JPS62226822A - Production of glass - Google Patents

Production of glass

Info

Publication number
JPS62226822A
JPS62226822A JP6898586A JP6898586A JPS62226822A JP S62226822 A JPS62226822 A JP S62226822A JP 6898586 A JP6898586 A JP 6898586A JP 6898586 A JP6898586 A JP 6898586A JP S62226822 A JPS62226822 A JP S62226822A
Authority
JP
Japan
Prior art keywords
bulk
dryer
atmosphere
drying
sol
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
Application number
JP6898586A
Other languages
Japanese (ja)
Inventor
Akihiko Yajima
矢島 明彦
Osamu Horibata
堀端 修
Seiji Sakai
清治 酒井
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.)
Seiko Epson Corp
Original Assignee
Seiko Epson Corp
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 Seiko Epson Corp filed Critical Seiko Epson Corp
Priority to JP6898586A priority Critical patent/JPS62226822A/en
Publication of JPS62226822A publication Critical patent/JPS62226822A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/12Other methods of shaping glass by liquid-phase reaction processes

Landscapes

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

Abstract

PURPOSE:To prevent uneven distribution of temp. in the inside of a dryer and to produce glass free from bulk cracking due to wind by separating bulk obtained by gelation from the atmosphere in the chamber of the dryer and forcedly convecting the outside atmosphere. CONSTITUTION:Bulk is obtained by using at least metallic oxide, metallic alkoxide and an acid catalyst and allowing the mixture to gel by a sol-gel process. The obtained bulk is separated from the atmosphere in the inside of a dryer in some degree and introduced into the dryer and dried while forcedly convecting the outside atmosphere.

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。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for manufacturing glass.

〔発明の概要〕[Summary of the invention]

ゾル−ゲル法によるガラスの製造方法とは、金属アルコ
キシドやシリク微粒子t−原料とし、ゲル化させて得ら
れたバルクを乾燥させ、ドライゲルとし焼結するもので
ある。
The method for producing glass by the sol-gel method involves using metal alkoxide or silic fine particles as a t-raw material, gelling the resulting bulk, drying it, and sintering it to form a dry gel.

本発明は、ゾル−ゲル法によるガラス製造の、バルク乾
燥工程において、バルクと乾燥器室内の雰囲気t−ある
程度隔離し、外側雰囲気を強制対流させることにより、
風によるバルクの割れを防止し、また乾燥器内の温度不
均一分布を防止し、乾燥歩留シを向上させるようにした
ものである。
In the bulk drying process of glass production using the sol-gel method, the present invention isolates the bulk from the atmosphere inside the dryer chamber to some extent and causes the outside atmosphere to undergo forced convection.
This prevents the bulk from cracking due to wind, prevents uneven temperature distribution within the dryer, and improves drying yield.

〔従来の技術〕[Conventional technology]

従来のゾル−ゲル法によるガラスの製造方法は、(I¥
!開昭58−257577 )の様に、バルクと乾燥器
室内の雰囲気を隔離せず、また外側雰囲気の強制対流も
行なわなかった。
The conventional method for manufacturing glass using the sol-gel method is (I¥
! Unlike in 1982-257577), the bulk and the atmosphere inside the dryer chamber were not isolated, nor was forced convection of the outside atmosphere performed.

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

しかし、前述の従来技術では、乾燥器室内に、温度不均
一分布が存在し、それt失くすために雰囲気を対流する
と風によりバルクの割れが生じ、歩v7Iシの安定化は
望めないという問題点を有する。
However, with the above-mentioned conventional technology, there is a problem that uneven temperature distribution exists in the dryer chamber, and when the atmosphere is convected to eliminate this, the bulk cracks occur due to the wind, and it is not possible to stabilize the dryer. Has a point.

そこで本発明はこのような問題点全解決するもので、そ
の目的とするところは乾燥歩留りの向上、安定化を提供
するところにある。
The present invention is intended to solve all of these problems, and its purpose is to improve and stabilize the drying yield.

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

上記問題点を解決するために、本発明のガラスの製造方
法は、ゲル化によ、り得られたバルクを乾燥する際に、
バルクと外側の雰囲気を隔離し、外側雰囲気全強制対流
させて乾燥することを#徴とする。
In order to solve the above problems, the method for producing glass of the present invention includes: when drying the bulk obtained by gelation,
The characteristics are that the bulk and the outside atmosphere are separated and the entire outside atmosphere is dried by forced convection.

〔作用〕[Effect]

ゾル−ゲル法により遺られたバルクは乾燥により大きく
収縮する。しかもその乾燥度合により収縮率は異なって
おり、部分的に不均一な乾燥が行なわれるとバルクに歪
ができ、応力に耐えられず割れることになる。また、同
じことは、バルクの表面と内側についても言える。すな
わち、バルクの表面の乾燥速度と内側から表面への拡散
が均衡を保っていないと表面と内部に歪による応力を生
じやはり割れる事になる。したがって乾燥工程において
は極力温度、風等による不均一な乾燥を排除し、安定な
乾燥条件ft提供することが重要となってくる。
The bulk left behind by the sol-gel process shrinks significantly upon drying. Furthermore, the shrinkage rate differs depending on the degree of drying, and if the drying is partially uneven, the bulk will become distorted and will not be able to withstand stress and will crack. The same can also be said about the surface and inside of the bulk. In other words, if the drying rate of the surface of the bulk and the diffusion from the inside to the surface are not balanced, stress due to strain will be generated on the surface and inside, which will also result in cracking. Therefore, in the drying process, it is important to eliminate uneven drying due to temperature, wind, etc. as much as possible and to provide stable drying conditions.

したがって本発明の上記の構成によれば乾燥器内温度不
均一分布の解消および風による割れの防止ができ、乾燥
歩留りの向上、安定化が可能である。
Therefore, according to the above configuration of the present invention, it is possible to eliminate uneven temperature distribution within the dryer and prevent cracking due to wind, and it is possible to improve and stabilize the drying yield.

〔実施例〕〔Example〕

テトラエチルオルソシリケート17.9tと101規定
塩酸2&5Lおよび微粉末シリカ10Kfi混合し、激
しく攪拌しながら加水分解を行ない、白色のゾルを得た
。このゾル溶液を25℃〜30℃に保ちながら28 K
Hzの超音波t−4時間印加しながら攪拌した。さらに
得られたゾル溶fLヲ遠心分離器にと45.1500G
を10分間印加し、粗粒を分離した後、うわずみ液を1
μmのフィルターで濾過して粗粒の無い均一なゾル溶液
を得た。
17.9 tons of tetraethyl orthosilicate, 2 and 5 L of 101 N hydrochloric acid, and 10 Kfi of finely powdered silica were mixed and hydrolyzed with vigorous stirring to obtain a white sol. This sol solution was heated at 28 K while keeping it at 25°C to 30°C.
The mixture was stirred while applying ultrasonic waves of Hz for t-4 hours. Furthermore, the obtained sol solution fL was transferred to a centrifuge at 45.1500G.
was applied for 10 minutes to separate coarse particles, and then 1
A uniform sol solution free of coarse particles was obtained by filtration through a μm filter.

得られたゾル溶液を01規定アンモニア水溶液でP)i
 i 4.2に調整してからポリプロピレン製容器(3
4備X 26cmX 10譚)に厚み1m仕込んだ。
P)i of the obtained sol solution with 01 N ammonia aqueous solution
i Adjust to 4.2 and then put in a polypropylene container (3
4 x 26 cm x 10 pieces) with a thickness of 1 m.

2日間密閉状態で放置したところゲル化し、線収縮率で
5X程収縮した。続いて開口率14%の穴のめいたふた
く替え、乾燥器に入れた。乾燥器内でポリプロピレン製
容器Tl−10個単位とし、そのまわシラポリプロピレ
ン裏のカーテンで囲んで乾燥器内の温風吹き出し口から
の温風が直接ポリプロピレン裏の容器に6&らないよう
にした。
When it was left in a sealed state for 2 days, it gelled and shrunk by about 5X in terms of linear shrinkage. Next, the lid with holes with an open area ratio of 14% was replaced, and the lid was placed in a dryer. Inside the dryer, polypropylene containers T1 were placed in units of 10 units, and the containers were surrounded by a curtain behind the polypropylene to prevent hot air from the hot air outlet in the dryer from directly entering the containers behind the polypropylene.

乾燥器内の温度″f:60℃に保ち、15日間この状喪
で乾燥上行ない約22cfRX17.5鋸X(L5.の
ドライゲルを得た。更にこのドライゲルを80℃の乾j
菓器に入れ2日間乾燥し、水分を十分除去した。
The temperature inside the dryer was maintained at 60°C, and drying was carried out in this state for 15 days to obtain a dry gel of approximately 22cfRX17.5cm (L5.).Furthermore, this dry gel was dried at 80°C.
It was placed in a confectionery container and dried for 2 days to sufficiently remove moisture.

得られた乾燥ゲル’kl囲気炉に仕込み昇温速度30℃
/時で200℃まで昇温し、200℃に保持し脱水を行
なった。再び昇温速度50 C/時で450℃まで昇温
し、450℃に6時間保持し、有機残基の酸化除去を行
なった。次に炉内をヘリウム雰囲気にかえ、再び昇温速
度60℃/時で700℃に昇温し、この温度で2時間保
持し友。同様にして昇温速度60℃/時で800℃、9
00℃、1000℃、1150℃の各温度で2時間保持
するプログラムにより1250℃まで昇温し九。
The resulting dry gel was placed in an air oven and heated at a rate of 30°C.
The temperature was raised to 200°C at a rate of 200°C/hour, and the temperature was maintained at 200°C for dehydration. The temperature was again raised to 450° C. at a heating rate of 50 C/hour and held at 450° C. for 6 hours to remove organic residues by oxidation. Next, the inside of the furnace was changed to a helium atmosphere, and the temperature was again raised to 700°C at a rate of 60°C/hour, and maintained at this temperature for 2 hours. Similarly, the heating rate was 60°C/hour to 800°C, 9
The temperature was raised to 1250°C using a program of holding each temperature for 2 hours at 00°C, 1000°C, and 1150°C.

得られた乳白色の不透明ガラス状物体を大気炉にいれ、
昇温速度200℃で1550℃まで昇温し、2時間この
温度に保持した後、自然放冷したところ大きさが1(L
5.XI五53X14−の石英ガラスが得られた。
The resulting milky white opaque glassy substance was placed in an atmospheric furnace.
The temperature was raised to 1550°C at a heating rate of 200°C, held at this temperature for 2 hours, and then allowed to cool naturally.
5. A quartz glass of XI553X14- was obtained.

〔発明の効果〕〔Effect of the invention〕

本発明は、以上説明したように乾燥工程においてバルク
と乾燥器室内の雰囲気を隔離し、外側雰囲気全強制対流
することにより、乾燥器内の温度不均一分布を防止し、
風によるバルクの割れ全防止し、乾燥歩留りを向上させ
るようにしたものである。
As explained above, the present invention prevents uneven temperature distribution within the dryer by isolating the bulk and the atmosphere inside the dryer chamber in the drying process and causing forced convection of the entire outside atmosphere.
This completely prevents bulk cracking due to wind and improves drying yield.

以上that's all

Claims (1)

【特許請求の範囲】[Claims] 少なくとも微粒子を用いるゾル−ゲル法によるグラスの
製造方法において、ゲル化により得られたバルクを乾燥
する際に、バルクと乾燥器室内の雰囲気をある程度隔離
し、外側雰囲気を強制対流させてバルクを乾燥すること
を特徴とするガラスの製造方法。
In a glass manufacturing method using at least a sol-gel method using fine particles, when drying the bulk obtained by gelation, the bulk is isolated to some extent from the atmosphere inside the dryer chamber, and the outside atmosphere is forced to circulate to dry the bulk. A method of manufacturing glass characterized by:
JP6898586A 1986-03-27 1986-03-27 Production of glass Pending JPS62226822A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6898586A JPS62226822A (en) 1986-03-27 1986-03-27 Production of glass

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6898586A JPS62226822A (en) 1986-03-27 1986-03-27 Production of glass

Publications (1)

Publication Number Publication Date
JPS62226822A true JPS62226822A (en) 1987-10-05

Family

ID=13389463

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6898586A Pending JPS62226822A (en) 1986-03-27 1986-03-27 Production of glass

Country Status (1)

Country Link
JP (1) JPS62226822A (en)

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