JPH0455331A - Production of silica glass - Google Patents
Production of silica glassInfo
- Publication number
- JPH0455331A JPH0455331A JP16248890A JP16248890A JPH0455331A JP H0455331 A JPH0455331 A JP H0455331A JP 16248890 A JP16248890 A JP 16248890A JP 16248890 A JP16248890 A JP 16248890A JP H0455331 A JPH0455331 A JP H0455331A
- Authority
- JP
- Japan
- Prior art keywords
- silica
- porous silica
- porous
- silica glass
- glass
- 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
Links
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 101
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 39
- 239000000843 powder Substances 0.000 claims abstract description 14
- 238000005245 sintering Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 abstract description 10
- 239000011521 glass Substances 0.000 abstract description 4
- 238000005336 cracking Methods 0.000 abstract 1
- 239000000499 gel Substances 0.000 description 12
- 239000000463 material Substances 0.000 description 6
- -1 Silicon alkoxide Chemical class 0.000 description 5
- 238000010304 firing Methods 0.000 description 4
- 229910052710 silicon Inorganic materials 0.000 description 4
- 239000010703 silicon Substances 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 3
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- VXEGSRKPIUDPQT-UHFFFAOYSA-N 4-[4-(4-methoxyphenyl)piperazin-1-yl]aniline Chemical compound C1=CC(OC)=CC=C1N1CCN(C=2C=CC(N)=CC=2)CC1 VXEGSRKPIUDPQT-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003779 heat-resistant material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000004065 semiconductor Substances 0.000 description 2
- 239000005049 silicon tetrachloride Substances 0.000 description 2
- 238000003980 solgel method Methods 0.000 description 2
- 229910002012 Aerosil® Inorganic materials 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- NWHAUAZVLJCRBB-UHFFFAOYSA-N [Si](=O)=O.[B] Chemical compound [Si](=O)=O.[B] NWHAUAZVLJCRBB-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N boron trioxide Inorganic materials O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000003349 gelling agent Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B20/00—Processes specially adapted for the production of quartz or fused silica articles, not otherwise provided for
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/06—Other methods of shaping glass by sintering, e.g. by cold isostatic pressing of powders and subsequent sintering, by hot pressing of powders, by sintering slurries or dispersions not undergoing a liquid phase reaction
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/06—Other methods of shaping glass by sintering, e.g. by cold isostatic pressing of powders and subsequent sintering, by hot pressing of powders, by sintering slurries or dispersions not undergoing a liquid phase reaction
- C03B19/066—Other methods of shaping glass by sintering, e.g. by cold isostatic pressing of powders and subsequent sintering, by hot pressing of powders, by sintering slurries or dispersions not undergoing a liquid phase reaction for the production of quartz or fused silica articles
Abstract
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.
シリカガラスは耐熱性、耐食性および光学的性質に優れ
ていることから、半導体の製造に欠かせない重要な材料
であり、さらには光ファイバやIC製造用フォトマスク
基、板、TPT基板などに使用され、その用途はますま
す拡大している。Because silica glass has excellent heat resistance, corrosion resistance, and optical properties, it is an important material indispensable for semiconductor manufacturing, and is also used for photomask substrates, plates, TPT substrates, etc. for optical fiber and IC manufacturing. and its uses are expanding more and more.
シリカガラスの製造法には、天然石英を電気炉または酸
水素炎により溶解する方法、あるいは四塩化ケイ素を酸
水素炎又はプラズマ炎中で高温酸化し溶解する方法があ
るが、いずれの方法も製造工程に2000℃あるいはそ
れ以上の高温を必要とするため大量のエネルギーを消費
し、また製造時にそのような高温に耐える材料が必要と
なるほか、更に高純度のものが得にくいなど経済的、品
質的にいくつかの問題点をもっている。Silica glass can be produced by melting natural quartz in an electric furnace or oxyhydrogen flame, or by oxidizing and melting silicon tetrachloride at high temperature in an oxyhydrogen flame or plasma flame. The process requires high temperatures of 2000°C or higher, which consumes a large amount of energy.In addition, materials that can withstand such high temperatures are required during manufacturing, and it is difficult to obtain materials with even higher purity, resulting in economical and quality issues. It has some problems.
これに対し、近年ゾル−ゲル法と呼ばれるシリカガラス
を低温で合成する方法が注目されている。On the other hand, in recent years, a method of synthesizing silica glass at low temperature called the sol-gel method has been attracting attention.
その概要を簡単に述べる。The outline will be briefly described below.
一般式Si (OR)4 (R:アルキル基)で表わさ
れるシリコンアルコキシド、あるいはその重縮合物、例
えば(RO)!S i・(O81(OR)2)n・O8
i (OR)3 (n=o 〜8、R:アルキル基)
に水(アルカリまたは酸でpHを調整してもよい)を加
え、加水分解し、シリカヒドロシル(本発明においては
シリカゾルという)とする。Silicon alkoxide represented by the general formula Si (OR) 4 (R: alkyl group) or its polycondensate, such as (RO)! S i・(O81(OR)2)n・O8
i (OR)3 (n=o ~8, R: alkyl group)
Water (pH may be adjusted with an alkali or acid) is added to the solution to hydrolyze it to obtain silica hydrosil (referred to as silica sol in the present invention).
この時、シリコンアルコキシドと水が均一な系となる様
、一般には溶媒として適当なアルコール等の有機溶媒が
添加されている。このシリカゾルを容器にとり、静置、
昇温、ゲル化剤の添加等によってゲル化させる。その後
、ゲルを蒸発乾燥することにより乾燥ゲル(シリカ多孔
質体)とする。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。At this time, an appropriate organic solvent such as alcohol is generally added as a solvent so that the silicon alkoxide and water form a uniform system. Take this silica sol in a container, leave it still,
It is gelled by raising the temperature, adding a gelling agent, etc. Thereafter, the gel is evaporated to dryness to obtain a dry gel (silica porous material). Silica glass is obtained by sintering this dried gel in a suitable atmosphere.
焼結する方法としては、サヤと呼ばれる耐熱材を多段構
造とし、各段に乾燥ゲルを重ならないように仕込んだの
ち焼成する方法、あるいは乾燥ゲルを重ねて焼成する方
法(特開昭60−65731号)等がある。Sintering methods include a method in which a heat-resistant material called a saya is made into a multi-stage structure, and dried gel is charged in each stage so as not to overlap, and then fired, or a method in which dried gel is stacked and fired (Japanese Patent Application Laid-Open No. 60-65731) No.) etc.
しかし、サヤと呼ばれる耐熱材を多段構造とする方法で
は、サヤの占める空間容積が大きいため効率よく乾燥ゲ
ルを焼成できない。また乾燥ゲルを重ねて焼成する方法
では、昇温時に乾燥ゲルと乾燥ゲルの接触面からのガス
の揮散がよくないため、焼結したシリカガラスどうしが
融着を起こしやすく、またクラックも発生しやすい。However, in the method of forming a multi-stage structure using a heat-resistant material called a pod, the dry gel cannot be fired efficiently because the pod occupies a large space. In addition, in the method of stacking dry gels and firing them, gas does not evaporate from the contact surface between the dry gels when the temperature rises, so the sintered silica glasses tend to fuse together, and cracks also occur. Cheap.
本発明は、シリカガラスを安価に製造する方法を提供す
ることを目的とする。An object of the present invention is to provide a method for manufacturing silica glass at low cost.
本発明は、シリカ多孔質体を焼結するシリカガラスの製
造法において、シリカ多孔質体とシリカ多孔質体のあい
だにシリカ微粉末を介在させながら、シリカ多孔質体を
重ねて焼結することを特徴とするシリカガラスの製造法
に関する。The present invention provides a method for producing silica glass by sintering porous silica bodies, in which porous silica bodies are stacked and sintered while fine silica powder is interposed between the porous silica bodies. The present invention relates to a method for producing silica glass characterized by the following.
本発明におけるシリカ多孔質体として好適なものはゾル
−ゲル法により調製された乾燥ゲルがある。しかし、こ
れに代え、四塩化ケイ素等の気相酸化により調製したシ
リカ多孔質体、二酸化ケイ素−三酸化ホウ素等の分相ガ
ラスのリーチングにより調製したシリカ多孔質体等を用
いることもできる。A suitable porous silica material in the present invention is a dry gel prepared by a sol-gel method. However, instead of this, a porous silica prepared by gas-phase oxidation of silicon tetrachloride or the like, a porous silica prepared by leaching of a phase-divided glass such as silicon dioxide-boron trioxide, etc. can also be used.
本発明の、シリカ多孔質体とシリカ多孔質体のあいだに
介在させるシリカ微粉末は、焼結シリカガラスを汚染し
ない程度に純度が高く、粒度は操作性を考慮して0.1
〜10μmが好ましい。このようなシリカ微粉末として
は、例えば、気相酸化により製造されたホワイトカーボ
ンであるエーロジル(Aerosil) (デグサ(
Deggussa )社の商品名〕やカーボジル(Ca
b−o−sil) [カボット(Cabot)社の商
品名〕、シリコンアルコキシド(テトラメトキシシラン
、テトラエトキシシラン等)から製造されたシリカ微粉
末等が挙げられる。The fine silica powder interposed between the porous silica bodies of the present invention has a high purity to the extent that it does not contaminate the sintered silica glass, and the particle size is 0.1 in consideration of operability.
~10 μm is preferred. Examples of such fine silica powder include Aerosil (Degussa), which is white carbon produced by gas phase oxidation.
Product name of Deggussa) and Carbosil (Ca
b-o-sil) (trade name of Cabot), silica fine powder produced from silicon alkoxide (tetramethoxysilane, tetraethoxysilane, etc.), and the like.
シリカ多孔質体とシリカ多孔質体のあいだに介在させる
シリカ微粉末の層の厚さは、操作のしやすさ、経済性、
効率を考慮し、0.1〜5mm、好ましくは0.5〜3
1E11がよい。The thickness of the layer of fine silica powder interposed between the porous silica materials is determined by the ease of operation, economic efficiency,
Considering efficiency, 0.1 to 5 mm, preferably 0.5 to 3
1E11 is good.
シリカ多孔質体とシリカ多孔質体のあいだに微粉末を介
在させながら、シリカ多孔質体を重ねて焼結することに
より、シリカ多孔質体中のガスの揮散が容易となり、更
に焼結ガラスどうしの融着を起こすことがない。このこ
とがシリカガラスのクラック発生の防止に寄与している
と考えられる。By stacking and sintering the porous silica bodies while interposing fine powder between the porous silica bodies, the gas in the porous silica bodies can be easily volatilized, and the sintered glass can also be bonded. No fusion will occur. It is thought that this contributes to preventing the occurrence of cracks in silica glass.
(実施例1)
テトラメトキシシラン(S i (OCH3) 4)
とメタノールを1=4のモル比になるように量りとり、
この溶液に濃度が0.01モル/Lのアンモニア水をテ
トラメトキシシラン1モルに対し水が4モルとなるよう
に加え、充分混合してシリカゾルを得た。得られたゾル
をポリフッ化エチレンでコーティングした200mm角
、深さ20mmのステンレスシャーレ10枚にそれぞれ
深さ10mmまで入れ、密封して室温でゲル化した。(Example 1) Tetramethoxysilane (S i (OCH3) 4)
Weigh out and methanol so that the molar ratio is 1=4,
Aqueous ammonia having a concentration of 0.01 mol/L was added to this solution in an amount of 4 mol of water per 1 mol of tetramethoxysilane, and the mixture was thoroughly mixed to obtain a silica sol. The obtained sol was placed in 10 stainless steel petri dishes, each 200 mm square and 20 mm deep, coated with polyfluoroethylene to a depth of 10 mm, sealed and gelatinized at room temperature.
ゲル化したのち、穴のある蓋に代えて60℃で10日間
乾燥し、その後150℃まで30℃/日の昇温速度で加
温し、乾燥ゲルを得た。第1図に示すように、得られた
乾燥ゲルのあいだにシリカ微粉末(デグサ社製0X−5
0)を、厚さが約1mmとなるように置き、乾燥ゲルを
10枚重ねて焼成炉中にセットした。先ず、700℃ま
で空気中、50℃/時の昇温速度で加熱し、次いで13
50℃までヘリウム中で50℃/時の速度で昇温し、焼
結させると、透明でクラックのないシリカガラスが10
枚得られた。After gelation, the gel was dried at 60° C. for 10 days using a lid with holes, and then heated to 150° C. at a rate of 30° C./day to obtain a dry gel. As shown in Figure 1, fine silica powder (0X-5 manufactured by Degussa)
0) was placed so that the thickness was about 1 mm, and 10 sheets of dry gel were stacked on top of each other and set in a firing furnace. First, it was heated to 700°C in air at a heating rate of 50°C/hour, then heated to 13°C.
When heated to 50°C in helium at a rate of 50°C/hour and sintered, transparent, crack-free silica glass becomes 10
I got one.
(実施例2)
シリカ微粉末として、シリコンアルコキシドから製造さ
れた多摩化学■製FFCを用いた以外は実施例1と同様
に操作した。透明でクラックのないシリカガラスが10
枚得られた。(Example 2) The same procedure as in Example 1 was carried out except that FFC manufactured from silicon alkoxide manufactured by Tama Kagaku ■ was used as the silica fine powder. Transparent and crack-free silica glass 10
I got one.
本発明によれば、焼成炉の空間を有効に利用することが
できるので、シリカガラスを安価に製造できる。また、
得られるシリカガラスは透明でクラックがないので、従
来から使用されてきたIC製造用フォトマスク基材、光
学材料等はもちろん、液晶表示用基材等にも応用が拡大
できる。According to the present invention, the space in the firing furnace can be used effectively, so silica glass can be manufactured at low cost. Also,
The resulting silica glass is transparent and has no cracks, so it can be used not only as photomask substrates for IC manufacturing, optical materials, etc. that have been conventionally used, but also as substrates for liquid crystal displays.
第1図は焼成炉中にセットされる際のシリカ多孔質体の
様子を示す斜視図である。
符号の説明
1 シリカ多孔質体
2 シリカ微粉末
3 敷板FIG. 1 is a perspective view showing the state of the porous silica body when it is set in a firing furnace. Explanation of symbols 1 Silica porous body 2 Silica fine powder 3 Floor plate
Claims (1)
おいて、シリカ多孔質体とシリカ多孔質体のあいだにシ
リカ微粉末を介在させ、シリカ多孔質体を重ねて焼結す
ることを特徴とするシリカガラスの製造法。1. A method for producing silica glass by sintering porous silica bodies, which is characterized by interposing fine silica powder between the porous silica bodies, stacking the porous silica bodies, and sintering the porous silica bodies. A method for producing silica glass.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16248890A JPH0455331A (en) | 1990-06-20 | 1990-06-20 | Production of silica glass |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16248890A JPH0455331A (en) | 1990-06-20 | 1990-06-20 | Production of silica glass |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0455331A true JPH0455331A (en) | 1992-02-24 |
Family
ID=15755569
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16248890A Pending JPH0455331A (en) | 1990-06-20 | 1990-06-20 | Production of silica glass |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0455331A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5667547A (en) * | 1994-05-26 | 1997-09-16 | Heraeus Quartzglas Gmbh | Method for manufacture of quartz glass plates |
DE102006046619A1 (en) * | 2006-09-29 | 2008-04-03 | Heraeus Quarzglas Gmbh & Co. Kg | Coatable silicon dioxide slip used in the production of layered quartz glass contains a dispersion liquid and amorphous nano-particles with a specified particle size of less |
-
1990
- 1990-06-20 JP JP16248890A patent/JPH0455331A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5667547A (en) * | 1994-05-26 | 1997-09-16 | Heraeus Quartzglas Gmbh | Method for manufacture of quartz glass plates |
DE102006046619A1 (en) * | 2006-09-29 | 2008-04-03 | Heraeus Quarzglas Gmbh & Co. Kg | Coatable silicon dioxide slip used in the production of layered quartz glass contains a dispersion liquid and amorphous nano-particles with a specified particle size of less |
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