JPS6186429A - Glass manufacturing method - Google Patents
Glass manufacturing methodInfo
- Publication number
- JPS6186429A JPS6186429A JP20803584A JP20803584A JPS6186429A JP S6186429 A JPS6186429 A JP S6186429A JP 20803584 A JP20803584 A JP 20803584A JP 20803584 A JP20803584 A JP 20803584A JP S6186429 A JPS6186429 A JP S6186429A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- gel
- sol
- torr
- degassed
- 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
- 239000011521 glass Substances 0.000 title claims description 16
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000000499 gel Substances 0.000 claims description 31
- 238000000034 method Methods 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 18
- 150000004703 alkoxides Chemical class 0.000 claims description 11
- 238000007872 degassing Methods 0.000 claims description 9
- 238000001035 drying Methods 0.000 claims description 8
- 239000002994 raw material Substances 0.000 claims description 5
- 229910052718 tin Inorganic materials 0.000 claims description 3
- 238000005245 sintering Methods 0.000 claims description 2
- 229910052732 germanium Inorganic materials 0.000 claims 1
- 229910052745 lead Inorganic materials 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 13
- 239000000203 mixture Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 239000011888 foil Substances 0.000 description 4
- 238000006460 hydrolysis reaction Methods 0.000 description 4
- CRNJBCMSTRNIOX-UHFFFAOYSA-N methanolate silicon(4+) Chemical compound [Si+4].[O-]C.[O-]C.[O-]C.[O-]C CRNJBCMSTRNIOX-UHFFFAOYSA-N 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000741 silica gel Substances 0.000 description 3
- 229910002027 silica gel Inorganic materials 0.000 description 3
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- -1 ethoxides Chemical class 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920001296 polysiloxane Polymers 0.000 description 2
- 238000003980 solgel method Methods 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 235000021190 leftovers Nutrition 0.000 description 1
- 150000004704 methoxides Chemical class 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003002 pH adjusting agent Substances 0.000 description 1
- 239000005373 porous glass Substances 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical class CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance 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)
- Glass Melting And Manufacturing (AREA)
- Silicon Compounds (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ガラスの製造方法に関するものであり、詳し
くは、金属アルコキシドを原料としてゾルゲル法により
ガラスを製造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing glass, and more particularly to a method for producing glass by a sol-gel method using a metal alkoxide as a raw material.
現在、光ファイバーのプリフォームを作製する方法とし
ては、’VAD法をはじめとする、5scz4等を火炎
中に通しガラス微粒子をターゲット上に堆積させ、得ら
れたガラス多孔質体を焼結しガラス塊を得る、という方
法が主流になっている。これは高純度の多孔質ガラスを
比較的安価に得られる優れた方法である。しかしこの方
法は気相反応であるため添加物として使える物質がガス
化できるものに限られる、という欠点があった。Currently, methods for producing optical fiber preforms include the 'VAD method, in which glass particles such as 5scz4 are passed through a flame and deposited on a target, and the resulting glass porous body is sintered to form a glass lump. The mainstream method is to obtain This is an excellent method for obtaining high-purity porous glass at a relatively low cost. However, since this method is a gas phase reaction, it has the disadvantage that the substances that can be used as additives are limited to those that can be gasified.
そこで、近年、この欠点を補う方法として、81 を
主体とした金属アルコキシドを加水分解し、シリカゲル
あるいは添加元素を含むシリカゲルを得、該シリカゲル
を乾燥させた後無孔化処理等を行い透明ガラスを得る方
法が盛んに研究されている。Therefore, in recent years, as a method to compensate for this drawback, metal alkoxides mainly composed of 81 are hydrolyzed to obtain silica gel or silica gel containing additive elements, and after drying the silica gel, a process such as making it non-porous is performed to make transparent glass. How to obtain it is being actively researched.
一例を挙げれば、シリコンテトラメトキシド等のSt
のアルコキシドをエタノールと充分に攪拌混合した後
、水を加え更に攪拌して加水分解する。この時水にはア
ンモニア等pH調整剤を加えておくことが好ましい。加
水分解反応の開始と共に粒子の析出が始まり、該反応溶
液を内面にシリコーンを塗った容器に移し、乾燥時間を
長くできるようにアルミ箔等で蓋をして例えば60℃程
度の恒温槽中にてゆっくり乾燥させることによシ、ゾル
液のゲル化およびゲルの乾燥を行う。乾燥するに従って
ゲルは収縮し、通常数日を経るとほぼ乾燥が終了する。For example, St such as silicon tetramethoxide
After thoroughly stirring and mixing the alkoxide with ethanol, water is added and further stirred for hydrolysis. At this time, it is preferable to add a pH adjuster such as ammonia to the water. Particles begin to precipitate with the start of the hydrolysis reaction, and the reaction solution is transferred to a container coated with silicone on the inside, covered with aluminum foil or the like to prolong the drying time, and placed in a constant temperature bath at, for example, 60°C. By slowly drying the sol solution, the sol solution is gelled and the gel is dried. The gel shrinks as it dries, and drying is usually completed after several days.
このようにして得たゲルを取り出し、例えば酸素を含む
He 雰囲気中にて加熱する等にょシ無孔化処理を行
い、透明ガラス化する方法かすでに知られている。A method is already known in which the gel thus obtained is taken out and subjected to a non-porous treatment such as heating in an oxygen-containing He 2 atmosphere to turn it into transparent glass.
このようないわゆるゾルゲル法は、アルコキシドが多く
の金属元素について作製できるので、B、 Gs、 A
I、、 Sb、 Ti、 Zr、 Sn、 Y、 Sr
、 Pb、 CB等各種の元素を容易に添加できるとい
う長所がある。This so-called sol-gel method can produce alkoxides for many metal elements, such as B, Gs, A
I, Sb, Ti, Zr, Sn, Y, Sr
, Pb, CB, and other various elements can be easily added.
しかしながら上記の方法においては、ゲルが乾燥あるい
は焼結の過程で割れ易い、という欠点もある。この、ゲ
ルが乾燥時に割れる原因の一つに、気泡の発生が挙げら
れる。However, the above method has the disadvantage that the gel tends to crack during the drying or sintering process. One of the causes of gel cracking during drying is the generation of air bubbles.
ゾル液がゲル化する際、あるいはゲル化後、気泡が発生
することがある。これは、ゾル液中のアルコールの量を
減らす、あるいはpHを高くするなどして、アルコキシ
ドの加水分解反応の速度を高めたときに起こりやすいよ
うである。Bubbles may be generated when or after the sol gels. This seems to occur more easily when the rate of alkoxide hydrolysis reaction is increased by reducing the amount of alcohol in the sol solution or increasing the pH.
気泡が発生すると、そのまわりに歪ができ、気泡のまわ
シに円盤状のクラックが入りやすい。When bubbles occur, distortion occurs around them, and disc-shaped cracks tend to form around the bubbles.
このクラックはゲルの乾燥とともに成長しゲルは割れて
しまう。These cracks grow as the gel dries and the gel breaks.
従ってゲルの割れという欠点を解消するために、気泡発
生を防止する方法の確立が求められている。Therefore, in order to eliminate the drawback of gel cracking, there is a need to establish a method for preventing the generation of bubbles.
本発明は、かかる現状にかんがみてなされたもので、ゾ
ル液を脱気処理することによシ、気泡の発生を防ぐと考
えついたことによるものである。The present invention was made in view of the current situation, and was based on the idea that the generation of air bubbles could be prevented by degassing the sol liquid.
すなわち本発明は原料の少なくとも一つをアルコキシド
とし、ゾル液を得、ゾル液をゲル化し、ゲルを乾燥させ
、その乾燥ゲルを焼結してガラス塊を製造する方法に於
いて、ゾル液を1Torr 以上、常圧未満の減圧下で
脱気処理することを特徴とするガラスの製造方法を提供
する。That is, the present invention uses at least one of the raw materials as an alkoxide, obtains a sol solution, gels the sol solution, dries the gel, and sinters the dried gel to produce a glass lump. Provided is a method for producing glass, characterized in that degassing is carried out under a reduced pressure of 1 Torr or more and less than normal pressure.
そして本発明の好ましい実施態様としては、上記方法に
おいて脱気する際の圧力がゾル液の蒸気圧以下の圧力で
あることが挙げられる。In a preferred embodiment of the present invention, the pressure during degassing in the above method is lower than the vapor pressure of the sol liquid.
さらに、別の好ましい実施態様としては上記方法におい
てゾル液がゲル化する際の圧力がゾル液の蒸気圧より高
い圧力でちることが挙げられる。Furthermore, as another preferred embodiment, in the above method, the pressure at which the sol liquid is gelled is set at a pressure higher than the vapor pressure of the sol liquid.
本発明のアルコキシドとしては、例えば、日!、B、G
o、P、kl、8b、Ti、Zr、 Sn、Y、Fb
bよびCS からなる群より選ばれる少なくとも1
種の元素のアルコキシドが好ましく、例えば上記元素の
メトキシド、エトキシド、プロポキシド、ブトキシド等
を用いることができる。As the alkoxide of the present invention, for example, day! ,B,G
o, P, kl, 8b, Ti, Zr, Sn, Y, Fb
At least one selected from the group consisting of b and CS
Alkoxides of certain elements are preferred, and for example, methoxides, ethoxides, propoxides, butoxides, etc. of the above elements can be used.
まだ少なくとも1以上のアルコキシドを含む原料からゾ
ル液を得るには、通常の加水分解反応等によればよく、
例えばアルコールおよび水を反応に好適濃度となるよう
混合すればよい。In order to obtain a sol solution from a raw material that still contains at least one alkoxide, a normal hydrolysis reaction etc. may be used.
For example, alcohol and water may be mixed to a suitable concentration for the reaction.
アルコールとしてはメタノール、エタノール、プロパツ
ール、ブタノール等から適宜選択される。I7かしこの
方法に限定されるものではなく、いずれの方法で得られ
たゾル液にも本発明方法を適用できる。The alcohol is appropriately selected from methanol, ethanol, propatool, butanol, and the like. I7 However, the method of the present invention is not limited to this method, and the method of the present invention can be applied to a sol obtained by any method.
ゾル液に、[L I Torr 以下の脱気処理を施こ
すことは、特公昭5B−167436号公報にて提案さ
れているが、本発明は、これをI Tarτ以上、常圧
以下の圧力で行なうことが望ましいことを見出したこと
によっている。It has been proposed in Japanese Patent Publication No. 5B-167436 to subject the sol liquid to a degassing treatment at a pressure of [L I Torr or less, but the present invention degassing the sol liquid at a pressure of I Tar or more and less than normal pressure. It is based on finding something desirable to do.
我々の研究によれば、ゾル液は数+TOrr 程度で
沸騰するためこのような脱気処理は、普通、ゾル液の蒸
気圧程度の圧力で行なえば十分である。ただし蒸気圧を
多少下回る程度の圧力で行なえば、脱気時間を短かくで
きる。ゾル液の蒸気圧は、原料の組成によって異なるが
、数十T Or r 程度である。従って脱気は、I
Torr から数十Torr 程度の圧力で行な
うことが望ましいが、これ以上の圧力であっても常圧未
満の圧力であれば効果はある。この際振動を加えること
により、やや脱気効果を高めることができる。According to our research, since the sol boils at about several + TOrr, it is usually sufficient to carry out such deaeration treatment at a pressure about the vapor pressure of the sol. However, if the degassing is carried out at a pressure slightly lower than the vapor pressure, the deaeration time can be shortened. The vapor pressure of the sol liquid varies depending on the composition of the raw material, but is approximately several tens of T Or r . Therefore, degassing is I
It is desirable to carry out the process at a pressure of about Torr to several tens of Torr, but even higher pressures are effective as long as they are lower than normal pressure. At this time, by adding vibration, the deaeration effect can be slightly enhanced.
圧力を、0.1 Torr 以下にすることは、ゾル液
が激しく沸騰し圧力を上げるため、技術的に極めて困難
である。0.1 Torr より高(I Torr未
溝の圧力にすることも困難であり、また必要がない。従
って、脱気は、I Torr 以上常圧未満、特に好ま
しくは20〜60 Torrの圧力、あるいは特にゾル
液の蒸気圧あるいは、それをやや下回る程度の圧力で行
なうことが望ましい。It is technically extremely difficult to reduce the pressure to 0.1 Torr or less because the sol liquid boils violently and the pressure increases. It is difficult and unnecessary to achieve a pressure higher than 0.1 Torr (I Torr), and it is not necessary. Therefore, deaeration is carried out at a pressure of I Torr or more and less than normal pressure, particularly preferably at a pressure of 20 to 60 Torr, or In particular, it is desirable to carry out the process at the vapor pressure of the sol liquid or at a pressure slightly lower than that.
次にゾルがゲル化する際には、ゾル液が沸騰しないよう
な、圧力をゾル液の蒸気圧より高す圧力にする必要があ
る。さもないと、ゲルが沸騰しかかったままゲル化し所
定の形のゲルが得られないからである。このゲル化時の
圧力は常圧以上であってもよいが、常圧より高い圧力に
することは意味のないことである。Next, when the sol gels, the pressure needs to be higher than the vapor pressure of the sol so that the sol does not boil. Otherwise, the gel will turn into a gel while it is about to boil, and a gel of the desired shape will not be obtained. The pressure during this gelation may be higher than normal pressure, but it is meaningless to set the pressure higher than normal pressure.
脱気処理後のゾル液は、公知技術によりゲル化し、ゲル
を乾燥させ、該乾燥ゲルを焼結して透明ガラス塊を得る
。The sol liquid after the deaeration treatment is gelled by a known technique, the gel is dried, and the dried gel is sintered to obtain a transparent glass lump.
以下本発明を例を挙げて説明する。 The present invention will be explained below by giving examples.
実施例1
シリコンテトラメトキシド9.5fと、エタノール&5
fを、マグネチツクスターラで混合し、その中に13%
アンモニア水3滴を加えた水9.Ofを加えさらに混合
した後、試験管4本に、それぞれ5分目になるように入
れた。試験管は、径12■、長さ105雪であり、内面
にシリコーンを塗布しておいた。Example 1 Silicon tetramethoxide 9.5f and ethanol &5
Mix f with a magnetic stirrer and add 13%
Water with 3 drops of ammonia water9. After adding Of and further mixing, the mixture was poured into four test tubes at the 5th minute mark. The test tube had a diameter of 12 cm and a length of 105 cm, and had silicone coated on its inner surface.
このうち2本はそのままゲル化させた。残り02本は6
0 Torr 程度のゾル液が沸騰する圧力で脱気して
から常圧でゲル化させた。すると脱気しなかったものは
2本とも気泡を含んでおり、脱気したものは2本とも気
泡を含んでいなかった。Two of these were allowed to gel as they were. The remaining 02 pieces are 6
The sol liquid was degassed at a boiling pressure of about 0 Torr, and then gelled at normal pressure. Both of the tubes that were not degassed contained air bubbles, and both of the tubes that were degassed contained no air bubbles.
この、4本の試験管1つ1つにアルミ箔で軽くフタをし
、60℃恒温槽に入れた。7日後には、ゲルはほとんど
乾燥していた。脱気しなかったものは、2本とも割れて
いた。脱気したものは2本とも割れなかった。Each of the four test tubes was lightly capped with aluminum foil and placed in a constant temperature bath at 60°C. After 7 days the gel was almost dry. The ones that were not degassed were both cracked. Both of the degassed bottles did not crack.
実施例2
つぎにシリコンテトラメトキシド957と、エタノール
a02を、マグネチツクスターラで混合し、その中に1
!1チアンモニア水3滴を加えた水907を加えさらに
混合した後、実施例1と同様の試験管4本に、それぞれ
5分目になるように入れた。Example 2 Next, silicon tetramethoxide 957 and ethanol a02 were mixed using a magnetic stirrer, and 1
! Water 907 containing 3 drops of 1-thiammonium water was added and further mixed, and the mixture was placed into four test tubes similar to those in Example 1 at the 5th minute mark.
このうち2本はそのままゲル化させた。残シの2本ば6
0 Torr 程度のゾル液が沸騰する圧力で脱気して
から常圧でゲル化させた。すると脱気しなかったものは
2本とも気泡を含んでおシ、脱気したものは2本とも気
泡を含んでいなかった。Two of these were allowed to gel as they were. Two leftovers 6
The sol liquid was degassed at a boiling pressure of about 0 Torr, and then gelled at normal pressure. Both of the tubes that were not degassed contained air bubbles, and both of the tubes that were degassed contained no air bubbles.
この、4本の試験管1つ1つにアルミ箔で軽く7タをし
、60℃恒温槽に入れた。7日後には、ゲルはほとんど
乾燥していた。脱気しなかったものは、2本とも割れて
いた。脱気したものは2本とも割れなかった。Each of the four test tubes was lightly wrapped with aluminum foil and placed in a constant temperature bath at 60°C. After 7 days the gel was almost dry. The ones that were not degassed were both cracked. Both of the degassed bottles did not crack.
実施例3
シリコンテトラメトキシド9.59と、エタノール11
.59を、マグネチツクスターラで混合し、その中に1
5チアンモニア水5滴を加えた水9. Ofを加えさら
に混合した後、実施例1と同様の試験管4本に、それぞ
れ5分目になるように入れた。Example 3 Silicon tetramethoxide 9.59 and ethanol 11
.. Mix 59 with a magnetic stirrer and add 1
5. Water with 5 drops of thiammonia added9. After adding Of and further mixing, the mixture was placed into four test tubes similar to those in Example 1 at the 5th minute mark.
このうち2本はそのままゲル化させた。残りの2本は6
0 Torr 程度のゾル液が沸騰する圧力で脱気して
から常圧でゲル化させた。すると脱気しなかったものの
うち1つは気泡を含んでおり、脱気したものは2本とも
気泡を含んでいなかった。Two of these were allowed to gel as they were. The remaining two are 6
The sol liquid was degassed at a boiling pressure of about 0 Torr, and then gelled at normal pressure. One of the tubes that had not been degassed contained bubbles, and both of the tubes that had been deaerated contained no bubbles.
この、4本の試験管1つ1つにアルミ箔で軽くフタをし
、60℃恒温槽に入れた。7日後には、ゲルはほとんど
乾燥していた。割れたゲルは無かったが、脱気しなかっ
たものの1つはゲル内に気泡を含んでいた。Each of the four test tubes was lightly capped with aluminum foil and placed in a constant temperature bath at 60°C. After 7 days the gel was almost dry. None of the gels were cracked, but one that was not degassed contained air bubbles within the gel.
脱気処理した6つのゲルを1300℃の温度で焼結し、
透明ガラスを得た。The six degassed gels were sintered at a temperature of 1300°C,
A transparent glass was obtained.
比較例1
真空容器内に何も入れないまま真空ポンプで引いたとこ
ろ、数分で10−’ Torr程度に達した。Comparative Example 1 When nothing was put into the vacuum container and the vacuum pump was used, the pressure reached about 10-' Torr in a few minutes.
次に実施例3と同一の組成のゾル液を上記の真空容器内
に入れ、真空ポンプで引いたところ、1、 OTorr
程度の圧力で激しく沸騰をはじめ、これ以下の圧力に
することはできなかった。Next, a sol solution with the same composition as in Example 3 was placed in the vacuum container described above and pulled with a vacuum pump, resulting in 1. OTorr.
It began to boil violently at a certain pressure, and it was not possible to reduce the pressure below this level.
次にこのゾル液の入った真空容器を一10℃に冷却しな
がら真空ポンプで引いたが、この温度では20 Tor
r 5度で激しく沸騰した。Next, the vacuum container containing this sol liquid was cooled to -10°C and pulled with a vacuum pump, but at this temperature, the pressure was 20 Torr.
r It boiled violently at 5 degrees.
以上の実験において60 Torr 、 20 T
orrは夫々常温、−10℃におけるゾル液の蒸気圧程
度の圧力であり、従ってI Torr 未満の圧力に
するのは非常に困難である。In the above experiments, 60 Torr and 20 T
orr is a pressure approximately equal to the vapor pressure of the sol liquid at room temperature and −10° C., and therefore it is very difficult to reduce the pressure to less than I Torr .
本発明によれば、気泡を含まない、従って乾燥時に割れ
にくhゲルを得ることが容易にできる優れた効果を有す
る。According to the present invention, it is possible to easily obtain a gel that does not contain air bubbles and therefore does not crack during drying.
Claims (4)
液を得、ゾル液をゲル化し、ゲルを乾燥させ、その乾燥
ゲルを焼結してガラス塊を製造する方法に於いて、ゾル
液を1Torr以上、常圧未満の減圧下で脱気処理する
ことを特徴とするガラスの製造方法。(1) In the method of producing a glass lump by using at least one of the raw materials as an alkoxide, obtaining a sol solution, gelling the sol solution, drying the gel, and sintering the dried gel, the sol solution is heated to 1 Torr. As described above, the method for producing glass is characterized in that the degassing treatment is carried out under reduced pressure below normal pressure.
、Sb、Ti、Zr、Sn、Y、PbおよびCsからな
る群より選ばれる少なくとも1種の元素のアルコキシド
である特許請求の範囲第(1)項記載のガラスの製造方
法。(2) The alkoxide is Si, B, Ge, P, Al
, Sb, Ti, Zr, Sn, Y, Pb and Cs.
より高い圧力である特許請求の範囲第(1)項記載のガ
ラスの製造方法。(3) The method for manufacturing glass according to claim (1), wherein the pressure at which the sol liquid gels is higher than the vapor pressure of the sol liquid.
力である特許請求の範囲第(1)項記載のガラスの製造
方法。(4) The method for producing glass according to claim (1), wherein the pressure during the degassing treatment is lower than the vapor pressure of the sol liquid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20803584A JPS6186429A (en) | 1984-10-05 | 1984-10-05 | Glass manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20803584A JPS6186429A (en) | 1984-10-05 | 1984-10-05 | Glass manufacturing method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6186429A true JPS6186429A (en) | 1986-05-01 |
Family
ID=16549577
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20803584A Pending JPS6186429A (en) | 1984-10-05 | 1984-10-05 | Glass manufacturing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6186429A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6296325A (en) * | 1985-10-21 | 1987-05-02 | Hoya Corp | Production of glass by sol gel method |
JPS6465029A (en) * | 1987-09-04 | 1989-03-10 | Toshiba Ceramics Co | Production of glass |
US5196383A (en) * | 1989-12-20 | 1993-03-23 | Sumitomo Electric Industries, Ltd. | Method for producing rare earth element-doped glass by sol-gel process |
-
1984
- 1984-10-05 JP JP20803584A patent/JPS6186429A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6296325A (en) * | 1985-10-21 | 1987-05-02 | Hoya Corp | Production of glass by sol gel method |
JPH0556292B2 (en) * | 1985-10-21 | 1993-08-19 | Hoya Corp | |
JPS6465029A (en) * | 1987-09-04 | 1989-03-10 | Toshiba Ceramics Co | Production of glass |
JP2577573B2 (en) * | 1987-09-04 | 1997-02-05 | 東芝セラミックス株式会社 | Glass manufacturing method |
US5196383A (en) * | 1989-12-20 | 1993-03-23 | Sumitomo Electric Industries, Ltd. | Method for producing rare earth element-doped glass by sol-gel process |
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