JPS61232231A - Silica glass manufacturing method - Google Patents
Silica glass manufacturing methodInfo
- Publication number
- JPS61232231A JPS61232231A JP7370685A JP7370685A JPS61232231A JP S61232231 A JPS61232231 A JP S61232231A JP 7370685 A JP7370685 A JP 7370685A JP 7370685 A JP7370685 A JP 7370685A JP S61232231 A JPS61232231 A JP S61232231A
- Authority
- JP
- Japan
- Prior art keywords
- sol
- quartz glass
- final filter
- glass
- passed
- 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 34
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 7
- -1 alkyl silicate Chemical compound 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims abstract description 6
- 238000003980 solgel method Methods 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims abstract description 4
- 238000001914 filtration Methods 0.000 claims description 6
- 239000011148 porous material Substances 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000000428 dust Substances 0.000 abstract description 6
- 239000011362 coarse particle Substances 0.000 abstract description 5
- 239000000463 material Substances 0.000 abstract description 2
- 239000000356 contaminant Substances 0.000 abstract 2
- 239000000843 powder Substances 0.000 abstract 1
- 239000011521 glass Substances 0.000 description 9
- 239000000126 substance Substances 0.000 description 5
- 238000000862 absorption spectrum Methods 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
- 238000005119 centrifugation Methods 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000499 gel Substances 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000005350 fused silica glass Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 229910002012 Aerosil® Inorganic materials 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 244000201986 Cassia tora Species 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 238000007500 overflow downdraw method Methods 0.000 description 1
- NCAIGTHBQTXTLR-UHFFFAOYSA-N phentermine hydrochloride Chemical compound [Cl-].CC(C)([NH3+])CC1=CC=CC=C1 NCAIGTHBQTXTLR-UHFFFAOYSA-N 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000011045 prefiltration Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000011882 ultra-fine particle 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
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/06—Glass compositions containing silica with more than 90% silica by weight, e.g. quartz
-
- 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
- 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
- C03C2201/00—Glass compositions
- C03C2201/02—Pure silica glass, e.g. pure fused quartz
-
- 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
- C03C2203/00—Production processes
- C03C2203/20—Wet processes, e.g. sol-gel process
- C03C2203/26—Wet processes, e.g. sol-gel process using alkoxides
-
- 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
- C03C2203/00—Production processes
- C03C2203/20—Wet processes, e.g. sol-gel process
- C03C2203/34—Wet processes, e.g. sol-gel process adding silica powder
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
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ゾル−ゲル法による石英ガラスの製造方法に
関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing quartz glass by a sol-gel method.
本発明は、ゾル−ゲル法による石英ガラスの製造方法に
おいて、ゾル調製f過プロセス中、最終フィルターを2
回以上通過させるかめるいは、循環させることによシ、
調製ゾルの濾過精度の向上をはかシ、焼結後のガラス中
の異物の原因物(粗大粒子、ゴミなど)を完全に除去す
ることを可能にしたものである。The present invention provides a method for producing quartz glass using the sol-gel method, in which the final filter is removed during the sol preparation process.
If it passes more than once, it can be circulated.
This improves the filtration accuracy of the prepared sol and makes it possible to completely remove foreign substances (coarse particles, dust, etc.) from the glass after sintering.
従来のアルキルシリケートおよび超微粒子シリカを主原
料として用いるゾル−ゲル法による石英ガラス製造にお
いては、調製ゾル中に存在するシリカの粗大粒子ならび
にゴミ等の異物の除去を目的とするf過プロセスでの最
終フィルターは、1回通過させるだけであった。In the production of quartz glass by the conventional sol-gel method using alkyl silicate and ultrafine silica as the main raw materials, a filtration process is used to remove foreign substances such as coarse silica particles and dust present in the prepared sol. The final filter was passed through only once.
〔発明が解決しようとする問題点及び目的〕しかし、前
述の従来技術では、単に最終フィルターを1回通過させ
るだけのために、ゴミおよび粗大粒子など異物の形状に
よっては、孔径以下の大きさのものでもある程度通過し
てしまうため、これらが、焼結後のガラス中にまで残存
し、欠陥となシ、高品質なガラスの製造が困難であると
仏う問題点を有する。[Problems and Objectives to be Solved by the Invention] However, in the above-mentioned conventional technology, since the final filter is simply passed through once, depending on the shape of foreign matter such as dust and coarse particles, particles with a size smaller than the pore diameter may be generated. Since these particles pass through to some extent, they remain in the glass after sintering, causing defects and making it difficult to manufacture high-quality glass.
そこで本発明はこのような問題点を解決するもので、そ
の目的とするところは、従来技術を改良することによる
f過精度の向上をはかシフルーゲル法による高品質な石
英ガラスの製造方法を提供するところKある。The present invention is intended to solve these problems, and its purpose is to provide a method for manufacturing high-quality quartz glass using the Schiflugel method, which improves f overaccuracy by improving the conventional technology. There is a place K.
本発明の石英ガラスの製造方法は、アルキルシリケート
および超微粒子シリカを主原料として用いるゾル−ゲル
法による石英ガラスの製造において、ゾル調製一過プロ
セス中に従来技術に加えて最終フィルター一過を複数回
行なうことを特徴とする。The method for producing quartz glass of the present invention includes, in addition to the conventional technique, a plurality of final filter passes during the sol preparation pass-through process in the production of quartz glass by the sol-gel method using alkyl silicate and ultrafine silica as main raw materials. It is characterized by rotating.
本発明によれば、調製ゾル中に残存するプレフィルタ−
によシ除去されなかった分散不充分および凝集した粗大
粒子や、ゴミなどの異物で、最終一過の際に通過したも
のをくシ返し該ゾルを一過するととKよシ減少化、さら
にf過精度を向上させることによシ全くなくすとと示可
能である。According to the invention, the prefilter remaining in the prepared sol
When the sol is passed through the sol by cycling the foreign substances such as insufficiently dispersed and agglomerated coarse particles and dust that were not removed by the sol, the K decreases. It can be shown that f overaccuracy can be completely eliminated by improving the accuracy.
〔実施例〕
(1)市販のエチルシリケ−) 28 (Si (Ow
let)4)152t、 Ilo 1 HTiOl
1084 および超微粒子シリカ(商品名 アエロジ
ルoxso(デグサ社))45Klを同時に混合し、デ
ィシルバー(攪拌分散装置)にて攪拌を4時間行ない、
エチルシリケートの加水分解反応ならびに超微粒子シリ
カがある程度分散したゾルを調製し、この後さらに分散
性を向上させるため該ゾルに、超音波照射(攪拌併用)
を5時間行なった、なお、この際、超音波照射による該
ゾル温度の上昇を防ぐため、冷却装置によシ該ゾル温度
を一定に保持した。[Example] (1) Commercially available ethyl silica) 28 (Si (Ow
let) 4) 152t, Ilo 1 HTiOl
1084 and ultrafine particle silica (trade name Aerosil oxso (Degussa)) 45Kl were mixed at the same time, and stirred for 4 hours using a Dissilver (stirring and dispersing device).
A sol in which ethyl silicate is hydrolyzed and ultrafine silica is dispersed to some extent is prepared, and then the sol is irradiated with ultrasonic waves (combined with stirring) to further improve dispersibility.
This was carried out for 5 hours. At this time, the sol temperature was kept constant using a cooling device in order to prevent the sol temperature from increasing due to ultrasonic irradiation.
次工程として、該ゾル中の半ばゲル化したゼリー状物や
不純物含有粗大粒子およびゴミなどを除去するため該ゾ
ルに対し遠心分離処理(3000rpH1,5Q wk
)を加えた。As the next step, the sol is subjected to centrifugation treatment (3000rpH1,5Q wk
) was added.
この後の濾過プロセスは以下のような構成で行なった。The subsequent filtration process was performed with the following configuration.
孔径10μm、 7μm、5μm、 3μm1μm
の各フィルターを順に通過された、従来法ではここまで
であったが、この後さらに孔径1μmのフィルターを通
過させた。Pore diameter 10μm, 7μm, 5μm, 3μm 1μm
In the conventional method, the sample was passed through each filter in order, but after this, the sample was further passed through a filter with a pore size of 1 μm.
一過したゾルに対し、アンモニア水などの弱塩基の滴下
によJ)pH値を3〜6に調製し、この際に生成したゲ
ル状物を除去するため再遠心分離処理を施した。この後
、最終フィルターとして孔径1μmのフィルターを従来
は一度通過させるだけであったのに対し、ここでは2,
4,10,20゜回とくシ返し通過させ、大きさ36X
24X12〔α〕 のポリプロピレン族の容器に各60
0g。J) The pH value of the passed sol was adjusted to 3 to 6 by dropwise addition of a weak base such as aqueous ammonia, and recentrifugation treatment was performed to remove the gel-like substance generated at this time. After this, conventionally, the final filter was passed through a filter with a pore size of 1 μm only once, but here, two
Pass through 4, 10, and 20° times, size 36X
60 each in a 24 x 12 [α] polypropylene container
0g.
40[1個に投入し密閉状態にてゲル化させ、この後、
収縮が始まった時点で、容器のフタを乾燥速度調節のた
めに穴のあいた所定の開孔率のものに変え、乾燥機に入
れ、室温から昇温速度5′C/r
で60〜80℃に加熱し、以後この温度に保持し10〜
15日間で大きさ25.3XIL8Xα5〔帰〕の乾燥
ゲルを得た。これらの乾燥ゲルを焼結炉に投入し、所定
の昇温方法により加熱焼結し1300〜1450℃にて
透明なガラス体を得た。このガラスノ大きさは1 &8
X 11.5XQ、35 (m〕テ重量は180g前後
であった。以上のようにして得たガラスを光学顕微鏡、
集光ランプを当てるなどして観察したところ、ガラス中
の異物は、以前に比べて著しく減少していた。しかも、
容器投入前の最終f過フィルターを〈シ返し通過させた
回数が多いものtlど少なく、10回以上通過させた場
合、はとんど異物は観察できなかった。また、とれらの
ガラスに関する諸物性分析の結果は、ビッカース硬度、
比重、熱膨張係数、赤外吸収スペクトル、近赤外吸収ス
ペクトル、屈折率など溶融石英ガラスの値と一致した。40[Pour it into one container and let it gel in a sealed state, then
When shrinkage begins, change the lid of the container to one with holes of a specified porosity to adjust the drying rate, place it in a dryer, and heat it from room temperature to 60-80°C at a heating rate of 5'C/r. Heat it to a temperature of 10~
A dried gel with a size of 25.3XIL8Xα5 was obtained in 15 days. These dried gels were put into a sintering furnace, and heated and sintered using a predetermined heating method to obtain a transparent glass body at 1300 to 1450°C. The size of this glass is 1 & 8
X 11.5XQ, 35 (m) Te weight was around 180g.
When the glass was observed using a condensing lamp, the amount of foreign matter in the glass was significantly reduced compared to before. Moreover,
The number of times the sample was passed through the final filtration filter before being put into the container was small, and in the cases where it was passed more than 10 times, no foreign matter could be observed. In addition, the results of physical property analysis of Tora's glass are Vickers hardness,
The specific gravity, coefficient of thermal expansion, infrared absorption spectrum, near-infrared absorption spectrum, refractive index, and other values matched those of fused silica glass.
(2)実施例1と同様に調製したゾルに、同様に遠心分
離、一過、pH値調整、再遠心分離の各処理を促した後
、SOZずつ5つのバッチに等分し、それぞれに対し、
最終フィルターをO,(15,1゜2.3時間、流量3
〜5t/―で循環させた。この後、実施例1を同様に、
各バッチ80個の容器に投入し、石英ガラスを得た。(2) After subjecting the sol prepared in the same manner as in Example 1 to centrifugation, passing, pH value adjustment, and re-centrifugation, the sol was equally divided into five batches each containing SOZ. ,
The final filter is O, (15,1°2.3 hours, flow rate 3
It was circulated at ~5t/-. After this, in the same manner as Example 1,
80 pieces of each batch were put into containers to obtain quartz glass.
ここで得られた石英ガラス中の異物は、最終フィルター
の循環時間が長い程、少なく1時間以上では、はとんど
観察されなかった。また、これらのガラスに関する諸物
性分析の結果は、ビッカース硬度、比重、熱膨張係数、
赤外吸収スペクトル。The longer the circulation time of the final filter, the fewer foreign substances in the quartz glass obtained here were observed, and they were hardly observed after 1 hour or more. In addition, the results of physical property analysis regarding these glasses include Vickers hardness, specific gravity, coefficient of thermal expansion,
Infrared absorption spectrum.
近赤外吸収スペクトル、屈折率など溶融石英ガラスと一
致した。The near-infrared absorption spectrum and refractive index matched those of fused silica glass.
このようにして、本発明により製造される石英ガラスは
、前述のような濾過方法を用いることによシ、焼結後の
石英ガラス中の異物の原因となるゾル中の粗大粒子、ゴ
ミなどをほぼ完全に除去可能であることから、非常に高
品質な石英ガラスである。In this way, the silica glass produced according to the present invention can be manufactured by using the above-described filtration method to remove coarse particles, dust, etc. in the sol that cause foreign matter in the silica glass after sintering. It is a very high quality quartz glass as it can be almost completely removed.
このように、溶融法などの従来の方法に比べ低コストで
あるなどの利点を有する上に、非常に高品質な石英ガラ
スが容易に製造可能であるため、これまで石英ガラスを
使用していた分野ではもちろんのこと、工C用フォトマ
スク基板、光フアイバー用母材など種々の分野に応用が
広がるものと考える。In this way, quartz glass has been used until now because it has the advantage of being lower cost than conventional methods such as the fusion method, and it is also easy to produce very high quality quartz glass. We believe that its application will expand to a variety of fields, including photomask substrates for engineering C, base materials for optical fibers, etc.
Claims (1)
料として用いるゾルゲル法による石英ガラスの製造にお
いて、ゾル調製濾過プロセス中に以下の処理方法を有す
ることを特徴とする石英ガラスの製造方法。 a)最終フィルター(孔径5μm以下)を2回以上通過
させる b)a)記載のフィルターを、所定時間、循環させる(1) A method for producing quartz glass, which includes the following treatment method during the sol preparation filtration process in producing quartz glass by a sol-gel method using alkyl silicate and ultrafine silica as main raw materials. a) Pass through the final filter (pore size 5 μm or less) twice or more b) Circulate the filter described in a) for a predetermined period of time
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7370685A JPS61232231A (en) | 1985-04-08 | 1985-04-08 | Silica glass manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7370685A JPS61232231A (en) | 1985-04-08 | 1985-04-08 | Silica glass manufacturing method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61232231A true JPS61232231A (en) | 1986-10-16 |
Family
ID=13525927
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7370685A Pending JPS61232231A (en) | 1985-04-08 | 1985-04-08 | Silica glass manufacturing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61232231A (en) |
-
1985
- 1985-04-08 JP JP7370685A patent/JPS61232231A/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS61232231A (en) | Silica glass manufacturing method | |
JPS62105936A (en) | Manufacturing method of flat quartz glass | |
JPS62246826A (en) | Production of glass | |
JPS59131538A (en) | Silica glass manufacturing method | |
JPS61168541A (en) | Production of quartz glass | |
JPS60239329A (en) | Manufacture of quartz glass | |
JPS61232232A (en) | Silica glass manufacturing method | |
JPS62207723A (en) | Glass manufacturing method | |
JPS6126524A (en) | Silica glass manufacturing method | |
JPS6291428A (en) | Glass manufacturing method | |
JPS62278135A (en) | Production of glass | |
JPS6158818A (en) | Silica glass manufacturing method | |
JPS638228A (en) | Production of quartz glass | |
JPS6140825A (en) | Preparation of quartz glass | |
JPS60108324A (en) | Production of quartz glass | |
JPS63107821A (en) | Production of glass | |
JPS62241837A (en) | Production of quartz glass | |
JPS62100427A (en) | Glass manufacturing method | |
JPH01203229A (en) | Production of glass | |
JPH0751445B2 (en) | Glass manufacturing method | |
JPS6054929A (en) | Silica glass manufacturing method | |
JPS61178427A (en) | Mass production method of quartz glass | |
JPS61168542A (en) | Silica glass manufacturing method | |
JPS63112435A (en) | Production of quartz glass | |
JPS63297234A (en) | Silica glass manufacturing method |