JPS63256539A - Production of silica glass - Google Patents
Production of silica glassInfo
- Publication number
- JPS63256539A JPS63256539A JP9376087A JP9376087A JPS63256539A JP S63256539 A JPS63256539 A JP S63256539A JP 9376087 A JP9376087 A JP 9376087A JP 9376087 A JP9376087 A JP 9376087A JP S63256539 A JPS63256539 A JP S63256539A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- silica glass
- water
- gel
- silica gel
- 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.)
- Granted
Links
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- -1 silicic acid ester Chemical class 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000000741 silica gel Substances 0.000 claims abstract description 14
- 229910002027 silica gel Inorganic materials 0.000 claims abstract description 14
- 239000002253 acid Substances 0.000 claims abstract description 9
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 6
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims abstract description 6
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 4
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims abstract description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 3
- 235000019253 formic acid Nutrition 0.000 claims abstract description 3
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 14
- 230000007062 hydrolysis Effects 0.000 claims description 9
- 238000006460 hydrolysis reaction Methods 0.000 claims description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 8
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 abstract description 3
- 235000012239 silicon dioxide Nutrition 0.000 abstract 3
- 239000000499 gel Substances 0.000 description 18
- 238000003980 solgel method Methods 0.000 description 6
- 235000019441 ethanol Nutrition 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 238000010304 firing Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000006184 cosolvent Substances 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 239000011888 foil Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002699 waste material Substances 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
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)
- Silicon Compounds (AREA)
- Glass Melting And Manufacturing (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は改良されたシリカガラスの製造法に関し、さら
に詳しくいえば、大型形状のシリカガラスを収率良くし
かも低温で製造する方法に関するものである1本発明に
よって得られるシリカガラスは、光通信ファイバーの材
料として利用するこ°ニー゛ゲ1ができる。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an improved method for producing silica glass, and more specifically, to a method for producing large-sized silica glass with high yield and at low temperatures. The silica glass obtained by the present invention can be used as a material for optical communication fibers.
1.1
9.〔従来の技術〕
融して作る方法、5iCI24を酸化して微粒子とした
後に焼結する方法、及びゾル・ゲル法と呼ばれる5i(
OC@Hzt+z)4を原料としてシリカゲルを得、こ
れを焼成してシリカガラスを得る方法の、大別して3種
の方法がある。本発明の方法はゾル・ゲル法に属するも
のである。ゾル・ゲル法では、極めて高純度のシリカガ
ラスを他の2種の方法よりもはるかに低い1200℃程
度の焼成温度で製造することができる。しかしながら、
ゾル・ゲル法においてはシリカゲル作成中あるいはシリ
カゲルの焼成中にゲルが割れ易く、大型形状の製品を収
率良く得ることは非常に困難であった。ゲルの割れを防
ぐために、特殊な化学薬品(例えばホルムアミド)を用
いたり、ゲルを溶媒の超臨界条件下で作成したりする方
法が提案されているが、そのような方法では、人体に有
害な廃棄物が副生物として出た、−リ2、大型の装置が
必要となる等の新たな問題点が1゜
生、しる。1.1 9. [Prior art] A method of melting 5iCI24, a method of oxidizing 5iCI24 to form fine particles, and then sintering it, and a method of sintering 5iCI24, which is called the sol-gel method.
There are three types of methods: silica gel is obtained using OC@Hzt+z)4 as a raw material, and silica glass is obtained by firing the silica gel. The method of the present invention belongs to the sol-gel method. The sol-gel method can produce extremely high-purity silica glass at a firing temperature of about 1200° C., which is much lower than the other two methods. however,
In the sol-gel method, the gel tends to break during the preparation or firing of the silica gel, making it extremely difficult to obtain large-sized products with good yield. In order to prevent gels from cracking, methods have been proposed that use special chemicals (for example, formamide) or create gels under supercritical conditions in solvents, but such methods do not contain substances that are harmful to the human body. New problems arise, such as the generation of waste as by-products and the need for large equipment.
:□ヵ’Ml& Lよう、オう□、つ。:□ka’Ml& Lyo, oh□, tsu.
!
、−二〕本発明の目的は、ゾル・ゲル法におけるシリカ
ガラス作成中のゲルの割れをなくし、大型形状のシリカ
ガラスを効率的に製造する方法を提供することにある。! ,-2] An object of the present invention is to provide a method for efficiently producing large-sized silica glass by eliminating gel cracking during the production of silica glass in the sol-gel method.
本発明者は前記目的を達成すべき鋭意研究を重ねた結果
、 5i(OC,H工+1)、で表わされるケイ酸エス
テルをあらかじめ部分的に加水分解させた後、さらに完
全な加水分解を得て重合させることにより割れのない強
固なシリカガラスを得、これを加熱処理することにより
大型形状のシリカガラスを収率良く製造し得ることを見
出し、この知見に基づいて本発明をなすに至った。As a result of extensive research to achieve the above object, the inventors of the present invention partially hydrolyzed the silicate ester represented by 5i (OC, H + 1), and then obtained further complete hydrolysis. The inventors discovered that strong silica glass without cracks can be obtained by polymerizing the silica glass, and that large-sized silica glass can be produced in good yield by heat-treating the same.Based on this knowledge, the present invention was developed. .
すなわち、本発明は、一般式5i(QC乳Hzl+x)
*(ただしnは1から8の整数)で表わされるケイ酸エ
ステルを酸と水とであらかじめ部分的に加水分解させ、
た後、さらに水を加えて完全に加水分解させることによ
り強固なシリカゲルとなし、これを加熱処理することに
よってシリカガラスを得ることを特徴とするシリカガラ
スの製造方法を提供するものである。That is, the present invention provides general formula 5i (QC milk Hzl+x)
A silicate ester represented by * (where n is an integer from 1 to 8) is partially hydrolyzed in advance with acid and water,
The present invention provides a method for producing silica glass, which is characterized in that the silica gel is then completely hydrolyzed by adding water to form a strong silica gel, which is then heat-treated to obtain silica glass.
Si (QC%H工+1)4で表わされる物質は、ケイ
酸エステルと呼ばれる液体であるが、これは(1)式の
ように加水分解をうけると共に、(2)式のように重合
してシリカゲルとなる。The substance represented by Si (QC%H+1)4 is a liquid called silicate ester, which undergoes hydrolysis as shown in equation (1) and polymerization as shown in equation (2). It becomes silica gel.
シリカガラスはSin、で表わされるが、上式の最終段
階までの反応を表わすと次のようになる。Silica glass is represented by Sin, and the reaction up to the final stage of the above equation is expressed as follows.
5i(oc、H,、,1)、+2H,on 5iOz+
4C++HzmtOH(3)(1)及び(2)の反応が
ある程度進行すると、ケイ酸エステルは固まってシリカ
ゲルとなる。このシリカゲルを1200℃以下の温度で
加熱処理することにより、(1)及び(2)式が完全に
進行し、シリカゲル中に生じた気孔も閉じて、シリカガ
ラスとなる。5i(oc,H,,,1),+2H,on 5iOz+
When the reactions of 4C++HzmtOH (3) (1) and (2) proceed to a certain extent, the silicate ester solidifies and becomes silica gel. By heat-treating this silica gel at a temperature of 1200° C. or lower, equations (1) and (2) proceed completely, the pores generated in the silica gel are also closed, and silica glass is formed.
(1)式の進行を促進するため、ケイ酸エステルめ分子
数の1万分の1ないし10分の1程度の酸が用いられる
。この場合、酸としては、酢酸、ギ酸。In order to promote the progression of the formula (1), an acid having a number of about 1/10,000 to 1/10 of the number of molecules of the silicate ester is used. In this case, the acid is acetic acid or formic acid.
塩酸、硝酸、硫酸等が用いられる。また、ケイ酸エステ
ルと水とは混合しないため、共溶媒として炭素数1から
8のアルコールが用いられる。Hydrochloric acid, nitric acid, sulfuric acid, etc. are used. Further, since silicate ester and water do not mix, an alcohol having 1 to 8 carbon atoms is used as a co-solvent.
ケイ酸エステルを加水分解し、重合させて得られるシリ
カゲルは、多孔質であり、温度や湿度の変化に対して弱
く、壊れ易い。したがって、ゲルの破壊が従来のゾル・
ゲル法の大きな問題点であった。しかし、本発明のよう
に、ケイ酸エステルの加水分解及び重合過程を調節する
ことにより、温度や湿度の変化に強い、強固なゲルを作
ることが可能である。従来のゾル・ゲル法においては、
完全な加水分解に必要な量の水を一度に加えていたため
、(1)式と(2)式が同時に進行し、ゲルの内部にお
いて、強度の高い所と低い所が不規則に分布しており、
これがゲルの強度低下の原因となっ七いた。Silica gel obtained by hydrolyzing and polymerizing a silicate ester is porous, sensitive to changes in temperature and humidity, and easily broken. Therefore, the destruction of the gel is different from that of the conventional sol.
This was a major problem with the gel method. However, as in the present invention, by controlling the hydrolysis and polymerization processes of silicate ester, it is possible to create a strong gel that is resistant to changes in temperature and humidity. In the conventional sol-gel method,
Because the amount of water required for complete hydrolysis was added at once, equations (1) and (2) proceeded simultaneously, and areas of high and low strength were irregularly distributed inside the gel. Ori,
This caused a decrease in the strength of the gel.
本発明においては、まずケイ酸エステルを完全に加水分
解せず、酸と、ケイ酸エステル1分子に対して0.5か
ら1.5分子の水を用いてケイ酸エステルを部分的に加
水分解する。このとき温度は室温ないし70℃で行なう
。この操作によってケイ酸エステルは全分子が均等に加
水分解をうけ、しかもそれが部分的であるために、ゲル
とはならず、当初の流動性を保っている。これを6時間
ないし3日間保持することにより、均等化を促進する。In the present invention, the silicate ester is not completely hydrolyzed first, but is partially hydrolyzed using an acid and 0.5 to 1.5 molecules of water per molecule of the silicate ester. do. At this time, the temperature is room temperature to 70°C. Through this operation, all molecules of the silicate ester undergo hydrolysis evenly, and because it is only partially hydrolyzed, it does not form a gel and maintains its original fluidity. By holding this for 6 hours to 3 days, equalization is promoted.
保持時間は、温度が高いほど短かくしても良い。この保
持操作により、後で得られるシリカゲルの内部の強度の
分布がなくなり、ゲルが割れにくくなる。The holding time may be made shorter as the temperature is higher. This holding operation eliminates the internal strength distribution of the silica gel that will be obtained later, making the gel less likely to crack.
保持を行なった後に、加水分解を完全に進行させるため
、さらに水を加える。この時加える水の量は、はじめに
加えた水の量と合計して、ケイ酸エステルの分子数比に
して2倍以上とする必要がある。また、水とケイ酸エス
テルとは混和しないため、適当量の共溶媒としてのアル
コールを加える。アルコールの量、及び加える時期は特
に限定しないが、溶液が不混和とならないように、望ま
しくはケイ酸エステルと同じ分子数以上を、初期に加え
ておく。After holding, more water is added to ensure complete hydrolysis. The amount of water added at this time needs to be at least twice the number of molecules of the silicate ester, including the amount of water added initially. Furthermore, since water and silicate ester are immiscible, an appropriate amount of alcohol as a co-solvent is added. The amount of alcohol and the timing of addition are not particularly limited, but it is desirable to add at least the same number of molecules as the silicate ester at the beginning so that the solution does not become immiscible.
水を加えた後は、溶液を室温から70℃の範囲に放置す
る。このとき、溶液の蒸発を抑える目的でおおいを施し
ても良い。溶液は数日以内で固まってゲルとなる。この
ゲルを毎分5℃以下の昇温速度で、最高1200℃の温
度まで加熱処理することによってシリカガラスが得られ
る。After adding water, the solution is left at a temperature ranging from room temperature to 70°C. At this time, a cover may be applied for the purpose of suppressing evaporation of the solution. The solution solidifies into a gel within a few days. Silica glass is obtained by heat-treating this gel at a heating rate of 5° C. or less per minute to a maximum temperature of 1200° C.
次に本発明を実施例によりさらに詳細に説明する。 Next, the present invention will be explained in more detail with reference to Examples.
実施例
5i(OCH,)、30.4 g 、水3.6g、酢酸
0.01モル、エチルアルコール40m Qを混合し、
24時間室温で撹拌して部分的な加水分解を進行させた
。その抜水22.4 g、エチルアルコール20mg、
酢酸0.01モルの混合液を加え、容器をアルミ箔でお
おって60℃に保持した。アルミ箔のおおいはその後1
日に1個の割合で針で穴をあけた。3日後、溶液はゲル
となった。ゲルは60℃でさらに1週間乾燥させ、そめ
後、電気炉で毎時10℃の昇温速度で900℃までの加
熱処理を行なった。ゲルの形状は容器と相似の円柱形(
直径1an、高さ5備)であり、得られたシリカガラス
は、ゲル中の気孔の消滅により直径8mm、高さ40!
11程度になっていたが、割れてぃなかった。得られた
シリカガラスは透明であり、通常のシリカガラスと同じ
2.20g/a&の密度であった。Example 5i (OCH,), 30.4 g, water 3.6 g, acetic acid 0.01 mol, ethyl alcohol 40 m Q were mixed,
Partial hydrolysis was allowed to proceed by stirring at room temperature for 24 hours. 22.4 g of drained water, 20 mg of ethyl alcohol,
A mixed solution of 0.01 mol of acetic acid was added, and the container was covered with aluminum foil and maintained at 60°C. Then cover the aluminum foil 1
A hole was made with a needle at a rate of one per day. After 3 days, the solution became a gel. The gel was further dried at 60° C. for one week, and after cooling, it was heated to 900° C. in an electric furnace at a temperature increase rate of 10° C./hour. The shape of the gel is a cylinder similar to the container (
The resulting silica glass has a diameter of 8 mm and a height of 40 mm due to the disappearance of pores in the gel.
It was about 11, but it wasn't broken. The obtained silica glass was transparent and had the same density as normal silica glass, 2.20 g/a&.
比較のために、同じ原料を同量、一度に全部加えたとこ
ろ、やはり3日後にゲルが得られだが、それは8片に割
れていた。さらにこれを同様に加熱処理したところ、6
50℃に到達する前に粉々に砕け、塊のガラスは得られ
なかった。For comparison, I added the same amount of the same ingredients all at once, and after 3 days I still got a gel, but it was broken into 8 pieces. Furthermore, when this was heat-treated in the same way, 6
It broke into pieces before reaching 50°C and no lump glass was obtained.
コノ実験により、本発明の方法の有効性が示された。The experiments demonstrated the effectiveness of the method of the present invention.
指定代理人 工業技術院北海道工業開発試験所長後藤藤
太部Designated Agent: Director of Hokkaido Industrial Development Testing Institute, Agency of Industrial Science and Technology, Taibe Goto
Claims (4)
(ただし、nは1から8の整数)で表わされるケイ酸エ
ステルを酸と水とであらかじめ部分的に加水分解させた
後、さらに水を加えて完全に加水分解させることにより
強固なシリカゲルとなし、これを加熱処理することによ
ってシリカガラスを得ることを特徴とするシリカガラス
の製造法。(1) General formula Si(OC_nH_2_n_+_1)_4
(However, n is an integer from 1 to 8) After partially hydrolyzing the silicate ester with acid and water, water is added to completely hydrolyze it to form a strong silica gel. A method for producing silica glass, characterized in that silica glass is obtained by heat-treating the silica glass.
に対し0.5〜1.5分子の水を用いる特許請求の範囲
第1項の方法。(2) The method according to claim 1, in which 0.5 to 1.5 molecules of water are used per molecule of silicate ester in the partial hydrolysis.
る特許請求の範囲第1項又は第2項の方法。(3) The method according to claim 1 or 2, in which acetic acid, formic acid, hydrochloric acid, nitric acid, or sulfuric acid is used as the acid.
ルコールを用いる特許請求の範囲第1項〜第3項のいず
れかの方法。(4) The method according to any one of claims 1 to 3, in which an alcohol having 1 to 8 carbon atoms is used as a solvent in the hydrolysis.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9376087A JPS63256539A (en) | 1987-04-15 | 1987-04-15 | Production of silica glass |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9376087A JPS63256539A (en) | 1987-04-15 | 1987-04-15 | Production of silica glass |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63256539A true JPS63256539A (en) | 1988-10-24 |
JPH0517173B2 JPH0517173B2 (en) | 1993-03-08 |
Family
ID=14091387
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9376087A Granted JPS63256539A (en) | 1987-04-15 | 1987-04-15 | Production of silica glass |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63256539A (en) |
-
1987
- 1987-04-15 JP JP9376087A patent/JPS63256539A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPH0517173B2 (en) | 1993-03-08 |
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JPH0551539B2 (en) | ||
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |