JPH0624993B2 - Quartz glass manufacturing method - Google Patents
Quartz glass manufacturing methodInfo
- Publication number
- JPH0624993B2 JPH0624993B2 JP62335444A JP33544487A JPH0624993B2 JP H0624993 B2 JPH0624993 B2 JP H0624993B2 JP 62335444 A JP62335444 A JP 62335444A JP 33544487 A JP33544487 A JP 33544487A JP H0624993 B2 JPH0624993 B2 JP H0624993B2
- Authority
- JP
- Japan
- Prior art keywords
- quartz glass
- cristobalite
- sol
- silicon dioxide
- surface area
- 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.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/10—Forming beads
- C03B19/1005—Forming solid beads
- C03B19/106—Forming solid beads by chemical vapour deposition; by liquid phase reaction
- C03B19/1065—Forming solid beads by chemical vapour deposition; by liquid phase reaction by liquid phase reactions, e.g. by means of a gel phase
-
- 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)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Dispersion Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Glass Melting And Manufacturing (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は石英ガラスの製造方法、特には高純度で天然石
英ガラスと同等の耐熱性を有する、したがってシリコン
単結晶引上げ用ルツボや熱処理炉の炉芯管などのような
半導体工業用に最適とされる石英ガラスの製造方法の改
良に関するものである。TECHNICAL FIELD The present invention relates to a method for producing quartz glass, and in particular, to a crucible for pulling a silicon single crystal and a heat treatment furnace, which has high purity and heat resistance equivalent to that of natural quartz glass. The present invention relates to an improvement in a method for producing quartz glass, which is most suitable for the semiconductor industry such as a furnace core tube.
(従来の技術) 高純度石英ガラスの製造については天然水晶を洗浄や選
別で精製するか、得られた天然石英ガラスを電気分解す
る方法(国際公開特許W086/02919参照)、あ
るい四塩化けい素などのけい素化合物を酸水素炎で火炎
加水分解させてシリカを担体上に堆積させ、これを溶融
ガラス化する方法が知られている。(Prior Art) For the production of high-purity quartz glass, a method of purifying natural quartz by washing or screening or electrolyzing the obtained natural quartz glass (see International Patent Publication W086 / 02919), or silicon tetrachloride A method is known in which a silicon compound such as silicon is flame-hydrolyzed with an oxyhydrogen flame to deposit silica on a carrier, and the silica is fused and vitrified.
しかし、この天然水晶を始発材とするものは半導体工業
用としては純度が不充分であり、四塩化けい素の火炎加
水分解で得たシリカを溶融して得た合成石英ガラスはこ
れに含有されるOH基量が800ppm以上と多いため耐
熱性に劣るという不利があり、これにはまた高価である
という欠点がある。However, the one using this natural quartz as a starting material has insufficient purity for the semiconductor industry, and synthetic quartz glass obtained by melting silica obtained by flame hydrolysis of silicon tetrachloride is included in this. Since the amount of OH groups is as large as 800 ppm or more, it has the disadvantage of being inferior in heat resistance, and this has the disadvantage of being expensive.
このため、本発明者らはさきにけい素化合物を酸水素火
炎中で火炎加水分解して得たシリカを加熱処理してクリ
ストバライト結晶としたのち溶融して耐熱性の高い高純
度石英ガラスとする方法(特開昭62−113729号
公報参照)、さらには上記のような高価ないわゆる合成
石英ガラスを原料とせずに、ゾル−ゲル法による安価な
シリカゲルを始発原料とし、このものを結晶化したのち
溶融ガラス化することにより、経済的に耐熱性の高い高
純度シリカガラスを製造する方法(特願昭61−312
770)を提案した。For this reason, the present inventors previously heat-processed silica obtained by flame hydrolysis of a silicon compound in an oxyhydrogen flame to form cristobalite crystals, and then melted to obtain high-purity quartz glass with high heat resistance. In addition to the method (see Japanese Patent Laid-Open No. 62-113729) and the so-called expensive synthetic quartz glass as a raw material, an inexpensive silica gel prepared by a sol-gel method was used as a starting raw material to crystallize this. A method for producing a high-purity silica glass that is economically highly heat-resistant by subsequent vitrification (Japanese Patent Application No. 61-312).
770) was proposed.
これらの方法では、高生産性のもとに実施する見地か
ら、結晶化(クリストバライト化)をアルカリ成分の存
在下に行うことが有利とされるのであるが、その場合、
溶融ガラス化に先立って脱アルカリを行うことが必要と
なる。しかし、現在のところ、この脱アルカリをより簡
便・安価にして確実に実施する技術は開発されておら
ず、この解決は切実な課題となっている。In these methods, it is advantageous to perform crystallization (cristobalite formation) in the presence of an alkaline component from the viewpoint of carrying out the production with high productivity.
It is necessary to carry out dealkalization prior to molten vitrification. However, at present, no technique has been developed to carry out this dealkalization more simply, cheaply and surely, and this solution is an urgent problem.
(発明の構成) 本発明はこのような課題を解決した石英ガラスの製造方
法に関するものであり、これは金属アルコキシドまたは
無機けい酸塩を原料としてゾルーゲル法で製造した非晶
質二酸化けい素をBET法による比表面積が50m2/g
より小さいものとし、これにアルカリ成分を加え加熱し
てβ−クリストバライトとしたのち、このものを冷却し
てα−クリストバライト粉末に転移させ、ついで溶融ガ
ラス化して石英ガラスとすることを特徴とするものであ
る。(Structure of the Invention) The present invention relates to a method for producing quartz glass which solves the above problems, in which an amorphous silicon dioxide produced by a sol-gel method using a metal alkoxide or an inorganic silicate as a raw material is BET. Specific surface area by the method is 50 m 2 / g
It is characterized in that it is made smaller, and after adding an alkali component to this to heat it to β-cristobalite, it is cooled and transformed into α-cristobalite powder, and then it is melted into vitrified silica glass. Is.
すなわち、本発明者らはゾル−ゲル法で得られたシリカ
をアルカリの存在下でクリストバライトとしたのちの脱
アルカリ工程における最適条件を見出すべく種々検試し
た結果、これについてはゾル−ゲル法で作られた非晶質
二酸化けい素の比表面積がのちの脱アルカリのしやすさ
に大きくかかわることを知見し、そのBET法による比
表面積を50m2/g以下とすれば加熱による脱アルカリ
が非常に容易となり、その残留量を極少とすることがで
きること、そしてこれを溶融ガラス化することにより高
純度で耐熱性の高い石英ガラスを得ることができること
を見出して本発明を完成させた。That is, the present inventors conducted various tests to find the optimum conditions in the dealkalization step after the silica obtained by the sol-gel method was used as cristobalite in the presence of alkali, and the results were obtained by the sol-gel method. It was found that the specific surface area of the produced amorphous silicon dioxide is greatly related to the ease of subsequent dealkalization, and if the specific surface area by the BET method is set to 50 m 2 / g or less, dealkalization by heating will be extremely difficult. The present invention has been completed by finding that it becomes easy and the residual amount can be minimized, and that it is possible to obtain a quartz glass having high purity and high heat resistance by converting this into a molten glass.
以下、本発明を各工程毎に説明する。Hereinafter, the present invention will be described for each step.
本発明の方法はまず、金属アルコキシドまたは無機けい
酸塩から非晶質二酸化けい素を製造するのであるが、こ
れは公知のゾルーゲル法で行なえばよい。このゾルーゲ
ル法は例えばけい酸エチル〔Si(OC2H5)4〕のよ
うな金属アルコキシドの水とエチルアルコールとの混合
液または水ガラスのような無機けい酸塩の水溶液を加温
下に寒天状にゾル化したのち、これを加熱してアルコー
ル、水を追い出して乾燥ゲルとして二酸化けい素を得る
ものであるが、この方法によれば二酸化けい素は非晶質
のものとして取得される。The method of the present invention firstly produces amorphous silicon dioxide from a metal alkoxide or an inorganic silicate, which may be performed by a known sol-gel method. In this sol-gel method, for example, a mixed solution of water and ethyl alcohol of a metal alkoxide such as ethyl silicate [Si (OC 2 H 5 ) 4 ] or an aqueous solution of an inorganic silicate such as water glass is heated under agar. After sol-formation, it is heated to drive out alcohol and water to obtain silicon dioxide as a dry gel. According to this method, silicon dioxide is obtained as an amorphous substance.
本発明の方法はついでこの公知のゾルーゲル法で得た非
晶質二酸化けい素をBET法による比表面積が50m2/
gより小さいものとするのであるが、この比表面積を5
0m2/g以下とする方法としては例えばこれを加熱処理
する方法がある。この加熱温度は1,000℃であれば
よいが生産性を考慮して、例えば加熱時間が2時間以内
というような条件を満たすには、1,100℃以上が好
ましい最高温度については、工業用炉の仕様が大幅に高
価なものになる境界である1,200℃以下とすること
が好ましい。According to the method of the present invention, the amorphous silicon dioxide obtained by the known sol-gel method has a specific surface area of 50 m 2 / BET method.
The specific surface area should be less than 5
As a method for adjusting the amount to 0 m 2 / g or less, for example, there is a method of heat-treating this. The heating temperature may be 1,000 ° C., but considering the productivity, for example, to satisfy the condition that the heating time is within 2 hours, 1,100 ° C. or higher is preferable. It is preferable to set the temperature to 1,200 ° C. or lower, which is a boundary at which the specifications of the furnace become significantly expensive.
このように、1,100〜1,200℃の温度範囲で
は、加熱時間は2〜3時間で充分である。一方またこの
比表面積を50m2/g以下とするにはゾルーゲル法で作
られた非晶質の二酸化けい素を化学的手法で処理しても
よく、これには例えばゾルーゲル法による金属アルコキ
シドまたは無機けい酸塩の加水分解反応をホルムアミド
の存在下で行なわせる方法(Mat. Res. Soc. Syp. Pro
c.Vo173、1986、P35〜47酸)がある。なお、こ
の方法で処理されたものをさらに加熱処理してもよい。As described above, in the temperature range of 1,100 to 1,200 ° C., the heating time of 2 to 3 hours is sufficient. On the other hand, in order to reduce the specific surface area to 50 m 2 / g or less, amorphous silicon dioxide prepared by the sol-gel method may be treated by a chemical method, for example, a metal alkoxide or an inorganic material by the sol-gel method. Method for allowing hydrolysis reaction of silicate in the presence of formamide (Mat. Res. Soc. Syp. Pro
c. Vo173, 1986, P35-47 acid). In addition, you may heat-process what was processed by this method.
本発明の方法はついでこのようにBET法による比表面
積が50m2/g以下とされた非晶質二酸化けい素を加熱
処理してβ−クリストバライトとするものであり、この
加熱はβ−クリストバライトの融点である1723℃以
下で行なわせる必要があるが、このクリストバライト化
はアルカリ化合物のような結晶化促進剤の存在下で行な
うと1,100〜1,200℃という工業炉で簡単に得
られる温度ですみやかに進行するので、これにはNaOH水
溶液のようなNa系のアルカリ化剤の存在下で1,100
〜1,200℃に加熱することがよい。また、このよう
にして得たβ−クリストバライトはα−クリストバライ
トとする必要があるが、これはβ−クリストバライトを
得るために加熱されたものを常温まで冷却すれば容易に
α−クリストバライトとすることができる。According to the method of the present invention, the amorphous silicon dioxide having a specific surface area of 50 m 2 / g or less according to the BET method is then heat-treated to give β-cristobalite, which is heated by β-cristobalite. It is necessary to carry out at a melting point of 1723 ° C. or lower, but when this cristobaliteization is carried out in the presence of a crystallization accelerator such as an alkali compound, a temperature of 1,100 to 1,200 ° C. which is easily obtained in an industrial furnace. It proceeds rapidly in the presence of a Na-based alkalizing agent such as an aqueous NaOH solution.
It is preferable to heat to 1,200 ° C. Further, the β-cristobalite thus obtained needs to be α-cristobalite, which can be easily converted to α-cristobalite by cooling the heated product to obtain β-cristobalite at room temperature. it can.
つぎに本発明の方法ではこのようにして得られたα−ク
リストバライトを加熱溶融して石英ガラスとするのであ
るが、このα−クリストバライトは二酸化けい素をβ−
クリストバライトとするためにアルカリ化合物が添加さ
れており、これが得られる石英ガラス中に混入してくる
ので、溶融ガラス化に先立ってこのアルカリ成分を除去
しておく必要がある。Next, in the method of the present invention, the α-cristobalite thus obtained is heated and melted to form a quartz glass. This α-cristobalite converts silicon dioxide into β-
An alkali compound is added to obtain cristobalite, and this is mixed in the obtained quartz glass. Therefore, it is necessary to remove this alkali component prior to the molten vitrification.
このクリストバライトの脱アルカリは、例えばハロゲン
ガス雰囲気中で1,300℃程度に加熱することによ
り、あるいは酸洗浄により行われる。しかし、工程の安
全性やその対策のための設備を考慮すると、単に加熱処
理のみで脱アルカリを行うことが好ましい。The dealkalization of cristobalite is performed, for example, by heating at about 1,300 ° C. in a halogen gas atmosphere or by acid cleaning. However, it is preferable to carry out dealkalization only by heat treatment, in consideration of process safety and equipment for countermeasures.
本発明の方法では、例えばアルカリ添加量が50ppmで
あった場合、1,500℃×5時間で達成される純度
は、もとのシリカの比表面積が50m2/g付近であると
1ppm以下となり、0.3m2/gでは0.2ppm以下とな
る。In the method of the present invention, for example, when the amount of alkali added is 50 ppm, the purity achieved at 1,500 ° C. for 5 hours is 1 ppm or less when the original specific surface area of silica is around 50 m 2 / g. , 0.3 m 2 / g, the amount becomes 0.2 ppm or less.
本発明の方法は、このような方法で脱アルカリされた高
純度α−クリストバライト粉を従来法にしたがって加熱
溶融することにより耐熱性にすぐれた高純度石英ガラス
を得るものである。前記第2表に示した純度値(Na含
有量)がほぼそのまま継承されていることがわかった。The method of the present invention is to obtain high-purity quartz glass excellent in heat resistance by heating and melting the high-purity α-cristobalite powder dealkalized by such a method according to a conventional method. It was found that the purity values (Na content) shown in Table 2 were inherited almost as they were.
他方、ベルヌイ法で石英ガラスインゴットを試作したと
ころ、Na含有量が減少する傾向が見られたが、第2表
の純度値の傾向(順位)は変化はなく、このことから原
料の純度が重要であることがうかがわれる。On the other hand, when a quartz glass ingot was prototyped by the Bernoulli method, the Na content tended to decrease, but the trend of purity values (rank) in Table 2 did not change, and therefore the purity of the raw material is important. It can be seen that
つぎに本発明の実施例をあげる。Next, examples of the present invention will be given.
実施例1 シリコンエトキシド(Si(OC2H5)4)1モルに対
し、0.01規定のアンモニア水を3モル、メタノール
を4モルの比率で混合撹拌してゾル液を作り、このゾル
をプラスチックビーカーに注入し恒温槽にて60℃で1
0時間放置したのち、さらに電気炉中で200℃にて2
時間加熱保持したところ、粉末状の非晶質二酸化けい素
(以下これをサンプル1と略記する)が得られたので、
これを石英ガラスボートに収容し、炭化けい素ヒーター
を備えた横型筒状炉中で900℃、1,000℃、1,
100℃、1,200℃、1,300℃で2時間加熱し
てサンプル2、3、4、5、6を作り、このようにして
得たサンプル1〜6の比表面積を窒素ガスを吸着ガスと
するBET法で測定したところ、つぎの第1表に示した
とおりの結果が得られた。Example 1 To 1 mol of silicon ethoxide (Si (OC 2 H 5 ) 4 ), 3 mol of 0.01N ammonia water and 4 mol of methanol were mixed and stirred to prepare a sol liquid. In a plastic beaker and in a constant temperature bath at 60 ° C for 1
After leaving it for 0 hours, it is further heated in an electric furnace at 200 ° C for 2 hours.
When heated and held for a period of time, powdery amorphous silicon dioxide (hereinafter abbreviated as sample 1) was obtained.
This was housed in a quartz glass boat and placed in a horizontal tubular furnace equipped with a silicon carbide heater at 900 ° C, 1,000 ° C, 1,
Samples 2, 3, 4, 5, and 6 were prepared by heating at 100 ° C., 1,200 ° C., and 1,300 ° C. for 2 hours. When measured by the BET method, the results shown in Table 1 below were obtained.
ついで、このようにして得たサンプル1〜6にNa換算で
50ppmのNaOH水溶液を加え、乾燥させたのち1,20
0℃で5時間化熱したところ、これらはβ−クリストバ
ライトとされたので常温まで冷却してα−クリストバラ
イトとし、さらにこれらを溶融アルミナボートに入れ、
けい化モリブデンヒーターを設けた電気炉中において
1,500℃で5時間加熱し、冷却後このα−クリスト
バライト中に含有されているNa含有量を原子吸光光度法
によってしらべたところ、つぎの第2表に示したとおり
の結果が得られた。 Then, to the samples 1 to 6 thus obtained, a 50 ppm NaOH aqueous solution in terms of Na was added and dried, then 1,20
When heated at 0 ° C. for 5 hours, they were determined to be β-cristobalite, so they were cooled to room temperature to obtain α-cristobalite, which were then placed in a fused alumina boat,
It was heated at 1,500 ° C. for 5 hours in an electric furnace equipped with a molybdenum silicide heater, and after cooling, the Na content contained in this α-cristobalite was examined by an atomic absorption photometry method. The results shown in the table were obtained.
つぎにこのようにして得られた脱アルカリ処理をしたα
−クリストバライトを回転モールド中に入れ、回転させ
ながらアーク溶融して口径8インチのルツボを作り、こ
ゝに得られた石英ガラス製のルツボについて調べたとこ
ろ、前記第2表に示した純度値(Na含有量)がほぼそ
のまま継承されていることがわかった。 Next, the dealkalized α obtained in this way
-Cristobalite was put into a rotary mold, arc-melted while being rotated to make a crucible having a diameter of 8 inches, and the obtained crucible made of quartz glass was examined, and the purity values shown in Table 2 ( It was found that the Na content) was inherited almost as it was.
他方、ベルヌイ法で石英ガラスインゴットを試作したと
ころ、Na含有量が減少する傾向が見られたが、第2表
の純度値の傾向(順位)は変化はなく、このことから原
料の純度が重要であることがうかがわれ、従って、アル
カリ添加前の中間生成物であるシリカ粉の比表面積が製
品の純度にとって重要であることがわかる。On the other hand, when a quartz glass ingot was prototyped by the Bernoulli method, the Na content tended to decrease, but the trend of purity values (rank) in Table 2 did not change, and therefore the purity of the raw material is important. Therefore, it can be seen that the specific surface area of the silica powder, which is an intermediate product before addition of alkali, is important for the purity of the product.
Claims (3)
料としてゾル−ゲル法で製造した非晶質二酸化けい素を
BET法による比表面積が50m2/gより小さいものとし、
これにアルカリ成分を加え加熱してβ−クリストバライ
トとしたのち、このものを冷却してα−クリストバライ
ト粉末に転移させ、脱アルカリ処理したのち、ついで溶
融ガラス化することを特徴とする石英ガラスの製造方
法。1. An amorphous silicon dioxide produced by a sol-gel method using a metal alkoxide or an inorganic silicate as a raw material having a specific surface area of less than 50 m 2 / g by the BET method,
Production of quartz glass characterized by adding an alkali component to this and heating it to obtain β-cristobalite, cooling this to transform it into α-cristobalite powder, subjecting it to dealkalization, and then subjecting it to molten vitrification Method.
けい素を、 1,000℃以上、好ましくは 1,100〜 1,200℃
に加熱することにより、BET法による比表面積を50m2
/gより小さいものとすることを特徴とする特許請求の範
囲第1項記載の石英ガラスの製造方法。2. Amorphous silicon dioxide produced by the sol-gel method is 1,000 ° C. or higher, preferably 1,100-1,200 ° C.
The specific surface area by BET method by heating to 50 m 2
The method for producing quartz glass according to claim 1, wherein the value is smaller than / g.
理が加熱処理、ハロゲン成分存在下での加熱処理または
酸洗浄処理のいずれかまたはそれらの組合せで行なわれ
る特許請求の範囲第1項記載の石英ガラスの製造方法。3. The quartz glass according to claim 1, wherein the dealkalizing treatment of the α-cristobalite powder is carried out by any one of heat treatment, heat treatment in the presence of a halogen component, acid washing treatment, or a combination thereof. Manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62335444A JPH0624993B2 (en) | 1987-12-28 | 1987-12-28 | Quartz glass manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62335444A JPH0624993B2 (en) | 1987-12-28 | 1987-12-28 | Quartz glass manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01176243A JPH01176243A (en) | 1989-07-12 |
| JPH0624993B2 true JPH0624993B2 (en) | 1994-04-06 |
Family
ID=18288627
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62335444A Expired - Lifetime JPH0624993B2 (en) | 1987-12-28 | 1987-12-28 | Quartz glass manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0624993B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008032698A1 (en) * | 2006-09-11 | 2008-03-20 | Tosoh Corporation | Fused quartz glass and process for producing the same |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3751326B2 (en) * | 1994-10-14 | 2006-03-01 | 三菱レイヨン株式会社 | Manufacturing method of high purity transparent quartz glass |
| US6376401B1 (en) | 1998-09-07 | 2002-04-23 | Tosoh Corporation | Ultraviolet ray-transparent optical glass material and method of producing same |
| US6360564B1 (en) * | 2000-01-20 | 2002-03-26 | Corning Incorporated | Sol-gel method of preparing powder for use in forming glass |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6230634A (en) * | 1985-08-02 | 1987-02-09 | Nippon Sanso Kk | Production of quartz glass |
-
1987
- 1987-12-28 JP JP62335444A patent/JPH0624993B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008032698A1 (en) * | 2006-09-11 | 2008-03-20 | Tosoh Corporation | Fused quartz glass and process for producing the same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01176243A (en) | 1989-07-12 |
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