JPS59121125A - Production unit of floating plate glass - Google Patents

Production unit of floating plate glass

Info

Publication number
JPS59121125A
JPS59121125A JP22853182A JP22853182A JPS59121125A JP S59121125 A JPS59121125 A JP S59121125A JP 22853182 A JP22853182 A JP 22853182A JP 22853182 A JP22853182 A JP 22853182A JP S59121125 A JPS59121125 A JP S59121125A
Authority
JP
Japan
Prior art keywords
molten metal
barrier
glass
bath
molten
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
JP22853182A
Other languages
Japanese (ja)
Inventor
Katsuji Fujimoto
藤本 勝司
Chiharu Hisamoto
久本 千春
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.)
Nippon Sheet Glass Co Ltd
Original Assignee
Nippon Sheet Glass 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 Nippon Sheet Glass Co Ltd filed Critical Nippon Sheet Glass Co Ltd
Priority to JP22853182A priority Critical patent/JPS59121125A/en
Publication of JPS59121125A publication Critical patent/JPS59121125A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B18/00Shaping glass in contact with the surface of a liquid
    • C03B18/02Forming sheets
    • C03B18/18Controlling or regulating the temperature of the float bath; Composition or purification of the float bath

Abstract

PURPOSE:A production unit of floating plate glass for lessening strain of molten glass ribbon made to flow on a metallic bath, suppressing variability in thickness, by making a fence along the side wall of the molten metallic bath, using it as a return path for the molten metal. CONSTITUTION:The molten metal bath 10 is filled with the molten metal 11 such as tin, etc., and a molten glass material is made to flow on the molten metal 11. As it is drawn by rollers, it is pulled up, the beltlike glass ribbon 12 is transferred on the molten metal 11, to give plate glass having given thickness and width. In this device, the fence 13 is set along the side wall 10a in the bath 10, to form the return path 16 for the molten metal 11. The cooled molten metal 11 is made to flow downward with the transfer of the glass ribbon 12, and allowed to flow along the return path 16 into the main flow 11a. If necessary, the return path 16 is equipped with a heater to heat the cooled molten metal 11. Consequently, the cooled molten metal 11 is not brought into contact with the glass ribbon 12 to give high-quality plate glass.

Description

【発明の詳細な説明】 本発明はスズなどの溶融金属上に溶融したガラスを流し
出して一定厚の板ガラスを製造するフロート式の板ガラ
ス製造装置に関する0 従来から板ガラスを製造する装置として、フロ−ト式の
板ガラス製造装置が用いられている。この製造装置は第
1図に示すように、スズなどの溶融金属1を満した浴2
上に溶融したガラス素地を流し出してガラスリボン3と
し、このガラスリボン3を浴2の途中に配設したヒータ
或いはクーラーで成形に適した温度にコントロールする
とともに、ガラスリボン3の端部にトップロール等を噛
み込ませて側方に引張りつつ、ガラスリボン3を浴2下
流端から所定の速度で引張ることで、適正な厚みと巾を
もっだ板ガラスを得るようにしだものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a float-type sheet glass manufacturing apparatus for manufacturing sheet glass of a constant thickness by pouring molten glass onto a molten metal such as tin. A type of plate glass manufacturing equipment is used. As shown in FIG. 1, this manufacturing apparatus consists of a bath 2 filled with molten metal 1 such as tin.
A molten glass base material is poured onto the bath 2 to form a glass ribbon 3, and a heater or cooler installed in the middle of the bath 2 controls the temperature of the glass ribbon 3 to a temperature suitable for molding. By pulling the glass ribbon 3 from the downstream end of the bath 2 at a predetermined speed while pulling it laterally using a roll or the like, a plate glass having an appropriate thickness and width is obtained.

そして斯かるフロート式の製造装置にあっては、ガラス
リボン3が溶融金属1上を移動するため、この移動につ
れて溶融金属1も上流から下流に向って移動する。そし
て浴2の下流端は堰止められているので、浴2の下流端
まできた溶融金属1は第1図に示すように、ガラスリボ
ン3と浴の側壁2aとの間、或いはガラスリボン3の下
方を通って上流に戻る。
In such a float-type manufacturing apparatus, the glass ribbon 3 moves over the molten metal 1, and as the glass ribbon 3 moves, the molten metal 1 also moves from upstream to downstream. Since the downstream end of the bath 2 is dammed, the molten metal 1 that has reached the downstream end of the bath 2 is deposited between the glass ribbon 3 and the side wall 2a of the bath, or between the glass ribbon 3 and the side wall 2a of the glass ribbon 3, as shown in FIG. Pass below and return upstream.

しかしながら、浴2の下流端まで移動した溶融金属はか
なり冷却されておシ、この冷却した溶融金属が上流に戻
る途中で高温のガラスリボン3と接触すると、ガラスリ
ボン3が歪み、伸び品質が悪くなる。特にこの悪影響は
ガラスリボン3と浴の側壁2aとの間を通る冷たい溶融
金属に原因する場合が多い。
However, the molten metal that has moved to the downstream end of the bath 2 has been cooled considerably, and when this cooled molten metal comes into contact with the hot glass ribbon 3 on its way back upstream, the glass ribbon 3 is distorted and its elongation quality is poor. Become. In particular, this negative effect is often caused by the cold molten metal passing between the glass ribbon 3 and the side wall 2a of the bath.

本発明は上記従来の問題を改善すべく成したものであっ
て、ガラスリボンの移動につれて浴の下流端まで移動し
て冷たくなった溶融金属が、上流まで戻る際に、その途
中でガラスリボンに接触することがないようにし、もっ
て歪が少なく伸び品質の良好な板状ガラスを製造し得る
フロート式の板ガラス製造装置を提供することを目的と
する。
The present invention has been made to improve the above-mentioned conventional problem.As the glass ribbon moves, the molten metal moves to the downstream end of the bath and becomes cold. It is an object of the present invention to provide a float-type sheet glass manufacturing apparatus that can prevent contact and thereby manufacture sheet glass with little distortion and good elongation quality.

上記目的を達成するため第1発明は、フロート式の板ガ
ラス製造装置における金属浴内部に金属浴の側壁に沿っ
た障壁を設け、この障壁の上流端と下流端を開口せしめ
、障壁と側壁との間に溶融金属の還流路を形成したこと
を要旨とし、また第2発明は上記第1発明の還流路内に
ヒータを配設したことを要旨とし、更に第3発明は上記
第1発明の上流端に設けた開口よシも若干上流側に堰を
設け、還流路から戻ってきた冷えた溶融金属を所定位置
において本流に流入せしめるようにしたことを要旨とし
ている。
In order to achieve the above object, the first invention provides a barrier along the side wall of the metal bath inside the metal bath in a float-type plate glass manufacturing apparatus, and opens the upstream and downstream ends of the barrier to connect the barrier and the side wall. The gist of the invention is that a reflux path for molten metal is formed between the molten metal, the gist of the second invention is that a heater is disposed in the reflux path of the first invention, and the third invention is a reflux path of the molten metal formed upstream of the first invention. The gist is that a weir is installed slightly upstream of the opening at the end, allowing the cooled molten metal returning from the reflux path to flow into the main stream at a predetermined position.

以下に各発明の実施例を添付図面に基づいて説明する。Embodiments of each invention will be described below based on the accompanying drawings.

第2図及び第3図は第1発−明の実施例を示し、第2図
は板ガラス製造装置の平面図、第3図は同装置の要部縦
断面図である0 10は耐火物によって構成される溶融金属浴であシ、こ
の浴10は千面略矩形状を力し下流部において両側壁1
0a、10a  の幅が狭くなっているOそして、浴1
0内にはスズなどの溶融金属11が満されておりこの溶
融金属11上に溶融したガラス素地を流し出し、且つこ
のガラス素地を浴10の下流端近傍に配設したローラで
引張りつつ引上げることで、溶融金属11上を帯状のガ
ラスリボン12が図中右方向へ移動するようにしている
2 and 3 show an embodiment of the first invention, FIG. 2 is a plan view of a sheet glass manufacturing apparatus, and FIG. 3 is a vertical sectional view of the main part of the apparatus. This bath 10 has a substantially rectangular shape with 1,000 sides, and both side walls 1 are formed in the downstream part.
0a, 10a width is narrower and bath 1
The bath 10 is filled with molten metal 11 such as tin, and a molten glass base is poured onto this molten metal 11, and this glass base is pulled up while being pulled by a roller disposed near the downstream end of the bath 10. This causes the band-shaped glass ribbon 12 to move on the molten metal 11 to the right in the figure.

なおこの場合、浴10の途中にはヒータ或いはクーラー
を設けることでガラスリボン12の温度コントロールを
行ない、またトップロールによってガラスリボン12の
巾が縮まないようにし、所定の厚さ及び巾を有する板ガ
ラスを得るようにしている。
In this case, the temperature of the glass ribbon 12 is controlled by providing a heater or cooler in the middle of the bath 10, and the width of the glass ribbon 12 is prevented from shrinking by the top roll, and a plate glass having a predetermined thickness and width is used. I'm trying to get it.

茸だ、上記浴10の内部には側壁10a、10aに沿っ
た障壁13.13を形成している。この障壁13は下端
部が浴10の敷上面に固定され、その材質は浴10のカ
ーボン又は敷煉瓦と同様の耐火物としている。そして、
障壁13の上流端及び下流端には浴10内の溶融金属1
1の本流11aと連通する開口14.15を形成してい
る。而して障壁13と側壁10aとの間には溶融金属の
還流路16が形成される0 ここで、上記障壁13の下流端と浴10の後端壁10b
との距離はあまり近接せしめると酸化錫除去の効果を減
少し、またあまシ離すと冷却された溶融金属が障壁内側
を還流する虞れがあるだめ、上記距離は1m〜3m程度
とするのが好ましい。
The interior of the mushroom bath 10 forms barriers 13.13 along the side walls 10a, 10a. The lower end of this barrier 13 is fixed to the flooring surface of the bath 10, and its material is carbon or a refractory material similar to the flooring bricks of the bath 10. and,
Molten metal 1 in bath 10 is located at the upstream and downstream ends of barrier 13.
Openings 14 and 15 are formed that communicate with the main stream 11a of No. 1. Thus, a reflux path 16 for molten metal is formed between the barrier 13 and the side wall 10a. Here, the downstream end of the barrier 13 and the rear end wall 10b of the bath 10 are
If the distance is too close to the barrier, the effectiveness of tin oxide removal will be reduced, and if it is too far apart, there is a risk that the cooled molten metal may flow back inside the barrier. preferable.

また、障壁13の上流部における還流路16の巾Aは障
壁13とガラスリボン12の側端との距離Bよりも大き
く、更に障壁13の下流部における還流路16の巾Cも
障壁13とガラスリボン12側端との距離りよシも大き
いこと、即ち、A≧B1C≧Dなる関係にあることが、
障壁13内側を還流することを防ぐ意味で好ましい。
Further, the width A of the return flow path 16 at the upstream portion of the barrier 13 is larger than the distance B between the barrier 13 and the side edge of the glass ribbon 12, and the width C of the return flow path 16 at the downstream portion of the barrier 13 is also larger than the distance B between the barrier 13 and the side edge of the glass ribbon 12. The distance from the side edge of the ribbon 12 is also large, that is, the relationship A≧B1C≧D exists.
This is preferable in that it prevents reflux inside the barrier 13.

また、障壁13の上流端位置は、溶融金属の本流11a
の温度700℃〜750 ’C七なっている部分とする
ことが好ましい。このようにすることで、冷えだ溶融金
属が本流11aに流れ込んでも大きな影響はない。
Further, the upstream end position of the barrier 13 is the main flow 11a of the molten metal.
It is preferable that the temperature be 700° C. to 750° C. By doing so, even if the cooled molten metal flows into the main flow 11a, there is no major influence.

更に図示例にあっては障壁13の上端部が溶融金属面S
かも突出しだものを宗しだが、障壁の上端が溶融金属面
よシも下方にあるようにしてもよい。この場合溶融金属
面Sからあま多犬きく障壁13を沈めると障壁の効果が
なくなるので、溶融金属面Sと障壁13上端との距離は
溶融金属11の深さHの1/3以下又は20m以下のう
ちいずれが小さい方を選択することが好ましい。
Furthermore, in the illustrated example, the upper end of the barrier 13 is the molten metal surface S.
Although it is preferable to have a protruding barrier, the upper end of the barrier may be below the molten metal surface. In this case, if the barrier 13 is sunk too far from the molten metal surface S, the barrier effect will be lost, so the distance between the molten metal surface S and the top of the barrier 13 is 1/3 or less of the depth H of the molten metal 11 or 20 m or less. It is preferable to select the smaller one among them.

上記した構成とすることで、ガラスリボン12の移動に
伴って流下し且つ冷却された溶融金属は還流路16内を
通って所定温度、つまシ冷えた溶融金属が合流してもさ
程影響のない本流11a部分に流入する。
With the above configuration, the molten metal that has flowed down and been cooled as the glass ribbon 12 moves passes through the reflux path 16 to a predetermined temperature, and even if the molten metal that has cooled down joins it, it will not be affected much. It flows into the main stream 11a where there is no water.

第4図及び第5図は第2発明の実施例を示すものであり
、第4図は第2図と同様の平面図、第5図は要部の縦断
面図である。
4 and 5 show an embodiment of the second invention, FIG. 4 being a plan view similar to FIG. 2, and FIG. 5 being a longitudinal sectional view of the main part.

この実施例の前記実施例と異なる点は、還流路16内に
ヒータ17を配設した点にある。このヒータ17は第5
図に示すように浴10の側壁10a内側に中空状の密閉
カーボンボックス18を取付け、このカーボンボックス
18内に電源とつながルヒータ線19を収納している。
This embodiment differs from the previous embodiments in that a heater 17 is disposed within the reflux path 16. This heater 17 is the fifth
As shown in the figure, a hollow sealed carbon box 18 is attached to the inside of the side wall 10a of the bath 10, and a heater wire 19 connected to a power source is housed within this carbon box 18.

尚、ヒータ17はこれに限らず、金属浴上面から加熱す
るヒータを用いてもよい。
Note that the heater 17 is not limited to this, and a heater that heats the metal bath from the upper surface may be used.

このように構成すれば、障壁13の上流端の位置につい
て考慮する必要がなく、任意の位置に開口14を設定す
ることができ、且つ溶融金属の本流11a の温度と等
しい温度になるまで冷えた溶融金属を加熱して合流せし
めることができるので、ガラスリボン12の歪等の心配
が全くない。
With this configuration, there is no need to consider the position of the upstream end of the barrier 13, the opening 14 can be set at any position, and the molten metal is cooled to a temperature equal to the temperature of the main stream 11a. Since the molten metal can be heated and merged, there is no need to worry about distortion of the glass ribbon 12.

まだ、第6図は第3発明の実施例を示すものであわ、こ
の実施例にあっては障壁13の上流端よシも更に若干上
流側の側壁10aから内方に向ってカーボン又は耐火物
製の堰20を設けている。
Still, FIG. 6 shows an embodiment of the third invention, and in this embodiment, the upstream end of the barrier 13 is also covered with carbon or refractory material from the side wall 10a slightly upstream. A weir 20 made of

このように堰20を設けると、還流路16の開口14か
ら流出した冷えた溶融金属は堰20に遮えぎられて上流
には流れず、そのまま本流11aに合流する。したがっ
て堰20を本流の温度が例えば700℃である箇所に設
けるとすれば、溶融金属11の本流11aの温度と、冷
えだ溶融金属の温度との差が大きくならないうちに戻す
ことができるので、温度差に原因する悪影響つまりガラ
スリボンの歪を可及的に小さくできる。
When the weir 20 is provided in this manner, the cooled molten metal flowing out from the opening 14 of the return flow path 16 is blocked by the weir 20 and does not flow upstream, but instead joins the main stream 11a. Therefore, if the weir 20 is installed at a location where the temperature of the main stream is, for example, 700°C, the temperature of the main stream 11a of the molten metal 11 and the temperature of the cold molten metal can be returned before the difference in temperature becomes large. Adverse effects caused by temperature differences, that is, distortion of the glass ribbon, can be minimized as much as possible.

以上説明したように第1発明によれば溶融金属浴の側壁
に沿って障壁を形成し、この障壁と側壁との間を還流路
として、冷えた溶融金属がガラスリボンに接触せずに上
流側に戻るようにしたので、ガラスリボンの歪を小さく
でき、且つ厚み変動を抑えることもでき、伸び品質を大
巾に向上することができる等多大の利点を有する。
As explained above, according to the first invention, a barrier is formed along the side wall of the molten metal bath, and the space between the barrier and the side wall is used as a reflux path, so that the cooled molten metal can flow toward the upstream side without contacting the glass ribbon. This has many advantages, such as reducing distortion of the glass ribbon, suppressing thickness fluctuations, and greatly improving elongation quality.

【図面の簡単な説明】[Brief explanation of drawings]

図面は従来例及び本発明の実施例を示すものであり、第
1図は従来のフロート式板ガラス製造装置の平面図、第
2図は第1発明に係るフロート式板ガラス製造装置の平
面図、第3図は同製造装置の要部縦断面図、第4図は第
2発明に係るフロート式板ガラス製造装置の平面図、第
5図は第2発明に係る装置の要部縦断面図、第6図は第
3発明に係るフロート式板ガラス製造装置の平面図であ
るO 尚、図面中10は金属浴、10aは側壁、11は溶融金
属、11aは本流、12はリボン状ガラス、13は障壁
、14.15は開口、16は還流路、17はヒータ、2
0は堰である。 特許出願人  日本板硝子株式会社
The drawings show a conventional example and an embodiment of the present invention, and FIG. 1 is a plan view of a conventional float type plate glass manufacturing apparatus, and FIG. 2 is a plan view of a float type plate glass manufacturing apparatus according to the first invention. 3 is a longitudinal cross-sectional view of a main part of the same manufacturing apparatus, FIG. 4 is a plan view of a float type sheet glass manufacturing apparatus according to the second invention, FIG. 5 is a longitudinal cross-sectional view of a main part of the apparatus according to the second invention, and FIG. The figure is a plan view of a float type plate glass manufacturing apparatus according to the third invention. 14.15 is an opening, 16 is a reflux path, 17 is a heater, 2
0 is a weir. Patent applicant Nippon Sheet Glass Co., Ltd.

Claims (1)

【特許請求の範囲】 し出してリボン状とし、このリボン状ガラスを引張シつ
つ引上げることで所定厚の板ガラスを得るようにしたフ
ロート式製造装置において、上記金属浴内部に金属浴の
側壁に沿った障壁を設け、この障壁の上流側端部及び下
流側端部を溶融金属の本流に開口せしめて障壁と側壁と
の間に溶融金属の還流路を形成したことを特徴とするフ
ロート式板ガラス製造装置。 (2)溶融金属を満した金属浴上に溶融ガラスを流し出
してリボン状とし、このリボン状ガラスを引張シつつ引
上げることで所定厚の板ガラスを得るようにしたフロー
ト式製造装置において、上記金属浴内部に金属浴の側壁
に沿った障壁を設け、この障壁の上流側端部及び下流側
端部を溶融金属の本流に開口せしめ−て障壁と側壁との
間に溶融金属の還流路を形成し、この還流路にヒータを
配設したことを特徴とするフロート式板ガラス製造装置
。 (3)溶融金属を満した金属浴上に溶融ガラスを流し出
してリボン状とし、このリボン状ガラスを引張シつつ引
上げることで所定厚の板ガラスを得るようにしたフロー
ト式製造装置において、上記金属浴内部に金属浴の側壁
に沿った障壁を設け、この障壁の上流側端部及び下流側
端部を溶融金属の本流に開口せしめて障壁と側壁との間
に溶融金属の還流路を形成し、更に上記障壁の上流側端
部に設けた開口よりも上流側に還流路から戻ってきた溶
融金属を本流に流入せしめるための堰を設けたことを特
徴とするフロート式板ガラス製造装置。
[Claims] In a float-type manufacturing apparatus in which a plate glass of a predetermined thickness is obtained by drawing out glass into a ribbon shape and pulling up the ribbon-shaped glass under tension, A float-type plate glass characterized in that a barrier is provided along the line, and the upstream and downstream ends of the barrier are opened to the main stream of molten metal to form a return path for molten metal between the barrier and the side wall. Manufacturing equipment. (2) In a float-type manufacturing apparatus, the molten glass is poured onto a metal bath filled with molten metal to form a ribbon, and the ribbon-shaped glass is pulled up under tension to obtain a plate glass of a predetermined thickness. A barrier is provided inside the metal bath along the side wall of the metal bath, and the upstream and downstream ends of this barrier are opened to the main flow of the molten metal to form a return path for the molten metal between the barrier and the side wall. 1. A float type sheet glass manufacturing apparatus characterized in that a heater is provided in the reflux path. (3) In a float-type manufacturing apparatus, the molten glass is poured onto a metal bath filled with molten metal to form a ribbon, and the ribbon-shaped glass is pulled up under tension to obtain a plate glass of a predetermined thickness. A barrier is provided inside the metal bath along the side wall of the metal bath, and the upstream and downstream ends of this barrier are opened to the main flow of the molten metal to form a reflux path for the molten metal between the barrier and the side wall. A float type plate glass manufacturing apparatus further comprising: a weir for allowing the molten metal returned from the reflux path to flow into the main flow upstream of the opening provided at the upstream end of the barrier.
JP22853182A 1982-12-27 1982-12-27 Production unit of floating plate glass Pending JPS59121125A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22853182A JPS59121125A (en) 1982-12-27 1982-12-27 Production unit of floating plate glass

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22853182A JPS59121125A (en) 1982-12-27 1982-12-27 Production unit of floating plate glass

Publications (1)

Publication Number Publication Date
JPS59121125A true JPS59121125A (en) 1984-07-13

Family

ID=16877864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22853182A Pending JPS59121125A (en) 1982-12-27 1982-12-27 Production unit of floating plate glass

Country Status (1)

Country Link
JP (1) JPS59121125A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010189259A (en) * 2009-02-13 2010-09-02 Lg Chem Ltd Apparatus for manufacturing float glass
JP2010189260A (en) * 2009-02-13 2010-09-02 Lg Chem Ltd Apparatus for manufacturing float glass
JP2010189258A (en) * 2009-02-13 2010-09-02 Lg Chem Ltd Apparatus for manufacturing float glass
WO2020153310A1 (en) * 2019-01-21 2020-07-30 Agc株式会社 Sheet glass production apparatus and sheet glass production method

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010189259A (en) * 2009-02-13 2010-09-02 Lg Chem Ltd Apparatus for manufacturing float glass
JP2010189260A (en) * 2009-02-13 2010-09-02 Lg Chem Ltd Apparatus for manufacturing float glass
JP2010189258A (en) * 2009-02-13 2010-09-02 Lg Chem Ltd Apparatus for manufacturing float glass
TWI391338B (en) * 2009-02-13 2013-04-01 Lg Chemical Ltd Apparatus for manufacturing float glass
TWI391337B (en) * 2009-02-13 2013-04-01 Lg Chemical Ltd Apparatus for manufacturing float glass
TWI391347B (en) * 2009-02-13 2013-04-01 Lg Chemical Ltd Apparatus for manufacturing float glass
KR101422161B1 (en) * 2009-02-13 2014-07-24 주식회사 엘지화학 Apparatus for manufacturing glass
WO2020153310A1 (en) * 2019-01-21 2020-07-30 Agc株式会社 Sheet glass production apparatus and sheet glass production method

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