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JP7022304B2 - Glass article manufacturing equipment and manufacturing method - Google Patents
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JP7022304B2 - Glass article manufacturing equipment and manufacturing method - Google Patents

Glass article manufacturing equipment and manufacturing method Download PDF

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JP7022304B2
JP7022304B2 JP2017246563A JP2017246563A JP7022304B2 JP 7022304 B2 JP7022304 B2 JP 7022304B2 JP 2017246563 A JP2017246563 A JP 2017246563A JP 2017246563 A JP2017246563 A JP 2017246563A JP 7022304 B2 JP7022304 B2 JP 7022304B2
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slope
flow
molten glass
manufacturing
width direction
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JP2019112255A (en
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剛大 榎本
勇二 小南
翼 加賀井
和人 中塚
康宏 西村
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Nippon Electric Glass Co Ltd
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Description

本発明は、ガラス物品の製造装置及び製造方法に関し、特に成形体の溶融ガラス流下面を改良することで、ガラスリボンの厚み寸法分布を改善するための技術に関する。 The present invention relates to an apparatus and a method for manufacturing a glass article, and more particularly to a technique for improving the thickness dimension distribution of a glass ribbon by improving the lower surface of a molten glass flow of a molded body.

周知のように、液晶ディスプレイ、プラズマディスプレイ、有機ELディスプレイなどのフラットパネルディスプレイ(FPD)用のガラス基板や、有機EL照明用のカバーガラスに代表されるように、各種分野に利用される薄板ガラスには、表面欠陥やうねりに対して厳しい製品品位が要求される場合がある。 As is well known, thin plate glass used in various fields such as glass substrates for flat panel displays (FPDs) such as liquid crystal displays, plasma displays, and organic EL displays, and cover glasses for organic EL lighting. May require strict product quality against surface defects and waviness.

そこで、この種の薄板ガラスの製造方法としては、平滑で欠陥のないガラス表面を得るために、オーバーフローダウンドロー法が多く利用されている。 Therefore, as a method for producing this kind of thin glass, an overflow down draw method is often used in order to obtain a smooth and defect-free glass surface.

ここで、オーバーフローダウンドロー法による成形を実施する装置としては、例えば特許文献1に記載のように、溶融ガラスが溢れ出るオーバーフロー溝と、オーバーフロー溝から溢れ出た溶融ガラスを流下させる一対の流下壁とを備えた成形体が一般的である。ここで、各流下壁は、垂直方向に延伸する垂直面部と、垂直面部とその下端で連続し、下方に向かうにつれて互いに接近する向きに傾斜して各々の下端で合流する逆斜面部とを有する。また、流下壁(垂直面部、逆斜面部)の幅方向両端部には、特許文献2に記載のように、流下壁から垂直に立設し、流下中の溶融ガラスの流路幅を規定して、溶融ガラスの流下を案内するためのガイド面が設けられている。 Here, as an apparatus for performing molding by the overflow down draw method, for example, as described in Patent Document 1, an overflow groove in which molten glass overflows and a pair of flow-down walls in which the molten glass overflowing from the overflow groove flows down. A molded body provided with and is generally used. Here, each flow-down wall has a vertical plane portion extending in the vertical direction, and a reverse slope portion that is continuous at the vertical plane portion and its lower end, is inclined toward each other as it goes downward, and joins at each lower end. .. Further, as described in Patent Document 2, the flow path width of the molten glass during the flow is defined by standing vertically from the flow wall at both ends in the width direction of the flow wall (vertical surface portion, reverse slope portion). Therefore, a guide surface for guiding the flow of the molten glass is provided.

特開2013-184876号公報Japanese Unexamined Patent Publication No. 2013-184876 特開2017-88446号公報Japanese Unexamined Patent Publication No. 2017-88446

ところで、上述のように、流下壁の幅方向両端部にガイド面が設けられている場合、例えば、ガイド面に対する溶融ガラスの濡れ性が比較的高いと、流下中の溶融ガラスが、ガイド面へ濡れ伝わって表面張力により引き上げられ、幅方向端部に偏ることがある(図6)。上述のように、溶融ガラスの引き上げが生じると、引き上げられた分だけ溶融ガラスの流下量が部分的に不足する領域が発生する。これでは、成形の結果得られるガラスリボンの製品部分に、所望の厚み寸法よりも小さい部分が残り、結果、製品の厚み寸法が幅方向でばらつくおそれが生じる。 By the way, as described above, when the guide surfaces are provided at both ends in the width direction of the flow-down wall, for example, when the wettability of the molten glass to the guide surface is relatively high, the molten glass flowing down reaches the guide surface. It is transmitted wet and pulled up by surface tension, and may be biased toward the end in the width direction (Fig. 6). As described above, when the molten glass is pulled up, there is a region where the flow amount of the molten glass is partially insufficient by the amount of the pulled up. In this case, a portion smaller than the desired thickness dimension remains in the product portion of the glass ribbon obtained as a result of molding, and as a result, the thickness dimension of the product may vary in the width direction.

以上の事情に鑑み、本発明では、溶融ガラスの流下量が幅方向で不足する事態を可及的に防止して、製品部分の厚み寸法のばらつきを抑制することを、解決すべき技術課題とする。 In view of the above circumstances, in the present invention, it is a technical problem to be solved to prevent the situation where the flow amount of the molten glass is insufficient in the width direction as much as possible and suppress the variation in the thickness dimension of the product part. do.

前記課題の解決は、本発明に係るガラス物品の製造装置により達成される。すなわち、この製造装置は、樋形状をなし溶融ガラスが溢れ出るオーバーフロー溝と、オーバーフロー溝から溢れ出た溶融ガラスが流下する一対の流下壁と、各流下壁の幅方向両端部に設けられ溶融ガラスの流下を案内する合計で二対のガイド部とを備え、一対の流下壁は、オーバーフロー溝が設けられた上端面に隣接し下方に延びる一対の第一流下面と、第一流下面の下方に位置し、下方に向かうにつれて互いに接近して下端で合流する逆斜面である一対の第二流下面とを有する、ガラス物品の製造装置であって、各ガイド部は、第一流下面の幅方向端部とつながり、第一流下面からその幅方向に遠ざかる向きに上り勾配となる第一斜面を有する点をもって特徴付けられる。 The solution to the above problems is achieved by the apparatus for manufacturing a glass article according to the present invention. That is, this manufacturing apparatus is provided at both ends in the width direction of an overflow groove having a gutter shape and overflowing molten glass, a pair of flowing down walls into which the molten glass overflowing from the overflow groove flows down, and molten glass. A total of two pairs of guides are provided to guide the flow of the glass, and the pair of flow walls are located adjacent to the upper end surface provided with the overflow groove and extending downward with a pair of lower surfaces of the first flow and below the lower surface of the first flow. It is a glass article manufacturing apparatus having a pair of second flow lower surfaces, which are reverse slopes that approach each other and merge at the lower end toward the lower side, and each guide portion is a widthwise end portion of the first flow lower surface. It is characterized by having a first slope that is connected to and has an upslope in the direction away from the lower surface of the first stream in the width direction.

このように、本発明に係る製造装置では、流下壁のうちオーバーフロー溝から溢れ出た溶融ガラスが流下を開始した直後に接触する第一流下面とその幅方向両端に位置するガイド部とに着目し、この第一流下面の幅方向端部に、第一流下面から幅方向に遠ざかる向きに上り勾配となる第一斜面を設けた。これにより、ガイド部に対する溶融ガラスの引き上げ状態が変化し、例えば第一斜面上の溶融ガラスの厚み方向寸法が均される。よって、従来のように、引き上げにより極端に厚み寸法の大きな部分と小さな部分が生じる事態が可及的に防止され、成形されるガラスリボンの製品部分に、相対的に厚み寸法の小さい部分が残る事態を回避することが可能となる。 As described above, in the manufacturing apparatus according to the present invention, attention is paid to the first flow lower surface and the guide portions located at both ends in the width direction thereof, which are in contact with the molten glass overflowing from the overflow groove in the flow wall immediately after the flow starts. At the widthwise end of the lower surface of the first stream, a first slope having an upward slope is provided in a direction away from the lower surface of the first stream in the width direction. As a result, the state in which the molten glass is pulled up with respect to the guide portion changes, and for example, the dimension in the thickness direction of the molten glass on the first slope is leveled. Therefore, as in the past, it is possible to prevent the situation where an extremely large portion and a small portion are generated due to pulling up, and a portion having a relatively small thickness dimension remains in the product portion of the molded glass ribbon. It is possible to avoid the situation.

また、本発明に係る製造装置においては、ガイド部が、第一流下面に対して立設したガイド面をさらに有し、第一斜面は、ガイド面と第一流下面とをつなぐ、一定の幅方向寸法及び第一流下面に対する一定の傾斜角を有するバンク面であってもよい。あるいは、第一斜面が、溶融ガラスの流下方向に見た場合に凹状に湾曲した断面形状を有する凹曲面であってもよい。 Further, in the manufacturing apparatus according to the present invention, the guide portion further has a guide surface erected with respect to the lower surface of the first stream, and the first slope is a constant width direction connecting the guide surface and the lower surface of the first stream. It may be a bank surface having a certain inclination angle with respect to the dimensions and the lower surface of the first stream. Alternatively, the first slope may be a concave curved surface having a concavely curved cross-sectional shape when viewed in the flow direction of the molten glass.

このように第一斜面を、一定の幅方向寸法及び一定の傾斜角を有するバンク面とするのであれば、比較的容易に第一斜面を第一流下面上に設けることができる。あるいは、第一斜面を上述のように凹状に湾曲した凹曲面とすることによって、第一斜面上における溶融ガラスの厚み方向寸法をより均等にすることができる。 As described above, if the first slope is a bank surface having a certain width direction dimension and a certain inclination angle, the first slope can be relatively easily provided on the lower surface of the first flow. Alternatively, by making the first slope a concave curved surface curved in a concave shape as described above, the dimensions of the molten glass on the first slope in the thickness direction can be made more uniform.

また、本発明に係る製造装置においては、各ガイド部が、上端面と第一斜面とを接続する接続面をさらに有してもよい。また、この場合、接続面は、例えば下方に向かうにつれて上り勾配が増加する上り勾配増加面であってもよい。 Further, in the manufacturing apparatus according to the present invention, each guide portion may further have a connecting surface for connecting the upper end surface and the first slope. Further, in this case, the connecting surface may be, for example, an ascending gradient increasing surface in which the ascending gradient increases as it goes downward.

このように、オーバーフロー溝が開口する上端面と第一斜面とを接続する接続面をさらに設けることで、溶融ガラスの第一斜面上への流入状態を調整することができる。例えば上述のように、接続面を、下方に向かうにつれて上り勾配が増加する上り勾配増加面とした場合には、オーバーフロー溝から溢れ出た直後の溶融ガラスはまず第一流下面と平行ないし平行に近い面(上り勾配像下面の上端部)上に流入し、次第に上り勾配となって第一斜面上へと案内される。これにより、溶融ガラスを円滑に第一斜面上へと案内して、溶融ガラスの流下開始時の乱れを抑制することが可能となる。 In this way, by further providing a connecting surface connecting the upper end surface where the overflow groove opens and the first slope, the inflow state of the molten glass onto the first slope can be adjusted. For example, as described above, when the connecting surface is an ascending slope increasing surface in which the ascending slope increases downward, the molten glass immediately after overflowing from the overflow groove is first parallel to or nearly parallel to the lower surface of the first flow. It flows onto the surface (upper end of the lower surface of the uphill slope image), gradually becomes an uphill slope, and is guided onto the first slope. This makes it possible to smoothly guide the molten glass onto the first slope and suppress turbulence at the start of flow of the molten glass.

また、本発明に係る製造装置においては、各ガイド部が、第二流下面の幅方向両端部とつながり、第二流下面に対し上り勾配となる第二斜面をさらに有してもよい。 Further, in the manufacturing apparatus according to the present invention, each guide portion may further have a second slope which is connected to both ends in the width direction of the lower surface of the second stream and has an upward slope with respect to the lower surface of the second stream.

このように、第一流下面の下方に位置する第二流下面の幅方向端部にも、第一流下面に対し上り勾配となる第二斜面を設けた。これにより、第二流下面に到達した溶融ガラスに対して引き続き第一斜面と同様の作用(ガイド部に対する溶融ガラスの引き上げ状態が変化し、第二斜面上の溶融ガラスの厚み方向寸法が均される)を付与することができる。よって、下端で合流するまでの間、上述した作用を維持して、ガラスリボンの製品部分に、相対的に厚み寸法の小さい部分が残る事態をより確実に回避することが可能となる。 As described above, the widthwise end of the lower surface of the second stream located below the lower surface of the first stream is also provided with a second slope having an upward slope with respect to the lower surface of the first stream. As a result, the same action as the first slope continues on the molten glass that has reached the lower surface of the second flow (the state in which the molten glass is pulled up with respect to the guide portion changes, and the thickness direction dimension of the molten glass on the second slope is leveled. ) Can be given. Therefore, it is possible to maintain the above-mentioned action until the glass ribbon merges at the lower end, and more reliably avoid a situation in which a portion having a relatively small thickness dimension remains in the product portion of the glass ribbon.

また、第二斜面を有する場合、本発明に係る製造装置においては、第一斜面と第二斜面とが、溶融ガラスの流下方向に沿って連続して設けられ互いにつながっていてもよい。また、この場合、第一斜面と第二斜面とが、幅方向に見た場合に凸状に湾曲した断面形状をなす凸面部を介してつながっていてもよい。 Further, when the second slope is provided, in the manufacturing apparatus according to the present invention, the first slope and the second slope may be continuously provided along the flow direction of the molten glass and connected to each other. Further, in this case, the first slope and the second slope may be connected via a convex surface portion having a cross-sectional shape curved in a convex shape when viewed in the width direction.

このように、第一流下面と第二流下面にそれぞれ第一斜面と第二斜面を設ける場合、双方の斜面同士を互いにつなげることで、好ましくは上述のように凸状に湾曲した形状をなす凸面部を介してつなげることで、第一斜面上を流下する溶融ガラスを円滑に第二斜面上に導入することができる。これにより、上述した第二斜面による作用を安定的に得ることが可能となる。 In this way, when the first slope and the second slope are provided on the lower surface of the first flow and the lower surface of the second flow, respectively, by connecting both slopes to each other, a convex surface having a convex curved shape as described above is preferable. By connecting via the portions, the molten glass flowing down on the first slope can be smoothly introduced onto the second slope. This makes it possible to stably obtain the action of the second slope described above.

また、前記課題の解決は、本発明に係るガラス物品の製造方法によっても達成される。すなわち、この製造方法は、樋形状をなし溶融ガラスが溢れ出るオーバーフロー溝と、オーバーフロー溝から溢れ出た溶融ガラスが流下する一対の流下壁と、各流下壁の幅方向両端部に設けられ溶融ガラスの流下を案内する合計で二対のガイド部とを備え、一対の流下壁は、オーバーフロー溝が設けられた上端面に隣接し下方に延びる一対の第一流下面と、第一流下面の下方に位置し、下方に向かうにつれて互いに接近して下端で合流する逆斜面である一対の第二流下面とを有する製造装置を用いて、ガラス物品を製造するガラス物品の製造方法であって、各ガイド部は、第一斜面の幅方向端部とつながり、第一流下面からその幅方向に遠ざかる向きに上り勾配となる第一斜面を有し、オーバーフロー溝から溶融ガラスを溢れ出させて、溶融ガラスが第一斜面と接しながら流下するようにした点をもって特徴付けられる。 Further, the solution to the above problems is also achieved by the method for manufacturing a glass article according to the present invention. That is, in this manufacturing method, an overflow groove having a gutter shape and overflowing molten glass, a pair of flowing down walls into which the molten glass overflowing from the overflow groove flows down, and molten glass provided at both ends in the width direction of each flowing down wall. A total of two pairs of guides are provided to guide the flow of the glass, and the pair of flow walls are located adjacent to the upper end surface provided with the overflow groove and extending downward, and below the lower surface of the first flow. A method for manufacturing a glass article, wherein the glass article is manufactured by using a manufacturing apparatus having a pair of second flow lower surfaces, which are reverse slopes that approach each other and merge at the lower end as the glass article is directed downward. Has a first slope that is connected to the widthwise end of the first slope and has an ascending slope in the direction away from the lower surface of the first flow in the width direction, and the molten glass overflows from the overflow groove, so that the molten glass becomes the first. It is characterized by the fact that it flows down while in contact with one slope.

このように、本発明に係る製造方法においても、第一流下面から幅方向に遠ざかる向きに上り勾配となる第一斜面を設けるようにした。よって、上述のようにオーバーフロー溝から溢れ出た溶融ガラスが第一流下面の幅方向両端部に位置する第一斜面と接しながら流下することで、ガイド部に対する溶融ガラスの引き上げ状態が変化し、例えば第一斜面上の溶融ガラスの厚み方向寸法が均される。よって、従来のように、引き上げにより極端に厚み寸法の大きな部分と小さな部分が生じる事態が可及的に防止され、成形されるガラスリボンの製品部分に、相対的に厚み寸法の小さい部分が残る事態を回避することが可能となる。 As described above, also in the manufacturing method according to the present invention, the first slope having an upward slope is provided in the direction away from the lower surface of the first flow in the width direction. Therefore, as described above, the molten glass overflowing from the overflow groove flows down while being in contact with the first slopes located at both ends in the width direction of the lower surface of the first flow, so that the state in which the molten glass is pulled up with respect to the guide portion changes, for example. The thickness direction dimension of the molten glass on the first slope is leveled. Therefore, as in the past, it is possible to prevent the situation where an extremely large portion and a small portion are generated due to pulling up, and a portion having a relatively small thickness dimension remains in the product portion of the molded glass ribbon. It is possible to avoid the situation.

また、本発明に係る製造方法においては、第一斜面の上り勾配を75°以上でかつ85°以下に設定した状態で、3000dPa・s以上でかつ10000dPa・s以下に調整した溶融ガラスを前記オーバーフロー溝から溢れ出させてもよい。 Further, in the manufacturing method according to the present invention, the molten glass adjusted to 3000 dPa · s or more and 10000 dPa · s or less in a state where the ascending slope of the first slope is set to 75 ° or more and 85 ° or less is overflowed. It may overflow from the groove.

あるいは、第一斜面の上り勾配を5°以上でかつ15°以下に設定した状態で、100dPa・s以下に調整した溶融ガラスをオーバーフロー溝から溢れ出させてもよい。 Alternatively, the molten glass adjusted to 100 dPa · s or less may overflow from the overflow groove with the ascending slope of the first slope set to 5 ° or more and 15 ° or less.

本発明者らが、本発明に係る第一斜面の上り勾配と溶融ガラスの粘度との関係について検証した結果、溶融ガラスの粘度域に応じて適切な上り勾配の範囲があることが判明した。具体的には、相対的に粘度が高い(3000dPa・s以上でかつ10000dPa・s以下の)溶融ガラスを使用する場合には、第一斜面の上り勾配を相対的に急に(75°以上でかつ85°以下に)設定することで、また相対的に粘度が低い(100dPa・s以下の)溶融ガラスを使用する場合には、第一斜面の上り勾配を相対的に緩やかに(5°以上でかつ15°以下に)設定することで、上述した作用を効果的にかつ安定的に享受することが可能となる。 As a result of verifying the relationship between the uphill slope of the first slope and the viscosity of the molten glass according to the present invention, the present inventors have found that there is an appropriate uphill slope range depending on the viscosity range of the molten glass. Specifically, when molten glass having a relatively high viscosity (3000 dPa · s or more and 10,000 dPa · s or less) is used, the uphill slope of the first slope is relatively steep (at 75 ° or more). And by setting it to 85 ° or less, and when using molten glass with a relatively low viscosity (100 dPa · s or less), the uphill slope of the first slope is relatively gentle (5 ° or more). And by setting it to 15 ° or less), it is possible to effectively and stably enjoy the above-mentioned action.

以上に述べたように、本発明によれば、溶融ガラスの流下量が幅方向で不足する事態を可及的に防止して、製品部分の厚み寸法のばらつきを抑制することが可能となる。 As described above, according to the present invention, it is possible to prevent the situation where the flow amount of the molten glass is insufficient in the width direction as much as possible, and to suppress the variation in the thickness dimension of the product portion.

本発明の第一実施形態に係るガラス物品の製造装置の斜視図である。It is a perspective view of the manufacturing apparatus of the glass article which concerns on 1st Embodiment of this invention. 図1に示す製造装置の正面図である。It is a front view of the manufacturing apparatus shown in FIG. 図2に示す製造装置のA-A断面図である。FIG. 2 is a cross-sectional view taken along the line AA of the manufacturing apparatus shown in FIG. 図2に示す製造装置のB-B断面図である。It is BB sectional view of the manufacturing apparatus shown in FIG. 図2に示す製造装置の(a)C-C断面図と、(b)D-D断面図である。It is (a) CC sectional view and (b) DD sectional view of the manufacturing apparatus shown in FIG. 従来構成のガイド部を使用した場合における溶融ガラスの流下態様を模式的に描いた製造装置の要部横断面図である。It is sectional drawing of the main part of the manufacturing apparatus which schematically depicts the flow | flow mode of the molten glass when the guide part of the conventional structure is used. 本発明の第二実施形態に係る製造装置の要部横断面図である。It is sectional drawing of the main part of the manufacturing apparatus which concerns on 2nd Embodiment of this invention. 本発明の第三実施形態に係る製造装置の要部横断面図である。It is sectional drawing of the main part of the manufacturing apparatus which concerns on 3rd Embodiment of this invention. 本発明の第四実施形態に係る製造装置の正面図である。It is a front view of the manufacturing apparatus which concerns on 4th Embodiment of this invention. 図9に示す製造装置の(a)E-E断面図と、(b)F-F断面図である。9A is a cross-sectional view taken along the line EE and (b) is a cross-sectional view taken along the line FF of the manufacturing apparatus shown in FIG. 本発明の第五実施形態に係る製造装置の(a)E-E断面図と、(b)F-F断面図である。It is (a) EE sectional view and (b) FF sectional view of the manufacturing apparatus which concerns on 5th Embodiment of this invention. 本発明の第六実施形態に係る製造装置の正面図である。It is a front view of the manufacturing apparatus which concerns on 6th Embodiment of this invention. 図12に示す製造装置の(a)E-E断面図と、(b)F-F断面図である。12 is a cross-sectional view taken along the line (a) EE and (b) a cross-sectional view taken along the line FF of the manufacturing apparatus shown in FIG. 本発明の第七実施形態に係る製造装置の要部拡大縦断面図である。It is an enlarged vertical sectional view of the main part of the manufacturing apparatus which concerns on 7th Embodiment of this invention.

以下、本発明に係る実施形態を添付図面に基づいて説明する。 Hereinafter, embodiments according to the present invention will be described with reference to the accompanying drawings.

(本発明の第一実施形態)
図1及び図2に示すように、本発明の第一実施形態に係るガラス物品の製造装置は、オーバーフローダウンドロー法による成形を実施するための成形体1を備えている。
(First Embodiment of the present invention)
As shown in FIGS. 1 and 2, the apparatus for manufacturing a glass article according to the first embodiment of the present invention includes a molded body 1 for carrying out molding by an overflow down draw method.

成形体1は、製造されるガラス物品(ここでは板ガラス或いはガラスシート)の幅方向に対応する方向に長尺な形状をなす。成形体1の頂部には、鉛直上方を向く上端面2が設けられ、上端面2には、その長手方向(すなわち成形体1の幅方向)に沿って形成されたオーバーフロー溝3が形成されている。成形体1の幅方向と直交する方向、すなわちオーバーフロー溝3の短手方向の両側には、一対の流下壁4,4が設けられている。オーバーフロー溝3から溢れ出た溶融ガラスGmは、各流下壁4に沿って流下する。本実施形態では、図1に示すXYZ直交座標系において、X方向及びY方向は水平方向であり、Z方向が鉛直方向である。この場合、X方向が上記の「幅方向」となり、Y方向が上記の「幅方向と直交する方向」となる。図2以降においても同様とする。 The molded body 1 has a long shape in a direction corresponding to the width direction of the glass article (here, a plate glass or a glass sheet) to be manufactured. An upper end surface 2 facing vertically upward is provided on the top of the molded body 1, and an overflow groove 3 formed along the longitudinal direction thereof (that is, the width direction of the molded body 1) is formed on the upper end surface 2. There is. A pair of flow-down walls 4 and 4 are provided on both sides in a direction orthogonal to the width direction of the molded body 1, that is, in the lateral direction of the overflow groove 3. The molten glass Gm that overflows from the overflow groove 3 flows down along each downflow wall 4. In the present embodiment, in the XYZ Cartesian coordinate system shown in FIG. 1, the X direction and the Y direction are horizontal directions, and the Z direction is a vertical direction. In this case, the X direction is the above-mentioned "width direction", and the Y direction is the above-mentioned "direction orthogonal to the width direction". The same applies to FIGS. 2 and later.

オーバーフロー溝3の幅方向一端側には、供給管5が接続されている。この供給管5を通じて、オーバーフロー溝3内に溶融ガラスGmが供給される。もちろん溶融ガラスGmの供給方法はこれに限定されず、例えば、オーバーフロー溝3の長手方向両端側から溶融ガラスGmを供給するようにしてもよい。 A supply pipe 5 is connected to one end side of the overflow groove 3 in the width direction. The molten glass Gm is supplied into the overflow groove 3 through the supply pipe 5. Of course, the method of supplying the molten glass Gm is not limited to this, and for example, the molten glass Gm may be supplied from both ends in the longitudinal direction of the overflow groove 3.

一対の流下壁4のそれぞれは、図3に示すように、第一流下面6と、第一流下面6の下方に位置する第二流下面7とを有する。第一流下面6,6は何れも、オーバーフロー溝3が設けられた上端面2と隣接し、互いに一定の距離を保った状態で下方に延びている。第二流下面7,7は、下方に向かうにつれて接近するよう互いに逆向きに傾斜しており、下端部7aで合流している。この際、下端部7aは、幅方向に延びる直線部で構成されている。第一流下面6,6は、本実施形態では、鉛直方向に延びているが、鉛直方向に対して多少の傾斜を有していてもよい。また、第二流下面7,7は、成形対象となるガラス物品(ここではガラスリボンGr)の厚み寸法などに応じて所定の傾斜角に設定される。 Each of the pair of downflow walls 4 has a first flow lower surface 6 and a second flow lower surface 7 located below the first flow lower surface 6, as shown in FIG. Each of the first flow lower surfaces 6 and 6 is adjacent to the upper end surface 2 provided with the overflow groove 3 and extends downward while maintaining a certain distance from each other. The lower surfaces 7 and 7 of the second stream are inclined in opposite directions so as to approach each other toward the lower side, and meet at the lower end portion 7a. At this time, the lower end portion 7a is composed of a straight portion extending in the width direction. In the present embodiment, the lower surfaces 6 and 6 of the first stream extend in the vertical direction, but may have a slight inclination with respect to the vertical direction. Further, the lower surfaces 7 and 7 of the second flow are set to a predetermined inclination angle according to the thickness dimension of the glass article (here, the glass ribbon Gr) to be molded.

成形体1の幅方向両端部には、各流下壁4を流下する溶融ガラスGmの幅方向両端部を案内する合計で二対(各流下壁4につき一対)のガイド部8,8が設けられている。各ガイド部8は、例えば図示は省略するが、ガイド部8に設けられた嵌合凹部を成形体1の幅方向端部に外側から嵌め込むことで、成形体1に固定されている。 A total of two pairs of guide portions 8 and 8 (a pair for each flow down wall 4) are provided at both ends in the width direction of the molded body 1 to guide both ends in the width direction of the molten glass Gm flowing down each flow down wall 4. ing. Although not shown, each guide portion 8 is fixed to the molded body 1 by fitting the fitting recess provided in the guide portion 8 into the widthwise end portion of the molded body 1 from the outside.

ここで、各ガイド部8は、図1に示すように、第一流下面6の幅方向両端部6a,6aとつながり、第一流下面6からその幅方向に遠ざかる向きに上り勾配となる第一斜面9,9を有する。本実施形態では第一斜面9,9は何れも、図4に示すように、第一流下面6の幅方向中央部6b側から幅方向端部6a側に向かうにつれて一定の上り勾配となるように傾斜している。また、第一斜面9,9は共に第一流下面6の流下方向(ここではZ方向)全域にわたって設けられており、各第一斜面9の第一流下面6に対する傾斜角θ1はその長手方向(ここではZ方向)全域にわたって一定である。また、各第一斜面9の幅方向寸法L1もその長手方向全域にわたって一定である。この場合、第一斜面9,9は、乗り上げた溶融ガラスGmの幅方向外側への流動を規制するバンク面ともいえる。 Here, as shown in FIG. 1, each guide portion 8 is connected to both end portions 6a, 6a in the width direction of the first flow lower surface 6, and has an upward slope in a direction away from the first flow lower surface 6 in the width direction. Has 9,9. In the present embodiment, as shown in FIG. 4, the first slopes 9 and 9 have a constant ascending slope from the widthwise central portion 6b side of the first flow lower surface 6 toward the widthwise end portion 6a side. It is tilted. Further, the first slopes 9 and 9 are both provided over the entire flow direction (here, the Z direction) of the first flow lower surface 6, and the inclination angle θ1 with respect to the first flow lower surface 6 of each first slope 9 is the longitudinal direction (here). In the Z direction), it is constant over the entire area. Further, the widthwise dimension L1 of each first slope 9 is also constant over the entire longitudinal direction thereof. In this case, the first slopes 9 and 9 can be said to be bank surfaces that regulate the flow of the molten glass Gm on the outside in the width direction.

なお、第一斜面9の傾斜角θ1は、使用する溶融ガラスGmの粘度に応じて設定するのがよい。一例として、粘度が3000dPa・s以上でかつ10000dPa・s以下を示す溶融ガラスGmをオーバーフロー溝3から溢れ出させる場合、第一斜面9の傾斜角θ1を75°以上でかつ85°以下に設定するのがよい。また、粘度が100dPa・s以下を示す溶融ガラスGmをオーバーフロー溝3から溢れ出させる場合、第一斜面9の傾斜角θ2を5°以上でかつ15°以下に設定するのがよい。 The inclination angle θ1 of the first slope 9 is preferably set according to the viscosity of the molten glass Gm to be used. As an example, when molten glass Gm having a viscosity of 3000 dPa · s or more and 10000 dPa · s or less overflows from the overflow groove 3, the inclination angle θ1 of the first slope 9 is set to 75 ° or more and 85 ° or less. Is good. Further, when the molten glass Gm having a viscosity of 100 dPa · s or less overflows from the overflow groove 3, it is preferable to set the inclination angle θ2 of the first slope 9 to 5 ° or more and 15 ° or less.

なお、本発明に使用可能なガラスとしては、上述の範囲に粘度を設定できる限りにおいて特に制限されない。一例として、フッ素を実質的に含んでいない(例えばフッ素の含有比が質量%で0.1%以下の)リン酸塩系ガラスを挙げることができる。また、そのガラス組成は、例えば、質量%で、P25:25~60%、Al23:2~19%、RO(ただしRは、Mg、Ca、Sr及びBaから選択される少なくとも一種):5~45%、ZnO:0~13%、K2O:8~20%、Na2O:0~12%、及びCuO:0.3~20%である。 The glass that can be used in the present invention is not particularly limited as long as the viscosity can be set within the above range. As an example, a phosphate-based glass containing substantially no fluorine (for example, a fluorine content ratio of 0.1% or less in mass%) can be mentioned. The glass composition thereof is, for example, P 2 O 5 : 25 to 60%, Al 2 O 3 : 2 to 19%, RO (where R is selected from Mg, Ca, Sr and Ba) in mass%. At least one type): 5 to 45%, ZnO: 0 to 13%, K 2 O: 8 to 20%, Na 2 O: 0 to 12%, and Cu O: 0.3 to 20%.

また、各ガイド部8は、図1に示すように、第二流下面7の幅方向両端部7bとつながり、第二流下面7からその幅方向に遠ざかる向きに上り勾配となる第二斜面10,10を有する。本実施形態では、第二斜面10,10は何れも、図5(a)及び(b)に示すように、第二流下面7の幅方向中央部7c側から幅方向両端部7b側に向かうにつれて一定の上り勾配となるように傾斜している。また、第二斜面10,10は共に第二流下面7の流下方向(ここではZ方向)全域にわたって設けられており、各第二斜面10の第二流下面7に対する傾斜角θ2はその長手方向(ここではZ方向)全域にわたって一定である(図5(a)及び(b)を参照)。一方で、第二斜面10は、幅方向寸法L2が一定の幅寸法一定部10a(図2を参照)と、幅方向寸法L2が下方に向かうにつれて一定の割合で減少する幅寸法減少部10b(図5(a)及び(b)を参照)とからなる。この場合、第二斜面10の幅方向寸法L2は第二流下面7の下端部7aで零となり、第二流下面7の幅方向寸法は下端部7aに近づくにつれて増加する。 Further, as shown in FIG. 1, each guide portion 8 is connected to both end portions 7b in the width direction of the second flow lower surface 7, and the second slope 10 has an ascending slope in a direction away from the second flow lower surface 7 in the width direction. , 10. In the present embodiment, as shown in FIGS. 5A and 5B, the second slopes 10 and 10 are directed from the widthwise central portion 7c side of the second flow lower surface 7 to the widthwise both end portions 7b side. It is inclined so that it becomes a constant uphill slope. Further, the second slopes 10 and 10 are both provided over the entire flow direction (here, the Z direction) of the second flow bottom surface 7, and the inclination angle θ2 with respect to the second flow bottom surface 7 of each second slope 10 is the longitudinal direction thereof. It is constant over the entire area (here, in the Z direction) (see FIGS. 5 (a) and 5 (b)). On the other hand, on the second slope 10, the width dimension constant portion 10a (see FIG. 2) in which the width direction dimension L2 is constant and the width dimension reduction portion 10b (see FIG. 2) in which the width direction dimension L2 decreases at a constant rate as the width direction dimension L2 moves downward. 5 (a) and 5 (b)). In this case, the widthwise dimension L2 of the second slope 10 becomes zero at the lower end portion 7a of the second flow lower surface 7, and the widthwise dimension of the second flow lower surface 7 increases as it approaches the lower end portion 7a.

また、第二斜面10,10は、図1及び図3に示すように、第一斜面9,9と屈曲部11を介してつながっている。屈曲部11の第一斜面側領域11aは第一斜面9と同一平面上にあり、屈曲部11の第二斜面側領域11bは第二斜面10と同一平面上にある。 Further, as shown in FIGS. 1 and 3, the second slopes 10 and 10 are connected to the first slopes 9 and 9 via the bent portion 11. The first slope side region 11a of the bent portion 11 is on the same plane as the first slope 9, and the second slope side region 11b of the bent portion 11 is on the same plane as the second slope 10.

次に、以上のように構成された製造装置による板ガラスの製造方法を説明する。 Next, a method of manufacturing a flat glass by the manufacturing apparatus configured as described above will be described.

まず図1及び図3に示すように、オーバーフロー溝3からその短手方向(Y方向)両側に溶融ガラスGmを溢れ出させる。そして、溢れ出た溶融ガラスGmを一対の流下壁4,4上に供給し、各流下壁4をなす第一流下面6そして第二流下面7に沿って溶融ガラスGmを流下させる。このようにして一方の第二流下面7を流下した溶融ガラスGmと、他方の第二流下面7を流下した溶融ガラスGmはその下端部7aで融合一体化され、一枚のガラスリボンGrとして連続的に成形される。 First, as shown in FIGS. 1 and 3, the molten glass Gm overflows from the overflow groove 3 on both sides in the lateral direction (Y direction). Then, the overflowing molten glass Gm is supplied onto the pair of downflow walls 4 and 4, and the molten glass Gm is allowed to flow down along the first flow lower surface 6 and the second flow lower surface 7 forming each of the downflow walls 4. In this way, the molten glass Gm flowing down the lower surface 7 of the second flow and the molten glass Gm flowing down the lower surface 7 of the other second flow are fused and integrated at the lower end 7a to form a single glass ribbon Gr. It is continuously molded.

ここで、図6に示すように、ガイド部8が、従来の如く、第一流下面6に対して垂直に立設するガイド面8aのみを有する場合、溶融ガラスGmの流下に伴い、第一流下面6の幅方向両端部6a,6aに隣接して設けたガイド面8aに溶融ガラスGmが引き上げられることがある。溶融ガラスGmの流下量は、目的とする成形品の諸元(例えば板ガラスの厚み寸法など)に応じて適正に管理されているため、上述のように、溶融ガラスGmの幅方向両端部にガイド面8aによる引き上げ部Gm1が生じると、引き上げられた分だけ溶融ガラスGmの流下量が不足する領域Gm2が幅方向に発生する。これでは、成形の結果得られるガラスリボンGrの製品部分に、周囲に比べて厚み寸法の小さい部分が残るおそれがあり好ましくない。 Here, as shown in FIG. 6, when the guide portion 8 has only the guide surface 8a that stands perpendicular to the first flow lower surface 6 as in the conventional case, the first flow lower surface is accompanied by the flow of the molten glass Gm. The molten glass Gm may be pulled up to the guide surface 8a provided adjacent to both ends 6a and 6a in the width direction of 6. Since the amount of flow of the molten glass Gm is appropriately controlled according to the specifications of the target molded product (for example, the thickness dimension of the plate glass), as described above, the molten glass Gm is guided to both ends in the width direction. When the pulled-up portion Gm1 by the surface 8a is generated, a region Gm2 in which the flow amount of the molten glass Gm is insufficient by the amount pulled up is generated in the width direction. This is not preferable because a portion having a thickness smaller than that of the periphery may remain in the product portion of the glass ribbon Gr obtained as a result of molding.

これに対して、本発明に係る成形体1では、各ガイド部8に、第一流下面6の幅方向両端部6a,6aとつながり、第一流下面6から幅方向に遠ざかる向きに上り勾配となる第一斜面9を設けるようにした(図4を参照)。これにより、上述のようにオーバーフロー溝3から溢れ出た溶融ガラスGmが第一流下面6の幅方向両端部6a,6aに位置する第一斜面9,9と接しながら流下することで、ガイド部8に対する溶融ガラスGmの引き上げ状態が変化し、例えば第一斜面9上の溶融ガラスGmの厚み方向寸法が均される。よって、従来のように、引き上げにより極端に厚み寸法の大きな部分(引き上げ部Gm1)と小さな部分(流下量が不足する領域Gm2)が生じる事態が可及的に防止され、成形されるガラスリボンGrの製品部分に、相対的に厚み寸法の小さい部分が残る事態を回避することが可能となる。 On the other hand, in the molded body 1 according to the present invention, each guide portion 8 is connected to both end portions 6a and 6a in the width direction of the first flow lower surface 6, and the slope is upward in the direction away from the first flow lower surface 6 in the width direction. The first slope 9 is provided (see FIG. 4). As a result, as described above, the molten glass Gm overflowing from the overflow groove 3 flows down while being in contact with the first slopes 9 and 9 located at both ends 6a and 6a in the width direction of the first flow lower surface 6, thereby causing the guide portion 8 to flow down. The pulling state of the molten glass Gm changes with respect to, for example, the thickness direction dimension of the molten glass Gm on the first slope 9 is leveled. Therefore, as in the conventional case, the situation where an extremely large portion (pulled portion Gm1) and a small portion (region Gm2 in which the flow amount is insufficient) is generated due to the pulling is prevented as much as possible, and the glass ribbon Gr that is formed is formed. It is possible to avoid a situation in which a portion having a relatively small thickness dimension remains in the product portion of the above.

以上、本発明の第一実施形態を説明したが、本発明に係るガラス物品の製造装置及び製造方法は、上記実施形態には限定されることなく、本発明の範囲内で種々の形態を採ることが可能である。 Although the first embodiment of the present invention has been described above, the manufacturing apparatus and manufacturing method for the glass article according to the present invention are not limited to the above embodiments, and various forms are adopted within the scope of the present invention. It is possible.

(本発明の第二実施形態)
図7は、本発明の第二実施形態に係る成形体21をその幅方向に沿って切断した際の横断面図(XY断面図)を示している。図7に示すように、本実施形態に係る成形体21は、第一実施形態とは異なる形状の第一斜面22,22をガイド部8に有する。詳述すると、この第一斜面22は、溶融ガラスGmの流下方向(Z方向)に見た場合に凹状に湾曲した断面形状(XY断面形状)をなしている。この場合、上り勾配は幅方向中央部6b側から幅方向両端部6a側に向かうにつれて増大する。なお、第一実施形態で説明した要素と実質的に同じ要素については、第一実施形態の場合と同じ符号を付し、詳細な説明を省略する。後述する第三実施形態以降についても同様の扱いとする。
(Second Embodiment of the present invention)
FIG. 7 shows a cross-sectional view (XY cross-sectional view) when the molded body 21 according to the second embodiment of the present invention is cut along the width direction thereof. As shown in FIG. 7, the molded body 21 according to the present embodiment has first slopes 22 and 22 having a shape different from that of the first embodiment in the guide portion 8. More specifically, the first slope 22 has a cross-sectional shape (XY cross-sectional shape) that is concavely curved when viewed in the flow direction (Z direction) of the molten glass Gm. In this case, the ascending gradient increases from the central portion 6b side in the width direction toward the both end portions 6a side in the width direction. The elements substantially the same as those described in the first embodiment are designated by the same reference numerals as those in the first embodiment, and detailed description thereof will be omitted. The same applies to the third and subsequent embodiments described later.

このように、第一斜面9を凹状に湾曲した断面形状にしても、溶融ガラスGmの極端な引き上げを抑制して、厚み方向寸法の分布をなだらかにすることが可能となる。 As described above, even if the first slope 9 has a concavely curved cross-sectional shape, it is possible to suppress the extreme pulling up of the molten glass Gm and to smooth the distribution of the dimensions in the thickness direction.

もちろん、第一斜面9(22)の形状は任意であり、例えば図示は省略するが、第一流下面6の幅方向中央部6b側から幅方向端部6a側に向かうにつれて断続的に上り勾配を有する形状をなすものであってもよい。あるいは、互いに異なる傾斜角を有する二種類の傾斜平面を幅方向につなげた形態としてもよく、上述した凹状湾曲面(例えば第二実施形態に係る第一斜面22)と傾斜平面とを幅方向につなげた形態としてもよい。 Of course, the shape of the first slope 9 (22) is arbitrary, and for example, although not shown, the uphill slope is intermittently increased from the width direction center portion 6b side to the width direction end portion 6a side of the first flow lower surface 6. It may have a shape to have. Alternatively, two types of inclined planes having different inclination angles may be connected in the width direction, and the concave curved surface (for example, the first slope 22 according to the second embodiment) and the inclined plane described above may be connected in the width direction. It may be in a connected form.

また、何れも図示は省略するが、第一斜面9(22)は、必ずしも第一流下面6の流下方向(Z方向)全域にわたって設けなくともよく、必要に応じて、第一流下面6の流下方向の一部にのみ第一斜面9(22)を設けてもよい。また、第一斜面9(22)の第一流下面6に対する傾斜角θ1がその長手方向全域にわたって必ずしも一定でなくてもよく、例えば下方に向かうにつれて傾斜角θ1が減少するようにしてもよい。また、第一斜面9(22)の幅方向寸法L1がその長手方向全域にわたって必ずしも一定でなくてよく、例えば図2に示す第二斜面10と同様、相対的に上方に位置し、幅方向寸法L1が一定の幅寸法一定部と、相対的に下方に位置し、幅方向寸法L1が下方に向かうにつれて減少する幅寸法減少部とで第一斜面9(22)を構成してもよい。 Although not shown, the first slope 9 (22) does not necessarily have to be provided over the entire flow direction (Z direction) of the first flow lower surface 6, and if necessary, the flow direction of the first flow lower surface 6. The first slope 9 (22) may be provided only on a part of the above. Further, the inclination angle θ1 with respect to the lower surface 6 of the first flow of the first slope 9 (22) does not necessarily have to be constant over the entire longitudinal direction thereof, and for example, the inclination angle θ1 may decrease as it goes downward. Further, the widthwise dimension L1 of the first slope 9 (22) does not necessarily have to be constant over the entire longitudinal direction thereof. For example, like the second slope 10 shown in FIG. 2, it is located relatively upward and has a widthwise dimension. The first slope 9 (22) may be formed by a constant width dimension portion where L1 is constant and a width dimension decrease portion which is located relatively downward and decreases as the width direction dimension L1 decreases downward.

(本発明の第三実施形態)
図8は、本発明の第三実施形態に係る成形体31の断面図を示している。この成形体31は、第一流下面6に対して所定の傾斜角θ1(<90°)をなす第一斜面9と、第一斜面9とその幅方向外端部9aでつながり、第一流下面6に対して垂直に立設するガイド面32とをガイド部8に有する。
(Third Embodiment of the present invention)
FIG. 8 shows a cross-sectional view of the molded body 31 according to the third embodiment of the present invention. The molded body 31 is connected to the first slope 9 having a predetermined inclination angle θ1 (<90 °) with respect to the first flow lower surface 6, the first slope 9 and its widthwise outer end portion 9a, and is connected to the first flow lower surface 6 The guide portion 8 has a guide surface 32 that stands perpendicular to the guide surface 32.

このように、第一斜面9の幅方向外端部9aとつながるガイド面32をさらに設けることで、第一斜面9上での溶融ガラスGmの流下量が多い場合であっても、流下量が多い状態を許容しつつ、溶融ガラスGmの幅方向端部における厚み方向寸法をできる限り均等にすることができる。 In this way, by further providing the guide surface 32 connected to the outer end portion 9a in the width direction of the first slope 9, the flow amount of the molten glass Gm on the first slope 9 is large even when the flow amount is large. The thickness direction dimension at the widthwise end portion of the molten glass Gm can be made as uniform as possible while allowing a large number of states.

もちろん、この場合も、ガイド面32と組み合わせる第一斜面9の形態は任意であり、例えば図7に示す形態の第一斜面22とガイド面32とを組み合わせてもよい。 Of course, also in this case, the form of the first slope 9 to be combined with the guide surface 32 is arbitrary, and for example, the first slope 22 and the guide surface 32 in the form shown in FIG. 7 may be combined.

(本発明の第四実施形態)
図9は、本発明の第四実施形態に係る成形体41の正面図を示している。各ガイド部8は、上端面2と第一斜面9とを接続する接続面42をさらに有する。この場合、接続面42の上端部が成形体41の上端面2の短手方向端部とつながっており、接続面42の下端部が第一斜面9の上端部とつながっている。この接続面42は、例えば図10(a)及び(b)に示すように、第一流下面6の幅方向中央部6b側から幅方向端部6a側への上り勾配が、下方に向かうにつれて増加する上り勾配増加面となっている。接続面42の第一流下面6に対する傾斜角θ3はその幅方向にわたって一定である。その一方で、この傾斜角θ3は下方に向かうにつれて増加し、その下端部で第一斜面9の傾斜角θ1と等しくなる。
(Fourth Embodiment of the present invention)
FIG. 9 shows a front view of the molded body 41 according to the fourth embodiment of the present invention. Each guide portion 8 further has a connecting surface 42 connecting the upper end surface 2 and the first slope 9. In this case, the upper end portion of the connecting surface 42 is connected to the lateral end portion of the upper end surface 2 of the molded body 41, and the lower end portion of the connecting surface 42 is connected to the upper end portion of the first slope 9. As shown in FIGS. 10A and 10B, for example, the ascending gradient of the first flow lower surface 6 from the widthwise central portion 6b side to the widthwise end portion 6a side increases in the connecting surface 42 as it goes downward. It is an uphill slope increasing surface. The inclination angle θ3 with respect to the first flow lower surface 6 of the connection surface 42 is constant over the width direction thereof. On the other hand, the inclination angle θ3 increases downward, and at the lower end thereof, it becomes equal to the inclination angle θ1 of the first slope 9.

また、接続面42の幅方向寸法L3は、下方に向かうにつれて一定の割合で増加し(図10(a)及び(b)を参照)、その下端部で第一斜面9の幅方向寸法L1と等しくなる。なお、本実施形態では、接続面42の幅方向寸法L3はその上端部において零であるが、上端部において一定の幅方向寸法L3を有する状態から、下方に向かうにつれて幅方向寸法L3が増加する形態をとることも可能である。 Further, the widthwise dimension L3 of the connecting surface 42 increases at a constant rate as it goes downward (see FIGS. 10A and 10B), and the widthwise dimension L1 of the first slope 9 is formed at the lower end thereof. Become equal. In the present embodiment, the widthwise dimension L3 of the connecting surface 42 is zero at the upper end portion thereof, but the widthwise dimension L3 increases as it goes downward from the state having a constant widthwise dimension L3 at the upper end portion. It is also possible to take the form.

このように、オーバーフロー溝3が開口する上端面2と第一斜面9との間に、上端面2と第一斜面9とを接続する接続面42を設けることによって、溶融ガラスGmの第一斜面9上への流入状態を調整することができる。例えば接続面42を、下方に向かうにつれて上り勾配(第一流下面6に対する傾斜角θ3)が増加する上り勾配増加面とすることによって(図10(a)及び(b)を参照)、オーバーフロー溝3から溢れ出た直後の溶融ガラスGmはまず接続面42のうち第一流下面6と平行ないし平行に近い勾配の領域上に流入し、次第に上り勾配となって第一斜面9上へと案内される。これにより、溶融ガラスGmを円滑に第一斜面9上へと案内して、溶融ガラスGmの流下開始時の乱れを抑制しつつ第一斜面9による引き上げ抑制作用を享受することが可能となる。 In this way, by providing the connecting surface 42 connecting the upper end surface 2 and the first slope 9 between the upper end surface 2 and the first slope 9 where the overflow groove 3 opens, the first slope of the molten glass Gm is provided. 9 The inflow state to the top can be adjusted. For example, by making the connecting surface 42 an ascending slope increasing surface in which the ascending slope (inclination angle θ3 with respect to the first flow lower surface 6) increases downward (see FIGS. 10A and 10B), the overflow groove 3 Immediately after overflowing from the molten glass Gm, the molten glass Gm first flows into the region of the connecting surface 42 having a gradient parallel to or close to the first flow lower surface 6, and gradually becomes an upward gradient and is guided onto the first slope 9. .. This makes it possible to smoothly guide the molten glass Gm onto the first slope 9 and enjoy the pull-up suppressing action of the first slope 9 while suppressing the turbulence at the start of the flow of the molten glass Gm.

(本発明の第五実施形態)
なお、接続面42は、上述した上り勾配増加面以外の形態をとることも可能である。図11(a)及び(b)は、本発明の第五実施形態に係る接続面42のXY断面図を示している。図11に示すように、本実施形態に係る接続面42は、下方に向かうにつれて幅方向寸法L4が増加する幅寸法増加面となっている。一方で、各接続面42の第一流下面6に対する傾斜角θ4はその長手方向(ここではZ方向)全域にわたって一定である。この場合、上り勾配となる幅方向領域が下方に向かうにつれて増加するので、オーバーフロー溝3から溢れ出た溶融ガラスGmを円滑に第一斜面9上へと案内することができる。
(Fifth Embodiment of the present invention)
The connecting surface 42 may take a form other than the above-mentioned uphill gradient increasing surface. 11 (a) and 11 (b) show an XY sectional view of a connecting surface 42 according to a fifth embodiment of the present invention. As shown in FIG. 11, the connecting surface 42 according to the present embodiment is a width dimension increasing surface in which the width direction dimension L4 increases toward the downward direction. On the other hand, the inclination angle θ4 of each connection surface 42 with respect to the first flow lower surface 6 is constant over the entire longitudinal direction (here, the Z direction). In this case, since the width direction region having an uphill slope increases downward, the molten glass Gm overflowing from the overflow groove 3 can be smoothly guided onto the first slope 9.

(本発明の第六実施形態)
図12は、本発明の第六実施形態に係る成形体41の正面図、図13(a)及び(b)は、接続面42のXY断面図を示している。図13に示すように、本実施形態に係る接続面42は、図10と同様、下方に向かうにつれて上り勾配(第一流下面6に対する傾斜角θ5が増加する上り勾配増加面である。一方で、図12に示すように、各接続面42の幅方向寸法L5はその長手方向全域にわたって一定であり、第一斜面9の幅方向寸法L1に等しい。このように接続面42の形状を定めることによって、溶融ガラスGmの流下開始時の乱れを効果的に抑制しつつ、第一斜面9による引き上げ抑制作用をさらに高めることが可能となる。
(Sixth Embodiment of the present invention)
12 is a front view of the molded body 41 according to the sixth embodiment of the present invention, and FIGS. 13 (a) and 13 (b) are XY cross-sectional views of the connecting surface 42. As shown in FIG. 13, the connection surface 42 according to the present embodiment is an upslope increasing surface in which the uphill slope (inclination angle θ5 with respect to the first flow lower surface 6 increases) as it goes downward, as in FIG. As shown in FIG. 12, the widthwise dimension L5 of each connecting surface 42 is constant over the entire longitudinal direction and is equal to the widthwise dimension L1 of the first slope 9. By defining the shape of the connecting surface 42 in this way. It is possible to further enhance the pull-up suppressing action of the first slope 9 while effectively suppressing the turbulence at the start of the flow of the molten glass Gm.

(本発明の第七実施形態)
図14は、本発明の第七実施形態に係る成形体51の縦断面図を示している。図14に示すように、この成形体51は、ガイド部8が第一斜面9と第二斜面10とを有すると共に、第一斜面9と第二斜面10とが、第一実施形態とは異なる形態でつながっている。すなわち、第一実施形態では、第一斜面9と第二斜面10とが屈曲部11(図3を参照)を介してつながっているのに対し、本実施形態では、幅方向に見た場合に凸状に湾曲した断面形状(YZ断面形状)をなす凸面部52を介してつながっている。なお、第一斜面9と第二斜面10の高さ(第一流下面6及び第二流下面7からの法線方向離間距離)は、図11に示すように同じであってもよいし、異なっていてもよい。
(Seventh Embodiment of the present invention)
FIG. 14 shows a vertical sectional view of the molded body 51 according to the seventh embodiment of the present invention. As shown in FIG. 14, in this molded body 51, the guide portion 8 has the first slope 9 and the second slope 10, and the first slope 9 and the second slope 10 are different from the first embodiment. It is connected in form. That is, in the first embodiment, the first slope 9 and the second slope 10 are connected via the bent portion 11 (see FIG. 3), whereas in the present embodiment, when viewed in the width direction. It is connected via a convex surface portion 52 having a convexly curved cross-sectional shape (YZ cross-sectional shape). The heights of the first slope 9 and the second slope 10 (distance in the normal direction from the first flow lower surface 6 and the second flow lower surface 7) may be the same or different as shown in FIG. May be.

このように、第一流下面と第二流下面にそれぞれ第一斜面と第二斜面を設ける場合、双方の斜面同士をつなげることで、好ましくは上述のように凸状に湾曲した断面形状をなす凸面部を介してつなげることで、第一斜面上を流下する溶融ガラスを円滑に第二斜面上に導入することができる。これにより、上述した第二斜面による作用を安定的に得ることが可能となる。 In this way, when the first slope and the second slope are provided on the lower surface of the first flow and the lower surface of the second flow, respectively, by connecting both slopes, it is preferable to form a convex surface having a convex curved cross-sectional shape as described above. By connecting via the portions, the molten glass flowing down on the first slope can be smoothly introduced onto the second slope. This makes it possible to stably obtain the action of the second slope described above.

1,21,31,41,51 成形体
2 上端面
3 オーバーフロー溝
4 流下壁
5 供給管
6 第一流下面
7 第二流下面
8 ガイド部
8a ガイド面
9,22 第一斜面
10 第二斜面
10a 幅寸法一定部
10b 幅寸法減少部
32 垂直面
42 勾配増加面
52 凸面部
Gm 溶融ガラス
Gm1 引き上げ部
Gm2 溶融ガラスが不足する領域
Gr ガラスリボン
1,21,31,41,51 Molded body 2 Upper end surface 3 Overflow groove 4 Flow down wall 5 Supply pipe 6 First flow lower surface 7 Second flow lower surface 8 Guide part 8a Guide surface 9, 22 First slope 10 Second slope 10a Width Constant dimension part 10b Width dimension decrease part 32 Vertical surface 42 Gradient increase surface 52 Convex surface part Gm Molten glass Gm1 Pulling part Gm2 Area where molten glass is insufficient Gr Glass ribbon

Claims (12)

樋形状をなし溶融ガラスが溢れ出るオーバーフロー溝と、前記オーバーフロー溝から溢れ出た前記溶融ガラスが流下する一対の流下壁と、前記各流下壁の幅方向両端部に設けられ前記溶融ガラスの流下を案内する合計で二対のガイド部とを備え、
前記一対の流下壁は、前記オーバーフロー溝が設けられた上端面に隣接し下方に延びる一対の第一流下面と、前記第一流下面の下方に位置し、下方に向かうにつれて互いに接近して下端で合流する逆斜面である一対の第二流下面とを有する、ガラス物品の製造装置であって、
前記各ガイド部は、前記第一流下面の幅方向端部とつながり、前記第一流下面から幅方向に遠ざかるのに伴って前記第一流下面から前記溶融ガラスが流下する側に向けて立ち上がる上り勾配となる第一斜面を有することを特徴とするガラス物品の製造装置。
An overflow groove that has a gutter shape and overflows the molten glass, a pair of flow-down walls through which the molten glass overflows from the overflow groove flows down, and the flow-down of the molten glass provided at both ends in the width direction of each of the flow-down walls. Equipped with a total of two pairs of guides to guide
The pair of downflow walls are located below the pair of first flow bottom surfaces that are adjacent to the upper end surface provided with the overflow groove and extend downward, and approach each other as they go downward and merge at the lower end. A device for manufacturing a glass article, which has a pair of second flow lower surfaces that are reverse slopes.
Each of the guide portions is connected to the widthwise end portion of the lower surface of the first stream, and has an ascending slope that rises from the lower surface of the first stream toward the side where the molten glass flows down as the surface moves away from the lower surface of the first stream in the width direction. A device for manufacturing a glass article, characterized by having a first slope.
前記ガイド部は、前記第一流下面に対して立設したガイド面をさらに有し、
前記第一斜面は、前記ガイド面と前記第一流下面とをつなぐ、一定の幅方向寸法及び前記第一流下面に対する一定の傾斜角を有するバンク面である請求項1に記載のガラス物品の製造装置。
The guide portion further has a guide surface erected with respect to the lower surface of the first flow.
The apparatus for manufacturing a glass article according to claim 1, wherein the first slope is a bank surface connecting the guide surface and the lower surface of the first stream and having a constant width direction dimension and a constant inclination angle with respect to the lower surface of the first stream. ..
前記第一斜面は、前記溶融ガラスの流下方向に見た場合に凹状に湾曲した断面形状を有する凹曲面である請求項1に記載のガラス物品の製造装置。 The apparatus for manufacturing a glass article according to claim 1, wherein the first slope is a concave curved surface having a concavely curved cross-sectional shape when viewed in the flow direction of the molten glass. 前記各ガイド部は、前記上端面と前記第一斜面とを接続する接続面をさらに有する請求項1に記載のガラス物品の製造装置。 The apparatus for manufacturing a glass article according to claim 1, wherein each guide portion further has a connecting surface connecting the upper end surface and the first slope. 前記接続面は、下方に向かうにつれて前記上り勾配が増加する上り勾配増加面である請求項4に記載のガラス物品の製造装置。 The apparatus for manufacturing a glass article according to claim 4, wherein the connecting surface is an ascending gradient increasing surface in which the ascending gradient increases as it goes downward. 前記各ガイド部は、前記第二流下面の幅方向両端部とつながり、前記第二流下面から幅方向に遠ざかるにつれて前記第二流下面から前記溶融ガラスが流下する側に向けて立ち上がる上り勾配となる第二斜面をさらに有する請求項1~4の何れか一項に記載のガラス物品の製造装置。 Each of the guide portions is connected to both ends in the width direction of the lower surface of the second stream, and has an ascending slope that rises from the lower surface of the second stream toward the side where the molten glass flows down as the distance from the lower surface of the second stream increases in the width direction. The apparatus for manufacturing a glass article according to any one of claims 1 to 4, further comprising a second slope. 前記第一斜面と前記第二斜面とが、前記溶融ガラスの流下方向に沿って連続して設けられ互いにつながっている請求項6に記載のガラス物品の製造装置。 The apparatus for manufacturing a glass article according to claim 6, wherein the first slope and the second slope are continuously provided along the flow direction of the molten glass and are connected to each other. 前記第一斜面と前記第二斜面とが、幅方向に見た場合に凸状に湾曲した断面形状をなす凸面部を介してつながっている請求項7に記載のガラス物品の製造装置。 The apparatus for manufacturing a glass article according to claim 7, wherein the first slope and the second slope are connected via a convex surface portion having a cross-sectional shape that is convexly curved when viewed in the width direction. 少なくとも前記第一斜面と、前記第一流下面とが、白金または白金合金により被覆されている請求項1~8の何れか一項に記載のガラス物品の製造装置。 The apparatus for manufacturing a glass article according to any one of claims 1 to 8, wherein at least the first slope and the lower surface of the first flow are coated with platinum or a platinum alloy. 樋形状をなし溶融ガラスが溢れ出るオーバーフロー溝と、前記オーバーフロー溝から溢れ出た前記溶融ガラスが流下する一対の流下壁と、前記各流下壁の幅方向両端部に設けられ前記溶融ガラスの流下を案内する合計で二対のガイド部とを備え、
前記一対の流下壁は、前記オーバーフロー溝が設けられた上端面に隣接し下方に延びる一対の第一流下面と、前記第一流下面の下方に位置し、下方に向かうにつれて互いに接近して下端で合流する逆斜面である一対の第二流下面とを有する製造装置を用いて、ガラス物品を製造するガラス物品の製造方法であって、
前記各ガイド部は、前記第一流下面の幅方向端部とつながり、前記第一流下面からその幅方向に遠ざかるのに伴って前記第一流下面から前記溶融ガラスが流下する側に向けて立ち上がる上り勾配となる第一斜面を有し、
前記オーバーフロー溝から前記溶融ガラスを溢れ出させて、前記溶融ガラスが前記第一斜面と接しながら流下するようにした、ガラス物品の製造方法。
An overflow groove that has a gutter shape and overflows the molten glass, a pair of flow-down walls through which the molten glass overflows from the overflow groove flows down, and the flow-down of the molten glass provided at both ends in the width direction of each of the flow-down walls. Equipped with a total of two pairs of guides to guide
The pair of downflow walls are located below the pair of first flow bottom surfaces that are adjacent to the upper end surface provided with the overflow groove and extend downward, and approach each other as they go downward and merge at the lower end. It is a method of manufacturing a glass article, which manufactures a glass article by using a manufacturing apparatus having a pair of second flow lower surfaces which are reverse slopes.
Each of the guide portions is connected to the widthwise end of the lower surface of the first stream, and rises from the lower surface of the first stream toward the side where the molten glass flows down as the lower surface of the first stream moves away from the lower surface of the first stream in the width direction. It has a first slope that becomes a slope,
A method for manufacturing a glass article, wherein the molten glass overflows from the overflow groove so that the molten glass flows down while being in contact with the first slope.
前記第一斜面の前記上り勾配を75°以上でかつ85°以下に設定した状態で、3000dPa・s以上でかつ10000dPa・s以下に調整した前記溶融ガラスを前記オーバーフロー溝から溢れ出させる請求項10に記載のガラス物品の製造方法。 10. Claim 10 for overflowing the molten glass adjusted to 3000 dPa · s or more and 10000 dPa · s or less in a state where the ascending slope of the first slope is set to 75 ° or more and 85 ° or less. The method for manufacturing a glass article according to. 前記第一斜面の前記上り勾配を5°以上でかつ15°以下に設定した状態で、100dPa・s以下に調整した前記溶融ガラスを前記オーバーフロー溝から溢れ出させる請求項10に記載のガラス物品の製造方法。 The glass article according to claim 10, wherein the molten glass adjusted to 100 dPa · s or less overflows from the overflow groove in a state where the uphill slope of the first slope is set to 5 ° or more and 15 ° or less. Production method.
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