TWI613158B - Method for producing glass substrate and device for manufacturing glass substrate - Google Patents

Method for producing glass substrate and device for manufacturing glass substrate Download PDF

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TWI613158B
TWI613158B TW104108355A TW104108355A TWI613158B TW I613158 B TWI613158 B TW I613158B TW 104108355 A TW104108355 A TW 104108355A TW 104108355 A TW104108355 A TW 104108355A TW I613158 B TWI613158 B TW I613158B
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rotating shaft
furnace
glass
slow cooling
temperature gradient
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TW104108355A
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TW201536697A (en
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Hirokazu Hiwatashi
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Avanstrate Inc
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    • 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
    • C03B17/067Forming glass sheets combined with thermal conditioning of the sheets

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

Description

玻璃基板之製造方法及玻璃基板之製造裝置 Method for producing glass substrate and device for manufacturing glass substrate

本發明係關於一種製造玻璃基板之玻璃基板之製造方法及製造裝置。 The present invention relates to a method and apparatus for producing a glass substrate for manufacturing a glass substrate.

用於液晶顯示器或電漿顯示器等平板顯示器之玻璃基板(以下,稱為「FPD(Flat Panel Display,平板顯示器)用玻璃基板」)係使用厚度薄至例如0.5~0.7mm之玻璃板。關於FPD用玻璃基板,例如第1代時尺寸為300×400mm,但第10代時尺寸成為2850×3050mm。 A glass substrate (hereinafter referred to as a "glass substrate for FPD (Flat Panel Display)) for a flat panel display such as a liquid crystal display or a plasma display is a glass plate having a thickness of, for example, 0.5 to 0.7 mm. The glass substrate for FPD has, for example, a size of 300×400 mm in the first generation, but a size of 2850×3050 mm in the tenth generation.

於製造FPD用玻璃基板時,存在使用溢流下拉法之情形。溢流下拉法包含如下步驟:於成形爐中藉由使熔融玻璃自成形體之上部溢出(溢流)而於成形體之下方成形薄片玻璃(板狀玻璃);以及冷卻步驟,其使薄片玻璃於緩冷爐中緩冷。於緩冷爐中,將薄片玻璃拉入至成對之輥間,利用輥將薄片玻璃一面向下方搬送一面拉長為所需之厚度,之後使薄片玻璃緩冷。此後,藉由將薄片玻璃切斷成特定尺寸而形成玻璃基板。 When manufacturing a glass substrate for FPD, there is a case where an overflow down-draw method is used. The overflow down-draw method includes the steps of: forming a sheet glass (sheet glass) under the formed body by overflowing (overflowing) the molten glass from the upper portion of the formed body in the forming furnace; and a cooling step of making the thin glass Slowly cool in a slow cooling furnace. In the slow cooling furnace, the sheet glass is pulled between the paired rolls, and the sheet glass is stretched to a desired thickness by the roller facing downward, and then the sheet glass is slowly cooled. Thereafter, the glass substrate is formed by cutting the sheet glass into a specific size.

於溢流下拉法中,薄片玻璃之緩冷係以高於應變點且低於緩冷點之溫度進行,搬送薄片玻璃之輥附近之溫度係保持為相對較高之狀態(溫度高時為600℃以上)。一般而言,使輥旋轉之旋轉軸由金屬製造,因此強度會隨著溫度上升而下降,從而容許應力下降而導致軸變形之危險性升高。若軸於已變形之狀態下旋轉,則安裝於軸前端附近之輥搬送玻璃基板之速度會產生週期性變動,而成為產生縱(拉伸)方 向上之厚度偏差、或翹曲之原因。於專利文獻1中揭示有如下內容:為了防止此種旋轉軸之變形,例如使軸為中空,並使熱介質於其中空空間內流動,藉此將旋轉軸冷卻。 In the overflow down-draw method, the slow cooling of the flake glass is performed at a temperature higher than the strain point and lower than the slow cooling point, and the temperature near the roll for conveying the flake glass is kept relatively high (600 when the temperature is high) °C or more). In general, since the rotating shaft for rotating the roller is made of metal, the strength is lowered as the temperature rises, thereby allowing the stress to drop and the risk of deformation of the shaft to rise. When the shaft rotates in a deformed state, the speed at which the roller attached to the front end of the shaft conveys the glass substrate periodically changes, and the longitudinal (stretching) side is generated. The thickness deviation in the upward direction, or the cause of the warpage. Patent Document 1 discloses that in order to prevent deformation of such a rotating shaft, for example, the shaft is hollow and the heat medium flows in the hollow space, whereby the rotating shaft is cooled.

[先前技術文獻] [Previous Technical Literature] [專利文獻] [Patent Literature]

[專利文獻1]日本專利特開平5-124826號公報 [Patent Document 1] Japanese Patent Laid-Open No. Hei 5-124826

且說,關於自成形體溢流之熔融玻璃,沿著熔融玻璃之流動方向預先設計薄片玻璃之寬度方向之溫度分佈,以使翹曲及應變不會超出需要地變大,且以使薄片玻璃成為所設計之溫度分佈之方式,使用冷卻裝置或加熱器等進行嚴格之溫度管理。因此,必須將與薄片玻璃接觸之輥維持為一定溫度。 In addition, regarding the molten glass overflowing from the molded body, the temperature distribution in the width direction of the sheet glass is previously designed along the flow direction of the molten glass so that the warpage and strain do not become larger than necessary, and the thin glass is made The temperature distribution is designed in such a way that strict temperature management is performed using a cooling device or a heater. Therefore, it is necessary to maintain the roller in contact with the sheet glass at a certain temperature.

另一方面,懸臂支持輥之旋轉軸係貫通成形爐之爐壁而設置,於爐壁內外產生溫度梯度。若旋轉軸之長度方向之溫度梯度變大,則存在如下問題:產生於旋轉軸之應力變大,而有旋轉軸產生變形之虞。亦考慮將容許應力大於溫度梯度所致之應力之材料用於旋轉軸,但能選擇之材料有限。製造用於FPD之低溫多晶矽TFT(Thin Film Transistor,薄膜電晶體)液晶用玻璃基板所使用之玻璃之應變點或緩冷點等玻璃特異點較高,因此成形時之溫度較高,於成形後進行緩冷時之溫度亦變高,於緩冷爐內外溫度梯度變大,上述問題變得顯著。 On the other hand, the rotation axis of the cantilever support roller is provided through the furnace wall of the forming furnace to generate a temperature gradient inside and outside the furnace wall. When the temperature gradient in the longitudinal direction of the rotating shaft becomes large, there is a problem that the stress generated on the rotating shaft becomes large, and the rotating shaft is deformed. Materials that allow stresses greater than those due to temperature gradients are also considered for rotating shafts, but materials that can be selected are limited. The glass singular point such as the strain point or the slow cooling point of the glass used for the glass substrate for the low temperature polycrystalline germanium TFT (Thin Film Transistor) for FPD is high, so the temperature at the time of molding is high, after the formation The temperature at the time of slow cooling also becomes high, and the temperature gradient inside and outside the slow cooling furnace becomes large, and the above problems become remarkable.

因此,本發明之目的在於提供一種能夠如所設計般精度良好地再現薄片玻璃之溫度分佈,且可使產生於搬送薄片玻璃之輥之旋轉軸之應力下降的玻璃基板之製造方法及製造裝置。 Accordingly, an object of the present invention is to provide a method and a manufacturing apparatus for a glass substrate which can accurately reproduce the temperature distribution of the sheet glass as designed, and which can reduce the stress generated on the rotating shaft of the sheet for conveying the sheet glass.

為了解決上述問題,本發明之第1態樣之特徵在於:其係如下一 種玻璃基板之製造方法,即,於成形爐中使熔融玻璃自成形體溢流而成形連續之薄片玻璃,且於緩冷爐中一面利用輥夾持上述薄片玻璃並向下方搬送一面進行緩冷;且上述緩冷爐具有壁,該壁劃分供搬送上述薄片玻璃之爐內、及外部空間之爐外,上述輥由貫通上述成形爐之上述壁之旋轉軸懸臂支持,且設置於上述緩冷爐之溫度梯度調節機構係以減小上述旋轉軸之長度方向之溫度梯度之方式進行調節。 In order to solve the above problems, the first aspect of the present invention is characterized in that it is as follows A method for producing a glass substrate, in which a molten glass is poured from a molded body in a forming furnace to form a continuous sheet glass, and the sheet glass is held by a roll in a slow cooling furnace and conveyed downward while being slowly cooled. And the slow cooling furnace has a wall which is divided into a furnace for conveying the sheet glass and an outer space, wherein the roller is supported by a rotating shaft that penetrates the wall of the forming furnace, and is disposed on the slow cooling The temperature gradient adjustment mechanism of the furnace is adjusted to reduce the temperature gradient in the longitudinal direction of the rotating shaft.

上述溫度梯度調節機構亦可為對上述旋轉軸進行保溫之保溫機構、或對上述旋轉軸進行加熱之加熱機構。 The temperature gradient adjusting mechanism may be a heat insulating mechanism that heats the rotating shaft or a heating mechanism that heats the rotating shaft.

上述保溫機構亦可藉由自上述成形爐之內壁面朝上述旋轉軸之上述輥側延伸之隔熱材料對上述旋轉軸進行保溫。 The heat insulating means may heat the rotating shaft by a heat insulating material extending from the inner wall surface of the forming furnace toward the roll side of the rotating shaft.

上述加熱機構亦可藉由向上述旋轉軸之內部供給介質而對上述旋轉軸進行加熱,該介質自上述旋轉軸之設置有上述輥之部分向貫通上述壁之部分輸送熱。 The heating means may heat the rotating shaft by supplying a medium to the inside of the rotating shaft, and the medium transports heat from a portion of the rotating shaft where the roller is provided to a portion penetrating the wall.

較佳為,以上述旋轉軸之長度方向之溫度梯度之最大值成為2500℃/m以下之方式進行調整。 Preferably, the temperature gradient in the longitudinal direction of the rotating shaft is adjusted so that the maximum value is 2500 ° C / m or less.

較佳為,以上述隔熱材料之上述輥側之端部位置上之上述旋轉軸之長度方向之溫度梯度成為1300℃/m以下之方式進行調整。 Preferably, the temperature gradient in the longitudinal direction of the rotating shaft at the position of the end portion on the roll side of the heat insulating material is adjusted to be 1300 ° C/m or less.

本發明之第2態樣係一種玻璃基板之製造裝置,其具有:成形爐,其具有使熔融玻璃溢流而成形連續之薄片玻璃之成形體;以及緩冷爐,其一面夾持上述薄片玻璃並向下方搬送一面進行緩冷;上述緩冷爐包括:壁,其劃分供搬送上述薄片玻璃之爐內及外部空間之爐外; 旋轉軸,其貫通上述壁;輥,其設置於上述旋轉軸之前端部,且由上述旋轉軸懸臂支持;以及溫度梯度調節機構,其以上述旋轉軸之長度方向之溫度梯度變小之方式進行調節。 A second aspect of the present invention provides a glass substrate manufacturing apparatus comprising: a molding furnace having a molded body in which molten glass is overflowed to form a continuous sheet glass; and a slow cooling furnace in which the sheet glass is sandwiched And transporting one side downward to perform slow cooling; the slow cooling furnace includes: a wall which is divided into a furnace for conveying the inside and outside of the sheet glass; a rotating shaft penetrating the wall; a roller disposed at a front end of the rotating shaft and supported by the rotating shaft cantilever; and a temperature gradient adjusting mechanism configured to reduce a temperature gradient in a longitudinal direction of the rotating shaft Adjustment.

根據本發明,藉由減小對搬送薄片玻璃之輥進行支持之旋轉軸之長度方向之溫度梯度,可使由溫度梯度引起而產生於旋轉軸之應力下降,從而能夠防止旋轉軸之變形。 According to the present invention, by reducing the temperature gradient in the longitudinal direction of the rotating shaft that supports the roller for conveying the sheet glass, the stress generated on the rotating shaft due to the temperature gradient can be lowered, and deformation of the rotating shaft can be prevented.

30‧‧‧輥 30‧‧‧ Roll

31‧‧‧旋轉軸 31‧‧‧Rotary axis

32‧‧‧內管 32‧‧‧Inside

33‧‧‧隔熱材料 33‧‧‧Insulation materials

100‧‧‧熔解裝置 100‧‧‧melting device

101‧‧‧熔解槽 101‧‧‧melting tank

102‧‧‧澄清槽 102‧‧‧Clarification tank

103‧‧‧攪拌槽 103‧‧‧Stirring tank

103a‧‧‧攪拌器 103a‧‧‧Agitator

104‧‧‧移送管 104‧‧‧Transfer tube

105‧‧‧移送管 105‧‧‧Transfer tube

106‧‧‧玻璃供給管 106‧‧‧Glass supply tube

200‧‧‧成形裝置 200‧‧‧Forming device

201‧‧‧成形爐 201‧‧‧Forming furnace

201A‧‧‧上部成形爐 201A‧‧‧Upper forming furnace

201B‧‧‧下部成形爐 201B‧‧‧ Lower forming furnace

202‧‧‧緩冷爐 202‧‧‧ Slow cooling furnace

2021、2022、…、202n‧‧‧間隔板 2031, 2022, ..., 202n‧‧‧ spacer

203‧‧‧壁 203‧‧‧ wall

210‧‧‧成形體 210‧‧‧Formed body

212‧‧‧溝槽 212‧‧‧ trench

213‧‧‧下方端部 213‧‧‧Lower end

220‧‧‧氛圍間隔構件 220‧‧‧Interval spacers

230‧‧‧冷卻構件 230‧‧‧Cooling components

240‧‧‧冷卻裝置 240‧‧‧Cooling device

241‧‧‧端部冷卻單元 241‧‧‧End cooling unit

242‧‧‧中央冷卻單元 242‧‧‧Central Cooling Unit

242a‧‧‧上段單元 242a‧‧‧Upper unit

242b‧‧‧中段單元 242b‧‧ mid-unit

242c‧‧‧下段單元 242c‧‧‧Next unit

2501、2502、…、250n‧‧‧搬送構件 2501, 2502, ..., 250n‧‧‧ transport components

2701、2702、270n‧‧‧溫度調整裝置 2701, 2702, 270n‧‧‧ temperature adjustment device

300‧‧‧切斷裝置 300‧‧‧cutting device

MG‧‧‧熔融玻璃 MG‧‧‧ molten glass

SG‧‧‧薄片玻璃 SG‧‧‧Sheet glass

ST1‧‧‧熔解步驟 ST1‧‧‧melting step

ST2‧‧‧澄清步驟 ST2‧‧‧Clarification steps

ST3‧‧‧均質化步驟 ST3‧‧‧ homogenization steps

ST4‧‧‧供給步驟 ST4‧‧‧ supply steps

ST5‧‧‧成形步驟 ST5‧‧‧ forming steps

ST6‧‧‧緩冷步驟 ST6‧‧‧ Slow cooling step

ST7‧‧‧切斷步驟 ST7‧‧‧cutting steps

圖1係表示玻璃基板之製造方法之流程之圖。 Fig. 1 is a view showing the flow of a method of manufacturing a glass substrate.

圖2係玻璃基板之製造裝置之概略圖。 2 is a schematic view showing a manufacturing apparatus of a glass substrate.

圖3係圖2所示之成形裝置之概略圖。 Figure 3 is a schematic view of the forming apparatus shown in Figure 2.

圖4係沿圖3之IV-IV之箭頭方向觀察之剖視圖。 Figure 4 is a cross-sectional view taken along the line of arrows IV-IV of Figure 3 .

圖5係圖3、圖4所示之搬送構件之剖視圖。 Fig. 5 is a cross-sectional view showing the conveying member shown in Figs. 3 and 4;

圖6係表示搬送輥之旋轉軸之長度方向之位置與溫度之關係的圖。 Fig. 6 is a view showing the relationship between the position in the longitudinal direction of the rotating shaft of the conveying roller and the temperature.

圖7係表示搬送輥之旋轉軸之長度方向之位置與應力之關係的圖。 Fig. 7 is a view showing the relationship between the position in the longitudinal direction of the rotating shaft of the conveying roller and the stress.

以下,對本發明之玻璃基板之製造方法及玻璃基板製造裝置進行說明。 Hereinafter, a method of producing a glass substrate and a glass substrate manufacturing apparatus of the present invention will be described.

圖1係表示本實施形態之玻璃基板之製造方法之步驟之一例的圖。 Fig. 1 is a view showing an example of a procedure of a method for producing a glass substrate of the embodiment.

(玻璃基板之製造方法之整體概要) (Overall outline of the manufacturing method of the glass substrate)

玻璃基板之製造方法主要包括熔解步驟(ST1)、澄清步驟(ST2)、 均質化步驟(ST3)、供給步驟(ST4)、成形步驟(ST5)、緩冷步驟(ST6)、以及切斷步驟(ST7)。此外,亦可包括研削步驟、研磨步驟、清洗步驟、檢查步驟、捆包步驟等。所製造之玻璃基板係視需要藉由捆包步驟被積層而搬送至交納目的地之業者。 The manufacturing method of the glass substrate mainly includes a melting step (ST1), a clarification step (ST2), The homogenization step (ST3), the supply step (ST4), the molding step (ST5), the slow cooling step (ST6), and the cutting step (ST7). In addition, a grinding step, a grinding step, a washing step, an inspection step, a baling step, and the like may also be included. The glass substrate to be produced is transported to the delivery destination by laminating steps as needed.

於熔解步驟(ST1)中,藉由對玻璃原料進行加熱而製作熔融玻璃。熔融玻璃之加熱可藉由通電加熱進行,上述通電加熱係使電流通而使熔融玻璃自身發熱從而將其加熱。進而,亦可利用燃燒器之火焰輔助性地進行加熱而熔解玻璃原料。 In the melting step (ST1), molten glass is produced by heating the glass raw material. The heating of the molten glass can be performed by electric heating, and the electric heating causes the electric current to pass, and the molten glass itself generates heat to heat it. Further, the glass raw material may be melted by assisting heating by a flame of a burner.

再者,熔融玻璃含有澄清劑。作為澄清劑,已知有氧化錫、亞砷酸、銻等,但並無特別限制。然而,就減輕環境負擔之方面來講,較佳為使用氧化錫作為澄清劑。 Further, the molten glass contains a clarifying agent. As the clarifying agent, tin oxide, arsenious acid, cerium, or the like is known, but is not particularly limited. However, in terms of reducing the environmental burden, it is preferred to use tin oxide as a fining agent.

於澄清步驟(ST2)中,藉由使熔融玻璃升溫,而產生包含熔融玻璃中所含之氧、CO2或SO2之氣泡。該氣泡吸收因澄清劑之還原反應產生之氧氣而成長,並浮起至熔融玻璃之液面而被釋放。其後,於澄清步驟中,使熔融玻璃之溫度下降,藉此,藉由澄清劑之還原反應而獲得之還原物質進行氧化反應。藉此,殘留於熔融玻璃之氣泡中之氧氣等氣體成分被再次吸收至熔融玻璃中,從而氣泡消失。利用澄清劑進行之氧化反應及還原反應係藉由控制熔融玻璃之溫度而進行。 In the clarification step (ST2), by heating the molten glass, bubbles containing oxygen, CO 2 or SO 2 contained in the molten glass are generated. The bubble is absorbed by the oxygen generated by the reduction reaction of the clarifying agent, and is floated to the surface of the molten glass to be released. Thereafter, in the clarification step, the temperature of the molten glass is lowered, whereby the reducing substance obtained by the reduction reaction of the clarifying agent is subjected to an oxidation reaction. Thereby, the gas component such as oxygen remaining in the bubbles of the molten glass is again absorbed into the molten glass, and the bubbles disappear. The oxidation reaction and the reduction reaction by the clarifying agent are carried out by controlling the temperature of the molten glass.

再者,澄清步驟亦可使用減壓消泡方式,該減壓消泡方式係使存在於熔融玻璃之氣泡於減壓氛圍中成長並消泡。減壓消泡方式於不使用澄清劑之方面有效。然而,減壓消泡方式會使裝置複雜化及大型化。因此,較佳為採用使用澄清劑並使熔融玻璃溫度上升之澄清方法。 Further, the clarification step may also employ a vacuum defoaming method in which bubbles existing in the molten glass are grown and defoamed in a reduced pressure atmosphere. The vacuum defoaming mode is effective in not using a clarifying agent. However, the vacuum defoaming method complicates and enlarges the apparatus. Therefore, it is preferred to use a clarifying method using a clarifying agent to raise the temperature of the molten glass.

於均質化步驟(ST3)中,藉由使用攪拌器對熔融玻璃進行攪拌,而進行玻璃成分之均質化。藉此,可減少引起條紋等之玻璃之組成不均。 In the homogenization step (ST3), the molten glass is stirred by using a stirrer to homogenize the glass component. Thereby, the composition unevenness of the glass which causes a stripe etc. can be reduced.

於供給步驟(ST4)中,將攪拌後之熔融玻璃供給至成形裝置。 In the supplying step (ST4), the molten glass after the stirring is supplied to the forming apparatus.

成形步驟(ST5)及緩冷步驟(ST6)係於成形裝置中進行。 The forming step (ST5) and the slow cooling step (ST6) are carried out in a forming apparatus.

於成形步驟(ST5)中,將熔融玻璃成形為薄片玻璃,並形成薄片玻璃之流動。於成形時使用溢流下拉法。 In the forming step (ST5), the molten glass is formed into a sheet glass, and a flow of the sheet glass is formed. An overflow down-draw method is used during forming.

於緩冷步驟(ST6)中,以成形並流動之薄片玻璃成為所需之厚度且不產生內部應變之方式、進而以不產生翹曲之方式進行冷卻。 In the slow cooling step (ST6), the sheet glass which is formed and flows has a desired thickness and does not generate internal strain, and is further cooled without causing warpage.

於切斷步驟(ST7)中,藉由將緩冷後之薄片玻璃切斷成特定之長度,而獲得板狀玻璃基板。經切斷之玻璃基板進而被切斷成特定之尺寸,而製作目標尺寸之玻璃基板。 In the cutting step (ST7), a sheet glass substrate is obtained by cutting the slowly cooled sheet glass to a specific length. The cut glass substrate is further cut into a specific size to produce a glass substrate of a target size.

圖2係進行本實施形態中之熔解步驟(ST1)~切斷步驟(ST7)之玻璃基板之製造裝置之概略圖。如圖2所示,玻璃基板之製造裝置主要包括熔解裝置100、成形裝置200、及切斷裝置300。熔解裝置100包括熔解槽101、澄清管120、攪拌槽103、移送管104、105、及玻璃供給管106。 Fig. 2 is a schematic view showing a manufacturing apparatus of a glass substrate on which the melting step (ST1) to the cutting step (ST7) in the present embodiment are performed. As shown in FIG. 2, the manufacturing apparatus of a glass substrate mainly includes the melting apparatus 100, the shaping apparatus 200, and the cutting apparatus 300. The melting apparatus 100 includes a melting tank 101, a clarification pipe 120, a stirring tank 103, transfer pipes 104 and 105, and a glass supply pipe 106.

於圖2所示之熔解槽101中設置有未圖示之燃燒器等加熱機構。向熔解槽投入添加有澄清劑之玻璃原料,而進行熔解步驟(ST1)。於熔解槽101中熔融後之熔融玻璃經由移送管104被供給至澄清管120。 A heating mechanism such as a burner (not shown) is provided in the melting tank 101 shown in Fig. 2 . The glass raw material to which the clarifying agent is added is supplied to the melting tank, and the melting step (ST1) is performed. The molten glass melted in the melting tank 101 is supplied to the clarification pipe 120 via the transfer pipe 104.

於澄清管120中,調整熔融玻璃MG之溫度,利用澄清劑之氧化還原反應進行熔融玻璃之澄清步驟(ST2)。澄清後之熔融玻璃經由移送管105被供給至攪拌槽。 In the clarification pipe 120, the temperature of the molten glass MG is adjusted, and the clarification step (ST2) of the molten glass is performed by the oxidation-reduction reaction of the clarifying agent. The clarified molten glass is supplied to the stirring tank via the transfer pipe 105.

於攪拌槽103中,利用攪拌器103a攪拌熔融玻璃而進行均質化步驟(ST3)。於攪拌槽103中均質化後之熔融玻璃經由玻璃供給管106被供給至成形裝置200(供給步驟ST4)。 In the stirring tank 103, the molten glass is stirred by the stirrer 103a, and the homogenization process (ST3) is performed. The molten glass which has been homogenized in the agitation tank 103 is supplied to the molding apparatus 200 via the glass supply pipe 106 (supply step ST4).

於成形裝置200中,利用溢流下拉法由熔融玻璃成形薄片玻璃(成形步驟ST5),並進行緩冷(緩冷步驟ST6)。 In the molding apparatus 200, the sheet glass is formed from the molten glass by the overflow down-draw method (forming step ST5), and the cooling is performed (slow cooling step ST6).

於切斷裝置300中,形成自薄片玻璃切出之板狀玻璃基板(切斷步 驟ST7)。 In the cutting device 300, a plate-shaped glass substrate cut out from the sheet glass is formed (cutting step) Step ST7).

(成形裝置之說明) (Description of forming device)

圖3係玻璃基板之成形裝置200之概略圖,圖4係沿圖3之IV-IV之箭頭方向觀察之剖視圖。 Fig. 3 is a schematic view of a molding apparatus 200 for a glass substrate, and Fig. 4 is a cross-sectional view taken along the line of arrows IV-IV of Fig. 3.

成形裝置200之爐壁由耐火磚、耐火隔熱磚、纖維系隔熱材料等耐火物形成。成形裝置200之內部空間被劃分為成形爐201(上部成形爐201A及下部成形爐201B)、以及成形爐201下部之緩冷爐202。於成形爐201中進行成形步驟(ST5),於緩冷爐202中進行緩冷步驟(ST6)。 The furnace wall of the forming apparatus 200 is formed of a refractory such as a refractory brick, a refractory heat insulating brick, or a fiber-based heat insulating material. The internal space of the molding apparatus 200 is divided into a forming furnace 201 (the upper forming furnace 201A and the lower forming furnace 201B) and a slow cooling furnace 202 at the lower portion of the forming furnace 201. The forming step (ST5) is performed in the forming furnace 201, and the slow cooling step (ST6) is performed in the slow cooling furnace 202.

於上部成形爐201A設置有成形體210。 A molded body 210 is provided in the upper forming furnace 201A.

通過圖2所示之玻璃供給管106自熔解裝置100對成形體210供給熔融玻璃。 The molten glass is supplied to the molded body 210 from the melting apparatus 100 by the glass supply pipe 106 shown in FIG.

成形體210係由耐火磚等構成之細長構造體,如圖4所示般剖面呈楔形狀。於成形體210之上部設置有成為引導熔融玻璃MG之流路之溝槽212。溝槽212與第3配管106連接,通過第3配管106流來之熔融玻璃MG沿著溝槽212流動。越靠熔融玻璃MG流動之下游,溝槽212之深度變得越淺,因此,於溝槽212中流動之熔融玻璃MG逐漸自溝槽212溢出,沿著成形體210兩側之側壁流下,並於成形體210之下方端部213合流而向鉛垂下方流下。藉此,於成形裝置200內製作自成形體210朝向鉛垂下方之薄片玻璃SG。 The formed body 210 is an elongated structure composed of refractory bricks or the like, and has a wedge-shaped cross section as shown in Fig. 4 . A groove 212 that serves as a flow path for guiding the molten glass MG is provided on the upper portion of the molded body 210. The groove 212 is connected to the third pipe 106, and the molten glass MG flowing through the third pipe 106 flows along the groove 212. The depth of the groove 212 becomes shallower as the flow of the molten glass MG flows downstream, and therefore, the molten glass MG flowing in the groove 212 gradually overflows from the groove 212, flows down the side walls of the molded body 210, and The lower end portion 213 of the molded body 210 merges and flows downward vertically. Thereby, in the molding apparatus 200, the sheet glass SG which is formed from the molded body 210 toward the vertical direction is formed.

再者,成形體210之下方端部213正下方之薄片玻璃SG之溫度為相當於105.7~107.5poise(柏)之黏度之溫度,例如為1000~1130℃。 Further, the temperature of the sheet glass SG directly under the lower end portion 213 of the molded body 210 is a temperature corresponding to a viscosity of 10 5.7 to 10 7.5 poise, for example, 1000 to 1130 °C.

氛圍間隔構件220設置於成形體210之下方端部213之下方附近,將成形爐201A之內部空間劃分為上部成形爐201A與下部成形爐201B。氛圍間隔構件220為一對板狀之隔熱材料,以自厚度方向(圖中X方向)之兩側隔著薄片玻璃SG之方式設置於薄片玻璃SG之厚度方向之兩側。於薄片玻璃SG與氛圍間隔構件220之間,以氛圍間隔構件 220不與薄片玻璃SG接觸之程度設置有間隙。氛圍間隔構件220藉由將成形裝置200之內部空間隔開,而阻斷熱在氛圍間隔構件220之上方之成形爐201與下方之緩冷爐202之間移動。 The atmosphere partition member 220 is disposed near the lower side of the lower end portion 213 of the molded body 210, and divides the internal space of the forming furnace 201A into the upper forming furnace 201A and the lower forming furnace 201B. The atmosphere partition member 220 is a pair of plate-shaped heat insulating materials, and is provided on both sides in the thickness direction of the sheet glass SG so as to be sandwiched by the sheet glass SG from both sides in the thickness direction (X direction in the drawing). Between the sheet glass SG and the ambience spacer member 220, the astigmatism spacer member The gap 220 is not provided with a degree of contact with the sheet glass SG. The atmosphere spacing member 220 blocks the movement between the forming furnace 201 above the ambient spacing member 220 and the slow cooling furnace 202 below by separating the internal space of the forming apparatus 200.

於下部成形爐201B設置有1對冷卻輥230、及冷卻機構240。 A pair of cooling rolls 230 and a cooling mechanism 240 are provided in the lower forming furnace 201B.

冷卻輥230及冷卻機構240係設置於氛圍間隔構件220之下方。 The cooling roller 230 and the cooling mechanism 240 are disposed below the ambience spacer 220.

如圖3、圖4所示,1對冷卻輥230以自厚度方向之兩側夾著薄片玻璃SG之方式設置於薄片玻璃SG之厚度方向之兩側。冷卻輥230以使薄片玻璃SG之寬度方向兩端部下降至相當於約109.0poise以上之黏度之溫度(例如900℃)以下之溫度之方式進行冷卻。冷卻輥230為中空,藉由向內部供給冷卻介質(例如空氣等)而急冷。冷卻輥230之直徑較下述搬送構件2501、2502、…、250n小,插入至爐內之長度亦較短,又,由於被急冷,故而產生變形(偏芯)之虞較少。 As shown in FIG. 3 and FIG. 4, the pair of cooling rolls 230 are provided on both sides in the thickness direction of the sheet glass SG so as to sandwich the sheet glass SG from both sides in the thickness direction. The cooling roll 230 is cooled such that both end portions in the width direction of the sheet glass SG are lowered to a temperature equal to or lower than a viscosity (for example, 900 ° C) of about 10 9.0 poise or more. The cooling roll 230 is hollow and is rapidly cooled by supplying a cooling medium (for example, air or the like) to the inside. The diameter of the cooling roll 230 is smaller than the following conveying members 2501, 2502, ..., 250n, and the length inserted into the furnace is also short, and since it is quenched, the deformation (eccentricity) is less.

冷卻機構240包含多個冷卻單元(端部冷卻單元241及中央冷卻單元242),對薄片玻璃SG進行冷卻。 The cooling mechanism 240 includes a plurality of cooling units (the end cooling unit 241 and the central cooling unit 242) to cool the sheet glass SG.

端部冷卻單元241以使薄片玻璃SG之寬度方向兩端部下降至相當於1014.5poise以上之黏度之溫度之方式進行冷卻。 The end portion cooling unit 241 cools so that both end portions in the width direction of the sheet glass SG are lowered to a temperature corresponding to a viscosity of 10 14.5 poise or more.

中央冷卻單元242將薄片玻璃SG之寬度方向之中央部自高於軟化點之溫度冷卻至緩冷點附近。此處,所謂薄片玻璃SG之中央部係除了於薄片玻璃成形後被切斷之對象以外之區域,且係以薄片玻璃SG之板厚變得均勻之方式製造之區域。 The central cooling unit 242 cools the central portion of the sheet glass SG in the width direction from the temperature higher than the softening point to the vicinity of the slow cooling point. Here, the center portion of the sheet glass SG is a region which is manufactured in a region other than the target to be cut after the sheet glass is formed, and is formed so that the sheet thickness of the sheet glass SG becomes uniform.

中央冷卻單元242例如於上下方向上包含3段單元(上段單元242a、中段單元242b、下段單元242c)。上段單元242a將遠離成形體210之下端213之薄片玻璃SG急冷至軟化點附近,中段單元242b及下段單元242c藉由緩慢之冷卻將薄片玻璃SG冷卻至緩冷點附近。 The central cooling unit 242 includes, for example, three-stage units (upper stage unit 242a, middle stage unit 242b, and lower stage unit 242c) in the up and down direction. The upper stage unit 242a quenches the sheet glass SG away from the lower end 213 of the formed body 210 to the vicinity of the softening point, and the middle stage unit 242b and the lower stage unit 242c cool the sheet glass SG to the vicinity of the slow cooling point by slow cooling.

緩冷爐202具有壁203。壁203劃分緩冷爐202之供搬送薄片玻璃SG之爐內、及外部空間之爐外。於緩冷爐202設置有多個搬送構件 2501、2502、…、250n、多個溫度調整裝置2701、2702、270n、及多個間隔板2021、2022、…、202n。 The slow cooling oven 202 has a wall 203. The wall 203 divides the inside of the furnace for transporting the sheet glass SG of the slow cooling furnace 202 and the outside of the furnace. The slow cooling furnace 202 is provided with a plurality of conveying members 2501, 2502, ..., 250n, a plurality of temperature adjustment devices 2701, 2702, 270n, and a plurality of spacers 2021, 2022, ..., 202n.

緩冷爐202藉由間隔板2021而與下部成形爐201B隔開,且緩冷爐202之內部空間由間隔板2021以外之多個間隔板2022、…、202n於高度方向上隔成多個空間。於由多個間隔板2021、2022、…、202n間隔出之各空間分別設置有搬送構件2501、2502、…、250n、多個溫度調整裝置2701、2702、…、270n。具體來講,於由間隔板2021及間隔板2022間隔出之空間設置有搬送構件2501及溫度調整裝置2701,於由間隔板2022及間隔板2023間隔出之空間設置有搬送構件2502及溫度調整裝置2702。 The slow cooling furnace 202 is separated from the lower forming furnace 201B by the partition plate 2021, and the internal space of the slow cooling furnace 202 is partitioned into a plurality of spaces in the height direction by a plurality of partition plates 2022, ..., 202n other than the partitioning plate 2021. . Each of the spaces partitioned by the plurality of partition plates 2021, 2022, ..., 202n is provided with transport members 2501, 2502, ..., 250n and a plurality of temperature adjusting devices 2701, 2702, ..., 270n. Specifically, a transport member 2501 and a temperature adjustment device 2701 are provided in a space partitioned by the partition plate 2021 and the partition plate 2022, and a transport member 2502 and a temperature adjustment device are provided in a space partitioned by the partition plate 2022 and the partition plate 2023. 2702.

間隔板2022與間隔板202n之間亦被未圖示之間隔板隔開,且於間隔出之各空間同樣地設置有其他未圖示之搬送構件及溫度調整裝置。再者,最下部之搬送構件250n及溫度調整裝置270n係設置於最下部之間隔板202n下部之空間。 The partition plate 2022 and the partition plate 202n are also partitioned by a partition plate (not shown), and other transport members (not shown) and temperature adjustment devices are provided in the same space. Further, the lowermost conveying member 250n and the temperature adjusting device 270n are provided in a space below the lowermost partition plate 202n.

各搬送構件2501、2502、…、250n係設置於薄片玻璃SG之厚度方向之兩側,且包括:1對旋轉軸,其等於爐壁之外部由未圖示之軸承懸臂支持;及1對搬送輥,其等安裝於各旋轉軸之前端。各溫度調整裝置2701、2702、…、270n包含設置於薄片玻璃SG之厚度方向之兩側之1對加熱器。各加熱器於薄片玻璃SG之寬度方向上具備多個熱源,可分別調整加熱量。多個熱源例如為鉻系發熱線等。 Each of the conveying members 2501, 2502, ..., 250n is disposed on both sides in the thickness direction of the sheet glass SG, and includes: a pair of rotating shafts which are equal to the outside of the furnace wall supported by a bearing cantilever (not shown); and a pair of conveying A roller, which is attached to the front end of each of the rotating shafts. Each of the temperature adjustment devices 2701, 2702, ..., 270n includes a pair of heaters provided on both sides in the thickness direction of the sheet glass SG. Each of the heaters has a plurality of heat sources in the width direction of the sheet glass SG, and the amount of heating can be adjusted separately. The plurality of heat sources are, for example, chromium-based heating wires.

利用上述冷卻構件230、冷卻裝置240及溫度調整裝置2701、2702、…、270n,例如,如下所述般以具有與預先設計之溫度分佈對應之溫度分佈之方式冷卻薄片玻璃SG。 The sheet glass SG is cooled by the cooling member 230, the cooling device 240, and the temperature adjusting devices 2701, 2702, ..., 270n so as to have a temperature distribution corresponding to a temperature distribution designed in advance, for example.

於黏性區域中,例如設計成薄片玻璃之寬度方向端部之溫度較中央區域之溫度低,且中央區域之溫度變得均勻般之溫度分佈(第1分佈)。藉此,可抑制寬度方向之收縮,並且使薄片玻璃之板厚均勻。 In the viscous region, for example, the temperature at the end portion in the width direction of the sheet glass is set to be lower than the temperature in the central portion, and the temperature in the central portion becomes uniform (temperature distribution) (first distribution). Thereby, the shrinkage in the width direction can be suppressed, and the sheet thickness of the sheet glass can be made uniform.

於黏彈性區域中,例如設計成薄片玻璃之溫度自中央部朝向端部沿寬度方向遞減般之溫度分佈(第2分佈)。 In the viscoelastic region, for example, the temperature of the sheet glass is designed to decrease in temperature in the width direction from the center portion toward the end portion (second distribution).

於玻璃應變點附近之溫度區域中,設計成薄片玻璃之寬度方向端部之溫度與中央部之溫度變得大致均勻之溫度分佈。 In the temperature region near the glass strain point, the temperature at which the temperature at the end portion in the width direction of the sheet glass and the temperature at the center portion become substantially uniform are designed.

藉由以按照上述設計好之溫度分佈之方式管理薄片玻璃之溫度,可減少薄片玻璃之翹曲及應變(殘留應力)。再者,薄片玻璃之中央區域係包含使板厚均勻之對象部分之區域,薄片玻璃之端部係包含於製造後被切斷之對象部分之區域。 The warpage and strain (residual stress) of the sheet glass can be reduced by managing the temperature of the sheet glass in accordance with the temperature distribution designed as described above. Further, the central portion of the sheet glass includes a region where the thickness of the object portion is uniform, and the end portion of the sheet glass is included in the region of the object portion to be cut after the production.

如以上所說明般,以薄片玻璃之翹曲及應變不超過容許值之方式實施上述緩冷步驟。於該緩冷步驟中,藉由來自與薄片玻璃之接觸部之熱傳導、來自薄片玻璃之輻射熱、來自緩冷爐202內之氛圍之熱傳導,而將搬送輥之旋轉軸自爐壁向緩冷爐202內突出之部分加熱。另一方面,由於爐壁之隔熱性較高,故而緩冷爐202之外部被維持為較緩冷爐202內低之溫度。 As described above, the above-described slow cooling step is carried out so that the warpage and strain of the sheet glass do not exceed the allowable value. In the slow cooling step, the rotating shaft of the conveying roller is moved from the furnace wall to the slow cooling furnace by heat conduction from the contact portion with the sheet glass, radiant heat from the sheet glass, and heat conduction from the atmosphere in the slow cooling furnace 202. The protruding portion of 202 is heated. On the other hand, since the heat insulating property of the furnace wall is high, the outside of the slow cooling furnace 202 is maintained at a lower temperature than that in the slow cooling furnace 202.

本案發明者獲得如下見解:於爐壁附近,旋轉軸之長度方向之溫度梯度變大,產生於旋轉軸之應力與溫度梯度之大小相應地變大,為了將產生於旋轉軸之應力設為使用環境下之容許應力以下,而對旋轉軸之溫度梯度之調整進行了研究。 The inventors of the present invention have obtained the following observations: in the vicinity of the furnace wall, the temperature gradient in the longitudinal direction of the rotating shaft becomes large, and the stress generated in the rotating shaft becomes larger in accordance with the magnitude of the temperature gradient, and the stress generated in the rotating shaft is used. The adjustment of the temperature gradient of the rotating shaft was studied below the allowable stress in the environment.

於本發明中,以對所設計之溫度分佈造成之影響儘可能減小且旋轉軸之長度方向之溫度梯度之最大值成為特定值以下之方式、具體來講以成為2500℃/m以下之方式,控制旋轉軸之溫度。以下,基於實施形態進行說明。 In the present invention, the influence on the designed temperature distribution is as small as possible and the maximum value of the temperature gradient in the longitudinal direction of the rotating shaft is equal to or less than a specific value, specifically, 2500 ° C / m or less. , control the temperature of the rotating shaft. Hereinafter, it demonstrates based on an embodiment.

圖5係搬送構件2501、2502、…、250n中之1個之剖視圖。 Fig. 5 is a cross-sectional view showing one of the conveying members 2501, 2502, ..., 250n.

搬送輥30於緩冷爐202內與薄片玻璃SG接觸,並將薄片玻璃SG向下方搬送。搬送輥30係固定於旋轉軸31之前端部。搬送輥30例如可聚集無機纖維而形成。 The conveyance roller 30 comes into contact with the sheet glass SG in the slow cooling furnace 202, and conveys the sheet glass SG downward. The conveying roller 30 is fixed to the front end portion of the rotating shaft 31. The conveying roller 30 can be formed, for example, by collecting inorganic fibers.

旋轉軸31為中空管狀。旋轉軸31之一端被堵塞,且於旋轉軸31之堵塞端之外周部固定有搬送輥30。旋轉軸31之中間部可旋轉地插通至設置於緩冷爐202之壁203之貫通孔。即,旋轉軸31貫通壁203。旋轉軸31之與搬送輥30為相反側之端部於壁203之外部被未圖示之軸承懸臂支持,並且連接於未圖示之排出管。如下所述,排出管用於排出對旋轉軸31供給之熱介質。 The rotating shaft 31 is a hollow tubular shape. One end of the rotating shaft 31 is blocked, and a conveying roller 30 is fixed to the periphery of the blocked end of the rotating shaft 31. The intermediate portion of the rotating shaft 31 is rotatably inserted into a through hole provided in the wall 203 of the slow cooling furnace 202. That is, the rotating shaft 31 penetrates the wall 203. An end portion of the rotating shaft 31 opposite to the conveying roller 30 is supported by a bearing cantilever (not shown) outside the wall 203, and is connected to a discharge pipe (not shown). The discharge pipe is for discharging the heat medium supplied to the rotary shaft 31 as will be described later.

旋轉軸31可使用耐熱性優異且硬度亦較高之材料。例如可將奧氏體(austenite)系不鏽鋼用於旋轉軸31。具體來講,可使用SUS310S、SUS303、SUS304、SUS316。再者,旋轉軸31之全長例如為1500mm以下,插入至爐內之量例如為500mm以下,可將外徑設為例如50mm以下,將內徑設為例如外徑之50~80%。 As the rotating shaft 31, a material excellent in heat resistance and high in hardness can be used. For example, austenite stainless steel can be used for the rotating shaft 31. Specifically, SUS310S, SUS303, SUS304, and SUS316 can be used. Further, the total length of the rotating shaft 31 is, for example, 1500 mm or less, and the amount inserted into the furnace is, for example, 500 mm or less, and the outer diameter can be, for example, 50 mm or less, and the inner diameter can be, for example, 50 to 80% of the outer diameter.

於旋轉軸31之中空之內部,與旋轉軸31之內壁相隔地配置有直徑小於旋轉軸31之內徑之內管32。內管32之搬送輥30側之端部開口,且該開口端遠離旋轉軸31之堵塞端。內管32之與開口端為相反側之端部於壁203之外部連接於未圖示之供給管。如下所述,供給管用於自內管32對旋轉軸31供給熱介質。熱介質既可為氣體,亦可為液體,由於液體之熱容較大,有使旋轉軸31之溫度過度下降之虞,故而較佳為氣體。 Inside the hollow of the rotating shaft 31, an inner tube 32 having a diameter smaller than the inner diameter of the rotating shaft 31 is disposed apart from the inner wall of the rotating shaft 31. The end of the inner tube 32 on the side of the conveying roller 30 is opened, and the open end is away from the blocked end of the rotating shaft 31. An end portion of the inner tube 32 opposite to the open end is connected to a supply tube (not shown) outside the wall 203. The supply pipe is used to supply the heat medium to the rotating shaft 31 from the inner pipe 32 as described below. The heat medium may be either a gas or a liquid, and since the heat capacity of the liquid is large and the temperature of the rotating shaft 31 is excessively lowered, it is preferably a gas.

於本實施形態中,自壁203之外部對內管32供給熱介質。熱介質自旋轉軸31之搬送輥30側之端部通過內管32之外側面與旋轉軸31之內壁面之間之間隙而流向壁203側,並向緩冷爐202之外部排出。熱介質係用以使旋轉軸31之搬送輥30側之端部之熱移動至與搬送輥30為相反側之端部的介質。即,於旋轉軸31之搬送輥30側之端部,熱介質吸收熱而使旋轉軸之溫度下降,並且溫度上升後之熱介質朝向緩冷爐202之外部沿著旋轉軸31之長度方向流動,藉此熱自旋轉軸31之搬送輥30側之端部沿著旋轉軸31之長度方向移動。藉此,可將因來自搬送輥30 之與薄片玻璃SG之接觸部之熱傳導而引起之旋轉軸31之長度方向之溫度梯度抑制得較低。於本實施形態中,藉由控制熱介質之流量,而以旋轉軸31之長度方向之溫度梯度變小之方式進行調整。藉此,可降低由溫度梯度引起並作用於旋轉軸31之應力,從而可防止旋轉軸31之變形。此處,較佳為以旋轉軸31之長度方向之溫度梯度之最大值成為2500℃/m以下之方式進行調整。其原因在於:於溫度梯度為2500℃/m以下時,作用於旋轉軸31之應力較緩冷爐202內之氛圍溫度(700℃~850℃)下之旋轉軸31之容許應力小。 In the present embodiment, the heat medium is supplied to the inner tube 32 from the outside of the wall 203. The end portion of the heat medium from the side of the conveying roller 30 of the rotating shaft 31 flows to the side of the wall 203 through the gap between the outer surface of the inner tube 32 and the inner wall surface of the rotating shaft 31, and is discharged to the outside of the slow cooling furnace 202. The heat medium is a medium for moving the heat of the end portion of the rotating shaft 31 on the side of the conveying roller 30 to the end opposite to the conveying roller 30. That is, at the end portion of the rotating shaft 31 on the side of the conveying roller 30, the heat medium absorbs heat to lower the temperature of the rotating shaft, and the heat medium after the temperature rises flows toward the outside of the slow cooling furnace 202 along the length of the rotating shaft 31. Thereby, the end portion of the hot rotating shaft 31 on the side of the conveying roller 30 moves along the longitudinal direction of the rotating shaft 31. Thereby, the reason can be derived from the conveying roller 30 The temperature gradient in the longitudinal direction of the rotating shaft 31 caused by the heat conduction with the contact portion of the sheet glass SG is suppressed to be low. In the present embodiment, by controlling the flow rate of the heat medium, the temperature gradient in the longitudinal direction of the rotary shaft 31 is adjusted to be small. Thereby, the stress caused by the temperature gradient and acting on the rotating shaft 31 can be reduced, so that the deformation of the rotating shaft 31 can be prevented. Here, it is preferable to adjust so that the maximum value of the temperature gradient in the longitudinal direction of the rotating shaft 31 becomes 2500 ° C / m or less. The reason for this is that when the temperature gradient is 2500 ° C / m or less, the stress acting on the rotating shaft 31 is smaller than the allowable stress of the rotating shaft 31 in the atmosphere temperature (700 ° C to 850 ° C) in the slow cooling furnace 202.

再者,亦可藉由利用未圖示之加熱器等熱源對旋轉軸31進行加熱而減小旋轉軸31之溫度梯度。 Further, the temperature gradient of the rotating shaft 31 can be reduced by heating the rotating shaft 31 by a heat source such as a heater (not shown).

較佳為設置有隔熱材料33,該隔熱材料33自緩冷爐202之供旋轉軸插通之貫通孔朝旋轉軸31之輥30側延伸,且被覆旋轉軸31之外側面。隔熱材料33可使用具備配置旋轉軸31之緩冷爐202內之氛圍溫度下之耐熱性之材料(例如耐熱磚、耐火隔熱磚、無機纖維等)。隔熱材料33能以被覆旋轉軸31之外側面之方式形成為圓筒形,但並非必須為圓筒狀。又,隔熱材料33無需被覆旋轉軸31外側之整個面,較佳為以獲得所需之溫度梯度之方式於旋轉軸31之緩冷爐202內側之部分至少被覆壁203側之端部。 Preferably, the heat insulating material 33 is provided, and the heat insulating material 33 extends from the through hole of the slow cooling furnace 202 through which the rotating shaft is inserted toward the roller 30 side of the rotating shaft 31, and covers the outer surface of the rotating shaft 31. As the heat insulating material 33, a material (for example, heat-resistant brick, fire-resistant heat insulating brick, inorganic fiber, or the like) having heat resistance at an ambient temperature in the slow cooling furnace 202 in which the rotating shaft 31 is disposed can be used. The heat insulating material 33 can be formed in a cylindrical shape so as to cover the outer surface of the rotating shaft 31, but it is not necessarily required to be cylindrical. Further, the heat insulating material 33 does not need to cover the entire outer surface of the rotating shaft 31, and it is preferable that the portion inside the slow cooling furnace 202 of the rotating shaft 31 is at least covered at the end on the side of the wall 203 so as to obtain a desired temperature gradient.

藉由設置隔熱材料33,可抑制因來自薄片玻璃之輻射熱或來自緩冷爐202內之氛圍之熱傳導而引起之旋轉軸31之溫度上升。藉此,可降低由隔熱材料33被覆之部分處之旋轉軸31之長度方向之溫度梯度。 By providing the heat insulating material 33, the temperature rise of the rotating shaft 31 due to the radiant heat from the sheet glass or the heat conduction from the atmosphere in the slow cooling furnace 202 can be suppressed. Thereby, the temperature gradient in the longitudinal direction of the rotating shaft 31 at the portion covered by the heat insulating material 33 can be reduced.

較佳為旋轉軸31於隔熱材料33之輥30側之端部位置上之溫度梯度為1300℃/m以下。於隔熱材料33之輥30側之端部位置上,於旋轉軸31之被隔熱材料33被覆之部分與未被隔熱材料33被覆之部分,溫度差變大,而有溫度梯度變大之傾向。又,其原因在於:旋轉軸31之未被 隔熱材料33被覆之部分曝露於緩冷爐202內之氛圍溫度(700℃~850℃)下而成為高溫,故而容許應力變小。溫度梯度為1300℃/m以下時作用於旋轉軸31之應力較緩冷爐202內之薄片玻璃SG下端部附近之氛圍溫度(700℃以上)下之容許應力小。 Preferably, the temperature gradient of the rotating shaft 31 at the end portion of the heat insulating material 33 on the side of the roller 30 is 1300 ° C / m or less. At the end portion of the heat insulating material 33 on the side of the roller 30, the portion of the rotating shaft 31 covered with the heat insulating material 33 and the portion not covered with the heat insulating material 33 have a large temperature difference, and the temperature gradient becomes large. The tendency. Moreover, the reason is that the rotating shaft 31 is not The portion covered with the heat insulating material 33 is exposed to the ambient temperature (700 ° C to 850 ° C) in the slow cooling furnace 202 to become a high temperature, so that the allowable stress is small. When the temperature gradient is 1300 ° C / m or less, the stress acting on the rotating shaft 31 is smaller than the allowable stress in the vicinity of the lower end portion of the sheet glass SG in the slow cooling furnace 202 (700 ° C or more).

[實施例] [Examples]

以下,利用實施例進一步具體地說明本發明。 Hereinafter, the present invention will be specifically described by way of examples.

將緩冷爐中之搬送構件之旋轉軸設為上述圖5所示之構造。將旋轉軸之長度方向上之隔熱材料距爐壁之長度設為0.26m,將緩冷爐內之溫度設為800℃,將緩冷爐外部之溫度設為30℃,旋轉軸之熱導率係假定SUS304而設為熱導率W/(m‧K)=0.013*溫度(℃)+15,並將隔熱材料之熱導率設為0.1W/(m‧K),從而計算旋轉軸之容許應力。 The rotation axis of the conveying member in the slow cooling furnace is set as shown in Fig. 5 described above. The length of the heat insulating material in the longitudinal direction of the rotating shaft is set to 0.26 m from the furnace wall, the temperature in the slow cooling furnace is set to 800 ° C, and the temperature outside the slow cooling furnace is set to 30 ° C, and the thermal conductivity of the rotating shaft The rate is assumed to be SUS304 and the thermal conductivity W/(m‧K)=0.013*temperature (°C)+15, and the thermal conductivity of the heat insulating material is set to 0.1 W/(m‧K), thereby calculating the rotation The allowable stress of the shaft.

<比較例> <Comparative example>

將旋轉軸之長度方向上之隔熱材料距爐壁之長度設為0.26m,將緩冷爐內之溫度設為(800)℃,將緩冷爐外部之溫度設為(30)℃,旋轉軸之熱導率係假定SUS304而設為熱導率W/(m‧K)=0.013*溫度(℃)+15,並將隔熱材料之熱導率設為(0.1)W/(m‧K),從而計算旋轉軸之容許應力。 The length of the heat insulating material in the longitudinal direction of the rotating shaft is set to 0.26 m from the furnace wall, the temperature in the slow cooling furnace is set to (800) ° C, and the temperature outside the slow cooling furnace is set to (30) ° C, and the rotation is performed. The thermal conductivity of the shaft is assumed to be SUS304 and is set to thermal conductivity W/(m‧K)=0.013*temperature (°C)+15, and the thermal conductivity of the insulating material is set to (0.1)W/(m‧ K), thereby calculating the allowable stress of the rotating shaft.

圖6係表示旋轉軸之長度方向之位置與溫度之關係之圖。將旋轉軸之長度方向之位置設為橫軸,將溫度設為縱軸。旋轉軸之長度方向之位置以爐壁作為基準而將緩冷爐側設為正。以實線表示實施例,以虛線表示比較例。 Fig. 6 is a view showing the relationship between the position in the longitudinal direction of the rotating shaft and the temperature. The position in the longitudinal direction of the rotating shaft is set to the horizontal axis, and the temperature is set to the vertical axis. The position in the longitudinal direction of the rotating shaft is set to be positive with respect to the slow cooling furnace side with the furnace wall as a reference. The embodiment is shown by a solid line, and the comparative example is shown by a broken line.

於實施例中,在隔熱材料之爐壁之位置,旋轉軸之長度方向之溫度梯度最大,該最大值為2500℃/m。又,隔熱材料之輥側之端部位置上之旋轉軸之長度方向之溫度梯度為1250℃/m。 In the embodiment, the temperature gradient in the longitudinal direction of the rotating shaft is the largest at the position of the furnace wall of the heat insulating material, and the maximum value is 2500 ° C / m. Further, the temperature gradient in the longitudinal direction of the rotating shaft at the end portion of the heat insulating material on the roll side was 1,250 ° C / m.

於比較例中,在隔熱材料之爐壁之位置,旋轉軸之長度方向之溫度梯度最大,該最大值為3600℃/m。又,隔熱材料之輥側之端部位 置上之旋轉軸之長度方向之溫度梯度為2350℃/m。 In the comparative example, the temperature gradient in the longitudinal direction of the rotating shaft was the largest at the position of the furnace wall of the heat insulating material, and the maximum value was 3600 ° C / m. Moreover, the end portion of the roller side of the heat insulating material The temperature gradient in the longitudinal direction of the rotating shaft placed was 2350 ° C / m.

圖7係表示圖6之旋轉軸之溫度下之旋轉軸之長度方向之位置與旋轉軸之應力之關係的圖。於實施例中,溫度梯度之最大值較比較例小,因此可知作用於旋轉軸之應力變小。 Fig. 7 is a view showing the relationship between the position in the longitudinal direction of the rotating shaft and the stress of the rotating shaft at the temperature of the rotating shaft of Fig. 6. In the examples, the maximum value of the temperature gradient is smaller than that of the comparative example, so that the stress acting on the rotating shaft is small.

以上,對本發明之玻璃基板之製造方法進行了詳細說明,但本發明並不限定於上述實施形態,當然亦可於不脫離本發明之主旨之範圍內進行各種改良或變更。 The method for producing the glass substrate of the present invention has been described in detail above. The present invention is not limited to the above-described embodiments, and various modifications and changes can be made without departing from the spirit and scope of the invention.

Claims (6)

一種玻璃基板之製造方法,其係於成形爐中使熔融玻璃自成形體溢流而成形連續之薄片玻璃,且於緩冷爐中利用輥夾持上述薄片玻璃並向下方搬送者;上述緩冷爐具有壁,該壁劃分供搬送上述薄片玻璃之爐內、及外部空間之爐外,上述輥由貫通上述壁之旋轉軸予以懸臂支持,且設置於上述緩冷爐之溫度梯度調節機構為藉由將至少上述旋轉軸之上述壁側之部分予以隔熱而對上述旋轉軸進行保溫之隔熱材料、對上述旋轉軸進行加熱之熱源、或藉由流動於上述旋轉軸中而對上述旋轉軸進行加熱之熱介質,且上述溫度梯度調節機構係以減小上述旋轉軸之長度方向之溫度梯度之方式進行調整。 A method for producing a glass substrate, wherein a molten glass is poured from a molded body in a forming furnace to form a continuous sheet glass, and the sheet glass is held by a roll in a slow cooling furnace and conveyed downward; The furnace has a wall which is divided into a furnace for conveying the sheet glass and an outer space, wherein the roller is supported by a rotating shaft passing through the wall, and the temperature gradient adjusting mechanism provided in the slow cooling furnace is borrowed a heat insulating material that heats the rotating shaft at least the portion on the wall side of the rotating shaft, a heat source that heats the rotating shaft, or flows through the rotating shaft to the rotating shaft The heating medium is heated, and the temperature gradient adjusting mechanism is adjusted to reduce the temperature gradient in the longitudinal direction of the rotating shaft. 如請求項1之玻璃基板之製造方法,其中上述隔熱材料係自上述成形爐之內壁面朝上述旋轉軸之上述輥側延伸。 The method for producing a glass substrate according to claim 1, wherein the heat insulating material extends from an inner wall surface of the forming furnace toward the roll side of the rotating shaft. 如請求項1之玻璃基板之製造方法,其中上述熱介質自上述旋轉軸之設置有上述輥之部分向貫通上述壁之部分輸送熱。 The method of producing a glass substrate according to claim 1, wherein the heat medium transfers heat from a portion of the rotating shaft on which the roller is provided to a portion penetrating the wall. 如請求項1至3中任一項之玻璃基板之製造方法,其中以上述旋轉軸之長度方向之溫度梯度之最大值成為2500℃/m以下之方式進行調整。 The method for producing a glass substrate according to any one of claims 1 to 3, wherein the maximum value of the temperature gradient in the longitudinal direction of the rotating shaft is adjusted to be 2,500 ° C / m or less. 如請求項1至3中任一項之玻璃基板之製造方法,其中以上述隔熱材料之上述輥側之端部位置上之上述旋轉軸之長度方向之溫度梯度成為1300℃/m以下之方式進行調整。 The method for producing a glass substrate according to any one of claims 1 to 3, wherein a temperature gradient in a longitudinal direction of the rotating shaft at an end portion of the heat insulating material on the side of the roll side is 1300 ° C / m or less Make adjustments. 一種玻璃基板之製造裝置,其具有:成形爐,其具有使熔融玻璃溢流而成形連續之薄片玻璃之成 形體;以及緩冷爐,其一面夾持上述薄片玻璃並向下方搬送一面進行緩冷;且上述緩冷爐包括:壁,其劃分供搬送上述薄片玻璃之爐內及外部空間之爐外;旋轉軸,其貫通上述壁;輥,其設置於上述旋轉軸之前端部且由上述旋轉軸懸臂支持;以及溫度梯度調節機構,其以減小上述旋轉軸之長度方向之溫度梯度之方式進行調節,其中上述溫度梯度調節機構為藉由將至少上述旋轉軸之上述壁側之部分予以隔熱而對上述旋轉軸進行保溫之隔熱材料、對上述旋轉軸進行加熱之熱源、或藉由流動於上述旋轉軸中而對上述旋轉軸進行加熱之熱介質。 A manufacturing apparatus for a glass substrate, comprising: a forming furnace having a sheet glass formed by overflowing molten glass to form a continuous sheet And a slow cooling furnace, wherein one side of the sheet glass is held and conveyed downward to perform slow cooling; and the slow cooling furnace comprises: a wall which is divided into a furnace for conveying the inside and outside of the sheet glass; a shaft penetrating the wall; a roller disposed at a front end of the rotating shaft and supported by the rotating shaft cantilever; and a temperature gradient adjusting mechanism configured to reduce a temperature gradient in a longitudinal direction of the rotating shaft The temperature gradient adjusting mechanism is a heat insulating material that heats the rotating shaft by heat-insulating at least the portion on the wall side of the rotating shaft, a heat source that heats the rotating shaft, or flows through the above A heat medium that rotates the shaft to heat the rotating shaft.
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