JPH0948623A - Quartz glass manufacturing method - Google Patents
Quartz glass manufacturing methodInfo
- Publication number
- JPH0948623A JPH0948623A JP19745395A JP19745395A JPH0948623A JP H0948623 A JPH0948623 A JP H0948623A JP 19745395 A JP19745395 A JP 19745395A JP 19745395 A JP19745395 A JP 19745395A JP H0948623 A JPH0948623 A JP H0948623A
- Authority
- JP
- Japan
- Prior art keywords
- silica powder
- quartz glass
- powder
- press
- water
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/06—Other 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
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/06—Other 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
- C03B19/066—Other 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
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B20/00—Processes specially adapted for the production of quartz or fused silica articles, not otherwise provided for
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2201/00—Type of glass produced
- C03B2201/02—Pure silica glass, e.g. pure fused quartz
- C03B2201/03—Impurity concentration specified
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Glass Compositions (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
(57)【要約】
【課題】 本発明の目的は、プレス成形に適した非晶質
シリカ粉末を使用し、半導体製造用治具及び液晶基板等
に有効な高純度透明石英ガラスを製造する方法を提供す
る。
【解決手段】 シリカ粉末のプレス成形体を焼成して石
英ガラスを製造する方法において、シリカ粉末として、
平均粒径が0.5〜10μmの範囲にあり、Na、K、
Fe、Ti、Alの各不純物が1ppm以下である非晶
質シリカ粉末に、ガラス転移点が−50℃〜0℃以下で
ある水溶性アクリル系樹脂を0.1〜10重量%添加し
て造粒した粉末を用いる。(57) Abstract: An object of the present invention is to produce a high-purity transparent quartz glass effective for a jig for semiconductor production, a liquid crystal substrate, etc., by using an amorphous silica powder suitable for press molding. I will provide a. SOLUTION: In the method for producing quartz glass by firing a press-molded body of silica powder, as silica powder,
The average particle size is in the range of 0.5 to 10 μm, and Na, K,
0.1 to 10% by weight of a water-soluble acrylic resin having a glass transition point of −50 ° C. to 0 ° C. is added to amorphous silica powder having Fe, Ti, and Al impurities of 1 ppm or less. Granulated powder is used.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、半導体製造用治工
具、ならびに液晶基板などに利用可能な高純度透明石英
ガラスの製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a jig for semiconductor manufacturing, and a method for manufacturing high-purity transparent quartz glass that can be used for liquid crystal substrates and the like.
【0002】[0002]
【従来の技術】従来、石英ガラスは、天然水晶を原料と
して真空炉で電気溶融して製造するか、あるいは酸水素
炎でベルヌーイ溶融するなどの方法で製造されている。
また、近年、SiCl4 などの合成原料を火炎加水分解
し、ガラスとして堆積する方法や一旦多孔質体として堆
積した後、焼結によりガラス化する方法も工業化されて
いる。2. Description of the Related Art Conventionally, quartz glass is manufactured by a method in which natural quartz is used as a raw material by electric melting in a vacuum furnace or by Bernoulli melting with an oxyhydrogen flame.
Further, in recent years, a method of flame-hydrolyzing a synthetic raw material such as SiCl 4 and depositing it as glass, and a method of once depositing it as a porous body and then vitrifying it by sintering have been industrialized.
【0003】さらに、開発段階では、シリカ粉末を各種
湿式成形法やプレスなどの乾式成形法で成形し焼結して
ガラス化することも行われている。Further, at the development stage, silica powder is molded by various wet molding methods or dry molding methods such as pressing, and is sintered to be vitrified.
【0004】[0004]
【発明が解決しようとする課題】現在工業化されている
製造方法はいずれも、コラムあるいはスラブ状の石英ガ
ラス塊を製造する方法であり、所望の形状を与えるため
には、切断、研削などの機械加工や溶融加工を必要とす
る。All of the manufacturing methods currently industrialized are methods for manufacturing a column or slab-shaped quartz glass ingot, and in order to give a desired shape, a machine such as cutting or grinding is used. Requires processing and melt processing.
【0005】一方、この加工労力を短縮するために、シ
リカ粉末を予め各種成形方法により所望の形状にした
後、焼成して石英ガラスを製造する方法が研究されてお
り、特に、乾式プレス成形を用いた場合、板状などの形
状を面精度よく製造できる可能性がある。しかし、現状
では、プレス成形体にラミネーションや欠けが発生しや
すい、焼成時にクラックが発生する、あるいは、製造さ
れた石英ガラスに大きな気泡が残存するなど種々の問題
があるために工業化に至っていない。On the other hand, in order to shorten the processing labor, a method of manufacturing silica glass by forming silica powder into a desired shape by various molding methods in advance and then firing the silica glass has been studied. In particular, dry press molding is performed. When used, there is a possibility that a plate-like shape can be manufactured with high surface accuracy. However, at present, it has not been industrialized due to various problems such as lamination and chipping of the press-molded body, cracks during firing, and large bubbles remaining in the manufactured quartz glass.
【0006】本発明はこれらの課題を解決することを目
的としてなされたものであり、特に工業的に有利なプレ
ス成形体を焼成してガラス化する方法における従来の問
題の多くはプレス成形の工程にその起因があり、したが
って成形に適したシリカ粉末を用いることで上記問題を
解決できることに着目して本発明をなすに至ったもので
ある。The present invention has been made for the purpose of solving these problems, and most of the conventional problems in the method of firing and vitrifying a press-molded article which is industrially advantageous are mostly the steps of the press-molding. The present invention has been made paying attention to the fact that the above problems can be solved by using a silica powder suitable for molding.
【0007】[0007]
【課題を解決するための手段】本発明者らは、上記課題
を解決するため鋭意検討した結果本発明に到達した。す
なわち、本発明の石英ガラスの製造方法の特徴の一つ
は、シリカ粉末のプレス成形体を焼成して石英ガラスを
製造する方法において、平均粒径が0.5〜10μmの
範囲にあり、Na、K、Fe、Ti、Alの各不純物が
1ppm以下である非晶質シリカ粉末に、ガラス転移点
が−50℃〜0℃である水溶性アクリル系樹脂を0.1
〜10重量%添加して造粒し、これを造粒した造粒粉末
を用いて上記プレス成形体を形成するようにしたところ
にある。The present inventors have arrived at the present invention as a result of extensive studies to solve the above problems. That is, one of the features of the method for producing quartz glass of the present invention is a method for producing quartz glass by firing a press-molded body of silica powder, wherein the average particle size is in the range of 0.5 to 10 μm, and Na Of water-soluble acrylic resin having a glass transition point of −50 ° C. to 0 ° C. to an amorphous silica powder having impurities of K, Fe, Ti, and Al of 1 ppm or less.
The above-mentioned press-molded body is formed by using the granulated powder obtained by adding 10 wt.
【0008】上記方法においては、ガラス転移点が−5
0℃〜0℃である水溶性アクリル系樹脂を0.1〜10
重量%添加して造粒した造粒粉末を用いて成形したプレ
ス成形体を用いて石英ガラスを製造するにあたり、この
プレス成形体を、500〜1300℃の温度で加熱して
含有する水溶性アクリル系樹脂を分解除去した後、真空
雰囲気下1300〜1600℃の温度で加熱焼結する緻
密化処理を行い、ついで窒素ガスあるいはアルゴンガス
の不活性ガス雰囲気下1700〜1850℃の温度で加
熱溶融後、放冷してガラス化することが好ましく、また
用いる非晶質シリカ粉末としては、アルカリ金属ケイ酸
塩水溶液と酸とを反応させて得た非晶質シリカ粉末が好
ましく用いられる。In the above method, the glass transition point is -5.
Water-soluble acrylic resin having a temperature of 0 ° C to 0 ° C is added in an amount of 0.1 to 10
A water-soluble acryl which is obtained by heating the press-molded product at a temperature of 500 to 1300 ° C. when manufacturing the quartz glass by using the press-molded product formed by using the granulated powder which is added by weight% and granulated. After decomposing and removing the system resin, densification treatment is performed by heating and sintering at a temperature of 1300 to 1600 ° C in a vacuum atmosphere, and then heating and melting at a temperature of 1700 to 1850 ° C in an inert gas atmosphere of nitrogen gas or argon gas. It is preferable that the amorphous silica powder is allowed to cool and vitrify, and the amorphous silica powder used is preferably an amorphous silica powder obtained by reacting an aqueous alkali metal silicate solution with an acid.
【0009】[0009]
【発明の実施の形態】以下、本発明をさらに詳細に説明
する。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in more detail below.
【0010】本発明で使用されるシリカ粉末は、平均粒
径0.5〜10μmの範囲にあり、かつNa、K、F
e、Ti、Alの各不純物が1ppm以下である微細な
高純度粉末であることが必要である。平均粒径が上記範
囲とされる理由は、粉末成形を可能とするためであり、
この範囲外の平均粒径をもつシリカ粉末ではプレス成形
が不可能ないし困難となる。ここでいう「平均粒径」
は、例えば粉末を液体に十分分散させて光散乱から測定
される一次粒子の粒子径の平均値をいい、造粒操作によ
って得られる二次粒子を対象とするものではない。The silica powder used in the present invention has an average particle size in the range of 0.5 to 10 μm and contains Na, K and F.
It is necessary to be a fine high-purity powder in which each impurity of e, Ti, and Al is 1 ppm or less. The reason that the average particle size is in the above range is to enable powder molding,
Press molding is impossible or difficult with silica powder having an average particle diameter outside this range. "Average particle size" here
Means an average value of particle diameters of primary particles measured by light scattering, for example, by sufficiently dispersing powder in a liquid, and does not target secondary particles obtained by a granulation operation.
【0011】また、含有されるNa、K、Fe、Ti、
Alの各不純物は1ppm以下であることが必要であ
り、これらの各不純物が1ppmを越えるシリカ粉末を
用いると、紫外線領域の光透過率が低下する傾向が大き
くなって、半導体製造にこの高純度透明ガラスを使用す
る場合には、製造が適当に行えないという不具合を招く
ために好ましくない。このような高純度粉末は、通常、
合成法により得られる。合成法としては、アルカリ金属
ケイ酸水溶液(水ガラス)を酸と反応させることにより
アルカリ金属を除去してシリカを得る方法、SiCl4
を加水分解してシリカとする方法、シリコンアルコキシ
ドを加水分解してシリカとする方法が挙げられるが、工
業的規模の生産には、ナトリウム,カリウム,リチウム
等のアルカリ金属と二酸化珪素からなるアルカリ金属ケ
イ酸塩水溶液(水ガラス)を硫酸,硝酸,塩酸等の無機
酸と反応させる方法で得られるものが好適である。Further, the contained Na, K, Fe, Ti,
It is necessary that each impurity of Al is 1 ppm or less, and if silica powder in which each of these impurities exceeds 1 ppm is used, the light transmittance in the ultraviolet region tends to decrease, and this high purity is used for semiconductor manufacturing. The use of transparent glass is not preferable because it causes a problem that the production cannot be appropriately performed. Such high-purity powder is usually
Obtained by a synthetic method. As a synthetic method, a method of obtaining silica by removing an alkali metal by reacting an alkali metal silicic acid aqueous solution (water glass) with an acid, SiCl 4
There are a method of hydrolyzing silica to silica and a method of hydrolyzing silicon alkoxide to silica. For industrial scale production, alkali metal such as sodium, potassium and lithium and an alkali metal composed of silicon dioxide are used. Those obtained by a method of reacting an aqueous silicate solution (water glass) with an inorganic acid such as sulfuric acid, nitric acid, hydrochloric acid are suitable.
【0012】本発明においては、プレス成形性を良好と
するために、上記非晶質シリカ粉末には、ガラス転移点
が−50℃〜0℃の水溶性アクリル系樹脂が0.1〜1
0重量%(いずれも乾燥状態での重量比)の割合になる
ように添加される。添加材として水溶性アクリル系樹脂
が選択されるのは、粉末の造粒のためにシリカ粉末を水
に分散させスラリー化する必要があり、このスラリー化
の際に水溶性のアクリル系樹脂はシリカスラリーとの均
一な混合が容易なためである。このような水溶性アクリ
ル系樹脂としては、ポリアクリル酸エステル,ポリメタ
クリル酸エステル,メトキシメチルメタクリレートとア
クリル酸との重合体等が例示される。In the present invention, in order to improve press moldability, the amorphous silica powder contains 0.1 to 1 of a water-soluble acrylic resin having a glass transition point of -50 ° C to 0 ° C.
It is added so as to have a ratio of 0% by weight (in each case, a weight ratio in a dry state). A water-soluble acrylic resin is selected as an additive because it is necessary to disperse silica powder in water to form a slurry for granulation of the powder, and when the slurry is formed, the water-soluble acrylic resin is silica. This is because uniform mixing with the slurry is easy. Examples of such water-soluble acrylic resins include polyacrylic acid esters, polymethacrylic acid esters, polymers of methoxymethyl methacrylate and acrylic acid, and the like.
【0013】また、添加される水溶性アクリル系樹脂が
そのガラス転移点を上記範囲とされるのは、プレス成形
体の密度が、最終的に得られるガラスの性状に大きく影
響を及ぼすことに原因する。すなわち、成形体密度が低
いと100μm径以上の大きな気泡が多数生じたり、ガ
ラス全体が大きく歪んでしまうが、成形体密度を高める
とこのような現象を避けることができるからである。他
方、ガラス転移点が常温あるいはそれ以上の温度である
水溶性アクリル系樹脂をシリカ粉末に添加すると、無添
加の場合に比べて、クラックなどの欠陥の発生を抑え、
密度の高いプレス成形体を得ることは可能ではあるが、
得られるガラスにおける気泡、変形の発生を抑制するに
は十分ではない。本発明においては常温よりも十分に低
い−50℃〜0℃のガラス転移点の水溶性アクリル系樹
脂を用いるので、樹脂自身が大きく塑性変形するため成
形体の密度はより大幅に向上し、このような成形体を焼
成することにより良質のガラスを得ることができる。こ
れらの理由から、本発明においてはガラス転移点が上記
範囲の水溶性アクリル系樹脂が好ましく用いられる。The glass transition point of the water-soluble acrylic resin added is set within the above range because the density of the press-formed product has a great influence on the properties of the finally obtained glass. To do. That is, when the compact density is low, a large number of large bubbles having a diameter of 100 μm or more are generated or the entire glass is greatly distorted, but such a phenomenon can be avoided by increasing the compact density. On the other hand, when a water-soluble acrylic resin having a glass transition point at room temperature or higher is added to silica powder, the occurrence of defects such as cracks can be suppressed as compared with the case of no addition,
Although it is possible to obtain a press-molded body with a high density,
It is not sufficient to suppress the occurrence of bubbles and deformation in the obtained glass. In the present invention, since a water-soluble acrylic resin having a glass transition point of -50 ° C to 0 ° C, which is sufficiently lower than room temperature, is used, the resin itself is largely plastically deformed, so that the density of the molded body is significantly improved. Good quality glass can be obtained by firing such a molded body. For these reasons, a water-soluble acrylic resin having a glass transition point in the above range is preferably used in the present invention.
【0014】添加量は、10重量%よりも多い場合には
プレス成形後の脱樹脂のための加熱において成形体にク
ラックが発生したり、得られたガラスに無数の大きな気
泡が発生する問題を招き、他方、添加量が0.1重量%
未満では効果が不十分であるため、上記の範囲とされ
る。If the amount added is more than 10% by weight, cracks may be generated in the molded product during heating for resin removal after press molding, or innumerable large bubbles may be generated in the obtained glass. On the other hand, the addition amount is 0.1% by weight
If it is less than the above range, the effect is insufficient, so the above range is set.
【0015】上記のシリカ粉末と水溶性アクリル系樹脂
を混合したスラリーは、限定されるものではないがスプ
レードライヤー等の造粒装置を用いて二次粒子に造粒さ
れて造粒粉末とされる。二次粒子に造粒するのは、粉末
の流動性を高めることによって、例えばプレス成形金型
への充填を容易とし、より高い密度の成形体が得られる
ようにするためであり、造粒粉末の粒子径(二次粒子
径)は一般に30〜200μmとされるのが好ましい場
合が多い。The slurry prepared by mixing the silica powder and the water-soluble acrylic resin is granulated into secondary particles by using a granulating device such as, but not limited to, a spray dryer. . The secondary particles are granulated in order to enhance the fluidity of the powder, for example, to facilitate the filling into a press molding die and to obtain a molded body having a higher density. In many cases, it is preferable that the particle diameter (secondary particle diameter) is generally 30 to 200 μm.
【0016】造粒された二次粒子の粉末(造粒粉末)
は、適宜の金型等の成形型に充填されて所定形状のプレ
ス成形体に成形される。成形圧は限定されるものではな
いが一般的には200〜2000kg/cm2 、好まし
くは500〜1000kg/cm2 程度とされるのがよ
い。Granulated secondary particle powder (granulated powder)
Is filled in a molding die such as an appropriate die and molded into a press-molded body having a predetermined shape. Molding pressure is limited by what is though not generally 200~2000kg / cm 2, preferably from being a 500~1000kg / cm 2 approximately.
【0017】成形体は、プレス成形後500〜1300
℃にて加熱し、含まれているアクリル系樹脂を除去する
脱樹脂処理が行われる。この脱樹脂処理時の雰囲気は大
気中とすることが良い。焼成後の成形体にアクリル系樹
脂が残存すると、最終的に得られるガラスに炭素分が残
り黒点となって現れ、また気泡発生の原因になるため該
脱樹脂処理は必要十分に行われることが望ましく、上記
温度範囲において通常2〜20時間、好ましくは5〜1
0時間保持される。The molded product is 500 to 1300 after press molding.
The resin is removed by heating at 0 ° C. to remove the contained acrylic resin. The atmosphere during this resin removal treatment is preferably atmospheric air. When the acrylic resin remains in the molded product after firing, carbon content remains in the finally obtained glass and appears as black spots, which causes bubbles to be generated, so that the resin removal treatment is necessary and sufficient. Desirably, in the above temperature range, usually 2 to 20 hours, preferably 5 to 1
Hold for 0 hours.
【0018】脱樹脂処理された成形体をガラス化するた
めの熱処理は、該成形体を平坦度の高いカーボン製平板
の上に置いて行われる。室温から1300〜1600℃
まで真空雰囲気中で加熱して緻密化させた後、引き続い
て窒素ガスあるいはアルゴンガスの不活性ガス雰囲気下
で1700〜1850℃まで昇温して緻密化した成形体
を加熱溶融し、一定時間保持した後、放冷することによ
り目的とする透明石英ガラスを得ることができる。緻密
化のための熱処理は、1300〜1600℃で1〜5時
間実施することが好ましい。また溶融のための熱処理
は、1700〜1850℃で好ましくは30分以内、よ
り好ましく5〜20分の間、保持することが好ましい。
この溶融温度の範囲を規定するのは、1700℃より低
温では、しばしば結晶化による亀裂が発生し、他方、1
850℃より高温では、溶融状態での粘性が大きく低下
するため、所望の形状のガラスを得ることが困難になる
からである。The heat treatment for vitrifying the resin-removed molded product is carried out by placing the molded product on a carbon flat plate having a high degree of flatness. From room temperature to 1300 to 1600 ℃
To densify by heating in a vacuum atmosphere until the temperature is increased to 1700 to 1850 ° C. in an inert gas atmosphere of nitrogen gas or argon gas to melt and densify the compacted body and hold for a certain period of time. After that, the target transparent quartz glass can be obtained by allowing to cool. The heat treatment for densification is preferably performed at 1300 to 1600 ° C. for 1 to 5 hours. Further, the heat treatment for melting is preferably held at 1700 to 1850 ° C. for preferably 30 minutes or less, more preferably 5 to 20 minutes.
This melting temperature range is defined by the fact that below 1700 ° C., cracks due to crystallization often occur, while
This is because at a temperature higher than 850 ° C., the viscosity in the molten state is greatly reduced, and it becomes difficult to obtain glass having a desired shape.
【0019】[0019]
【実施例】以下の実施例により、本発明を具体的に説明
するが、本発明はこれらの実施例により、何等限定され
るものでない。The present invention will be specifically described with reference to the following examples, but the present invention is not limited to these examples.
【0020】実施例1 ケイ酸ソーダと酸を反応させた後、加熱処理、粉砕して
平均粒径1.6μmに調製した非晶質シリカ粉末(日東
化学工業製、商品名シリカエースA、含有不純物の分析
結果は下記表1に示す)を水に分散させ、50重量%の
スラリーを調製した。Example 1 Amorphous silica powder (trade name Silica Ace A, manufactured by Nitto Kagaku Kogyo Co., Ltd.) was prepared by reacting sodium silicate with an acid and then heat-treating and pulverizing the mixture to prepare an average particle size of 1.6 μm. Impurity analysis results are shown in Table 1 below) was dispersed in water to prepare a 50 wt% slurry.
【0021】[0021]
【表1】 [Table 1]
【0022】このスラリーに、ガラス転移点が−8℃で
あるアクリル共重合樹脂水溶液(中央理化工業製、商品
名リカボンドSA−200)を、アクリル共重合樹脂が
シリカ粉末中に2重量%(乾燥重量比:以下同様)含ま
れるように添加し、十分に撹拌した。To this slurry, an aqueous solution of an acrylic copolymer resin having a glass transition point of -8 ° C. (manufactured by Chuo Rika Kogyo, trade name Ricabond SA-200) was added, and the acrylic copolymer resin was contained in silica powder in an amount of 2% by weight (dry). (Weight ratio: same below) Added so that it was included, and stirred sufficiently.
【0023】撹拌後、スプレードライヤーを用いて造粒
し(平均造粒粒子径:70μm)、プレス成形用の二次
粉末(造粒粉末)を得た。この粉末を金型に充填し、一
軸プレス機で500kg/cm2 の圧力を印加して、2
00×200×1.5mm(厚さ)の大きさの成形体を
得た。成形体を目視観察したところ周辺部のクラックは
認められなかった。After stirring, granulation was performed using a spray dryer (average granulated particle size: 70 μm) to obtain a secondary powder (granulated powder) for press molding. This powder was filled in a mold, and a pressure of 500 kg / cm 2 was applied by a uniaxial press machine to
A compact having a size of 00 × 200 × 1.5 mm (thickness) was obtained. When the molded product was visually observed, no cracks were found in the peripheral portion.
【0024】この成形体を大気中、1050℃に10時
間保持して成形体中のアクリル共重合樹脂を脱樹脂し
た。なお、脱樹脂後の成形体の密度は1.35g/cm
3 であった。これをカーボン平板(225×225×5
mm(厚さ):東洋炭素社製,E252で作製)上に載
せて電気炉に入れ、真空中1450℃まで100℃/h
rで昇温して5時間保持した後、炉内を窒素ガス雰囲気
とし、1800℃まで300℃/hrで昇温して5分間
保持し、石英ガラスを得た。This molded body was kept at 1050 ° C. for 10 hours in the atmosphere to remove the acrylic copolymer resin in the molded body. The density of the molded product after resin removal is 1.35 g / cm.
Was 3 . This is a carbon flat plate (225 x 225 x 5
mm (thickness: manufactured by Toyo Tanso Co., Ltd., manufactured by E252), placed in an electric furnace, and heated to 1450 ° C. in vacuum at 100 ° C./h.
After the temperature was raised at r and held for 5 hours, the inside of the furnace was made into a nitrogen gas atmosphere, the temperature was raised to 1800 ° C. at 300 ° C./hr, and the temperature was held for 5 minutes to obtain quartz glass.
【0025】得られたガラス(サイズ:180×180
×1.25mm(厚さ))について、平坦度、厚さむら
を測定した結果を表2に示す。The obtained glass (size: 180 × 180
Table 2 shows the results of measuring the flatness and the thickness unevenness for x1.25 mm (thickness).
【0026】[0026]
【表2】 [Table 2]
【0027】なお、ここでいう平坦度とは、表面粗さ、
反りおよびうねりの3つの量で表され、反りとはガラス
板内に1〜2回現れる大きな周期の変形、うねりとは反
りよりも短い周期の凹凸、表面粗さとはうねりよりもさ
らに短い周期の表面の凹凸であり、それらの値は1周期
内の高さの最大値と最小値の差で定義される。厚さむら
とは、ガラス板指定点5点以上で厚さを測定した時の最
大値と最小値の差で定義される。また、ガラス中の不純
物分析を行い、表3の結果を得た。また、気泡を目視検
査したところ、100μm径の気泡が1個観察されたの
みであった。The flatness referred to here is the surface roughness,
It is expressed by three amounts: warpage and undulation. Warpage is a large periodic deformation that appears once or twice in a glass plate, undulation is irregularity with a period shorter than warpage, and surface roughness is a period shorter than undulation. Surface irregularities, whose values are defined by the difference between the maximum and minimum heights within one period. The thickness unevenness is defined as the difference between the maximum value and the minimum value when the thickness is measured at five or more designated points on the glass plate. In addition, the impurities in the glass were analyzed and the results shown in Table 3 were obtained. In addition, when the bubbles were visually inspected, only one bubble having a diameter of 100 μm was observed.
【0028】[0028]
【表3】 [Table 3]
【0029】実施例2 実施例1と同様の手法で調製した平均粒径5μmの非晶
質シリカ粉末(日東化学工業製、商品名シリカエース
A、含有不純物の分析結果は下記表1に示す)に実施例
1と同様の操作を施して、実施例1で用いたアクリル共
重合樹脂が2重量%含有されたプレス成形用の二次粉末
(造粒粒子径:150μm)を得た。この粉末を金型に
充填し、一軸プレス機で500kg/cm2 の圧力を印
加して、200×200×1.5mm(厚さ)の大きさ
の成形体を得た。成形体を目視観察したところ周辺部の
クラックは認められなかった。Example 2 Amorphous silica powder having an average particle size of 5 μm prepared in the same manner as in Example 1 (trade name: silica ace A, manufactured by Nitto Chemical Industry, analysis results of contained impurities are shown in Table 1 below). The same operation as in Example 1 was performed to obtain a secondary powder (granulated particle size: 150 μm) for press molding containing 2% by weight of the acrylic copolymer resin used in Example 1. This powder was filled in a mold, and a pressure of 500 kg / cm 2 was applied with a uniaxial press to obtain a compact having a size of 200 × 200 × 1.5 mm (thickness). When the molded product was visually observed, no cracks were found in the peripheral portion.
【0030】この成形体を大気中、1050℃に10時
間保持して成形体中のアクリル共重合樹脂を脱樹脂し
た。なお、脱樹脂後の成形体密度は1.32g/cm3
であった。The molded body was kept at 1050 ° C. for 10 hours in the atmosphere to remove the acrylic copolymer resin in the molded body. The density of the molded body after the resin removal is 1.32 g / cm 3.
Met.
【0031】次いでこの成形体に実施例1と同じ操作を
施して石英ガラスを得た。得られたガラス(サイズ:1
80×180×1.25mm(厚さ))について、平坦
度、厚さむらを測定した結果を表2に示す。また、ガラ
ス中の不純物分析を行い、表3の結果を得た。Next, this molded body was subjected to the same operations as in Example 1 to obtain quartz glass. Resulting glass (size: 1
Table 2 shows the results of measuring the flatness and the thickness unevenness for 80 × 180 × 1.25 mm (thickness). In addition, the impurities in the glass were analyzed and the results shown in Table 3 were obtained.
【0032】また、気泡を目視検査したところ、150
μm径の気泡が1個観察されたのみであった。Further, when the bubbles were visually inspected, it was found to be 150
Only one bubble having a diameter of μm was observed.
【0033】実施例3 実施例1で調製したプレス成形用の二次粉末を、金型に
充填し、一軸プレス機で500kg/cm2 の圧力を印
加し、金型から成形体を取り出した。さらにこの成形体
をゴム製の袋に装填して、冷間静水圧プレスで2000
kg/cm2 の圧力を印加し、200×200×10.
0mm(厚さ)の大きさの成形体を得た。成形体を目視
観察したところ周辺部のクラックは認められなかった。Example 3 The secondary powder for press molding prepared in Example 1 was filled in a mold and a pressure of 500 kg / cm 2 was applied by a uniaxial press machine, and the molded body was taken out from the mold. Further, this molded body is loaded into a rubber bag, and 2000
A pressure of kg / cm 2 is applied, and 200 × 200 × 10.
A molded body having a size of 0 mm (thickness) was obtained. When the molded product was visually observed, no cracks were found in the peripheral portion.
【0034】この成形体を大気中、1050℃に10時
間保持して成形体中のアクリル共重合樹脂を脱樹脂し
た。なお、脱樹脂後の成形体密度は1.40g/cm3
であった。The molded body was kept at 1050 ° C. for 10 hours in the atmosphere to remove the acrylic copolymer resin in the molded body. The density of the molded body after the resin removal is 1.40 g / cm 3
Met.
【0035】これに実施例1と同じ操作を施して石英ガ
ラスを得た。得られたガラス(サイズ183×183×
8.30mm(厚さ))について、平坦度、厚さむらを
測定した結果を表2に示す。また、ガラス中の不純物分
析を行い、表3の結果を得た。また、気泡を目視検査し
たところ、50μm径の気泡が1個観察されたのみであ
った。The same operation as in Example 1 was carried out to obtain quartz glass. The resulting glass (size 183 x 183 x
Table 2 shows the results of measuring the flatness and the thickness unevenness for 8.30 mm (thickness). In addition, the impurities in the glass were analyzed and the results shown in Table 3 were obtained. Further, when the bubbles were visually inspected, only one bubble having a diameter of 50 μm was observed.
【0036】比較例1 実施例1と同一の非晶質シリカ粉末を水に分散させ、5
0重量%のスラリーを調製した。このスラリーに、ガラ
ス転移点が17℃であるアクリル共重合樹脂水溶液(中
央理化工業製、商品名リカボンドSA−203)を、乾
燥時においてアクリル共重合樹脂がシリカ粉末中に2重
量%含まれるように添加し、十分に撹拌した。撹拌後、
スプレードライヤーを用いて造粒し(平均造粒粒子径:
70μm)、プレス成形用の二次粉末を得た。この粉末
を金型に充填し、一軸プレス機で500kg/cm2 の
圧力を印加して、200×200×1.5mm(厚さ)
の大きさの成形体を得た。この成形体を大気中、105
0℃に10時間保持して成形体中のアクリル共重合樹脂
を脱樹脂した。なお、脱樹脂後の成形体密度は1.15
g/cm3 であった。Comparative Example 1 The same amorphous silica powder as in Example 1 was dispersed in water, and 5
A 0 wt% slurry was prepared. To this slurry, an acrylic copolymer resin aqueous solution having a glass transition point of 17 ° C. (Chuo Rika Kogyo, trade name Ricabond SA-203) was added so that the acrylic copolymer resin was contained in the silica powder in an amount of 2% by weight when dried. And stirred well. After stirring,
Granulate using a spray dryer (average granulated particle size:
70 μm) to obtain a secondary powder for press molding. This powder was filled in a mold, and a pressure of 500 kg / cm 2 was applied by a uniaxial press machine to obtain 200 × 200 × 1.5 mm (thickness).
A molded body having a size of This molded body was exposed to air at 105
It was kept at 0 ° C. for 10 hours to remove the acrylic copolymer resin in the molded body. The molded product density after resin removal is 1.15.
It was g / cm 3 .
【0037】これに実施例1と同じ操作を施して石英ガ
ラスを得た。得られたガラス(サイズ:180×180
×1.25mm(厚さ))について、平坦度、厚さむら
を測定した結果を表2に示す。また、気泡を目視検査し
たところ、100μm径以上の気泡が500個観察され
た。The same operation as in Example 1 was carried out to obtain quartz glass. Obtained glass (size: 180 x 180
Table 2 shows the results of measuring the flatness and the thickness unevenness for x1.25 mm (thickness). In addition, when visually inspecting bubbles, 500 bubbles having a diameter of 100 μm or more were observed.
【0038】比較例2 実施例1と同一の非晶質シリカ粉末を水に分散させ、5
0重量%のスラリーを調製した。このスラリーをスプレ
ードライヤーを用いて造粒し(平均造粒粒子径:70μ
m)、プレス成形用の二次粉末を得た。この粉末を金型
に充填し、一軸プレス機で500kg/cm2 の圧力を
印加して、200×200×1.5mm(厚さ)の大き
さの成形体を得た。得られた成形体の周辺部には細かな
クラックが多数発生していた。この成形体を大気中、1
050℃に10時間保持した。なお、焼成後の成形体密
度は1.12g/cm3 であった。Comparative Example 2 The same amorphous silica powder as in Example 1 was dispersed in water, and
A 0 wt% slurry was prepared. This slurry was granulated using a spray dryer (average granulated particle size: 70μ
m), a secondary powder for press molding was obtained. This powder was filled in a mold, and a pressure of 500 kg / cm 2 was applied with a uniaxial press to obtain a compact having a size of 200 × 200 × 1.5 mm (thickness). Many fine cracks were generated in the peripheral portion of the obtained molded body. This molded body was exposed to the air 1
It was kept at 050 ° C for 10 hours. The compact density after firing was 1.12 g / cm 3 .
【0039】これに実施例1と同じ操作を施して石英ガ
ラスを得た。得られたガラス(サイズ:180×180
×1.25mm(厚さ))について、平坦度、厚さむら
を測定した結果を表2に示す。また、気泡を目視検査し
たところ、100μm径以上の気泡が600個観察され
た。The same operation as in Example 1 was carried out to obtain quartz glass. Obtained glass (size: 180 x 180
Table 2 shows the results of measuring the flatness and the thickness unevenness for x1.25 mm (thickness). In addition, when visually inspecting bubbles, 600 bubbles having a diameter of 100 μm or more were observed.
【0040】実施例4 実施例1及び2で得られたガラス板を各々10枚研磨
し、厚さ1.1mmの基板ガラスを作製した。得られた
基板ガラスは表面粗さ0.005μm、うねり13μ
m、厚さむら50μmであった。比較のため、比較例1
及び比較例2によるガラス板を同様の面精度まで研磨し
たところ、約2倍の研磨工程が必要であった。Example 4 Ten glass plates each obtained in Examples 1 and 2 were polished to produce a substrate glass having a thickness of 1.1 mm. The obtained substrate glass has a surface roughness of 0.005 μm and a waviness of 13 μ.
m and the thickness unevenness was 50 μm. Comparative Example 1 for comparison
And, when the glass plate according to Comparative Example 2 was polished to the same surface accuracy, about twice as many polishing steps were required.
【0041】[0041]
【発明の効果】以上のように本発明の製造方法によれ
ば、工業生産的に有利であるプレス成形法を用いて気泡
量、変形量が極めて少ない透明石英ガラスを作製するこ
とができるという効果が得られる。As described above, according to the manufacturing method of the present invention, it is possible to manufacture a transparent quartz glass having an extremely small amount of bubbles and a small amount of deformation by using the press molding method which is advantageous in industrial production. Is obtained.
【0042】したがって、各種半導体製造用治具の構成
材料、ポリシリコンTFT用やカラーフィルター用など
の液晶表示用基板、フォトマスクなどに利用できる透明
石英ガラスを安価に提供することが可能となる。Therefore, it is possible to inexpensively provide a transparent quartz glass which can be used as a constituent material of various semiconductor manufacturing jigs, a substrate for liquid crystal display such as a polysilicon TFT or a color filter, and a photomask.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 原 幸伸 青森県八戸市江陽三丁目1番109号 日東 化学工業株式会社内 (72)発明者 長田 裕也 茨城県土浦市富士崎1−18−7 (72)発明者 工藤 正行 茨城県稲敷郡江戸崎町月出里447−22 (72)発明者 加茂 賢治 茨城県つくば市天久保2丁目4−17 (72)発明者 岡村 敏彦 茨城県つくば市天久保2丁目4−17 (72)発明者 津久間 孝次 茨城県土浦市富士崎1−18−7−901 (72)発明者 須藤 一 山形県山形市十日町2丁目4−7 (72)発明者 菊地 義一 山形県寒河江市大字寒河江字鶴田43−7 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Yukinobu Hara 3-1-1, Koyo, Hachinohe City, Aomori Nitto Chemical Industry Co., Ltd. (72) Inventor Yuya Nagata 1-18-7 Fujisaki, Tsuchiura City, Ibaraki Prefecture (72) ) Inventor Masayuki Kudo 447-22 Tsukisato, Edozaki-cho, Inashiki-gun, Ibaraki Prefecture (72) Inventor Kenji Kamo 2-17 Amakubo, Tsukuba City, Ibaraki Prefecture 4-17 (72) Toshihiko Okamura 2 Amakubo, Tsukuba City, Ibaraki Prefecture 4-17 (72) Inventor Koji Tsukuma 1-18-7-901 Fujisaki, Tsuchiura City, Ibaraki Prefecture (72) Inventor Kazuichi Sudo 2-7 Tokamachi, Yamagata City Yamagata Prefecture Yoshikazu Kikuchi Sagae Yamagata Prefecture 43-7 Tsuruta, Sagae City
Claims (3)
英ガラスを製造する方法において、平均粒径が0.5〜
10μmの範囲にあり、かつNa、K、Fe、Ti、A
lの各不純物が1ppm以下である非晶質シリカ粉末
に、ガラス転移点が−50℃〜0℃である水溶性アクリ
ル系樹脂を0.1〜10重量%添加し、これを造粒した
造粒粉末を用いて上記プレス成形体を形成することを特
徴とする石英ガラスの製造方法。1. A method for producing quartz glass by firing a press-molded body of silica powder, wherein the average particle size is 0.5 to 0.5.
Within the range of 10 μm, and Na, K, Fe, Ti, A
0.1 to 10% by weight of a water-soluble acrylic resin having a glass transition point of −50 ° C. to 0 ° C. was added to 1 part of an amorphous silica powder having impurities of 1 ppm or less, and granulated by granulation. A method for producing quartz glass, characterized in that the press-formed product is formed using granular powder.
脂を0.1〜10重量%含有する造粒粉末により形成し
た上記プレス成形体を、500〜1300℃の温度で加
熱して含有する水溶性アクリル系樹脂を分解除去した
後、真空雰囲気下1300〜1600℃の温度で加熱焼
結する緻密化処理を行い、ついで窒素ガスあるいはアル
ゴンガスの不活性ガス雰囲気下1700〜1850℃の
温度で加熱溶融後、放冷してガラス化することを特徴と
する石英ガラスの製造方法。2. The water-soluble composition as set forth in claim 1, wherein the press-formed product formed from granulated powder containing 0.1 to 10% by weight of a water-soluble acrylic resin is heated at a temperature of 500 to 1300 ° C. After decomposing and removing the water-soluble acrylic resin, densification treatment is performed by heating and sintering at a temperature of 1300 to 1600 ° C in a vacuum atmosphere, and then heating at a temperature of 1700 to 1850 ° C in an inert gas atmosphere of nitrogen gas or argon gas. A method for producing quartz glass, which comprises melting and then allowing to cool and vitrify.
粉末は、アルカリ金属ケイ酸塩水溶液と酸とを反応させ
て得た非晶質シリカ粉末であることを特徴とする石英ガ
ラスの製造方法。3. The production of quartz glass according to claim 1, wherein the amorphous silica powder is an amorphous silica powder obtained by reacting an aqueous alkali metal silicate solution with an acid. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19745395A JPH0948623A (en) | 1995-08-02 | 1995-08-02 | Quartz glass manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19745395A JPH0948623A (en) | 1995-08-02 | 1995-08-02 | Quartz glass manufacturing method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0948623A true JPH0948623A (en) | 1997-02-18 |
Family
ID=16374769
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19745395A Pending JPH0948623A (en) | 1995-08-02 | 1995-08-02 | Quartz glass manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0948623A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003037807A1 (en) * | 2001-10-30 | 2003-05-08 | Nippon Sheet Glass Co., Ltd. | Method for producing silica glass |
| JP2007070201A (en) * | 2005-09-09 | 2007-03-22 | Yokohama National Univ | Transparent silica sintered body and method for producing the same |
| EP2070883A4 (en) * | 2006-09-11 | 2012-09-12 | Tosoh Corp | QUARTZ GLASS AND PROCESS FOR PRODUCING THE SAME |
| JP2018002526A (en) * | 2016-06-30 | 2018-01-11 | クアーズテック株式会社 | Silica-sintered article |
| JP2020169103A (en) * | 2019-04-01 | 2020-10-15 | 信越化学工業株式会社 | Moldable transparent silica glass composition, transparent silica glass and method for producing the same |
| JP2022052419A (en) * | 2020-09-23 | 2022-04-04 | 三菱ケミカル株式会社 | Production method of transparent glass |
| KR20230064208A (en) * | 2021-11-03 | 2023-05-10 | 목포대학교산학협력단 | Manufacturing Method of Transparent Silica Sintered Body Using Amorphous Silica Nano Powder |
-
1995
- 1995-08-02 JP JP19745395A patent/JPH0948623A/en active Pending
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003037807A1 (en) * | 2001-10-30 | 2003-05-08 | Nippon Sheet Glass Co., Ltd. | Method for producing silica glass |
| GB2398564A (en) * | 2001-10-30 | 2004-08-25 | Nippon Sheet Glass Co Ltd | Method for producing silica glass |
| GB2398564B (en) * | 2001-10-30 | 2005-07-20 | Nippon Sheet Glass Co Ltd | Method for producing silica glass |
| JP2007070201A (en) * | 2005-09-09 | 2007-03-22 | Yokohama National Univ | Transparent silica sintered body and method for producing the same |
| EP2070883A4 (en) * | 2006-09-11 | 2012-09-12 | Tosoh Corp | QUARTZ GLASS AND PROCESS FOR PRODUCING THE SAME |
| JP2018002526A (en) * | 2016-06-30 | 2018-01-11 | クアーズテック株式会社 | Silica-sintered article |
| JP2020169103A (en) * | 2019-04-01 | 2020-10-15 | 信越化学工業株式会社 | Moldable transparent silica glass composition, transparent silica glass and method for producing the same |
| JP2022052419A (en) * | 2020-09-23 | 2022-04-04 | 三菱ケミカル株式会社 | Production method of transparent glass |
| KR20230064208A (en) * | 2021-11-03 | 2023-05-10 | 목포대학교산학협력단 | Manufacturing Method of Transparent Silica Sintered Body Using Amorphous Silica Nano Powder |
| WO2023080306A1 (en) * | 2021-11-03 | 2023-05-11 | 목포대학교산학협력단 | Method for producing transparent silica sintered body using amorphous silica nanopowder |
| JP2024539762A (en) * | 2021-11-03 | 2024-10-30 | モッポ ナショナル ユニバーシティ インダストリー-アカデミア コーオペレイション グループ | Method for manufacturing transparent sintered silica using amorphous silica nanopowder |
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