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JPH0359015B2 - - Google Patents
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JPH0359015B2 - - Google Patents

Info

Publication number
JPH0359015B2
JPH0359015B2 JP28573886A JP28573886A JPH0359015B2 JP H0359015 B2 JPH0359015 B2 JP H0359015B2 JP 28573886 A JP28573886 A JP 28573886A JP 28573886 A JP28573886 A JP 28573886A JP H0359015 B2 JPH0359015 B2 JP H0359015B2
Authority
JP
Japan
Prior art keywords
glass
platinum
mold
tank
outflow
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
Application number
JP28573886A
Other languages
Japanese (ja)
Other versions
JPS63139020A (en
Inventor
Ikuaki Unno
Kunio Takeuchi
Takao Igari
Akimi Kitayama
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.)
Hoya Corp
Original Assignee
Hoya 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 Hoya Corp filed Critical Hoya Corp
Priority to JP28573886A priority Critical patent/JPS63139020A/en
Publication of JPS63139020A publication Critical patent/JPS63139020A/en
Publication of JPH0359015B2 publication Critical patent/JPH0359015B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B17/00Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
    • C03B17/06Forming glass sheets
    • C03B17/068Means for providing the drawing force, e.g. traction or draw rollers
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B17/00Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
    • C03B17/06Forming glass sheets
    • C03B17/061Forming glass sheets by lateral drawing or extrusion

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Glass Compositions (AREA)
  • Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ガラスを板状に成形するために用い
る成形用型に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a mold used for molding glass into a plate shape.

〔従来の技術〕[Conventional technology]

従来、板ガラスの成形方法としては、ロール法
がある。これは、タンクから溶融ガラスを連続的
に流し出し、それを2個のロールの間に通して板
状にするもので、代表的な方式に、自動車用窓ガ
ラスの製造を目的としたフオード(Ford)法が
ある。この方法では、フオアハースの先端(リツ
プ)から数ftの幅でガラスを流出し、これが大小
2個で対をなすロールによつて一定の厚さの板に
成形され、引き続き長い徐冷窯に送り込まれる
(成瀬省「ガラス工学」p161〜162共立出版、昭
和44年)。
Conventionally, there is a roll method as a method for forming plate glass. This method involves continuously pouring molten glass from a tank and passing it between two rolls to form a plate. Ford) law. In this method, glass flows out from the tip (lip) of the floor hearth in a width of several feet , is formed into a plate of a certain thickness by a pair of large and small rolls, and is then passed through a long slow-cooling kiln. Sent (Naruse ``Glass Engineering'' p161-162 Kyoritsu Publishing, 1962).

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

上述したフオード法は、自動車用窓ガラスのよ
うな、内部品質をあまり問題とせず、かつその単
位時間当りの引上量も大きい場合に適した製法で
ある。
The above-mentioned Ford method is a manufacturing method suitable for cases where internal quality is not a major concern and the amount of pulling up per unit time is large, such as for automobile window glass.

これに対し、光学的に高い内部均質度が要求さ
れる光学グレードの板ガラスの製造には、一般に
溶解槽として白金もしくは白金合金製の槽または
それらによつてライニングされた槽が使用され、
窓ガラス用の溶解炉等とは溶解炉の構造が大きく
異なり、炉端部に溶融ガラスを最終的に均一化す
るための撹拌機構を備えた作業槽を有する。溶融
ガラスは、この最終槽である作業槽の底部に取り
付けられた白金パイプより流し出されるが、この
流出ガラス量、つまり引上量は、光学ガラス溶解
炉においてはきわめて少なく、通常数百キログラ
ム〜数トン/日である。このように引上量の少な
い小径の流出パイプから流出する溶融ガラスにつ
いて、効率良く任意の厚みの板ガラスに成形する
技術は、従来確立されてはいなかつた。なお、光
学ガラスを板ガラスに形成する方法として、作業
槽から導かれた白金製流出パイプの先端を徐々に
平たく広げて行き、先端部をスリツト状にしたノ
ズルから板状に流出させることが試みられてきた
が、パイプ内のヘツド差と粘性によりスリツト中
央部の流量が多くなり、うまくいかなかつた。
On the other hand, in the production of optical grade plate glass that requires high optical internal homogeneity, a tank made of platinum or a platinum alloy, or a tank lined with these, is generally used as the melting tank.
The structure of the melting furnace is significantly different from that of window glass melting furnaces, etc., and has a working tank at the end of the furnace equipped with a stirring mechanism to ultimately homogenize the molten glass. The molten glass is flowed out from a platinum pipe attached to the bottom of the working tank, which is the final tank, but the amount of glass flowing out, or the amount of glass pulled up, is extremely small in optical glass melting furnaces, and is usually several hundred kilograms. Several tons/day. Conventionally, no technology has been established for efficiently forming molten glass flowing out from such a small-diameter outflow pipe with a small pulling amount into a plate glass of any desired thickness. In addition, as a method for forming optical glass into plate glass, an attempt was made to gradually widen the tip of a platinum outflow pipe led from a working tank into a flattened shape, and then let it flow out in the form of a plate through a nozzle with a slit-shaped tip. However, due to the head difference and viscosity in the pipe, the flow rate in the center of the slit increased, and it did not work.

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

本発明は、供給源から供給される溶融ガラスを
いつたん特殊な形状を有する成形用型に受け、そ
こから板状のガラスを取り出すようにしたもので
ある。すなわち、本発明の成形用型は、最も深い
ガラス溜りを構成するガラス流入部、それに続い
て徐々に浅くかつ幅が広がるように構成された、
上り勾配の底面を有する誘導傾斜部およびこの誘
導傾斜部の頂部に連なる下り勾配面からなる流出
リツプ部を備える。
In the present invention, molten glass supplied from a supply source is once received in a mold having a special shape, and a plate-shaped glass is taken out from there. That is, the mold of the present invention is configured such that the glass inlet part constitutes the deepest glass reservoir, and the glass inlet part gradually becomes shallower and wider.
The guide slope has an upwardly sloped bottom surface and an outflow lip section having a downwardly sloped surface connected to the top of the guiding slope.

〔作用〕[Effect]

ガラス流入部に流入した溶融ガラスは、直ちに
成形用型から流出することなく、誘導傾斜部を順
次流出リツプ部へ向かつて、層流となりかつその
幅を広げつつ流れる。これにより、成形用型に流
入する溶融ガラスは、もとの高い内部均質度を保
持する。そして、流出リツプ部の頂部において、
一定の幅を維持した状態でオーバーフローし、そ
のまま流出リツプ部を流れ落ちることから、折れ
込み等の欠陥のない板状ガラスとなる。
The molten glass that has flowed into the glass inflow portion does not immediately flow out of the mold, but sequentially moves along the guiding slope toward the outflow lip portion, forming a laminar flow and flowing while widening its width. Thereby, the molten glass flowing into the mold maintains its original high internal homogeneity. Then, at the top of the outflow lip,
The glass overflows while maintaining a constant width and flows down the outflow lip, resulting in sheet glass without defects such as folds.

〔実施例〕〔Example〕

第1図および第2図は、本発明の一実施例を示
す概略構成図で、第2図は平面図、第1図はそれ
を中央部で切断した断面図である。
1 and 2 are schematic configuration diagrams showing one embodiment of the present invention, with FIG. 2 being a plan view and FIG. 1 being a sectional view taken at the center thereof.

成形用型1は、白金製流出パイプ2の直下に設
置され、保護耐火物槽3およびその内部に形成さ
れた白金製受槽4からなる。白金製受槽4は、保
護耐火物槽3に合せて成形し、その内面に接する
ように設置したが、保護耐火物槽3の内面に白金
をライニングしたものを成形用型としてもよい。
また、白金の代りに、例えば白金―ロジウムなど
の白金合金を用いてもよい。
The mold 1 is installed directly below the platinum outflow pipe 2 and consists of a protective refractory tank 3 and a platinum receiving tank 4 formed inside the protective refractory tank 3. Although the platinum receiving tank 4 was molded to match the protective refractory tank 3 and installed so as to be in contact with the inner surface thereof, a mold in which the inner surface of the protective refractory tank 3 is lined with platinum may also be used.
Furthermore, instead of platinum, a platinum alloy such as platinum-rhodium may be used.

白金受槽4の底面は、この受槽にパイプ2より
最初に溶融ガラス5が流入する部分(ガラス流入
部)においては平坦であるが、これに続いて上り
勾配の誘導傾部6があり、さらにその頂部に連続
して下り勾配の流出リツプ部7がある。このた
め、流出パイプ2より流入した溶融ガラス5は、
直ちにこの受槽4から流出することはなく、誘導
傾斜部6の頂部まで溜め込まれた後、連続的に流
出リツプ部7の先端より流れ出る。このとき、誘
導傾斜部6は、その頂部に向けて幅が緩やかに拡
大する構造を有しているため、溶融ガラス5は、
それに応じた幅をもつようになる。そして誘導傾
斜部6の頂部よりオーバーフローしたガラスは、
その幅を維持したまま流出リツプ部7の下り勾配
面を伝つて流れ落ちる。
The bottom surface of the platinum receiving tank 4 is flat at the part where the molten glass 5 first flows into the receiving tank from the pipe 2 (glass inflow part), but there is an upward slope guiding slope part 6 following this part, and then At the top, there is an outflow lip 7 which has a continuous downward slope. Therefore, the molten glass 5 flowing from the outflow pipe 2 is
The water does not immediately flow out of the receiving tank 4, but is stored up to the top of the guiding slope 6 and then continuously flows out from the tip of the outflow lip 7. At this time, since the guiding inclined portion 6 has a structure in which the width gradually increases toward the top thereof, the molten glass 5
It will have a corresponding width. The glass that overflowed from the top of the guiding slope 6 was
It flows down along the downwardly sloped surface of the outflow lip portion 7 while maintaining its width.

誘導傾斜部6の勾配は、受槽4内の溶融ガラス
5が部分的に停滞することなく層流となつて連続
的に流出して行くためには緩やかな方が良く、
10゜前後が好ましいが、求める板ガラスの品質に
応じて適宜選択すればよい。
The slope of the guiding slope part 6 is preferably gentle so that the molten glass 5 in the receiving tank 4 continuously flows out in a laminar flow without becoming partially stagnant.
The angle is preferably around 10°, but may be selected as appropriate depending on the desired quality of the plate glass.

流出リツプ部7の勾配も同様で、好ましい角度
は約45゜であるが、適宜選択すればよい。特に、
比較的薄肉の板ガラスを得ようとするときにはこ
の勾配は大きめに、比較的厚肉の板ガラスを得よ
うとするときには小さめにする。
The same applies to the slope of the outflow lip portion 7, and the preferred angle is about 45°, but it may be selected as appropriate. especially,
This slope is made larger when a relatively thin plate glass is to be obtained, and is made smaller when a relatively thick plate glass is to be obtained.

流出リツプ部7の先端より離れたガラスは、直
ちにロール8,9の間を通り、一定の厚さの板ガ
ラス10となつて徐冷炉(図示せず)へと送り込
まれる。ガラスの厚みは、ロール8,9の回転速
度および隙間の調整によつて任意の厚みに制御す
ることができるが、さらに、先に徐冷炉(レア
ー)中に送り込まれた板ガラス部分と連続してい
ることから、その移動によつて引張り力を受け
る。ロール8,9を通つた直後の部分は未だ固化
していないため、この引張り力、つまりレアース
ピードによつてその板厚は影響を受け、レアース
ピードが大きいほど板ガラスの厚みは薄くなる。
The glass that has left the tip of the outflow lip portion 7 immediately passes between rolls 8 and 9, becomes a plate glass 10 of a constant thickness, and is sent to a lehr (not shown). The thickness of the glass can be controlled to any desired thickness by adjusting the rotational speed and gap of the rolls 8 and 9, but furthermore, the glass plate is continuous with the plate glass portion that was previously fed into the lehr. Therefore, it receives a tensile force due to its movement. Since the portion immediately after passing through the rolls 8 and 9 has not yet solidified, the thickness of the sheet glass is affected by this tensile force, that is, the rare speed, and the higher the rare speed, the thinner the glass sheet becomes.

なお、受槽4は、その温度制御を正確に行なう
ため、適宜加熱が可能な構造とすることが望まし
い。第3図は、そのために給電フランジを取付け
た構造を示す。
Note that, in order to accurately control the temperature of the receiving tank 4, it is desirable that the receiving tank 4 has a structure that can be appropriately heated. FIG. 3 shows a structure in which a power supply flange is attached for this purpose.

一般に溶融ガラス5の温度は、流出する方向中
央部が側端部に対して高く、したがつて中央部の
流出速度が側端部に対して大きくなりがちであ
る。このため、成形開始直後は、受槽4の比較的
中央部を選択的に加熱するために給電フランジ1
1,12間および13,14間に通電加熱し、流
出リツプ部7から定常的にガラスが流れ始めた後
は、給電フランジ11,13間および12,14
間に通電し、受槽4の側部を主として加熱する。
この受槽4に必要な加熱熱量は、板ガラスの成形
速度およびその板厚と密接な関係にあり、適宜調
整する必要がある。特に、受槽4に流入する単位
時間当りのガラス量が多いときは、受槽4の底部
の冷却を必要とすることから、適宜、水冷もしく
は空冷の冷却手段を併設してもよい。このような
加熱および冷却手段を設けることにより、溶融ガ
ラスの温度を最適成形温度に自在に調節すること
が可能である。
Generally, the temperature of the molten glass 5 is higher at the center in the outflow direction than at the side edges, and therefore the outflow velocity at the center tends to be higher than at the side edges. For this reason, immediately after the start of molding, the power supply flange 1 is used to selectively heat the relatively central portion of the receiving tank 4.
After the glass begins to steadily flow from the outflow lip portion 7 by applying electricity and heating between the power supply flanges 11 and 12 and between the power supply flanges 13 and 14,
Electricity is applied between them to mainly heat the sides of the receiving tank 4.
The amount of heating heat required for this receiving tank 4 is closely related to the forming speed of the plate glass and its plate thickness, and needs to be adjusted appropriately. In particular, when the amount of glass flowing into the receiving tank 4 per unit time is large, it is necessary to cool the bottom of the receiving tank 4, so a cooling means such as water cooling or air cooling may be provided as appropriate. By providing such a heating and cooling means, it is possible to freely adjust the temperature of the molten glass to the optimum molding temperature.

次に、成形方法の具体例を説明する。 Next, a specific example of the molding method will be explained.

光学ガラスとして最も使用量の多いホウケイ酸
クラウン系ガラスBSC7(HOYA商品名)を溶
解炉で溶解・清澄し、作業槽を経て泡・脈理のな
い、かつ十分に均質化された光学グレードの内容
品質のガラスとする。この溶融ガラスを、流出パ
イプ2より受槽4に連続的に供給する。このと
き、流出パイプ2から流出するガラスの温度は
1120℃、受槽4に供給された後の誘導傾斜部6の
中央付近での溶融ガラス5の温度は1080℃であつ
た。なお、成形用型1は、図示されていないが加
熱手段を備えた保温炉内に全体が納められてお
り、その雰囲気温度は850℃であつた。また、流
出リツプ部7の中央付近でのガラス温度は970℃、
その左右側端部付近でのガラス温度は920℃であ
つた。
Borosilicate crown glass BSC7 (HOYA product name), which is the most commonly used optical glass, is melted and clarified in a melting furnace, and then passed through a working tank to produce a fully homogenized optical grade without bubbles or striae. With quality glass. This molten glass is continuously supplied to a receiving tank 4 from an outflow pipe 2. At this time, the temperature of the glass flowing out from the outflow pipe 2 is
The temperature of the molten glass 5 near the center of the induction slope portion 6 after being supplied to the receiving tank 4 was 1120°C and 1080°C. The mold 1 was entirely housed in a heat-retaining furnace equipped with heating means (not shown), and the ambient temperature therein was 850°C. In addition, the glass temperature near the center of the outflow lip part 7 is 970℃,
The glass temperature near the left and right ends was 920°C.

溶融ガラス5は、誘導傾斜部6、流出リツプ部
7を経てロール8,9に供給され、板幅250mm、
板厚3.5mmの板ガラス10となつて徐冷炉に供給
された。なお、板幅は流出リツプ部7の幅に応じ
て決まり、このときその幅は300mmであつた。ま
た、板厚は、前述したように主としてロール8,
9の間隔に応じて決まるが、レアースピードによ
つても変化し、これを10m/hrとすることによ
り、上記板ガラスは最終的に板幅250mm、板厚3.0
mmとなつた。
The molten glass 5 is supplied to the rolls 8 and 9 through the guiding slope part 6 and the outflow lip part 7, and the rolls 8 and 9 have a plate width of 250 mm.
A glass plate 10 having a thickness of 3.5 mm was formed and supplied to a lehr. Note that the plate width was determined according to the width of the outflow lip portion 7, and at this time, the width was 300 mm. In addition, as mentioned above, the plate thickness is mainly determined by the roll 8,
9, but it also changes depending on the rare speed. By setting this to 10m/hr, the above plate glass will finally have a width of 250mm and a thickness of 3.0mm.
It became mm.

このようにして、脈理、泡、異物等のない、均
質度の高い光学グレードの板ガラスが得られた。
なお、流出パイプ2からの溶融ガラスの流出量、
そのガラス温度、受槽4内の溶融ガラス5の温
度、ロール8,9間の隙間、レアースピード、さ
らに流出リツプ部7の幅、これらは、得ようとす
る板ガラスの幅と厚みに対して相関関係をもつも
のであり、適宜選択する必要がある。
In this way, a highly homogeneous optical grade plate glass free of striae, bubbles, foreign matter, etc. was obtained.
In addition, the amount of molten glass flowing out from the outflow pipe 2,
The temperature of the glass, the temperature of the molten glass 5 in the receiving tank 4, the gap between the rolls 8 and 9, the lair speed, and the width of the outflow lip 7 are all correlated to the width and thickness of the glass plate to be obtained. Therefore, it is necessary to select it appropriately.

また、流出リツプ部7を離れたガラスを、ロー
ル8,9の間を通して彼冷炉に送る例について述
べたが、本発明はこれに限定されるものではな
く、必ずしもロールを用いなければならないもの
ではない。
In addition, although an example has been described in which the glass that has left the outflow lip section 7 is sent to the cooling furnace through between the rolls 8 and 9, the present invention is not limited to this, and the glass that has left the outflow lip section 7 is sent to the cooling furnace. isn't it.

以上、保護耐火物を白金(もしくは白金合金)
との組合せからなる成形用型を例に説明したが、
本発明の成形用型はこれに限定されるものではな
く、カーボンその他、例えば電鋳レンガ、焼成レ
ンガなどの耐熱耐火物を所望の形状にしたものを
用いてもよい。
In the above, the protective refractory is platinum (or platinum alloy)
The explanation was given using an example of a molding die consisting of a combination of
The mold of the present invention is not limited to this, and may be made of carbon or other heat-resistant refractories such as electroformed bricks and fired bricks into a desired shape.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、ガラス流入部、それに続いて
徐々に浅く幅が広がるように構成された上り勾配
の底面を有する誘導傾斜部およびその頂部に連な
る下り勾配面からなる流出リツプ部を備えた成形
用型を用い、上記ガラス流入部に溶融ガラスを供
給することにより、流出パイプからのガラスの流
出量の多少にかかわらず、任意の幅と厚みをもつ
た板ガラスを製造することができる。特に、ガラ
ス流入部に流入した溶融ガラスは、誘導傾斜部を
順次流出リツプ部へ向かつて、層流となつてその
幅を広げつつ流れて行くため、内部均質度がきわ
めて高く、しかも折れ込み等の欠陥のない光学グ
レードの板ガラスが得られる。
According to the present invention, a molding comprising a glass inflow portion, a guiding slope portion having an upwardly sloped bottom surface configured to gradually become shallower and wider, and an outlet lip portion consisting of a downwardly sloped surface continuous to the top of the guiding slope portion. By supplying molten glass to the glass inlet using a mold, it is possible to manufacture plate glass having any desired width and thickness, regardless of the amount of glass flowing out from the outflow pipe. In particular, the molten glass that has flowed into the glass inflow section sequentially moves through the guiding slope toward the outflow lip section, becoming a laminar flow and flowing while widening its width. Optical-grade sheet glass without any defects is obtained.

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

第1図は本発明の一実施例を示す断面図、第2
図は同じく平面図、第3図は給電フランジ付き成
形用型の構成例を示す平面図である。 1…成形用型、2…流出パイプ、3…保護耐火
物槽、4…白金製受槽、5…溶融ガラス、6…誘
導傾斜部、7…流出リツプ部、10…板ガラス、
11〜14…給電フランジ。
FIG. 1 is a cross-sectional view showing one embodiment of the present invention, and FIG.
This figure is also a plan view, and FIG. 3 is a plan view showing an example of the configuration of a molding die with a power supply flange. DESCRIPTION OF SYMBOLS 1... Molding mold, 2... Outflow pipe, 3... Protective refractory tank, 4... Platinum receiver tank, 5... Molten glass, 6... Guiding slope part, 7... Outflow lip part, 10... Plate glass,
11-14...Power supply flange.

Claims (1)

【特許請求の範囲】 1 最も深いガラス溜りを構成するガラス流入
部、このガラス流入部に続き徐々に浅くなるとと
もに幅が広がるように構成された、上り勾配の底
面を有する誘導傾斜部およびこの誘導傾斜部の頂
部に連なる下り勾配面からなる流出リツプ部を備
えたことを特徴とする板ガラスの成形用型。 2 保護耐火物槽に白金もしくは白金合金からな
る受槽を内接させまたは保護耐火物槽の内面に白
金もしくは白金合金をライニングすることにより
構成したことを特徴とする特許請求の範囲第1項
記載の板ガラスの成形用型。 3 給電フランジを備えたことを特徴とする特許
請求の範囲第1項または第2項記載の板ガラスの
成形用型。
[Scope of Claims] 1. A glass inflow section constituting the deepest glass reservoir, a guiding slope section having an upwardly sloped bottom surface and configured to gradually become shallower and wider following the glass inflow section, and the guide. A mold for forming plate glass, characterized in that it is provided with an outflow lip section consisting of a downwardly sloped surface connected to the top of the slope section. 2. The method according to claim 1, characterized in that the protective refractory tank is constructed by inscribing a receiving tank made of platinum or a platinum alloy, or by lining the inner surface of the protective refractory tank with platinum or a platinum alloy. A mold for forming plate glass. 3. A mold for forming plate glass according to claim 1 or 2, characterized in that it is provided with a power supply flange.
JP28573886A 1986-11-29 1986-11-29 Die for forming sheet glass Granted JPS63139020A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28573886A JPS63139020A (en) 1986-11-29 1986-11-29 Die for forming sheet glass

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28573886A JPS63139020A (en) 1986-11-29 1986-11-29 Die for forming sheet glass

Publications (2)

Publication Number Publication Date
JPS63139020A JPS63139020A (en) 1988-06-10
JPH0359015B2 true JPH0359015B2 (en) 1991-09-09

Family

ID=17695404

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28573886A Granted JPS63139020A (en) 1986-11-29 1986-11-29 Die for forming sheet glass

Country Status (1)

Country Link
JP (1) JPS63139020A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008062602A1 (en) 2008-12-17 2010-06-24 Moravsky, Miroslav, Dr. Apparatus for the production of flat glass
CN102153270A (en) * 2010-11-19 2011-08-17 河南安彩高科股份有限公司 Integrated lip brick for solar low-iron ultra-white rolled glass and manufacturing method of integrated lip brick
JP6740746B2 (en) * 2016-06-22 2020-08-19 日本電気硝子株式会社 Glass plate manufacturing method and glass plate manufacturing apparatus

Also Published As

Publication number Publication date
JPS63139020A (en) 1988-06-10

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