JPS598625A - Preparation of quartz glass - Google Patents
Preparation of quartz glassInfo
- Publication number
- JPS598625A JPS598625A JP11756782A JP11756782A JPS598625A JP S598625 A JPS598625 A JP S598625A JP 11756782 A JP11756782 A JP 11756782A JP 11756782 A JP11756782 A JP 11756782A JP S598625 A JPS598625 A JP S598625A
- Authority
- JP
- Japan
- Prior art keywords
- alkoxysilane
- water
- quartz glass
- gel
- ethanol
- 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
Abstract
Description
【発明の詳細な説明】
本発明はゾル−ゲル法を用いて、アルコキシシランの加
水分解を溶媒のアルコールを加えず水との二成分系で行
なう石英ガラスの製造法に関するゾル−ゲル法は金属ア
ルコキシドを加水分解し、ゲル化させ得られた乾燥ゲル
を加熱する非溶融ガラス製造法である。金属アルコキシ
ドを出発原料とすると原料精製が容易であり、溶融法で
作ることが困難な組成でも均質なガラスを比較的低温で
作ることができる。溶融法により石英ガラスを作製する
場合、原料の調整が困難なうえ純度も低く1700〜2
000℃の高温を必要とするが、ゾル−ゲル法を用いる
と1000℃以下でガラス化が起こり石英ガラスが得ら
れる。しかし、一般に加水分解後のゲル化収縮過程、あ
るいは乾燥ゲルの加熱の途中で破砕しやすいという欠点
があるゲル化収縮過程での割れを防ぐためには収縮率が
小さいこと、すなわち加水分解反応液中のテトラヒドロ
キシシランの濃度が高いことが必要である。また乾燥ゲ
ルの加熱の途中での破砕を防ぐためには加水分解を完全
に行なうことが必要である。反応が速く、終了が容易に
確認できることが望ましい。Detailed Description of the Invention The present invention uses a sol-gel method to hydrolyze alkoxysilane in a two-component system with water without adding alcohol as a solvent. This is a non-melting glass manufacturing method in which alkoxides are hydrolyzed and the resulting dry gel is heated. When a metal alkoxide is used as a starting material, it is easy to purify the raw material, and homogeneous glass can be produced at a relatively low temperature even if the composition is difficult to produce by a melting method. When producing quartz glass by the melting method, it is difficult to adjust the raw materials and the purity is low, 1700~2
Although a high temperature of 1,000°C is required, when the sol-gel method is used, vitrification occurs at a temperature of 1,000°C or lower and quartz glass can be obtained. However, in order to prevent cracking during the gelation shrinkage process after hydrolysis, or during the gelation shrinkage process, which has the disadvantage that it tends to break during the heating of the dry gel, it is necessary to have a small shrinkage rate. A high concentration of tetrahydroxysilane is required. Further, in order to prevent the dried gel from being crushed during heating, it is necessary to completely hydrolyze the gel. It is desirable that the reaction be quick and that completion can be easily confirmed.
従来のアルコキシシランの加水分解反応は溶媒としてア
ルコールを加え、均−系で行なっていた。アルコキシシ
ランと水を溶解させるためにはアルコールが相当な量必
要であるためゲル化が遅く、ゲル化後の収縮率が大きい
ため割れやゆるみを生じた。また均−系であるため反応
の進み方が遅く、どの程度加水分解が終ったかわからな
いため、必要以上の時間攪拌を続けなければならなかっ
た。原料費の中のアルコールの占める割合も多く、乾燥
の際大量のアルコールが蒸発して危険である。量産の場
合、低コスト・安全を目ざす意味でゲル化に仕込む加水
分解反応溶液中のアルコール量は少ない方がよい。Conventionally, the hydrolysis reaction of alkoxysilane has been carried out homogeneously by adding alcohol as a solvent. Since a considerable amount of alcohol is required to dissolve the alkoxysilane and water, gelation is slow, and the shrinkage rate after gelation is large, resulting in cracking and loosening. Furthermore, since the reaction is a homogeneous system, the reaction progresses slowly and it is not possible to determine how much hydrolysis has been completed, so stirring had to be continued for a longer time than necessary. Alcohol accounts for a large proportion of the raw material cost, and a large amount of alcohol evaporates during drying, which is dangerous. In the case of mass production, the amount of alcohol in the hydrolysis reaction solution used for gelation should be small in order to aim for low cost and safety.
本発明はかかる欠点を除去したものでアルコキシシラン
と水とを二層のまま激しく攪拌することにより、短時間
で加水分解反応を終了させる。系が発熱して均一溶液に
なることにより、その終了を確認できる。そして加水分
解反応溶液中のアルコール量を減らし、テトラヒドロキ
シシランの濃度を高くすることにより、安全で収縮によ
り割れることなく乾燥ゲルを得ることができた。The present invention eliminates this drawback, and by vigorously stirring the alkoxysilane and water in two layers, the hydrolysis reaction is completed in a short time. The completion of the process can be confirmed by the system generating heat and becoming a homogeneous solution. By reducing the amount of alcohol in the hydrolysis reaction solution and increasing the concentration of tetrahydroxysilane, it was possible to obtain a dry gel safely and without cracking due to shrinkage.
以下実験例に基づいて本発明の詳細な説明する1、畠
現在塊状石英ガラスをゾル−ゲル法で製造する場合、オ
ルトケイ酸エチルに対し水をモル比で(H2O) /
(5BoazHs)4)が5〜15となる条件で加水分
解が行なわれている。反応は(1)式及び(2)式で示
される。The present invention will be described in detail below based on experimental examples. 1. When producing bulk quartz glass by the sol-gel method, the molar ratio of water to ethyl orthosilicate (H2O) /
Hydrolysis is carried out under conditions such that (5BoazHs)4) is 5 to 15. The reaction is shown by formulas (1) and (2).
n5i(002H6)4+4nH20→n5i(OH)
4十4n02H50H−−・(g
nSi(oH) 4 →m5102−1−2nH20・
・−(2)水の量が5倍モル以下だと充分に加水分解せ
ず、その乾燥ゲルをその後高温で加熱しても黒化して透
明になりにくい。また15倍モル以上の量の水は無意味
かつ、ゲル化時間を遅らせるのみで不要である。n5i(002H6)4+4nH20→n5i(OH)
4102-1-2nH20・(g nSi(oH) 4 →m5102-1-2nH20・
-(2) If the amount of water is less than 5 times the mole, sufficient hydrolysis will not occur, and even if the dried gel is subsequently heated at a high temperature, it will become black and difficult to become transparent. Moreover, water in an amount of 15 times the mole or more is meaningless and is unnecessary because it only delays the gelation time.
オルトケイ酸エチル22 m l (0,1mot )
に10倍モルの水18 m t (i、 Omot)
を加えると完全に21mに分れた。これを均−系にす
るためにはエタノール36 m l (0,6mat
)が必要であり、容積は約2倍になってしまう。そこで
加水分解反応の触媒として塩酸を(Hal ) / (
sl(oc+as)4〕が0.02となるように加え、
溶媒としてエタム)
ノールを全く加えずに2層のまま室温にて激しく攪拌し
た。約5分後に透明な均−系に変わり、発熱して糸の温
度が40℃以上まで上昇した。Ethyl orthosilicate 22 ml (0.1 mot)
10 times the molar amount of water 18 m t (i, Omot)
When added, it was completely divided into 21 meters. To make this a homogeneous system, add 36 ml of ethanol (0.6 ml).
) is required, and the volume will approximately double. Therefore, hydrochloric acid was used as a catalyst for the hydrolysis reaction (Hal) / (
sl(oc+as)4] is 0.02,
The two layers were vigorously stirred at room temperature without adding any ethanol (etham as a solvent). After about 5 minutes, the yarn turned into a transparent homogeneous system and generated heat, raising the temperature of the yarn to over 40°C.
液体クロマトグラフィ分析により、原料のオルトケイ酸
エチルがなくなり、エタノールが生成したのが確認され
た。この(0式の反応により23mt(0−4mOL
)のエタノールが生成したことになる〜
このようにエタノールを溶媒に用いずに加水分解を行な
って得られた乾燥ゲルを焼結しても1000℃以下の同
一温度で同様に石英ガラスが得られた。比重・ビッカー
ス硬度・屈折率・近赤外吸収スペクトル等の分析結果に
おいて、両者の間に差異が認められなかった。加水分解
反応を均−系で行なわなくても石英ガラスの製造におい
て何ら影響がないことが判明した。Liquid chromatography analysis confirmed that the raw material ethyl orthosilicate had disappeared and ethanol had been produced. This (0-4 mOL reaction resulted in 23 mt (0-4 mOL)
) ethanol was produced ~ Even if the dry gel obtained by hydrolysis without using ethanol as a solvent is sintered, silica glass can be similarly obtained at the same temperature below 1000°C. Ta. No difference was observed between the two in the analysis results of specific gravity, Vickers hardness, refractive index, near-infrared absorption spectrum, etc. It has been found that there is no effect on the production of quartz glass even if the hydrolysis reaction is not carried out in a homogeneous system.
前述のように0.1モルのオルトケイ酸エチルの加水分
解を均−系で行なうにはa6モル以上のエタノールが必
要であり、反応終了後には生成した0、4モルのエタノ
ールと共に結局は除去しなければならない。オルトケイ
酸エチルと塩酸水溶液のみで加水分解を行なえばエタノ
ールの費用がかからないばかりか、容積が約半分になり
操作がしやすくなる。また除去するエタノール量が減る
ためゲル化時間が短縮され、乾燥収縮過程をこおける体
積収縮率が小さくなる。さらに乾燥時間も短かくてすむ
ため、作業効率が上がる。As mentioned above, in order to homogeneously hydrolyze 0.1 mole of ethyl orthosilicate, more than a6 mole of ethanol is required, and after the reaction is completed, it is eventually removed along with the 0.4 mole of ethanol produced. There must be. If hydrolysis is carried out using only ethyl orthosilicate and an aqueous hydrochloric acid solution, not only will the cost of ethanol be eliminated, but the volume will be reduced to about half, making it easier to operate. Furthermore, since the amount of ethanol to be removed is reduced, the gelation time is shortened, and the volumetric shrinkage rate during the drying shrinkage process is reduced. Furthermore, drying time is shortened, increasing work efficiency.
以上のように本発明はアルコールを加えずに加水分解す
ることにより、費用の減少、安全性・作業効率の向上に
加えて、乾燥ゲル作製条件を良くする特徴を有する。As described above, the present invention has the characteristics of reducing costs, improving safety and work efficiency, and improving dry gel production conditions by performing hydrolysis without adding alcohol.
以 上that's all
Claims (1)
おいて、アルコキシシランと水とを二層のまま激しく攪
拌して加水分解反応させることにより、乾燥ゲルを作製
することを特徴とする石英ガラスの製造法。(1) A quartz glass manufacturing method using a sol-gel method, characterized in that a dry gel is produced by vigorously stirring alkoxysilane and water in two layers to cause a hydrolysis reaction. manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11756782A JPS598625A (en) | 1982-07-06 | 1982-07-06 | Preparation of quartz glass |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11756782A JPS598625A (en) | 1982-07-06 | 1982-07-06 | Preparation of quartz glass |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS598625A true JPS598625A (en) | 1984-01-17 |
Family
ID=14715005
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11756782A Pending JPS598625A (en) | 1982-07-06 | 1982-07-06 | Preparation of quartz glass |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS598625A (en) |
-
1982
- 1982-07-06 JP JP11756782A patent/JPS598625A/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0328715A1 (en) | A catalyst for sol-gel method using metal alkoxide and sol-gel method using the same | |
CN107083168B (en) | A kind of glass nano transparent insulating coating and its application | |
JPS598625A (en) | Preparation of quartz glass | |
JPH0328382B2 (en) | ||
JPH0558650A (en) | Double oxide glass and its production | |
JPS5992924A (en) | Preparation of quartz glass | |
CN101746980B (en) | Method for preparing high-performance light-weight insulating brick by using quartz mine | |
JPH02184514A (en) | Cylindrical quartz glass powder and production thereof | |
JPH0249259B2 (en) | KETSUSHOKAGARASUTOSONOSEIZOHOHO | |
KR100605793B1 (en) | Method for fabricating silica glass by sol-gel process | |
JPS6259515A (en) | Production of high-purity silicic acid hydrate | |
JPS62246835A (en) | Production of base material for quartz glass optical fiber | |
JPS58185442A (en) | Preparation of quartz glass | |
JPS6369724A (en) | Production of glass | |
JPS61201627A (en) | Production of low oh glass | |
JPH03159911A (en) | Production of spherical silica particle | |
JPH0517173B2 (en) | ||
JPH0466811B2 (en) | ||
JPS6086035A (en) | Production of quartz glass | |
JPS58185441A (en) | Preparation of colored glass | |
JPH0645452B2 (en) | Method for producing silica gel | |
JPS582239A (en) | Glaze composition | |
JPS6065733A (en) | Production of quartz glass | |
JPH0264031A (en) | Production of lumpy glass | |
JPH01160843A (en) | Production of neodymium-containing quartz glass |