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JPH0717389B2 - Method for producing synthetic quartz glass - Google Patents
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JPH0717389B2 - Method for producing synthetic quartz glass - Google Patents

Method for producing synthetic quartz glass

Info

Publication number
JPH0717389B2
JPH0717389B2 JP1139619A JP13961989A JPH0717389B2 JP H0717389 B2 JPH0717389 B2 JP H0717389B2 JP 1139619 A JP1139619 A JP 1139619A JP 13961989 A JP13961989 A JP 13961989A JP H0717389 B2 JPH0717389 B2 JP H0717389B2
Authority
JP
Japan
Prior art keywords
silica
quartz glass
synthetic quartz
reduced pressure
torr
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 - Fee Related
Application number
JP1139619A
Other languages
Japanese (ja)
Other versions
JPH035329A (en
Inventor
政俊 滝田
孝明 清水
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP1139619A priority Critical patent/JPH0717389B2/en
Publication of JPH035329A publication Critical patent/JPH035329A/en
Publication of JPH0717389B2 publication Critical patent/JPH0717389B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/10Forming beads
    • C03B19/1095Thermal after-treatment of beads, e.g. tempering, crystallisation, annealing
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/06Other methods of shaping glass by sintering, e.g. by cold isostatic pressing of powders and subsequent sintering, by hot pressing of powders, by sintering slurries or dispersions not undergoing a liquid phase reaction
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/06Other methods of shaping glass by sintering, e.g. by cold isostatic pressing of powders and subsequent sintering, by hot pressing of powders, by sintering slurries or dispersions not undergoing a liquid phase reaction
    • C03B19/066Other methods of shaping glass by sintering, e.g. by cold isostatic pressing of powders and subsequent sintering, by hot pressing of powders, by sintering slurries or dispersions not undergoing a liquid phase reaction for the production of quartz or fused silica articles
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/10Forming beads
    • C03B19/1005Forming solid beads
    • C03B19/106Forming solid beads by chemical vapour deposition; by liquid phase reaction
    • C03B19/1065Forming solid beads by chemical vapour deposition; by liquid phase reaction by liquid phase reactions, e.g. by means of a gel phase
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B20/00Processes specially adapted for the production of quartz or fused silica articles, not otherwise provided for

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Dispersion Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Glass Melting And Manufacturing (AREA)
  • Silicon Compounds (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は合成石英ガラスの製造方法、特には高純度で粘
度が高く、ガス放出量が少ないことからプロセスチュー
ブ、ボート、カンチレバーなどの半導体用耐熱治具に好
適とされる合成石英ガラスの製造方法に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a method for producing synthetic quartz glass, particularly for semiconductors such as process tubes, boats, and cantilevers because of its high purity, high viscosity, and low gas emission. The present invention relates to a synthetic quartz glass manufacturing method suitable for a heat-resistant jig.

[従来の技術] 石英ガラスの製造については天然の水晶粉を減圧下に2,
000℃付近の温度で溶融する方法がよく知られており、
これについては炭化けい素を内張りした黒鉛ルツボに水
晶粉を入れ、10-2〜10-4トールの減圧下に2,000℃で溶
融し、冷却の際に減圧を解除し、炭酸ガスによって圧力
を加えて泡を肉眼では見えないように小さくするという
方法がヘルベルゲル法と呼ばれている。そして、この方
法で作られた石英ガラスはOH基含有量が極端に少なく、
−Si−Si−結合を含んでいるので高粘度であり、不純物
拡散も遅いという特性をもっているので、半導体拡散部
材、ランプなどに多く使用されている。
[Prior Art] For the production of quartz glass, use natural quartz powder under reduced pressure.
Well known is the method of melting at temperatures around 000 ° C,
For this, crystal powder was placed in a graphite crucible lined with silicon carbide, melted at 2,000 ° C under a reduced pressure of 10 -2 to 10 -4 Torr, the reduced pressure was released during cooling, and pressure was applied by carbon dioxide gas. The method of making bubbles so small that they cannot be seen with the naked eye is called the Herberger method. And the quartz glass made by this method has extremely low OH group content,
Since it contains a —Si—Si— bond, it has high viscosity and slow diffusion of impurities. Therefore, it is widely used in semiconductor diffusion members, lamps and the like.

また、この石英ガラスの製造については発煙状シリカを
バインダーを用いて成形し、減圧下に1,300〜1,500℃で
焼結させ、連続的に管引きするという方法、四塩化けい
素の火炎加水分解法で生成した微粉末シリカスートをタ
ーゲットに付着、成長させて得た多孔室ガラス部材を減
圧下で焼結させる方法も知られており、さらにはアルコ
キシシランを加水分解して得たシリカゾルをコロイダル
シリカと混合し、成形したのち、減圧下に焼結するゾル
−ゲル法も知られている。
For the production of this quartz glass, fumed silica is molded using a binder, sintered at 1,300-1,500 ° C under reduced pressure, and continuously piped, a flame hydrolysis method for silicon tetrachloride. It is also known that the fine powder silica soot produced in step 1 is attached to a target, and the porous chamber glass member obtained by growing is sintered under reduced pressure. Further, silica sol obtained by hydrolyzing alkoxysilane is colloidal silica. A sol-gel method is also known in which the materials are mixed, molded, and then sintered under reduced pressure.

[発明が解決しようとする課題] しかし、この天然石英を真空溶解する方法で得られる石
英ガラスは純度がわるく、例えばAlが20ppm、Feが1pp
m、Na,K,Li,Caが1〜2ppmであるために、これを半導体
の拡散炉部材として使用すると不純物の拡散によってシ
リコンウエーハが汚染されてしまい、シリコン素子の集
積度向上に大きな問題を与えるという不利があり、発煙
状シリカを使用する方法には安価であるけれどもこれも
Al,Feが500ppb,Na,K,Li,Caが2〜300ppbで純度がそれ程
良くなく、粘度も高くないという不利がある。
[Problems to be solved by the invention] However, the purity of the quartz glass obtained by the method of melting the natural quartz in vacuum is poor, for example, Al is 20 ppm and Fe is 1 pp.
Since m, Na, K, Li, and Ca are 1 to 2 ppm, if they are used as a semiconductor diffusion furnace member, the silicon wafer will be contaminated by the diffusion of impurities, which poses a major problem in improving the integration of silicon devices. It has the disadvantage of giving, and the method of using fuming silica is cheap, but this also
Al, Fe are 500 ppb, Na, K, Li, Ca are 2 to 300 ppb, and the purity is not so good and the viscosity is not high.

また、上記した四塩化けい素の火炎加水分解によるスー
ト法は使用する酸水素の量が製品重量に比較して多量で
コスト的に不利であるし、量産化、大型化が難しいとい
う欠点がある。なお、シリカゾルとコロイダルシリカと
を混合し成形するゾル−ゲル法は、乾燥と仮焼、焼結の
速度が速いと割れてしまい、特に大型品にその傾向が強
く、コスト高で量産化、大型化が難しいという欠点があ
り、さらに純度を高くするためには試薬、道具類の選択
は勿論のこと、乾燥、仮焼、焼結をクリーンルーム内で
行なわなければならないという不利がある。
Further, the soot method by flame hydrolysis of silicon tetrachloride described above has a disadvantage that the amount of oxyhydrogen used is large compared to the weight of the product and it is disadvantageous in terms of cost, and mass production and enlargement are difficult. . The sol-gel method of mixing and molding silica sol and colloidal silica is broken when the drying, calcination, and sintering speeds are high, and this tendency is strong especially for large products, mass production at high cost, large size However, in order to further increase the purity, not only the selection of reagents and tools but also the disadvantage of drying, calcination and sintering in a clean room is disadvantageous.

[課題を解決するための手段] 本発明はこのような不利、欠点を解決した合成石英ガラ
スの製造方法に関するものであり、これはメチルシリケ
ートをアルコールの添加なしで水の存在下に40〜50℃で
水よりなる系で加水分解し、重縮合させて粒径400〜1,0
00nmのシリカ粒子を生成させ、固液分離し、脱水し、乾
燥して粉末としたのち、これを酸化雰囲気において加熱
して脱炭後、耐熱ケースに詰め、10-2〜10-4トールの減
圧下に1,500〜1,700℃で焼結し、ついで常圧下あるいは
加圧下に1,800〜2,200℃に加熱することを特徴とするも
のである。
[Means for Solving the Problems] The present invention relates to a method for producing synthetic quartz glass, which solves the above disadvantages and drawbacks, in which methyl silicate is added in the presence of water in the presence of water at 40-50%. Hydrolyzed in a system consisting of water at ℃, polycondensed to a particle size of 400-1,0
After producing 00nm silica particles, solid-liquid separation, dehydration, and drying to powder, heat this in an oxidizing atmosphere to decarburize it, then pack it in a heat-resistant case and store at 10 -2 to 10 -4 Torr. It is characterized in that it is sintered at 1,500 to 1,700 ° C under reduced pressure and then heated to 1,800 to 2,200 ° C under normal pressure or pressure.

すなわち、本発明者らは高純度で粘度が高く、無泡で透
明性のよい合成石英ガラスを得る方法について種々検討
した結果、ゾル−ゲル法において始発材とされるアルコ
キシシランを粘度が低いためにアルコールなどの溶媒に
希釈する必要がなく、そのまま添加できるメチルシリケ
ートに特定し、これを充分精製したうえでアルコールの
添加なしでアンモニア水の存在下に40〜50℃で水よりな
る系で加水分解させると、固液分離が容易にできる粒径
が大きく、孔径も大きい三次元マトリックス構造をもつ
球状のシリカが容易に得られ、これを粉末にしてカーボ
ンケースなどの耐熱容器に詰め、10-2〜10-4トールの減
圧下で焼結し、ついで1,800℃以上の高温で加熱すれば
透明、高純度で、粘度の高く、しかも不純物の拡散速度
の極めて遅い合成石英ガラスを得ることができることを
見出し、この焼結条件、事後の加熱処理条件についての
研究を進めて本発明を完成させた。
That is, as a result of various studies on the method for obtaining synthetic silica glass having high purity, high viscosity, bubble-free and good transparency, the present inventors have found that alkoxysilane, which is a starting material in the sol-gel method, has low viscosity. It is not necessary to dilute it with a solvent such as alcohol, and it is specified as methyl silicate that can be added as it is.After sufficiently purifying it, hydrolysis with a system consisting of water at 40-50 ° C in the presence of ammonia water without the addition of alcohol is carried out. When is decomposed, particle size solid-liquid separation can be easily large, spherical silica can be easily obtained with a three-dimensional matrix structure larger pore size, which is packed into the heat-resistant container such as carbon case with the powder, 10 - 2-10 -4 sintered under a reduced pressure of torr, then 1,800 ° C. transparent by heating at a higher temperature than at a high purity, high viscosity, yet very slow synthetic quartz diffusion rate of the impurity It found that it is possible to obtain a lath, this sintering conditions, and completed the present invention by studying on heat treatment conditions of the posterior.

以下にこれをさらに詳述する。This will be described in more detail below.

[作用] 本発明の合成石英ガラスの製造方法はメチルシリケート
をアルコールの添加なしでアンモニア水の存在下に40〜
50℃で水よりなる系で加水分解してシリカ粒子を生成さ
せたのち、これを脱炭し、焼結し、加熱処理して石英ガ
ラスとするものである。
[Operation] The method for producing synthetic quartz glass of the present invention is performed by adding methyl silicate in the presence of ammonia water in the presence of ammonia water without adding alcohol.
The silica particles are hydrolyzed at 50 ° C. in a system consisting of water, and then silica particles are decarburized, sintered, and heat-treated to obtain quartz glass.

本発明の方法における始発材は粘度が低くアルコール希
釈が不要で、また反応性に富んでおり、アンモニア水の
存在下でアルコールのような溶媒なしの水よりなる系に
添加してでも容易に反応して粒径が400〜1,000nmである
径の大きな球状シリカを生成し、殆どが水よりなる系で
あることから分離が容易にできるということからメチル
シリケートが選択されるが、このメチルシリケートは目
的とする合成石英ガラスを高純度のものとするというこ
とから事前に蒸留操作などにより充分に精製したものと
して供給する必要がある。
The starting material in the method of the present invention has a low viscosity, does not require alcohol dilution, and is highly reactive, and easily reacts even when added to a system consisting of water without a solvent such as alcohol in the presence of aqueous ammonia. Methyl silicate is selected because it produces large spherical silica with a particle size of 400 to 1,000 nm, and because it is a system consisting mostly of water, it can be easily separated, but this methyl silicate is Since the target synthetic quartz glass is of high purity, it must be supplied in advance as being sufficiently purified by distillation or the like.

このメチルシリケートは加水分解によってシリカゾルと
されるのであるが、この加水分解は公知の塩酸のような
酸触媒の存在下で行なうと得られるシリカが粒子の小さ
いものとなるので、アンモニア触媒の存在下で行なう必
要がある。したがってこのメチルシリケートをアルコー
ルの添加なしでアンモニア水の存在下に40〜50℃で水よ
りなる系で加水分解すると、得られるシリカは粒径が40
0〜1,000nmの大きい球状物となるし、このものはその表
面に大きな孔をもっている非常に規則的な三次元マトリ
ックス構造をもつものになる。
This methyl silicate is hydrolyzed to form a silica sol. When this hydrolysis is carried out in the presence of a known acid catalyst such as hydrochloric acid, the silica obtained has a small particle size, and therefore in the presence of an ammonia catalyst. You need to do it in. Therefore, if this methyl silicate is hydrolyzed in the presence of aqueous ammonia at 40-50 ° C in a system consisting of water without the addition of alcohol, the resulting silica will have a particle size of 40
It becomes a large sphere with a size of 0 to 1,000 nm, which has a very regular three-dimensional matrix structure with large pores on its surface.

この水系での加水分解反応は40℃未満ではシリカの粒径
が400nm未満となり、また50℃を超えると大きな塊とな
っていしまうので、40〜50℃で行なわせることが必要
で、このようにして得られたシリカはフィルタープレス
を使用すれば水系より容易に固液分離してシリカとす
る。
If the hydrolysis reaction in this water system is less than 40 ° C, the particle size of silica will be less than 400 nm, and if it exceeds 50 ° C, it will become a large lump, so it is necessary to perform it at 40-50 ° C. The silica thus obtained is subjected to solid-liquid separation more easily than silica by using a filter press to obtain silica.

このようにして得られたシリカを乾燥して得られたシリ
カ粉末はついでこれをカーボンケースに詰め、減圧下で
焼結するのであるが、この減圧は10-2トールを超えると
脱泡が充分でなくなるため10-2トール以下、好ましくは
10-2〜10-4トールとすることが必要である。また、この
焼結温度は1,500℃未満では充分な焼結が行なわれず、
したがって次段における加熱によって外観上不透明なも
のとなるし、1,700℃より高い温度とするとシリカ粒子
に含有されている泡が成長して大きくなり、この泡が最
後まで残るようになるので、これは1,500〜1,700℃の範
囲とする必要がある。
The silica powder obtained by drying the silica thus obtained is then packed in a carbon case and sintered under reduced pressure, but when the reduced pressure exceeds 10 -2 Torr, defoaming is sufficient. Less than 10 -2 Torr, preferably
It should be 10 -2 to 10 -4 torr. Also, if the sintering temperature is less than 1,500 ° C, sufficient sintering cannot be performed,
Therefore, the heating in the next stage makes it opaque in appearance, and when the temperature is higher than 1,700 ° C, the bubbles contained in the silica particles grow and grow, and the bubbles remain until the end. It must be in the range of 1,500 to 1,700 ° C.

この焼結によってシリカは合成ガラスとされるが、本発
明の方法ではこのようにして得た石英ガラスをさらに1,
800〜2,200℃に加熱処理する。すなわち、このようにし
て得られた焼結物としての石英ガラスは炉外に取り出し
たのち再度加熱するのであるが、この加熱温度は1,800
〜2,200℃とすると石英ガラスの粘度が低くなって前段
の減圧焼結で発生した泡が圧力差でつぶれ易くなり、目
視でわかる泡がなくなるという有利性が与えられるけれ
ども、これを2,000℃以上とするとSiOの蒸気が激しく発
生するので、これは好ましくは1,800〜2,000℃の範囲と
することがよい。なお、この加熱は常圧で行なえばよい
が、これは1〜10気圧での加圧下で行なってもよく、加
圧とすればますます泡がつぶれ、目視では全く分らなく
なるという有利性が与えられる。
Silica is made into synthetic glass by this sintering, but in the method of the present invention, the silica glass thus obtained is
Heat to 800-2,200 ℃. That is, the quartz glass as a sintered product thus obtained is taken out of the furnace and then heated again. The heating temperature is 1,800.
If the temperature is set to ~ 2,200 ° C, the viscosity of the quartz glass becomes low and the bubbles generated in the pressure reduction sintering in the previous stage are easily collapsed due to the pressure difference, which gives the advantage that there is no visible bubble. Then, SiO vapor is violently generated, so this is preferably in the range of 1,800 to 2,000 ° C. It should be noted that this heating may be performed at normal pressure, but this may be performed under pressure at 1 to 10 atm, and if pressure is applied, the bubbles will collapse more and more and it will not be visible at all. To be

[実施例] つぎに本発明の実施例および比較例をあげる。[Examples] Next, examples and comparative examples of the present invention will be described.

実施例1 1m3のグラスライニング反応器に20重量%のNH4OH水300
lを入れ、これに充分精製したメチルシリケート265lを
滴下し、40〜50℃で加水分解反応を行なわせ、この反応
液をフィルタープレスで固液分離してシリカ粉135kgを
作った。
Example 1 1 m 3 of glass-lined reactor 20 wt% of aqueous NH 4 OH 300
1 liter was added, and 265 liters of sufficiently purified methyl silicate was added dropwise to the mixture to cause a hydrolysis reaction at 40 to 50 ° C. The reaction solution was subjected to solid-liquid separation with a filter press to prepare 135 kg of silica powder.

ついで、このシリカを石英製容器に入れ、清浄な空気の
存在下に800℃で20時間加熱処理して脱水し、脱炭した
ところ、シリカ粉は95kgとなったので、この50kgを外径
300mmφ×内径280mmφの容積1,000lのカーボンケースに
詰め、10-3トールの減圧下に50℃/時の昇温速度で1,60
0℃まで昇温して2時間焼結し、降温後取り出したとこ
ろ、外観上不透明な径が278mmφで容積75lの石英インゴ
ットが得られた。
Then, put this silica in a quartz container, heat-treat it at 800 ° C for 20 hours in the presence of clean air to dehydrate it, and decarburize it. As a result, the silica powder weighed 95 kg.
It is packed in a carbon case with a volume of 1,000 liters of 300 mmφ × inner diameter 280 mmφ and decompressed at 10 -3 torr at a heating rate of 50 ° C / hour for 1,60
When the temperature was raised to 0 ° C., sintering was performed for 2 hours, the temperature was lowered, and the product was taken out to obtain a quartz ingot having an outer diameter of 278 mmφ and a volume of 75 l.

つぎにこのインゴットをアルゴンガス雰囲気下で2,000
℃に1時間加熱処理したところ、径が470mmφで容積が2
5lの透明なインゴット44kgが得られ、このものの不純物
量(化学分析値)、粘度、不純物の拡散速度(Na+イオ
ンの拡散係数)をしらべたところ、第1表に示したとお
りの結果が得られた。
Next, this ingot was placed under an argon gas atmosphere for 2,000
When heat-treated at ℃ for 1 hour, the diameter is 470mmφ and the volume is 2
A transparent ingot (44 kg) of 5 liters was obtained, and the amount of impurities (chemical analysis value), viscosity, and diffusion rate of impurities (diffusion coefficient of Na + ions) were examined, and the results shown in Table 1 were obtained. Was given.

しかし、比較のために天然の水晶粉を10-3トールの減圧
下に2,000℃で溶融して作った石英(比較例1)、発煙
状シリカをポリビニルアルコールを用いて円柱状に成形
し、10-3トールの減圧下に1,500℃で焼結して作った石
英(比較例2)、テトラエチルシリケートを塩酸の存在
下で加水分解して得たシリカゾルをコロイダルシリカと
混合し、成形したのち、10-1トールの減圧下に1,800℃
で焼結して得た石英(比較例3)について、その化学分
析値、粘度、不純物の拡散速度をしらべたところ、第1
表に併記したとおりの結果が得られ、本発明の方法で得
られた石英がすぐれた物性を示すことが確認された。
However, for comparison, quartz produced by melting natural quartz powder at 2,000 ° C. under a reduced pressure of 10 −3 Torr (Comparative Example 1) and fuming silica were molded into a columnar shape using polyvinyl alcohol, Quartz made by sintering at 1,500 ° C. under a reduced pressure of −3 Torr (Comparative Example 2), silica sol obtained by hydrolyzing tetraethyl silicate in the presence of hydrochloric acid was mixed with colloidal silica, and then molded. -1,800 ° C under reduced pressure of -1 Torr
When the chemical analysis value, the viscosity, and the diffusion rate of impurities were examined for the quartz (Comparative Example 3) obtained by sintering at.
The results as shown in the table were obtained, and it was confirmed that the quartz obtained by the method of the present invention has excellent physical properties.

実施例2 実施例1で得られた不透明な石英インゴットを円研加工
して250mmφ×70lのインゴットを作り、この中心に50mm
φの穴をあけ、1,950℃の電気炉中で延伸して外径70m
m、内径60mmのパイプを作り、また上記の不透明インゴ
ットについてはこれを円研加工によって100mmφ×70lの
インゴットとしたのち酸水素火炎バーナーを用いて10mm
φのムク棒を試作した。
Example 2 The opaque quartz ingot obtained in Example 1 was subjected to circular polishing to make a 250 mmφ × 70 l ingot, and the center of which was 50 mm.
Drill a φ hole and stretch in an electric furnace at 1,950 ° C to obtain an outer diameter of 70 m.
A pipe with a diameter of 60 mm and an inner diameter of 60 mm was made, and for the above opaque ingot, this was made into a 100 mmφ × 70 l ingot by circular grinding and then 10 mm using an oxyhydrogen flame burner.
A φ Muku rod was prototyped.

つぎにこのようにして作った石英パイプおよび棒の物性
をしらべたところ、実施例1の第1表と同じ特性を示し
た。
Next, when the physical properties of the quartz pipe and the rod thus produced were examined, they showed the same characteristics as in Table 1 of Example 1.

[発明の効果] 本発明の合成石英ガラスの製造方法は前記したように、
メチルシリケートをアルコールの添加なしでアンモニア
水の存在下に40〜50℃で、水よりなる系で加水分解し、
縮重合させて得たシリカ粉末を酸化雰囲気で加熱して脱
炭後、これを耐熱容器に入れ、10-2〜10-4トールの減圧
下に1,500〜1,700℃で焼結し、ついで1,800〜2,200℃に
加熱するものであるが、これによれば高純度で粘度が高
く、無泡で透明性がよく、不純物の拡散速度が極めて遅
い合成石英ガラスを得ることができるので、プロセスチ
ューブ、ボート、カンチレバーなどの半導体用耐熱治具
として、またハロゲンランプ、赤外線ヒーターなどの封
管材として有用とされる合成石英ガラスを容易に、かつ
安価に得ることができるという有利性が与えられる。
[Effects of the Invention] As described above, the method for producing the synthetic quartz glass of the present invention is as follows.
Methyl silicate is hydrolyzed in the system consisting of water at 40-50 ° C in the presence of aqueous ammonia without the addition of alcohol,
The silica powder obtained by polycondensation is heated in an oxidizing atmosphere to decarburize it, put it in a heat-resistant container, sinter it under a reduced pressure of 10 -2 to 10 -4 Torr at 1,500 to 1,700 ° C, and then 1,800 to It is heated to 2,200 ° C. According to this, it is possible to obtain synthetic quartz glass with high purity, high viscosity, bubble-free, good transparency, and extremely slow diffusion rate of impurities. The advantage is that synthetic quartz glass, which is useful as a heat-resistant jig for semiconductors such as cantilevers and as a sealing tube material such as halogen lamps and infrared heaters, can be easily and inexpensively obtained.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】メチルシリケートをアルコールの添加なし
で、アンモニア水の存在下に40〜50℃で水よりなる系で
加水分解し、縮重合させて粒径400〜1,000nmのシリカ粒
子を生成させ、固液分離し、脱水し、乾燥して粉末とし
たのち、これを酸化雰囲気において加熱して脱炭後、耐
熱ケースに詰め、10-2トール以下の減圧下に1,500〜1,7
00℃で焼結し、ついで常圧あるいは加圧下に1,800〜2,2
00℃に加熱することを特徴とする合成石英ガラスの製造
方法。
1. Methyl silicate is hydrolyzed in the presence of aqueous ammonia at 40 to 50 ° C. in a system consisting of water without addition of alcohol and polycondensed to produce silica particles having a particle size of 400 to 1,000 nm. , Solid-liquid separation, dehydration, drying to powder, heating in an oxidizing atmosphere to decarburize, packing in a heat-resistant case, and 1,500 to 1,7 under a reduced pressure of 10 -2 torr or less.
Sinter at 00 ℃, and then under normal pressure or pressure, 1,800-2,2
A method for producing synthetic quartz glass, which comprises heating to 00 ° C.
JP1139619A 1989-06-01 1989-06-01 Method for producing synthetic quartz glass Expired - Fee Related JPH0717389B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1139619A JPH0717389B2 (en) 1989-06-01 1989-06-01 Method for producing synthetic quartz glass

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1139619A JPH0717389B2 (en) 1989-06-01 1989-06-01 Method for producing synthetic quartz glass

Publications (2)

Publication Number Publication Date
JPH035329A JPH035329A (en) 1991-01-11
JPH0717389B2 true JPH0717389B2 (en) 1995-03-01

Family

ID=15249509

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1139619A Expired - Fee Related JPH0717389B2 (en) 1989-06-01 1989-06-01 Method for producing synthetic quartz glass

Country Status (1)

Country Link
JP (1) JPH0717389B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0912322A (en) * 1995-06-29 1997-01-14 Tosoh Corp High-purity transparent quartz glass and method for producing the same
JPH0940434A (en) * 1995-07-28 1997-02-10 Tosoh Corp High-purity quartz glass and method for producing the same
DE60123878T2 (en) 2000-06-28 2007-05-24 Japan Super Quartz Corp. Synthetic quartz powder, method of manufacture and synthetic quartz crucible

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2529110B1 (en) * 1982-06-23 1985-08-23 Valeo METHOD FOR MOUNTING AT LEAST ONE TUBE ON A PLATE, TOOLS FOR CARRYING OUT THIS METHOD AND THE RADIATORS, PARTICULARLY FOR MOTOR VEHICLES OBTAINED BY THIS PROCESS, AND OTHER APPLICATIONS
JPS60226418A (en) * 1984-04-20 1985-11-11 Nippon Kogaku Kk <Nikon> Preparation of quartz glass mass
JPS63100025A (en) * 1986-10-15 1988-05-02 Seiko Epson Corp Silica glass manufacturing method

Also Published As

Publication number Publication date
JPH035329A (en) 1991-01-11

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