JPH0238324A - Production of silica glass - Google Patents
Production of silica glassInfo
- Publication number
- JPH0238324A JPH0238324A JP18929688A JP18929688A JPH0238324A JP H0238324 A JPH0238324 A JP H0238324A JP 18929688 A JP18929688 A JP 18929688A JP 18929688 A JP18929688 A JP 18929688A JP H0238324 A JPH0238324 A JP H0238324A
- Authority
- JP
- Japan
- Prior art keywords
- gel
- morpholine
- silica glass
- silicon alkoxide
- silica
- 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 44
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- YNAVUWVOSKDBBP-UHFFFAOYSA-N Morpholine Chemical compound C1COCCN1 YNAVUWVOSKDBBP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000010703 silicon Substances 0.000 claims abstract description 14
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 14
- -1 silicon alkoxide Chemical class 0.000 claims abstract description 14
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 10
- 238000001035 drying Methods 0.000 claims abstract description 9
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract 2
- 239000010419 fine particle Substances 0.000 claims description 7
- 238000010304 firing Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- 239000002904 solvent Substances 0.000 abstract description 7
- 230000007062 hydrolysis Effects 0.000 abstract description 4
- 238000006460 hydrolysis reaction Methods 0.000 abstract description 4
- 239000003054 catalyst Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 238000001354 calcination Methods 0.000 abstract 2
- 239000008187 granular material Substances 0.000 abstract 2
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000000499 gel Substances 0.000 description 27
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000003980 solgel method Methods 0.000 description 5
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000012298 atmosphere Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000004031 devitrification Methods 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 238000001879 gelation Methods 0.000 description 2
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical class O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 2
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005229 chemical vapour deposition Methods 0.000 description 1
- OEYIOHPDSNJKLS-UHFFFAOYSA-N choline Chemical compound C[N+](C)(C)CCO OEYIOHPDSNJKLS-UHFFFAOYSA-N 0.000 description 1
- 229960001231 choline Drugs 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000003349 gelling agent Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000007530 organic bases Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL 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
- C03C1/00—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
- C03C1/006—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels to produce glass through wet route
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/12—Other methods of shaping glass by liquid-phase reaction processes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Glass Melting And Manufacturing (AREA)
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.
(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.
一般式5t(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)i
(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。General formula 5t(OR)= (where R represents an alkyl group)
Silicon alkoxides and/or polycondensates thereof, such as (RO)ssi(O5i(OR))nO5i(OR)i
(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. Let this silica sol solution stand still, raise the temperature,
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.
fil 5iC1,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 or the like using fil 5iC1, 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%
(へP=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. In addition, this stress is expressed by the following formula % formula % (P = stress, γ = surface tension, θ = wetting angle, r = pore diameter), and the larger the surface tension is, the smaller the pore diameter is, the larger it becomes. .
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
ックを防止するため沸点が水より高い溶媒、例えば1−
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。Furthermore, Japanese Patent Application Laid-open No. 183129/1983 discloses that solvents with a boiling point higher than water, such as 1-
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、クラン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 without cracking or cracking.
(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、モルホリン及び/又
はN−モルホリンを用い、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, morpholine and/or N-morpholine is used as a solvent for silicon alkoxide, and silica fine particles are further 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
(CHzOンasi(05N(QC)Is)x)nO5
i(QC)lx)z (n −0〜 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, (CHzO on asi(05N(QC)Is)
i(QC)lx)z(n-0~8). One or more of these can be used. The alkyl group of silicon alkoxide is
A methyl group, an ethyl group, a propyl group, a 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モルホリン及び/又は
N−モルホリン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。さらにケトン類、エステル類を併用することもで
きる。The amount of morpholine and/or N-morpholine added to the silicon alkoxide is preferably 0.1 to 5.0 times (molar ratio) to the silicon alkoxide, and commonly used alcohols such as ethanol may also be used together. can. 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。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とモルホリン及び/又はN−モル
ホリン、シリカ微粒子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子などを用いてよ
く混合する。また超音波を照射してもよい。The silicon alkoxide, morpholine and/or N-morpholine, silica fine particles, and water are thoroughly mixed using a starrer or the like in order 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〜b
(作用)
モルホリン及び/又はN−モルホリン並びにシリカ微粒
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。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
50~b at 0°C (Action) Although the details of the action of morpholine and/or N-morpholine and silica fine particles are unknown, the formation of silica fine particles in the gel, the bonding between these silica fine particles in the gel,
It is thought that this contributes to the relaxation of stress generated in the gel during the drying process, making it possible to increase the size of the gel.
実施例1
モルホリンに粒径約7On+sのシリカ微粒子を重量比
でモルホリンに対し2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/ It水溶液をテトラメトキシ
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 mm
のステンレスシャーレに深さ10m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170nm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ックや発泡などのない直径
約110−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 7 On+s were added to morpholine in a weight ratio of 2 to 0.1 times the weight of the morpholine, and after uniformly dispersing the mixture, tetramethoxysilane was added in an amount of 0.9 times the weight of the morpholine. A homogeneous solution was prepared by mixing, and a 0.01 mol/It aqueous solution of choline was added at a weight ratio of 0.64 times that of tetramethoxysilane, and the mixture was sufficiently mixed to obtain a silica sol. The obtained sol was made into a diameter of 200 mm.
The mixture was placed in a stainless steel petri dish to a depth of 10 m, sealed, and allowed to gel at room temperature for 5 days. Thereafter, it was dried at 60°C for 7 days and further dried at 120°C for 1 day to obtain a dried gel with a diameter of about 170 nm. 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 a silica glass having a diameter of about 110° 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:モルホリン=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170m−の乾燥ゲルを得た。Example 2 A dry gel having a diameter of about 170 m was obtained in the same manner as in Example 1, except that a mixed solvent having a volume ratio of methanol:morpholine of 7:3 was used.
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l10m−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。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 m without cracks or foaming. This silica glass has no devitrification or bubbles and is of high quality.
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。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(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 (its shape is not limited to plate-like ones, but rod-like and tubular ones can also be manufactured, and it can be manufactured at a lower cost than before).
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)
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モルホリン及び/又はN−モル
ホリン並びに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 form a sol solution, gelling the sol, drying the gel, and firing, morpholine and/or A method for producing silica glass, characterized by adding N-morpholine and silica fine particles.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18929688A JPH0238324A (en) | 1988-07-28 | 1988-07-28 | Production of silica glass |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18929688A JPH0238324A (en) | 1988-07-28 | 1988-07-28 | Production of silica glass |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0238324A true JPH0238324A (en) | 1990-02-07 |
Family
ID=16238958
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18929688A Pending JPH0238324A (en) | 1988-07-28 | 1988-07-28 | Production of silica glass |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0238324A (en) |
-
1988
- 1988-07-28 JP JP18929688A patent/JPH0238324A/en active Pending
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