3 parts by weight were charged, 58.7 parts by weight of pure water was further added all at once, and then carbon dioxide gas was blown in. The hydrolysis reaction was performed in the same manner as in Example 1 to obtain a cloudy gel-like substance in about 20 minutes. Further, the mixture was maintained under reflux conditions for 1 hour, and white favorable silica was obtained in the same manner as in Example 1.

実施例5 テトラメトキシシラン100重量部とメタノール16.
7重量部とを仕込み、炭酸ガスを吹き込みながら200
r.p.m.で攪拌し、還流条件下に純水58.7重量部を4
分割し1時間毎に添加して加水分解反応を行なった。約
260分程でゲル状物が得られた。さらに還流条件下で
1時間保持し、実施例1と同様にして白色の良好なシリ
カを得た。
Example 5 100 parts by weight of tetramethoxysilane and methanol 16.
With 7 parts by weight, while blowing carbon dioxide gas, 200
Stir at rpm and add 48.7 parts by weight of pure water under reflux conditions.
The mixture was divided and added every hour to carry out a hydrolysis reaction. A gel-like substance was obtained in about 260 minutes. Further, the mixture was maintained under reflux conditions for 1 hour, and white favorable silica was obtained in the same manner as in Example 1.

実施例6 テトラメトキシシラン100重量部とメタノール16.
7重量部とを仕込み、炭酸ガスを吹き込みながら200
r.p.m.で攪拌し還流条件下に保った。これに純水58.
7重量部を5.2ml/分の速度で定量ポンプで連続添加
して加水分解反応を行なった。約30分でゲル状物が得
られた。そのまま還流条件下で1時間保持し、実施例1
と同様にして白色の良好なシリカを得た。
Example 6 100 parts by weight of tetramethoxysilane and methanol 16.
With 7 parts by weight, while blowing carbon dioxide gas, 200
It was stirred at rpm and kept under reflux conditions. Pure water 58.
The hydrolysis reaction was carried out by continuously adding 7 parts by weight with a metering pump at a rate of 5.2 ml / min. A gel was obtained in about 30 minutes. Example 1 was kept under reflux conditions for 1 hour.
A good white silica was obtained in the same manner as in.

比較例1 ガラス製反応容器にテトラメトキシシラン100重量部
とメタノール16.7重量部とを仕込み、さらに純水3
3.0重量部を一括添加し、次いで炭酸ガスを吹込ん
だ。その後実施例1と同様にして加水分解反応を行なっ
た。約150分でゲル状物を得た。さらにそのまま還流
条件下で3時間保持し、実施例1と同様に乾燥・焼結し
たところ、シリカ中に異色炭化物が発生した。
Comparative Example 1 A glass reaction vessel was charged with 100 parts by weight of tetramethoxysilane and 16.7 parts by weight of methanol, and further purified water 3
3.0 parts by weight was added all at once, and then carbon dioxide gas was blown in. Then, the hydrolysis reaction was performed in the same manner as in Example 1. A gel was obtained in about 150 minutes. Further, it was kept under reflux condition for 3 hours and dried and sintered in the same manner as in Example 1. As a result, a different color carbide was generated in silica.

比較例2 テトラメトキシシラン100重量部とメタノール17重
量部とを仕込み、さらに純水58.7重量部を一括添加
し、次いで炭酸ガスを吹込んだ。室温で攪拌しながら加
水分解反応を行なった。ゲル状物を得るのに約250分
を要した。得られたゲル状物をさらに室温で1日間保持
して乾燥し、さらに1,100℃で焼結したところ、炭
化物が少量混ざっているシリカを得た。この方法で良好
なシリカを得るには、ゲル状物を室温で3日間以上保持
する必要があった。
Comparative Example 2 100 parts by weight of tetramethoxysilane and 17 parts by weight of methanol were charged, 58.7 parts by weight of pure water was added all at once, and then carbon dioxide gas was blown in. The hydrolysis reaction was carried out while stirring at room temperature. It took about 250 minutes to obtain a gel. The obtained gel-like material was further kept at room temperature for 1 day, dried and further sintered at 1,100 ° C. to obtain silica containing a small amount of carbide. In order to obtain good silica by this method, it was necessary to keep the gel at room temperature for 3 days or more.

[発明の効果] 本発明によれば、従来に比べ加水分解反応時に添加する
水の量が少なく、また、極めて短時間にゲル構造の完結
したシリカゲルを得ることができるので、プロセス経済
上極めて有利であり、工業上効率的にシリカゲルを製造
することができる。また、本発明方法で得られたシリカ
ゲルは焼結後に炭化物が生成せず、白色の良好な物性を
有するシリカとなる。
[Effects of the Invention] According to the present invention, the amount of water added during the hydrolysis reaction is smaller than in the prior art, and silica gel having a completed gel structure can be obtained in an extremely short time. Therefore, silica gel can be produced industrially efficiently. In addition, the silica gel obtained by the method of the present invention does not generate carbides after sintering, and becomes white silica having good physical properties.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】テトラアルコキシシランを加水分解してシ
リカゲルを製造する方法において、水/テトラアルコキ
シシランのモル比3以上、かつ、還流条件下に加水分解
反応及びゾル・ゲル反応を行うことを特徴とするシリカ
ゲルの製造方法。
1. A method for producing silica gel by hydrolyzing tetraalkoxysilane, wherein the hydrolysis reaction and the sol-gel reaction are carried out under a reflux condition under a water / tetraalkoxysilane molar ratio of 3 or more. And a method for producing silica gel.
【請求項2】加水分解反応をアルコールの存在下に行う
特許請求の範囲第1項記載のシリカゲルの製造方法。
2. The method for producing silica gel according to claim 1, wherein the hydrolysis reaction is carried out in the presence of alcohol.
JP61276666A 1986-11-21 1986-11-21 Method for producing silica gel Expired - Lifetime JPH0645452B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61276666A JPH0645452B2 (en) 1986-11-21 1986-11-21 Method for producing silica gel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61276666A JPH0645452B2 (en) 1986-11-21 1986-11-21 Method for producing silica gel

Publications (2)

Publication Number Publication Date
JPS63134511A JPS63134511A (en) 1988-06-07
JPH0645452B2 true JPH0645452B2 (en) 1994-06-15

Family

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JP61276666A Expired - Lifetime JPH0645452B2 (en) 1986-11-21 1986-11-21 Method for producing silica gel

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WO2024071055A1 (en) * 2022-09-27 2024-04-04 国立大学法人 東京大学 METHOD FOR PRODUCING SiO2-CONTAINING MATERIAL IN WHICH RAW MATERIALS CONTAINING SiO2 ARE DIRECTLY JOINED

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JPS63134511A (en) 1988-06-07

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