JPH0238325A - Production of silica glass - Google Patents
Production of silica glassInfo
- Publication number
- JPH0238325A JPH0238325A JP18929788A JP18929788A JPH0238325A JP H0238325 A JPH0238325 A JP H0238325A JP 18929788 A JP18929788 A JP 18929788A JP 18929788 A JP18929788 A JP 18929788A JP H0238325 A JPH0238325 A JP H0238325A
- Authority
- JP
- Japan
- Prior art keywords
- gel
- silica glass
- silica
- methyl
- silicon alkoxide
- 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
- 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
- 238000001035 drying Methods 0.000 claims abstract description 9
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 8
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract 2
- 239000010419 fine particle Substances 0.000 claims description 5
- 238000010304 firing Methods 0.000 claims 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 abstract description 9
- 239000002904 solvent Substances 0.000 abstract description 6
- 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
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 238000001354 calcination Methods 0.000 abstract 2
- 239000008187 granular material Substances 0.000 abstract 2
- 239000000499 gel Substances 0.000 description 28
- 238000000034 method Methods 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 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
- 239000002245 particle 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
- YNAVUWVOSKDBBP-UHFFFAOYSA-N Morpholine Chemical compound C1COCCN1 YNAVUWVOSKDBBP-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
- 230000015572 biosynthetic process Effects 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
- 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
- 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
- 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
- 230000007423 decrease Effects 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
- ARYZCSRUUPFYMY-UHFFFAOYSA-N methoxysilane Chemical compound CO[SiH3] ARYZCSRUUPFYMY-UHFFFAOYSA-N 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
- 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
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 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
- 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
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (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スmり
である。The method for producing silica glass by the sol-gel method is as follows.
一般式5i(OR)n(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)isi(OSi(OR))nO5i(OR)+
(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。Silicon alkoxides and/or polycondensates thereof represented by the general formula 5i(OR)n (where R represents an alkyl group), such as (RO)isi(OSi(OR))nO5i(OR)+
(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.
(115iC14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 115iC14 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6
(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。(2) Since it can be used as a raw material in a liquid state, it can be easily purified and highly purified.6 (3) It can be mixed in a liquid phase at room temperature, so it can form a homogeneous glass 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ックや割れが発生
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。クラックや
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ン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一応力、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 cracks and fractures are likely to occur in the gel during the process of drying the gel, making it difficult to produce a monolithic large-sized dried gel with a good 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 it is thought that if this stress is greater than the strength of the gel, the gel will crack or crack. 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Igさ
れている。In addition, JP-A-61-183129 discloses that solvents with boiling points higher than water, such as 1-
A method of adding butanol, 1-pentanol, 1-hexanol, and toluene to silicon alkoxide has been described.
(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ッ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7容媒としてN−メチル−ピロリ
ドンを用い、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 has been developed to prevent the occurrence of such large stress. In order to avoid this problem, N-methyl-pyrrolidone is used as the silicon alkoxide medium 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
(CH30) isi (O5i(OCHs) z)n
O3i(OCI+3) 3(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, (CH30) isi (O5i (OCHs) z) n
O3i(OCI+3)3(n=O~8) can be mentioned. 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 preferable.
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N−メチル−ピロリド
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 N-methyl-pyrrolidone added to silicon alkoxide is 0.1 to 5% based on silicon alkoxide.
.. 0 times (molar ratio) is preferred. Moreover, commonly used alcohols such as ethanol can also be used together. 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、N−メチル−ピロリドン、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ラ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, N-methyl-pyrrolidone, silica fine particles, and water are thoroughly mixed using a stirrer 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.
その後ゲルーゾル法で焼結することによりシリカガラス
を製造する。Silica glass is then produced by sintering using the 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、O’C
〜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1000〜13
00℃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, O'C
Leave at ~100°C for several minutes to several 10 days, leave at room temperature ~100°C for several hours to several 10 days, and leave at room temperature ~100°C for 1000 to 13 days in an appropriate atmosphere.
For example, heating to 00°C at a temperature increase rate of 50 to 200°C/hour.
(作用)
N−メチル−ピロリドン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 action of N-methyl-pyrrolidone and silica particles are unknown, but the formation of silica particles in the gel, the bonding between these silica particles in the gel, and the formation of silica particles in the gel during the drying process. It is thought that this contributes to stress relaxation and the like, making it possible to increase the size of the gel.
実施例I
N−メチル−ピロリドンに粒径約7001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 mo171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。Example I After adding silica fine particles having a particle size of about 7001 to N-methyl-pyrrolidone at a weight ratio of 0.1 times the weight ratio of morpholine and uniformly dispersing the particles, silica particles having a particle size of about 7001 mm were added to N-methyl-pyrrolidone and dispersed uniformly. Methoxysilane was mixed to create a homogeneous solution, and 0.01 mo171 aqueous solution of choline was added in a weight ratio of 0.64 times that of tetramethoxysilane, and thoroughly mixed to obtain a silica sol.
得られたゾルを直径200mのステンレスシャーレに深
さ100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170mm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0.65 g /cdで
ありクラッ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。The obtained sol was placed in a stainless steel Petri dish with a diameter of 200 m to a depth of 100 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 mm. The bulk density of the dry gel thus obtained was 0.65 g/cd, with no cracks or breaks. This dried gel was heated in air to 1250° C. at a rate of 60° C./hour to obtain silica glass having 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;N−メチル−ピロリドン=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1701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 2 A dry gel having a diameter of about 170 mm was obtained in the same manner as in Example 1, except that a mixed solvent having a volume ratio of methanol:N-methyl-pyrrolidone=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 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.
(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
りクラッ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 generating cracks or breaks. 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, it can be used not only in fields such as photomask substrates for IC manufacturing, which have been conventionally 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N−メチル−ピロリドン及びシ
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 form a sol solution, gelling the sol, drying the gel, and firing, N-methyl- A method for producing silica glass, characterized by adding pyrrolidone and silica fine particles.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18929788A JPH0238325A (en) | 1988-07-28 | 1988-07-28 | Production of silica glass |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18929788A JPH0238325A (en) | 1988-07-28 | 1988-07-28 | Production of silica glass |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0238325A true JPH0238325A (en) | 1990-02-07 |
Family
ID=16238975
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18929788A Pending JPH0238325A (en) | 1988-07-28 | 1988-07-28 | Production of silica glass |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0238325A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0345519A (en) * | 1989-07-13 | 1991-02-27 | Toyo Ink Mfg Co Ltd | Production of glass from liquid phase |
-
1988
- 1988-07-28 JP JP18929788A patent/JPH0238325A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0345519A (en) * | 1989-07-13 | 1991-02-27 | Toyo Ink Mfg Co Ltd | Production of glass from liquid phase |
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