JPH0520364B2 - - Google Patents

Info

Publication number
JPH0520364B2
JPH0520364B2 JP59189665A JP18966584A JPH0520364B2 JP H0520364 B2 JPH0520364 B2 JP H0520364B2 JP 59189665 A JP59189665 A JP 59189665A JP 18966584 A JP18966584 A JP 18966584A JP H0520364 B2 JPH0520364 B2 JP H0520364B2
Authority
JP
Japan
Prior art keywords
gel
glass
dispersion medium
drying
particles
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
Application number
JP59189665A
Other languages
Japanese (ja)
Other versions
JPS6168329A (en
Inventor
Ichiro Yoshida
Minoru Watanabe
Tsunehisa Kyodo
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.)
Sumitomo Electric Industries Ltd
Original Assignee
Sumitomo Electric Industries 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 Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP59189665A priority Critical patent/JPS6168329A/en
Priority to CA000489925A priority patent/CA1256115A/en
Priority to ZA856889A priority patent/ZA856889B/en
Publication of JPS6168329A publication Critical patent/JPS6168329A/en
Publication of JPH0520364B2 publication Critical patent/JPH0520364B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/12Other methods of shaping glass by liquid-phase reaction processes
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL 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
    • C03C1/00Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
    • C03C1/006Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels to produce glass through wet route

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Glass Melting And Manufacturing (AREA)
  • Manufacture, Treatment Of Glass Fibers (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、ガラスの製造方法に関するものであ
り、詳しくは、金属アルコキシドを原料としてゾ
ルゲル法によりガラスを製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing glass, and more particularly to a method for producing glass by a sol-gel method using a metal alkoxide as a raw material.

〔従来の技術〕[Conventional technology]

現在、光フアイバーのプリフオームを作製する
方法としては、VAD法をはじめとする、Sicl4
を火炎中に通しガラス微粒子をターゲツト上に堆
積させ、得られたガラス多孔質体を焼結しガラス
塊を得る、という方法が主流になつている。これ
は高純度の多孔質ガラスを比較的安価に得られる
優れた方法である。しかしこの方法は気相反応で
あるため、添加物として使える物質がガス化でき
るものに限られる、という欠点があつた。
Currently, methods for producing optical fiber preforms include the VAD method, in which glass particles such as SiCl 4 are passed through a flame and deposited on a target, and the resulting glass porous body is sintered to form a glass lump. The method of obtaining is becoming mainstream. This is an excellent method for obtaining high-purity porous glass at a relatively low cost. However, since this method is a gas phase reaction, it has the disadvantage that the substances that can be used as additives are limited to those that can be gasified.

そこで、近年、この欠点を補う方法として、Si
を主体とした金属アルコキシドを加水分解し、シ
リカゲルあるいは添加元素を含むシリカゲルを
得、該シリカゲルを乾燥させた後無孔化処理等を
行い透明ガラスを得る方法が盛んに研究されてい
る。
Therefore, in recent years, Si
A method of obtaining transparent glass by hydrolyzing a metal alkoxide mainly containing silica gel or silica gel containing additive elements, drying the silica gel, and performing a nonporous treatment, etc. is being actively researched.

一例を挙げれば、シリコンテトラメトキシド等
のSiのアルコキシドを、エタノールと充分に攪拌
混合した後、水を加え更に攪拌して加水分解す
る。この時水にはアンモニア等PH調整剤を加えて
おくことが好ましい。加水分解反応の開始と共に
粒子の折出が始まり、該反応溶液を内面にシリコ
ーンを塗つた容器に移し、乾燥時間を長くできる
ようにアルミ箔等で蓋をして例えば60℃程度の恒
温槽中にてゆつくり乾燥させることにより、ゾル
液のゲル化およびゲルの乾燥を行う。乾燥するに
従つてゲルは収縮し、通常数日を経るとほぼ乾燥
が終了する。このようにして得たゲルを取り出
し、例えば酸素を含むHe雰囲気中にて加熱する
等により無孔化処理を行い、透明ガラス化する方
法がすでに知られている。
For example, after a Si alkoxide such as silicon tetramethoxide is thoroughly stirred and mixed with ethanol, water is added and further stirred to hydrolyze it. At this time, it is preferable to add a pH adjuster such as ammonia to the water. As the hydrolysis reaction begins, particles begin to separate out, and the reaction solution is transferred to a container coated with silicone on the inside, covered with aluminum foil or the like to prolong the drying time, and placed in a constant temperature bath at, for example, 60°C. By slowly drying the sol solution, the sol solution is gelled and the gel is dried. The gel shrinks as it dries, and drying is usually completed after several days. A method is already known in which the gel thus obtained is taken out and subjected to a porosity treatment such as heating in an oxygen-containing He atmosphere to turn it into transparent glass.

このようないわゆるゾルゲル法は、アルコキシ
ドが多くの金属元素について作製できるので、各
種の物質を容易に添加できるという長所がある。
This so-called sol-gel method has the advantage that alkoxides can be prepared for many metal elements, and various substances can be easily added.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、上記の方法においては、ゲルが
焼結の過程で割れ易い、という欠点もある。この
焼結時の割れは、ゲルの細孔径が小さく、焼結時
に、水、アルコールなどが抜ける前に閉気孔が生
ずるためと考えられる。閉気孔が生じた後、これ
をさらに加熱すると、閉気孔内の圧力が上昇し、
割れが生ずる。逆に細孔径が大きく閉気孔ができ
にくいゲルは焼結しやすい。従つて、ガラス塊を
安定して得るには、細孔径の大きいゲルを安定し
て得ることが必要である。
However, the above method also has the disadvantage that the gel tends to crack during the sintering process. This cracking during sintering is thought to be due to the small pore diameter of the gel, which causes closed pores to form before water, alcohol, etc. escape during sintering. After closed pores are formed, when they are further heated, the pressure inside the closed pores increases,
Cracks occur. On the other hand, gels with large pore diameters that are difficult to form closed pores are easily sintered. Therefore, in order to stably obtain a glass lump, it is necessary to stably obtain a gel with a large pore size.

細孔径の制御は、ゲルのかさ密度を制御するこ
とにより可能であるが、従来はゲルのかさ密度の
制御は困難であつた。ゲルのかさ密度は乾燥時の
収縮の度合いで決まるが、その収縮力は、表面張
力によるものであり、収縮の度合いはおおむね、
粒径と分散媒の表面張力で決まる。従来ゲルのか
さ密度制御が困難だつたのは、第一に、構成粒子
の粒径を制御できないからであり、第二に、分散
媒に任意のものを選べないからである。
The pore diameter can be controlled by controlling the bulk density of the gel, but conventionally it has been difficult to control the bulk density of the gel. The bulk density of a gel is determined by the degree of shrinkage during drying, but the shrinkage force is due to surface tension, and the degree of shrinkage is approximately
It is determined by the particle size and the surface tension of the dispersion medium. Conventionally, it has been difficult to control the bulk density of gels, firstly because it is not possible to control the particle size of the constituent particles, and secondly because it is not possible to select an arbitrary dispersion medium.

粒径については、濃度の高い溶液を加水分解し
て粒子を生成すると、色々の粒径のものができて
しまい、粒制の制御が難しい。しかし希薄溶液を
適当な条件で加水分解してゾルを作り、そのゾル
を噴霧乾燥等、生成粒子の粒径制御の容易な方法
で乾燥させることにより、任意の粒径の粒径分布
幅の狭い粒子が得られる。(文献Stober et al
COlloid Interface Science,vol.26 1968
P.62;セラミツクス vol.16 NO.10 1981 P.851)
従来、ゲルを構成する粒子の粒径を制御できなか
つたのは、希薄な溶液を加水分解したのでは、ゾ
ルはできてもゲル化しないので、濃度の高い溶液
を使わざるを得なかつたためである。
Regarding particle size, when particles are generated by hydrolyzing a highly concentrated solution, particles of various sizes are produced, making it difficult to control the particle size. However, by hydrolyzing a dilute solution under appropriate conditions to create a sol, and then drying the sol using a method that makes it easy to control the particle size of the resulting particles, such as spray drying, it is possible to create a narrow particle size distribution for any particle size. particles are obtained. (Reference Stober et al.
COlloid Interface Science, vol. 26 1968
P.62; Ceramics vol.16 NO.10 1981 P.851)
In the past, it was not possible to control the particle size of the particles that make up a gel because if a dilute solution was hydrolyzed, a sol could be formed but it would not gel, so a highly concentrated solution had to be used. be.

分散媒については、従来は水とアルコールの混
合物以外の選択はできなかつた。しかも、加水分
解の条件を一定にするならば、水とアルコールの
比まで決まつてしまう。また、分散媒に多量のア
ルコールが含まれているため、かさ密度の制御の
容易な乾燥法である凍結乾燥法は極めて低い温度
を必要とし実用的でなかつた。
As for the dispersion medium, conventionally it was not possible to select anything other than a mixture of water and alcohol. Moreover, if the conditions for hydrolysis are constant, the ratio of water to alcohol is also fixed. Furthermore, since the dispersion medium contains a large amount of alcohol, the freeze-drying method, which is a drying method that allows easy control of bulk density, requires extremely low temperatures and is not practical.

本発明は、以上詳述した従来のゾルゲル法にお
ける欠点を解消し、かさ密度制御が容易で、大き
な細孔径を持つ易焼結なゲルを安定して得られ、
それによりガラスを製造する方法を提供すること
を目的とする。
The present invention eliminates the drawbacks of the conventional sol-gel method detailed above, allows easy bulk density control, and stably obtains easily sinterable gels with large pore diameters.
It is an object of the present invention to provide a method for manufacturing glass.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは、かかる現状に鑑み、鋭意研究の
結果、粒子を作る工程と、ゲル化・乾燥する工程
を分けることにより、かさ密度の制御を容易に
し、易焼結ゲルを安定して得ることができるによ
り、上記の問題点を解決できることに想到した。
In view of the current situation, the present inventors conducted intensive research and found that by separating the process of making particles and the process of gelling and drying, the bulk density can be easily controlled and an easily sinterable gel can be stably obtained. We have come up with the idea that the above problems can be solved by doing this.

すなわち本発明は、金属アルコキシドを加水分
解してガラスを製造する方法に於いて、加水分解
により得られた粒子を一旦該加水分解の分散媒か
ら分離した後、任意の分散媒と混合し、しかる後
に乾燥せしめ乾燥ゲルを得、無孔化処理を含む処
理を施してなることを特徴とするガラスの製造方
法を提供する。
That is, the present invention provides a method for producing glass by hydrolyzing a metal alkoxide, in which particles obtained by hydrolysis are once separated from a dispersion medium for said hydrolysis, and then mixed with an arbitrary dispersion medium. Provided is a method for producing glass, characterized in that the glass is subsequently dried to obtain a dry gel, which is then subjected to treatment including nonporous treatment.

本発明の特に好ましい実施態様として、上記に
おいて金属アルコキシドがSi,B,Ge,P,Al,
Sb,Ti,Zr,Sn,Y,PbおよびCsからなる群よ
り選ばれる少なくとも1種の元素のアルコキシド
であるガラスの製造方法が挙げられる。
As a particularly preferred embodiment of the present invention, in the above, the metal alkoxide is Si, B, Ge, P, Al,
Examples include a method for producing a glass that is an alkoxide of at least one element selected from the group consisting of Sb, Ti, Zr, Sn, Y, Pb, and Cs.

また本発明の特に好ましい別の実施態様とし
て、前記任意の分散媒に、添加物としてB,Ge,
P,Al,Sb,Ti,Zr,Sn,Y,Sr,Pbおよび
Csからなる群より選ばれる元素又は元素の化合
物の少なくとも1種以上を添加し、それにより製
造されたガラス中に該元素を含有せしめる上記の
ガラスの製造方法をも挙げることができる。
In another particularly preferred embodiment of the present invention, B, Ge,
P, Al, Sb, Ti, Zr, Sn, Y, Sr, Pb and
The above-mentioned method for producing glass may also be mentioned, in which at least one element selected from the group consisting of Cs or a compound of the element is added and the element is contained in the glass produced thereby.

本発明のガラスの製造方法においては、粒子を
つくる工程では、ゲル化に必要な濃度などを考慮
することなく、粒径の制御が容易な条件、例えば
希薄な溶液を加水分解し噴霧乾燥する方法などに
より粒子を作製する。これによつて得られた粒子
を適当な表面張力をもつ任意の液体(分散媒)に
加え、しかる後に徐々に乾燥させる。このように
して、大きな細孔径を持つ易焼結な乾燥ゲルを少
ないバラツキで得ることができる。また、その液
体に水を用いることにより、かさ密度の制御が容
易な凍結乾燥を、−10℃以上の比較的高温でも行
なうことができる。さらに、分散媒の中に適当な
物質を加えておくことにより、その物質をガラス
に添加しガラスの性質を変えることも可能であ
る。例えば分散媒に水を用い、その水の中にホウ
酸を加えておくことにより、製造されたガラスの
屈折率を下げることができる。
In the glass manufacturing method of the present invention, in the step of creating particles, the particle size can be easily controlled without considering the concentration required for gelation, for example, by hydrolyzing a dilute solution and spray drying. Particles are produced by methods such as The particles thus obtained are added to any liquid (dispersion medium) having an appropriate surface tension, and then gradually dried. In this way, an easily sinterable dry gel having a large pore size can be obtained with little variation. Furthermore, by using water as the liquid, freeze-drying, which allows easy control of bulk density, can be performed even at a relatively high temperature of -10°C or higher. Furthermore, by adding an appropriate substance to the dispersion medium, it is possible to add the substance to the glass to change the properties of the glass. For example, by using water as a dispersion medium and adding boric acid to the water, the refractive index of the manufactured glass can be lowered.

本発明の方法に用いられる金属アルコキシドと
しては、例えばSi,B,Ge,P,Al,Sb,Ti,
Zr,Sn,Y,PbおよびCs等のメトキシド、エト
キシド、プロポキシド、ブトキシド等が挙げら
れ、例えば石英系ガラスを製造する場合にはSiの
アルコキシド又はSiのアルコキシドと上記のB以
下のアルコキシドの1種又はそれ以上を混合した
ものを加水分解する。
Examples of metal alkoxides used in the method of the present invention include Si, B, Ge, P, Al, Sb, Ti,
Examples include methoxides, ethoxides, propoxides, butoxides of Zr, Sn, Y, Pb, and Cs, etc. For example, when producing quartz glass, Si alkoxides or Si alkoxides and one of the above alkoxides below B are used. Hydrolyze the mixture of seeds or more.

本発明における金属アルコキシドの加水分解は
通常の方法、すなわちアルコールおよび水を加水
分解反応に好ましい濃度となるように混合するこ
とによればよい。アルコールとしてはメタノー
ル、エタノール、プロパノール、ブタノール等か
ら適宜選択される。
The metal alkoxide in the present invention may be hydrolyzed by a conventional method, that is, by mixing alcohol and water to a concentration suitable for the hydrolysis reaction. The alcohol is appropriately selected from methanol, ethanol, propanol, butanol, and the like.

加水分解終了後、得られた粒子を一旦加水分解
の分散媒、すなわちアルコールと水から分離する
方法は、通常の分離・乾燥手段によればよい。例
えば折出粒子を取後乾燥する、あるいは分散媒
を蒸発させて粉末を得る等であり、また一般に粉
末乾燥手段として用いられる高温中への噴霧、熱
風吹きつけ、真空乾燥、凍結乾燥等の手段を用い
ることができる。
After completion of hydrolysis, the obtained particles can be separated from the dispersion medium for hydrolysis, that is, alcohol and water, by a conventional separation/drying method. For example, the precipitated particles are taken and dried, or the dispersion medium is evaporated to obtain a powder, and the methods generally used for drying the powder include spraying into a high temperature, blowing hot air, vacuum drying, freeze drying, etc. can be used.

このようにして得られた粒子を再び任意の分散
媒と混合するが、この場合はゲル化に好適な濃度
とすることができる。
The particles thus obtained are again mixed with an arbitrary dispersion medium, but in this case the concentration can be adjusted to a concentration suitable for gelation.

任意の分散媒としては、例えばFe,Cu,Co等
の光学特性に有害な不純物の含有が少なければい
ずれの液体でもよく、例えば水、アルコール類、
アセトン等が挙げられるが、これらに限定される
ものではない。
The optional dispersion medium may be any liquid as long as it contains only a small amount of impurities harmful to optical properties such as Fe, Cu, Co, etc., such as water, alcohols, etc.
Examples include, but are not limited to, acetone.

また上記の任意の分散媒中には、添加物として
B,Ge,P,Al,Sb,Ti,Zr,Sn,Y,Sr,
PbおよびCsからなる群より選ばれる元素又は化
合物の少なくとも1種以上を加えることにより、
製造されたガラス中に該元素を含有せしめること
ができる。これらの元素は例えば塩、アルコキシ
ド等を水溶液、鉱酸溶液等として添加することが
できる。このような元素の添加により製品ガラス
の屈折率を変化させることができる。
In addition, the above arbitrary dispersion medium contains additives such as B, Ge, P, Al, Sb, Ti, Zr, Sn, Y, Sr,
By adding at least one element or compound selected from the group consisting of Pb and Cs,
The element can be included in the manufactured glass. These elements can be added as salts, alkoxides, etc. in the form of aqueous solutions, mineral acid solutions, etc. By adding such elements, the refractive index of the product glass can be changed.

以上により生成したゲルを乾燥して乾燥ゲルを
得るが、急激に乾燥するとゲルが収縮して歪みで
割れる場合があるので、ゆつくり乾燥させるか、
凍結乾燥するとこのような割れを避けることがで
きる。
Dry the gel produced as described above to obtain a dry gel, but if it dries too quickly, the gel may shrink and crack due to distortion, so dry it slowly or
Freeze-drying can avoid this type of cracking.

前記の如く、任意の分散媒として水を用いれ
ば、かさ密度制御が容易な点で有利な凍結乾燥
を、−10℃以上という比較的高温でも行うことが
できる。
As mentioned above, if water is used as an optional dispersion medium, freeze-drying, which is advantageous in terms of easy bulk density control, can be performed even at a relatively high temperature of -10°C or higher.

次いで乾燥ゲルの無孔化処理を行うが、例えば
好適な雰囲気中にて、成分の融点より低い温度で
焼結する方法が挙げられ、例えばシリカを主成分
とする乾燥ゲルについては、He雰囲気中にて
1200〜1500℃程度の温度で焼結を行う。
Next, the dried gel is made non-porous, for example, by sintering it in a suitable atmosphere at a temperature lower than the melting point of the components. At
Sintering is performed at a temperature of about 1200-1500℃.

〔実施例〕〔Example〕

以下実施例により本発明のガラスの製造方法を
具体的に説明する。
EXAMPLES The method for manufacturing glass of the present invention will be specifically explained below with reference to Examples.

実施例 1 エタノール3モル中に、実験直前に再蒸留した
テトラメチルシリケート1/8モルを加え、マグネ
チツクスターラで充分に混合した。その後この中
に、エタノール2モルに飽和アンモニア水10mlを
加え混合したものを加え激しくかきまぜた。その
後、緩やかにかきまぜながら3時間室温に保つた
後、800℃の高温中に噴霧し、乾燥した。こうし
て得られた粉末の粒子径は、0.1ミクロン程度で
バラツキは少なかつた。
Example 1 1/8 mole of tetramethyl silicate redistilled immediately before the experiment was added to 3 moles of ethanol and thoroughly mixed with a magnetic stirrer. Thereafter, a mixture of 2 moles of ethanol and 10 ml of saturated aqueous ammonia was added and stirred vigorously. Thereafter, the mixture was kept at room temperature for 3 hours with gentle stirring, and then sprayed in a high temperature of 800°C and dried. The particle size of the powder thus obtained was approximately 0.1 micron with little variation.

この粉末1gをエタノール50mlに加え超音波で
分散させた後、湯煎で加熱し濃縮した。流動性が
高くなつたところで加熱をやめ、内面にシリコー
ンを塗つた、径12mm、長さ105mmの試験管5本に
移し、アルミ箔でかるくフタをして60℃の恒温槽
に入れた。このまま5日間乾燥し、径8mm程度、
長さ14mm程度の乾燥シリカゲルを得た。この乾燥
ゲルのかさ密度は、平均0.52g/cm3標準偏差0.01
g/cm3であり、これをHe雰囲気中、1300℃で焼
結し、5つの乾燥ゲルすべてについてクラツクの
無い透明ガラスを得た。
1 g of this powder was added to 50 ml of ethanol, dispersed using ultrasonic waves, and concentrated by heating in a water bath. When fluidity became high, heating was stopped and the tubes were transferred to five test tubes with a diameter of 12 mm and a length of 105 mm, each coated with silicone on the inside, capped loosely with aluminum foil, and placed in a constant temperature bath at 60°C. Leave to dry for 5 days, and the diameter will be approximately 8 mm.
Dry silica gel with a length of about 14 mm was obtained. The bulk density of this dry gel is an average of 0.52 g/cm 3 and a standard deviation of 0.01.
g/cm 3 and was sintered at 1300° C. in a He atmosphere to obtain crack-free transparent glass for all five dried gels.

実施例 2 実施例1で作つた粉末1gを0.1%ホウ酸水溶
液50mlに加え超音波で分散させた後、加熱し濃縮
した。流動性が高くなつたところで加熱をやめ前
記と同一の試験管5本に移し、アルミ箔でかるく
フタをして60℃の恒温槽に入れた。このまま2日
間乾燥し、長さが15mm程度になつたところで取り
だし、冷凍車(−20℃)でゆつくりと冷却し凍結
後、氷、塩化ナトリウム寒剤で冷却しながら凍結
したまま真空乾燥し乾燥ゲルを得た。この乾燥ゲ
ルの平均かさ密度は、0.49g/cm3標準偏差は、
0.01g/cm3であり、これをHe雰囲気中、1300℃
で焼結し、5つの乾燥ゲルすべてについてクラツ
クの無い透明ガラスを得た。
Example 2 1 g of the powder prepared in Example 1 was added to 50 ml of a 0.1% boric acid aqueous solution, dispersed using ultrasonic waves, and then heated and concentrated. When fluidity became high, heating was stopped and the tubes were transferred to the same five test tubes as above, capped loosely with aluminum foil, and placed in a constant temperature bath at 60°C. Let it dry for 2 days, then take it out when it has a length of about 15 mm, slowly cool it in a freezer car (-20℃), freeze it, and then vacuum-dry it while cooling it with ice and sodium chloride cryogen to dry the gel. I got it. The average bulk density of this dry gel is 0.49 g/cm 3 The standard deviation is:
0.01g/ cm3 , and this was heated at 1300℃ in a He atmosphere.
A crack-free transparent glass was obtained for all five dried gels.

比較例 シリコンテトラメトキシド1/16モルと、エタノ
ール1/4モルを、マグネチツクスターラで混合、
その中に13%アンモニア水3滴を加えた水1/2モ
ルを加えさらに混合した後、前記と同一の試験管
5本に移しアルミ箔で軽くフタをし、60℃恒温槽
に入れた。7日後には、ほぼ完全に乾燥してお
り、径は6mm程度、長さは11mm程度であつた。こ
の乾燥ゲルのかさ密度は平均0.78g/cm3標準偏差
は0.06g/cm3であつた。この乾燥ゲルを、He雰
囲気中1300℃で焼結したところ、5つの内、3つ
には割れが生じ極めて小さな透明ガラスしか得ら
れなかつた。
Comparative example: Mix 1/16 mole of silicon tetramethoxide and 1/4 mole of ethanol using a magnetic stirrer.
After adding 1/2 mole of water to which 3 drops of 13% ammonia water had been added and further mixing, the mixture was transferred to the same five test tubes as above, capped loosely with aluminum foil, and placed in a constant temperature bath at 60°C. After 7 days, it was almost completely dry, with a diameter of about 6 mm and a length of about 11 mm. The average bulk density of this dry gel was 0.78 g/cm 3 and the standard deviation was 0.06 g/cm 3 . When this dried gel was sintered at 1300°C in a He atmosphere, three of the five pieces were cracked and only extremely small pieces of transparent glass were obtained.

〔発明の効果〕〔Effect of the invention〕

以上の実施例、比較例の結果から明らかなよう
に、本発明の方法は従来法によるよりかさ密度の
小さい乾燥ゲルを、粒径分布幅を小さく得ること
ができ、該乾燥ゲルは易焼結である。
As is clear from the results of the above Examples and Comparative Examples, the method of the present invention can produce dry gels with a lower bulk density and a narrower particle size distribution width than those obtained by the conventional method, and the dry gels are easily sinterable. It is.

また加水分解により生じた粒子を一旦分離後、
任意の分散媒中にてゲル化するので、任意の分散
媒として水を用いれば、従来法の多量にアルコー
ルを含有する場合に比べて、比較的高温にて凍結
乾燥できるため実用上有利である。
In addition, once the particles generated by hydrolysis are separated,
Since it gels in any dispersion medium, if water is used as any dispersion medium, it is practically advantageous because it can be freeze-dried at a relatively high temperature compared to the conventional method that contains a large amount of alcohol. .

したがつて本発明によれば、従来、制御が困難
であつた、ゲルを構成する粒子の粒径を容易に制
御することができ、また乾燥ゲルのかさ密度を容
易に制御することができ、その結果、割れ無しに
焼結することのできる乾燥ゲルを容易に得ること
のできる優れた効果を有する。
Therefore, according to the present invention, it is possible to easily control the particle size of the particles constituting the gel, which has been difficult to control in the past, and the bulk density of the dried gel can be easily controlled. As a result, it has the excellent effect of easily obtaining a dry gel that can be sintered without cracking.

Claims (1)

【特許請求の範囲】 1 金属アルコキシドを加水分解してガラスを製
造する方法に於いて、加水分解により得られた粒
子を一旦該加水分解の分散媒から分離した後、任
意の分散媒と混合し、しかる後に乾燥せしめ乾燥
ゲルを得、無孔化処理を含む処理を施してなるこ
とを特徴とするガラスの製造方法。 2 金属アルコキシドがSi,B,Ge,P,Al,
Sb,Ti,Zr,Sn,Y,PbおよびCsからなる群よ
り選ばれる少なくとも1種の元素のアルコキシド
である特許請求の範囲第1項に記載のガラスの製
造方法。 3 任意の分散媒に、添加物としてB,Ge,P,
Al,Sb,Ti,Zr,Sn,Y,Sr,PbおよびCsか
らなる群より選ばれる元素又は元素の化合物の少
なくとも1種以上を添加し、それにより製造され
たガラス中に該元素を含有せしめる特許請求の範
囲第1項記載のガラスの製造方法。
[Claims] 1. In a method for producing glass by hydrolyzing a metal alkoxide, particles obtained by hydrolysis are once separated from a dispersion medium for said hydrolysis, and then mixed with an arbitrary dispersion medium. , and then drying to obtain a dry gel, which is then subjected to a treatment including a nonporous treatment. 2 Metal alkoxide is Si, B, Ge, P, Al,
The method for producing glass according to claim 1, wherein the glass is an alkoxide of at least one element selected from the group consisting of Sb, Ti, Zr, Sn, Y, Pb and Cs. 3 Add B, Ge, P, as additives to any dispersion medium.
Adding at least one element or compound of an element selected from the group consisting of Al, Sb, Ti, Zr, Sn, Y, Sr, Pb, and Cs, thereby causing the glass produced to contain the element. A method for producing glass according to claim 1.
JP59189665A 1984-09-12 1984-09-12 Glass manufacturing method Granted JPS6168329A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP59189665A JPS6168329A (en) 1984-09-12 1984-09-12 Glass manufacturing method
CA000489925A CA1256115A (en) 1984-09-12 1985-09-03 Platinum complexes
ZA856889A ZA856889B (en) 1984-09-12 1985-09-09 Platinum complexes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59189665A JPS6168329A (en) 1984-09-12 1984-09-12 Glass manufacturing method

Publications (2)

Publication Number Publication Date
JPS6168329A JPS6168329A (en) 1986-04-08
JPH0520364B2 true JPH0520364B2 (en) 1993-03-19

Family

ID=16245123

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59189665A Granted JPS6168329A (en) 1984-09-12 1984-09-12 Glass manufacturing method

Country Status (2)

Country Link
JP (1) JPS6168329A (en)
ZA (1) ZA856889B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63277527A (en) * 1987-05-11 1988-11-15 Ube Nitto Kasei Kk Production of very small spherical silica glass
JP2768442B2 (en) * 1989-04-17 1998-06-25 正行 野上 Manufacturing method of semiconductor-containing glass

Also Published As

Publication number Publication date
JPS6168329A (en) 1986-04-08
ZA856889B (en) 1986-05-28

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