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JPH0238323A - Production of silica glass - Google Patents

Production of silica glass

Info

Publication number
JPH0238323A
JPH0238323A JP18929588A JP18929588A JPH0238323A JP H0238323 A JPH0238323 A JP H0238323A JP 18929588 A JP18929588 A JP 18929588A JP 18929588 A JP18929588 A JP 18929588A JP H0238323 A JPH0238323 A JP H0238323A
Authority
JP
Japan
Prior art keywords
gel
silica glass
silicon alkoxide
silica
sol
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.)
Pending
Application number
JP18929588A
Other languages
Japanese (ja)
Inventor
Yoichi Machii
洋一 町井
Fusaji Hayashi
林 房司
Koichi Takei
康一 武井
Toshikatsu Shimazaki
俊勝 嶋崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Hitachi Chemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP18929588A priority Critical patent/JPH0238323A/en
Publication of JPH0238323A publication Critical patent/JPH0238323A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C1/00Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
    • C03C1/006Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels to produce glass through wet route

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Glass Melting And Manufacturing (AREA)

Abstract

PURPOSE:To obtain a silica glass prevented from crack or fissure development by gelling a sol solution prepared by hydrolyzing a silicon alkoxide incorporated with cellosolve and silica fine granules, followed by drying and calcination. CONSTITUTION:A silicon alkoxide or its polycondensate is incorporated with 0.1-5.0 molar times of cellosolve and silica fine granules and the resultant system is homogeneously dispersed in the presence of a solvent followed by addition of water in the presence of a catalyst to effect hydrolysis, thus preparing a sol solution. Thence, this solution is gelled at >=0 deg.C and the resultant gel is left to stand at 0-100 deg.C for several minutes to several tens days to effect drying followed by calcination by heating at a rate of 50-200 deg.C/hr to 1000-1300 deg.C.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は光学用、半導体工業用、電子工業用、理化学用
等に使用されるシリカガラスの製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for producing silica glass used for optics, semiconductor industry, electronic industry, physics and chemistry, etc.

(従来の技術) 近年、シリカガラスの新たな製造法として注目をあびて
いるのが、ゾル−ゲル法である。
(Prior Art) In recent years, the sol-gel method has been attracting attention as a new method for producing silica glass.

ゾル−ゲル法によるシリカガラスの製造法は次の通りで
ある。
The method for producing silica glass using the sol-gel method is as follows.

−a式Si (OR) + (但しRはアルキル基を表
す)で示されるシリコンアルコキシド及び/又はその重
縮合物、例えば (RO)ssi(O5i(OR))nO5i(OR)s
(n = O〜8 )に水(あらかじめ触媒として酸、
アルカリを加えておいてもよい)を加え、加水分解しシ
リカヒドロシルとする。この時、シリコンアルコキシド
と水とが均一な系となる様に溶媒として適当なアルコー
ルを加えてもよい、このシリカゾル溶液を静置、昇温、
ゲル化剤添加等によりゲル化させる。
-A silicon alkoxide and/or its polycondensate represented by the formula Si (OR) + (where R represents an alkyl group), such as (RO)ssi(O5i(OR))nO5i(OR)s
(n = O~8) with water (acid as a catalyst in advance,
(Optionally, an alkali may be added in advance) and hydrolyze it to form silica hydrosil. At this time, an appropriate alcohol may be added as a solvent so that the silicon alkoxide and water form a homogeneous system.The silica sol solution is allowed to stand, heated,
It is gelled by adding a gelling agent or the like.

その後、ゲルを乾燥することによりシリカゲルとする。Thereafter, the gel is dried to obtain silica gel.

この乾燥ゲルを適当な雰囲気中で焼結することによりシ
リカガラスを得る。
Silica glass is obtained by sintering this dried gel in a suitable atmosphere.

このゾル−ゲル法には以下の特長がある。This sol-gel method has the following features.

(11S i C1+等を原料とする火炎加水分解等に
より生成するスートを焼結してガラス化する従来の気相
化学蒸着法よりも低温で製造できるため、省エネルギー
で低コスト化できる。
(Since it can be produced at a lower temperature than the conventional vapor phase chemical vapor deposition method in which the soot produced by flame hydrolysis etc. using 11S i C1+ etc. as a raw material is sintered and vitrified, it can save energy and reduce costs.

(2)原料として液体状態で使用可能のため、精製が容
易に行え高純度化できる。
(2) Since it can be used as a raw material in a liquid state, it can be easily purified and highly purified.

(3)室温で液相混合できるため、他成分と混合した場
合も均質かガラスができる。
(3) Since liquid phase mixing is possible at room temperature, homogeneous glass can be produced even when mixed with other components.

このように種々の特長をもつゾル−ゲル法によるシリカ
ガラスの製造にもまだ未解決の問題が残されている。
There are still unresolved problems in the production of silica glass by the sol-gel method, which has various advantages as described above.

特にゲルを乾燥する過程でゲルにクランクや割れが発生
し易く、モノリシックな大形の乾燥ゲルを歩留りよく製
造することが困難であるという問題である。クランクや
割れの発生する原因の一つにゲル乾燥時に水やアルコー
ル等の蒸発に伴いゲル中に応力が発生し、この応力がゲ
ルの強度より大きいとゲルはクラックや割れが発生する
と考えられている。またこの応力は次式 %式% (ΔP=応力、γ=表面張力、θ=ぬれ角、r −細孔
径)で表されるように、表面張力が大きい程また細孔径
が小さい程大きくなる。
In particular, the problem is that the gel tends to crack or crack during the drying process, making it difficult to produce a large, monolithic dried gel with a high yield. One of the causes of cracks and cracks is that stress is generated in the gel as water, alcohol, etc. evaporate during gel drying, and if this stress is greater than the strength of the gel, it is thought that the gel will crack or break. There is. Further, this stress increases as the surface tension increases and as the pore diameter decreases, as expressed by the following formula % (ΔP=stress, γ=surface tension, θ=wetting angle, r−pore diameter).

そこでこのような割れやクランクを防止する方法として
、ゾル溶液中の水の量を多くしてゲル強度を上げる方法
、加水分解温度を高くして細孔径を大きくする方法など
の方策が講じられている。
Therefore, as a method to prevent such cracks and cranks, measures have been taken such as increasing the amount of water in the sol solution to increase the gel strength, and increasing the hydrolysis temperature to increase the pore diameter. There is.

又、特開昭61−183129号公報には、割れやクラ
ンクを防止するため沸点が水より高い溶媒、例えばl−
ブタノール、1−ペンタノール、1−ヘキサノール、ト
ルエンをシリコンアルコキシドに添加する方法が提案さ
れている。
In addition, JP-A-61-183129 discloses that a solvent with a boiling point higher than that of water, such as l-
A method has been proposed in which butanol, 1-pentanol, 1-hexanol, and toluene are added to silicon alkoxide.

(発明が解決しようとする課題) しかしながら上記の方法ではいずれも十分に大きな乾燥
ゲル体を得るのは困難で、シリカガラス体となった時の
寸法があまり大きなものは得られなかった。
(Problems to be Solved by the Invention) However, in all of the above methods, it was difficult to obtain a sufficiently large dry gel body, and it was not possible to obtain a silica glass body whose dimensions were very large.

本発明は、クラックや割れの発生しないシリカガラスの
製造を提供するものである。
The present invention provides the production of silica glass that does not generate cracks or breaks.

(課題を解決するための手段) 本発明は、ゲル乾燥中、水やアルコール等の蒸発に伴っ
て発生する応力がクランクや割れの一因になるものと考
え、このような大きな応力の発生を回避するために、シ
リコンアルコキシドの溶媒としてセルソルブを用い、更
にゲル中にシリカ微粒子を添加するものである。
(Means for Solving the Problems) The present invention considers that stress generated due to evaporation of water, alcohol, etc. during gel drying is a cause of cracks and cracks, and the present invention aims to prevent the generation of such large stress. In order to avoid this problem, Cellsolve is used as a solvent for silicon alkoxide, and silica fine particles are added to the gel.

本発明に用いるシリコンアルコキシドはシリコンアルコ
キシド単量体のみでなく重縮合物を用いてもよい、例え
ば (CHsO)*5i(O5i(OCHz)、)nO5i
(OCHs)s (n = O〜8 )を挙げることが
できる。これらは一種でも複数でも使用可能である。シ
リコンアルコキシドのアルキル基としては、メチル基、
エチル基、プロピル基、ブチル基等が好ましい。
As the silicon alkoxide used in the present invention, not only silicon alkoxide monomers but also polycondensates may be used. For example, (CHsO)*5i (O5i (OCHz), ) nO5i
(OCHs)s (n = O~8). One or more of these can be used. As the alkyl group of silicon alkoxide, methyl group,
Ethyl group, propyl group, butyl group, etc. are preferred.

加水分解のために加える水は予め触媒として塩酸、硝酸
などの鉱酸、ギ酸、酢酸などの有機酸、また塩基として
アンモニアばかりでなくエチレンジアミンなどの有機塩
基を加えておいても良い。
To the water added for hydrolysis, mineral acids such as hydrochloric acid and nitric acid, organic acids such as formic acid and acetic acid as catalysts, and not only ammonia but also organic bases such as ethylenediamine as bases may be added in advance.

シリコンアルコキシドに添加するエチルセルソルブ、メ
チルセルソルブ等のセルソルブの添加量はシリコンアル
コキシドに対して0.1〜5.0倍(モル比)が好まし
い。また通常使用されるエタノール等のアルコールを併
用することもできる。
The amount of cellosolve such as ethyl cellosolve or methyl cellosolve added to silicon alkoxide is preferably 0.1 to 5.0 times (molar ratio) to the silicon alkoxide. Moreover, commonly used alcohols such as ethanol can also be used together.

さらにケトン類、エステル類を併用することもできる。Furthermore, ketones and esters can also be used in combination.

シリカ微粒子は水を加え加水分解する前に溶媒或いは溶
媒とシリコンアルコキシドの混合溶液に均一に分散させ
ておく。このとき分散性を良くするために界面活性剤を
使用すると効果的である。
The silica fine particles are uniformly dispersed in a solvent or a mixed solution of a solvent and silicon alkoxide before being hydrolyzed by adding water. At this time, it is effective to use a surfactant to improve dispersibility.

シリコンアルコキシド、セルソルブ、シリカ微粒子及び
並びに水とは生成するゾルをできるだけ均一なものとす
るためにスタークなどを用いてよく混合する。また超音
波を照射してもよい。
Silicon alkoxide, Cellsolve, silica fine particles, and water are thoroughly mixed using a Stark or the like to make the resulting sol as uniform as possible. Alternatively, ultrasonic waves may be irradiated.

生成したゾル溶液は手早く他の容器に移してゲル化させ
る。ゲル化時には生成したゲルからの溶媒の発散を防ぐ
ために容器を密封することが好ましく、またゲル化時の
温度は0℃以上が好ましい。
The generated sol solution is quickly transferred to another container and allowed to gel. During gelation, it is preferable to seal the container to prevent the solvent from escaping from the generated gel, and the temperature during gelation is preferably 0° C. or higher.

乾燥する工程では穴のある蓋に代えて、適当な雰囲気下
で乾燥収縮固化させて乾燥ゲルとする。
In the drying process, instead of using a lid with holes, the gel is dried and shrunk and solidified in an appropriate atmosphere to form a dry gel.

その後ゲル−ゾル法で焼結することによりシリカガラス
を製造する。
Thereafter, silica glass is manufactured by sintering using a gel-sol method.

ゲル化する工程、乾燥する工程、焼結する工程は一般に
用いられる条件が使用される。例えばそれぞれ、0℃〜
100℃で数分〜数10日放置、室温〜100℃で数時
間〜数10日放置、適当な雰囲気下で1000〜130
0℃に50〜200℃/時間の昇温速度で加熱する等で
ある。
Generally used conditions are used for the gelling step, drying step, and sintering step. For example, each
Leave at 100℃ for a few minutes to several 10 days, leave at room temperature to 100℃ for several hours to several 10 days, 1000 to 130 in an appropriate atmosphere
For example, heating to 0°C at a temperature increase rate of 50 to 200°C/hour.

(作用) セルソルブ及びシリカ微粒子の作用の詳細は不明である
が、ゲル中でのシリカ微粒子の生成、ゲル中でのこれら
のシリカ微粒子間の結合、乾燥過程でゲル中に発生する
応力の緩和等に寄与し、ゲルの大形化が可能となるもの
と考えられる。
(Function) The details of the effects of Cellsolve and silica particles are unknown, but they include the generation of silica particles in the gel, the bonding between these silica particles in the gel, and the relaxation of stress generated in the gel during the drying process. It is thought that this contributes to the growth of the gel, making it possible to increase the size of the gel.

実施例1 エチルセルソルブに粒径約70n−のシリカ微粒子を重
量比でモルホリンに対して0.1倍添加し均一に分散さ
せた後、重量比でモルホリンに対して0.9倍のテトラ
メトキシシランを混合し均一な溶液を作成し、さらにコ
リンの0.01 mol/ 1水?8?fLをテトラメ
トキシシランに対して重量比で0.64倍添加し、充分
混合してシリカゾルを得た。得られたゾルを直径200
nのステンレスシャーレに深さLotmまで入れ密封し
て室温でゲル化させ5日放置した。その後60℃で7日
間乾燥、さらに120℃で1日乾燥して直径約170f
fi+mの乾燥ゲルを得た。こうして得られた乾燥ゲル
のかさ密度は0.65g/−でありクランクや割れのな
いものであった。この乾燥ゲルを空気中1250℃まで
60℃/時間の速度で昇温加熱してクランクや発泡など
のない直径約110mmのシリカガラスを得た。このシ
リカガラスには失透や気泡はなく品質の高いものである
。又分析の結果、このシリカガラスは市販のシリカガラ
スとその特性が一致した。
Example 1 Fine silica particles having a particle size of approximately 70 n- were added to ethyl cellosolve in a weight ratio of 0.1 times the weight of morpholine, and after uniformly dispersing the mixture, tetramethoxy Mix silane to create a homogeneous solution, then add 0.01 mol of choline/1 water? 8? fL was added in a weight ratio of 0.64 times to tetramethoxysilane and thoroughly mixed to obtain a silica sol. The diameter of the obtained sol is 200
The mixture was placed in a stainless steel Petri dish of size Lotm to a depth of Lotm, sealed, and allowed to gel at room temperature for 5 days. After that, it was dried for 7 days at 60℃, and then dried for 1 day at 120℃, making it approximately 170f in diameter.
A dry gel of fi+m was obtained. The bulk density of the dry gel thus obtained was 0.65 g/-, with no cracks or cracks. This dried gel was heated in air to 1250° C. at a rate of 60° C./hour to obtain silica glass with a diameter of about 110 mm without cracks or foaming. This silica glass has no devitrification or bubbles and is of high quality. Further, as a result of analysis, the properties of this silica glass matched those of commercially available silica glass.

実施例2 メタノール:メチルセルソルブ=7:3の体積比になる
ようにした混合溶媒を使用する以外は実施例1と同様に
して直径約 170n+mの乾燥ゲルを得た。こうして得られた乾燥
ゲルはクランクや割れのないものであった。この乾燥ゲ
ルを実施例1と同様にして加熱してクラックや発泡など
のない直径約110n+mのシリカガラスを得た。この
シリカガラスには失透や気泡はなく品質の高いものであ
る。又分析の結果、このシリカガラスは市販のシリカガ
ラスとその特性が一致した。
Example 2 A dry gel with a diameter of about 170 nm+m was obtained in the same manner as in Example 1, except that a mixed solvent having a volume ratio of methanol:methylcellosolve=7:3 was used. The dried gel thus obtained was free of cracks and cracks. This dried gel was heated in the same manner as in Example 1 to obtain silica glass having a diameter of about 110 nm+m without cracks or foaming. This silica glass has no devitrification or bubbles and is of high quality. Further, as a result of analysis, the properties of this silica glass matched those of commercially available silica glass.

(発明の効果) 本発明によれば、大型のシリカガラスをゾルゲル法によ
りクランクや割れを発生することなく、容易に製造が可
能となる。その大きさは基本的には制約がなく形状も板
状の物に限らず棒状、管状のものも製造可能となり従来
よりも安価に製造することができる。
(Effects of the Invention) According to the present invention, large-sized silica glass can be easily manufactured by the sol-gel method without causing cracks or cracks. There are basically no restrictions on its size, and its shape is not limited to plate-like ones, but also rod-like and tubular ones, which can be manufactured at a lower cost than in the past.

又、本発明によりシリカガラスは従来より安価に製造で
きるため、従来から使用されてきたIC製造用フォトマ
スク基材等の分野はもちろんのこと、これまで高価格の
ため使用されていなかった分野での需要の拡大も可能と
なる。
In addition, since silica glass can be manufactured at a lower cost than before with the present invention, it can be used not only in fields such as photomask substrates for IC manufacturing, which have traditionally been used, but also in fields where it has not been used due to its high price. It will also be possible to expand demand for

代理人 弁理士 廣 瀬   章Agent Patent Attorney Akira Hirose

Claims (1)

【特許請求の範囲】[Claims] 1、シリコンアルコキシドを加水分解してゾル溶液とす
る工程、ゾルをゲル化する工程、ゲルを乾燥する工程及
び焼成する工程とからなるシリカガラスの製造において
、ゾル溶液とする工程でセルソルブ及びシリカ微粒子を
添加することを特徴とするシリカガラスの製造法。
1. In the production of silica glass, which consists of the steps of hydrolyzing silicon alkoxide to make a sol solution, gelling the sol, drying the gel, and firing, cell solve and silica fine particles are removed in the step of making the sol solution. A method for producing silica glass characterized by adding.
JP18929588A 1988-07-28 1988-07-28 Production of silica glass Pending JPH0238323A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18929588A JPH0238323A (en) 1988-07-28 1988-07-28 Production of silica glass

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18929588A JPH0238323A (en) 1988-07-28 1988-07-28 Production of silica glass

Publications (1)

Publication Number Publication Date
JPH0238323A true JPH0238323A (en) 1990-02-07

Family

ID=16238940

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18929588A Pending JPH0238323A (en) 1988-07-28 1988-07-28 Production of silica glass

Country Status (1)

Country Link
JP (1) JPH0238323A (en)

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