JPH02188430A - Production of glass - Google Patents
Production of glassInfo
- Publication number
- JPH02188430A JPH02188430A JP598689A JP598689A JPH02188430A JP H02188430 A JPH02188430 A JP H02188430A JP 598689 A JP598689 A JP 598689A JP 598689 A JP598689 A JP 598689A JP H02188430 A JPH02188430 A JP H02188430A
- Authority
- JP
- Japan
- Prior art keywords
- glass
- molten glass
- stirring
- viscosity
- bubbles
- 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
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/225—Refining
- C03B5/2252—Refining under reduced pressure, e.g. with vacuum refiners
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/18—Stirring devices; Homogenisation
- C03B5/187—Stirring devices; Homogenisation with moving elements
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Compositions (AREA)
Abstract
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、ガラスの製造法に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a method for manufacturing glass.
(従来の技術)
清澄を終了した溶融ガラスを撹拌すると、溶融ガラス中
に気泡が発生し、この気泡が製品に混入する。そのため
高度に気泡の除去されたガラスの製造法としては、溶融
ガラスを撹拌して均質化し、この均質化した溶融ガラス
を高温度に長時間保持してガラスに発生した気泡を浮上
させ除去し、これを所定形状に成形する方法が採用され
ている。(Prior Art) When molten glass that has been refined is stirred, air bubbles are generated in the molten glass, and these air bubbles are mixed into the product. Therefore, the manufacturing method for glass with a high degree of air bubble removal is to stir molten glass to homogenize it, hold the homogenized molten glass at high temperature for a long time, and float and remove air bubbles generated in the glass. A method of molding this into a predetermined shape is adopted.
しかしながら、かかる方法においては気泡を除去する過
程で溶融ガラスが不均質となり、気泡は高度に除去され
ているものの均質性の低下した製品が得られるという課
題があった。However, this method has a problem in that the molten glass becomes non-uniform during the process of removing air bubbles, and although the air bubbles are removed to a high degree, a product with reduced homogeneity is obtained.
(発明の解決しようとする課題)
本発明は従来の技術が有していた上記課題を解消し、高
度に気泡が除去され、かつ均質性に優れたガラスの製造
法の提供を目的とする。(Problems to be Solved by the Invention) It is an object of the present invention to solve the above-mentioned problems that the conventional techniques had, and to provide a method for producing glass in which air bubbles are removed to a high degree and the glass is excellent in homogeneity.
(課題を解決するための手段)
本発明は溶融ガラスを減圧下で脱泡し、該脱泡した溶融
ガラスを撹拌して均質化し、該均質化したガラスを所定
形状に成形するガラスの製造法を提供するものである。(Means for Solving the Problems) The present invention is a method for producing glass, which includes defoaming molten glass under reduced pressure, stirring the defoamed molten glass to homogenize it, and molding the homogenized glass into a predetermined shape. It provides:
本発明におけるガラスの組成としては特に限定されるも
のではないが、清澄域即ち粘度が10”〜101ボイズ
になるときの温度が比較的高温度であり、かつ均質性の
要求されるものに特に適している。かかるガラスとして
は、アルカリ金属の含有の少ない低アルカリガラス、ア
ルカリ金属を含有しない無アルカリガラス、SrO,B
aOを比較的多量に含有するカラーブラウン管のパネル
用ガラス等が例示される。Although the composition of the glass in the present invention is not particularly limited, it is particularly suitable for glass in which the temperature in the clear region, that is, when the viscosity reaches 10" to 101 voids, is relatively high and homogeneity is required. Such glasses include low-alkali glass containing little alkali metal, alkali-free glass containing no alkali metal, SrO, B
Examples include glass for panels of color cathode ray tubes containing a relatively large amount of aO.
本発明において、溶融ガラスを減圧下で脱泡するに当っ
ては、溶融ガラスの粘度が10’〜10”ボイスである
ときに行うことが好ましい。In the present invention, defoaming of the molten glass under reduced pressure is preferably carried out when the viscosity of the molten glass is 10' to 10'' voice.
粘度が103ボイスより大きい場合、脱泡に長時間を要
したり、脱泡が実質的に行われなくなるので好ましくな
い、一方、粘度が10”ボイズより小さい場合は、脱泡
は短時間で行うことが可能であるが、加える熱エネルギ
ーが多大となり、省エネルギー上、好ましくない。If the viscosity is greater than 103 Boise, it is undesirable because it takes a long time for defoaming or defoaming is not substantially performed. On the other hand, if the viscosity is less than 10" Boise, defoaming is performed in a short time. Although this is possible, it requires a large amount of heat energy, which is not preferable in terms of energy conservation.
また、その際の圧力としては、高過ぎると脱泡効果が少
なくなり、低過ぎると減圧にするための装置が複雑にな
り、減圧を得るためのエネルギーが極めて大きくなるの
で、いずれも好ましくない。好ましい圧力はl/20〜
1/3気圧の範囲である。Furthermore, as for the pressure at that time, if the pressure is too high, the defoaming effect will be reduced, and if it is too low, the equipment for reducing the pressure will be complicated and the energy required to obtain the reduced pressure will be extremely large, so neither is preferable. The preferred pressure is l/20~
It is in the range of 1/3 atmospheric pressure.
更に、かかる減圧下に保持する時間としては、30分〜
90分間が好ましい。この保持時間が30分間より短い
場合は脱泡効果が充分に得られず、90分間を越えると
ガラスの生産性が低下するのでいずれも好ましくない。Furthermore, the time for holding under such reduced pressure is 30 minutes to
90 minutes is preferred. If this holding time is shorter than 30 minutes, a sufficient defoaming effect cannot be obtained, and if it exceeds 90 minutes, glass productivity decreases, which is not preferable.
かくして脱泡されたガラスは撹拌され均質化される。か
かる撹拌は通常大気圧下で行われるが、減圧下で行うこ
ともできる。The defoamed glass is stirred and homogenized. Such stirring is usually carried out under atmospheric pressure, but can also be carried out under reduced pressure.
かかる撹拌はガラスの粘度がIQl、 S〜103・6
ボイズの範囲にあるものについて行うことが好ましい、
その理由は次の通りである。即ち、ガラスの粘度が10
”・5ボイズより大きい場合は均質化されたガラスを得
るのに、時間がかかるので好ましくない、またガラスの
粘度10”°6ボイズより小さい場合は、熱エネルギー
を多く消費するので好ましくない。より望ましくはガラ
スの粘度が101〜103Sボイズの範囲にある間に撹
拌することである。Such stirring is performed when the viscosity of the glass is IQl, S ~ 103.6
It is preferable to do this for things within the Boise range.
The reason is as follows. That is, the viscosity of glass is 10
If the viscosity of the glass is larger than 10"°.6 voids, it is undesirable because it takes time to obtain a homogenized glass. If the viscosity of the glass is smaller than 10"°6 voids, it is undesirable because a lot of thermal energy is consumed. More preferably, stirring is carried out while the viscosity of the glass is within the range of 101 to 103 S voids.
撹拌に当っては、通常使用されているものが広範囲に使
用される。例えば、回転軸に対し放射状に羽根を設け、
これを溶融ガラス中に浸漬し回転することにより溶融ガ
ラスを撹拌するタイプのもの、複数の凸起部材を設け、
この凸起部材を溶融ガラス中に浸漬してこれを往復運動
させることにより溶融ガラスを撹拌するタイプのものが
例示される。For stirring, a wide range of commonly used materials can be used. For example, by providing blades radially to the rotating shaft,
A type that stirs the molten glass by immersing it in the molten glass and rotating it, with a plurality of protruding members,
An example is a type in which the convex member is immersed in the molten glass and moved back and forth to stir the molten glass.
攪拌は強過ぎると次の欠点を生じ易くなるので好ましく
ない。即ち、キャビテーション現象により、羽根のまわ
りに新たに泡が発生しやすのなる。又、ガラス素地上方
より、空気が巻き込む恐れを生じる。Too strong stirring is not preferred because it tends to cause the following drawbacks. That is, new bubbles are likely to be generated around the blades due to the cavitation phenomenon. Additionally, there is a risk that air may be drawn in from above the glass substrate.
撹拌か弱過ぎると均質化が不充分となるので好ましくな
い。Too weak stirring is not preferred because homogenization will be insufficient.
好ましくは前者のタイプにおいては羽根の周速度が0.
5〜1.5 rmI分の範囲である。一方、後者のタイ
プにおいては凸起部材の速度が1〜2m/分の範囲にな
るようにすることが好ましい。Preferably, in the former type, the circumferential speed of the blade is 0.
It ranges from 5 to 1.5 rmI minutes. On the other hand, in the latter type, it is preferable that the speed of the convex member is in the range of 1 to 2 m/min.
また、撹拌時間としては10〜30分間が好ましく、撹
拌時間が10分間より短い場合は均質化が不充分となり
易(なるので好ましくなく、30分間より長くなるとガ
ラスの生産性が低下するので好ましくない。In addition, the stirring time is preferably 10 to 30 minutes; if the stirring time is shorter than 10 minutes, homogenization tends to be insufficient (so it is undesirable), and if it is longer than 30 minutes, the productivity of glass decreases, which is undesirable. .
か(して、均質化された溶融ガラスは次いで板状等の目
的とする形状に成形される。(Thus, the homogenized molten glass is then formed into a desired shape, such as a plate shape.
本発明においては、上記各工程を連続溶融タンクの如く
ガラスの流動径路に設け、ガラスが流動する過程で上記
処理を行ってもよ(、ルツボの如く溶融したガラスを減
圧脱泡し、次いで撹拌する工程を繰返すいわゆるバッチ
処理で行うこともできる。In the present invention, each of the above steps may be provided in the flow path of the glass, such as in a continuous melting tank, and the above treatments may be performed while the glass is flowing. It can also be carried out by so-called batch processing in which the steps are repeated.
(実施例)
表に記載の目標組成となるように調整したバッチ又はカ
レットをsoo g秤量し、白金坩堝に入れ、加熱し溶
融ガラスを得た。加熱に当ってはガラスの粘度が約10
”ボイスになる温度で、砂利、泡が消失するまで保持し
た。(Example) A batch or cullet prepared to have the target composition shown in the table was weighed, placed in a platinum crucible, and heated to obtain molten glass. When heating, the viscosity of glass is approximately 10
``I held it at the temperature where it became voiced until the gravel and bubbles disappeared.
次いでこの溶融ガラスを減圧下に保持し、脱泡した。こ
の際のガラスの粘度、圧力、保持時間は同表に記載した
。This molten glass was then held under reduced pressure to defoam. The viscosity, pressure, and holding time of the glass at this time are listed in the same table.
次いでこのガラスを粘度約lOsボイズにし撹拌した。The glass was then brought to a viscosity of about 1Os and stirred.
撹拌方法としては、20X 50mm四方の羽根を有す
るスターラをガラス中に挿入し、lO〜20r、 po
mの回転速度で10〜30分間行った。As for the stirring method, a stirrer with 20×50 mm square blades was inserted into the glass, and
It was carried out for 10 to 30 minutes at a rotation speed of m.
次いで、このガラスを板状に成形した後、気泡を測定し
た。その結果を同表に併記した。同表において、減圧処
理なしは比較例であり、同一条件で溶融し清澄したガラ
スを減圧処理を行なうことなく同一条件で撹拌したガラ
スを板状に成形し、それについて測定したものである。Next, this glass was formed into a plate shape, and then the air bubbles were measured. The results are also listed in the same table. In the same table, the case without vacuum treatment is a comparative example, in which glass was melted and clarified under the same conditions and stirred under the same conditions without vacuum treatment, then formed into a plate shape, and the glass was measured.
同図より明らかなように清澄により、−旦消滅した気泡
が撹拌により発生するが、本発明によればかかる気泡の
発生が極めて少な−い。As is clear from the figure, bubbles that had previously disappeared due to fining are generated by stirring, but according to the present invention, the generation of such bubbles is extremely small.
また、図には省略したが、本発明によるガラスは肉眼に
より脈理がほとんど見出されないが、撹拌を行なわなか
ったものは脈理が多量に見出される。Further, although not shown in the figure, in the glass according to the present invention, almost no striae can be seen with the naked eye, but in the glass that was not stirred, a large amount of striae was found.
(発明の効果)
本発明によれば均質性に優れ泡のないガラスが得られ歩
留りが向上する。(Effects of the Invention) According to the present invention, a glass with excellent homogeneity and no bubbles can be obtained, and the yield can be improved.
特に均質性、気泡点で厳しい品質の要求される、例えば
カラーブラウン管のパネルガラス等には特に上記効果が
大きい。The above-mentioned effect is particularly great for panel glass for color cathode ray tubes, etc., which require strict quality in terms of homogeneity and bubble point.
また、撹拌を従来のものより粘度の高い領域で行なえる
ので撹拌の工程管理が容易となり熱エネルギーの節約に
もなる。Furthermore, since stirring can be performed in a region with higher viscosity than in conventional methods, the stirring process can be easily controlled and thermal energy can be saved.
Claims (1)
撹拌して均質化し、該均質化したガラスを所定形状に成
形するガラスの製造法。A method for manufacturing glass, which includes defoaming molten glass under reduced pressure, stirring and homogenizing the defoamed molten glass, and molding the homogenized glass into a predetermined shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP598689A JPH02188430A (en) | 1989-01-17 | 1989-01-17 | Production of glass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP598689A JPH02188430A (en) | 1989-01-17 | 1989-01-17 | Production of glass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02188430A true JPH02188430A (en) | 1990-07-24 |
Family
ID=11626125
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP598689A Pending JPH02188430A (en) | 1989-01-17 | 1989-01-17 | Production of glass |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02188430A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0775671A1 (en) | 1995-11-21 | 1997-05-28 | Asahi Glass Company Ltd. | Method and apparatus for refining molten glass under reduced pressure |
| EP1044929A1 (en) * | 1999-04-13 | 2000-10-18 | Asahi Glass Company Ltd. | Vacuum degassing method for molten glass flow |
| WO2002098810A1 (en) * | 2001-06-06 | 2002-12-12 | Schott Glas | Vacuum refining method |
| WO2003106361A1 (en) * | 2002-06-13 | 2003-12-24 | Schott Glas | Method for vacuum refining alkali-borosilicate glass melts |
| DE10304973A1 (en) * | 2003-02-06 | 2004-08-26 | Schott Glas | Control unit for melting and/or refining glass has control devices which form at least two regulating circuits |
-
1989
- 1989-01-17 JP JP598689A patent/JPH02188430A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0775671A1 (en) | 1995-11-21 | 1997-05-28 | Asahi Glass Company Ltd. | Method and apparatus for refining molten glass under reduced pressure |
| EP1044929A1 (en) * | 1999-04-13 | 2000-10-18 | Asahi Glass Company Ltd. | Vacuum degassing method for molten glass flow |
| US6536238B2 (en) | 1999-04-13 | 2003-03-25 | Asahi Glass Company, Limited | Vacuum degassing method for molten glass flow |
| EP1655268A2 (en) | 1999-04-13 | 2006-05-10 | Asahi Glass Company, Limited | Vacuum degassing method for molton glass flow |
| EP1655268A3 (en) * | 1999-04-13 | 2006-06-07 | Asahi Glass Company, Limited | Vacuum degassing method for molton glass flow |
| KR100667643B1 (en) * | 1999-04-13 | 2007-01-12 | 아사히 가라스 가부시키가이샤 | Vacuum Defoaming Method of Molten Glass Flow |
| WO2002098810A1 (en) * | 2001-06-06 | 2002-12-12 | Schott Glas | Vacuum refining method |
| WO2003106361A1 (en) * | 2002-06-13 | 2003-12-24 | Schott Glas | Method for vacuum refining alkali-borosilicate glass melts |
| DE10304973A1 (en) * | 2003-02-06 | 2004-08-26 | Schott Glas | Control unit for melting and/or refining glass has control devices which form at least two regulating circuits |
| DE10304973B4 (en) * | 2003-02-06 | 2006-08-17 | Schott Ag | Devices, control device and control method for the refining of glass |
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