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TW201247566A - Production method for glass sheet and glass sheet production device - Google Patents

Production method for glass sheet and glass sheet production device Download PDF

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Publication number
TW201247566A
TW201247566A TW101111564A TW101111564A TW201247566A TW 201247566 A TW201247566 A TW 201247566A TW 101111564 A TW101111564 A TW 101111564A TW 101111564 A TW101111564 A TW 101111564A TW 201247566 A TW201247566 A TW 201247566A
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TW
Taiwan
Prior art keywords
glass
glass ribbon
roller
speed
temperature
Prior art date
Application number
TW101111564A
Other languages
Chinese (zh)
Other versions
TWI428296B (en
Inventor
Tetsuo Kimijima
Kimihiko Nakashima
Shinji Yamazaki
Original Assignee
Avanstrate Inc
Avanstrate Korea Inc
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Application filed by Avanstrate Inc, Avanstrate Korea Inc filed Critical Avanstrate Inc
Publication of TW201247566A publication Critical patent/TW201247566A/en
Application granted granted Critical
Publication of TWI428296B publication Critical patent/TWI428296B/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B18/00Shaping glass in contact with the surface of a liquid
    • C03B18/02Forming sheets
    • C03B18/04Changing or regulating the dimensions of the molten glass ribbon
    • C03B18/06Changing or regulating the dimensions of the molten glass ribbon using mechanical means, e.g. restrictor bars, edge rollers
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B17/00Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
    • C03B17/06Forming glass sheets
    • C03B17/064Forming glass sheets by the overflow downdraw fusion process; Isopipes therefor
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B17/00Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
    • C03B17/06Forming glass sheets
    • C03B17/068Means for providing the drawing force, e.g. traction or draw rollers
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B18/00Shaping glass in contact with the surface of a liquid
    • C03B18/02Forming sheets
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/50Glass production, e.g. reusing waste heat during processing or shaping
    • Y02P40/57Improving the yield, e-g- reduction of reject rates

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

Abstract

When producing a glass sheet, a glass raw material is melted to create molten glass, the molten glass is molded using the downdraw method, a glass ribbon is formed, and the glass ribbon is drawn downwards and annealed while being sandwiched between a plurality of roller pairs disposed along the conveyance direction for the glass ribbon. During molding, both ends of the glass ribbon are cooled while the glass ribbon continues to be sandwiched between the roller pairs and drawn downwards. Each roller in a first roller pair, which is one of the roller pairs used either in molding or annealing, is rotatably driven on the basis of a roller rotation speed determined so as to compensate for roller diameter change.

Description

201247566 六、發明說明: 【發明所屬之技術領域】 本發明係有關於一種玻璃板之製造方法及破螭板製造震 置。 【先前技術】 利用下拉法之玻璃板之製造方法係玻璃帶藉由利用搬送 報對夹持著朝向下方曳引’而拉伸至所需之厚度,進而, 以避免内部產生應變,又,以避免玻璃帶翹曲之方式,進 行冷卻。玻璃帶被切斷為特定之.尺寸,隔著失紙等相互承 載,或者,進而進行搬送,於後續步驟中實施處理(例如 形狀加工、離子更換之化學強化處理)。 作為先前之利用下拉法之玻璃板之製造方法,已知藉由 以搬送輥對之各搬送輥受到相同之負載之方式控制其旋轉 驅動’防止因搬送輥間之外徑差而產生之滑移,而抑制一 搬送輥空轉(專利文獻1)。據此,實現可防止玻璃表面及搬 送輥之破損。 且說,於遍及玻璃帶之搬送方向環境溫度及玻璃帶之溫 度進行變化之徐冷爐中,較為理想的是設置於玻璃帶之搬 送方向之各位置的搬送輥之圓周速度與玻璃帶之搬送速度 之間之相對速度為0,但由於玻璃之熱膨脹係數與搬送輥 之熱膨脹係數不同,而且其溫度依存性亦不同,故而於複 數個搬送輥對之間’不僅相對速度不為〇,而且於相對速 度中產生差值。如此之相對速度之差係例如因玻璃帶之搬 送速度或厚度之變化、產生於徐冷爐内之氣流變動等導致 163507.doc 201247566 徐冷爐内之環玲θ 4 衣境/m度或玻璃帶之溫度變化而產生。 因此如專利文獻1所述,即便以搬送輥對之各搬送輥 負載成為同等之方式進行控制亦無法消除於複數個搬 送輥對之間產生的玻璃帶之實際之搬送速度即真實搬送速 度與搬送觀之圓周速度之相對速度之S,從而無法防止因 滑移導致之玻璃表面之損傷之產生。 又,若於複數個搬送輥對之間,在作為玻璃帶之搬送之 目標速度的必要搬送速度與搬送輥之圓周速度之間,相對 速度不固定、即產生相對速度之差,則於玻璃帶之真實搬 送速度慢於必要搬送速度之條件下,玻璃帶會於搬送輕對 之上方殘餘而導致變形’相反地,於真實搬送速度快於必 要搬送速度快之條件下’存在玻璃帶朝向下方拉伸,因產201247566 VI. Description of the Invention: [Technical Field of the Invention] The present invention relates to a method for producing a glass sheet and a shock for manufacturing a broken board. [Prior Art] The manufacturing method of the glass plate by the down-draw method is that the glass ribbon is stretched to a desired thickness by being pulled downward by the conveyance report, and further, to avoid strain inside, and Avoid the way the glass ribbon is warped and cool. The glass ribbon is cut to a specific size, and is loaded with each other via paper loss or the like, or conveyed in the subsequent step (for example, chemical processing of shape processing and ion exchange). As a method of manufacturing a glass sheet using the down-draw method, it is known that the rotation of each of the transport rollers is controlled by the same load to prevent slippage due to the difference in outer diameter between the transfer rollers. On the other hand, the transfer roller is prevented from being idling (Patent Document 1). According to this, it is possible to prevent breakage of the glass surface and the conveyance roller. Further, in the quenching furnace in which the ambient temperature and the temperature of the glass ribbon are changed in the direction in which the glass ribbon is conveyed, it is preferable to provide the circumferential speed of the conveying roller at each position in the conveying direction of the glass ribbon and the conveying speed of the glass ribbon. The relative speed is 0, but since the thermal expansion coefficient of the glass is different from the thermal expansion coefficient of the conveying roller, and the temperature dependence thereof is also different, the relative speed is not the same between the plurality of conveying roller pairs, and in the relative speed. Produce a difference. Such a difference in relative speed is caused, for example, by a change in the conveying speed or thickness of the glass ribbon, a change in the airflow generated in the quenching furnace, etc., resulting in a change in the temperature of the ring θ 4 clothing/m degree or the glass ribbon in the chilling furnace of the 163507.doc 201247566 And produced. Therefore, as described in Patent Document 1, it is impossible to eliminate the actual conveyance speed of the glass ribbon generated between the plurality of conveyance roller pairs, that is, the actual conveyance speed and conveyance even if the conveyance roller load of the conveyance roller pair is controlled to be equivalent. The S of the relative speed of the circumferential speed is observed, so that the damage of the glass surface caused by the slip cannot be prevented. Further, when between the plurality of conveying roller pairs, the relative speed is not fixed between the required conveying speed of the target speed of the conveyance of the glass ribbon and the peripheral speed of the conveying roller, that is, the difference in relative speed occurs. Under the condition that the actual conveying speed is slower than the necessary conveying speed, the glass ribbon will be deformed above the moving light and cause deformation. On the contrary, under the condition that the real conveying speed is faster than the necessary conveying speed, the glass ribbon is pulled downward. Stretch

S 生於其表面之微細之損傷而破碎之虞。 又,由於長時間連續地進行玻璃帶之成形及徐冷,故 而’玻璃板之製造裝置出現經時變化β因此,即便以可製 造向品質(内部應變、赵曲較小)之玻璃板之方式,初始設 定成形及徐冷時之製造條件,亦因長時間連續操作,而未 必能夠維持高品質之玻璃板。尤其,與玻璃帶接觸之搬送 報產生直徑變化,對玻璃板之品質會造成較大之影響。 [先前技術文獻] [專利文獻] [專利文獻1]曰本專利特表2008-501605號公報 【發明内容】 [發明所欲解決之問題] 163507.doc 201247566 因此,為解決上述問題,本發明之第1目的在於提供一 種即便製造設備因長時間之玻璃板之連續製造而產生經時 變化’亦可維持高品質之玻璃板之製造的玻璃板之製造方 法。第2目的在於提供一種可將因搬送輥之直徑變化而變 化之搬送輥之圓周速度維持為設定之圓周速度分佈,於複 數個搬送輥對間避免搬送輥之圓周速度與玻璃帶之搬送速 度的相對速度產生差值’藉此,可製造表面品質優異之玻 璃板的玻璃板之製造方法及玻璃板製造裝置。 [解決問題之技術手段] 本發明之一態樣係一種玻璃板之製造方法。 該製造方法包括: 熔解步驟,其將玻璃原料熔解而製作熔融玻璃; 成形步驟’其使許拉法將熔融玻鼓形,而形成玻璃 帶;及 徐冷步驟,其將上述玻璃帶由沿著上述玻璃帶之搬送方 向設置之複數個輥夾持並朝向下方氧引而進行徐冷。 上述成形步料括將上述玻㈣—面由輥料持並朝向 下方贫引,一面冷卻上述玻璃帶之兩端部之步驟。 上述成形步驟及上述徐冷步驟之任—者所使用之上述報 對中之至少任-個之輥對即第i輕對之各輥,係基於以補 償輥之直禋變化之方式決定之輥 視之%轉速度予以旋轉驅 動。 本發明之另一態樣係一種玻璃板之製造方法。 該製造方法包括: 163507.doc 201247566 炫解步驟, 成形步驟, 帶;及 其將玻璃原料熔解而製作熔融玻璃; 其使用下拉法將熔融玻璃成形,而形成玻璃 2冷步驟,其將上述玻璃帶由沿著上述玻璃帶之搬送方 "又置之複數個報對夾持並朝向下方良引而進行徐冷。 於上述徐冷步驟中,上述輥對中之至少任—個報對即第 1親對之各輥’係基於以補償輥之直徑變化之方式決定之 輥之旋轉速度予以旋轉驅動。 此時,較佳為,上述徐冷步驟包括:' 檢測步驟,其藉由沿著上述玻璃帶之搬送方向設置之檢 測部而檢測上述第1輕對之各輥之直控變化;及. 速度控制步驟’其基於檢測出之上述第i輥對之上述各 輥之直徑變化,決定上述各輥之旋轉速度,而使上述第i 輥對之上述各輥旋轉驅動。 較佳為’上述ΙΠ輥對之各輥係設置於上述徐冷步驟之 至少上述玻璃帶中央部之溫度成為玻璃轉移點以上且軟化 點以下之溫度區域内,且 在上述徐冷步驟中,以補償上述第1輥對之各輥之直徑 變化之方式,決定上述第1輥對之各輥之旋轉速度而2 上述第1輥對之各輥旋轉驅動。 較佳為上述成形步驟及上述徐冷步驟以如下方式進行 上述玻璃帶之溫度控制。 订 於上述玻璃帶之中央部之溫度為玻璃軟化點以上之區域 内’以上述玻璃帶之寬度方向之端部低於由上述端部所夾 163507.docS is born from the damage of the surface of the fine damage and broken. Further, since the glass ribbon is continuously formed and cold-cooled for a long period of time, the manufacturing apparatus of the glass sheet undergoes a change with time β, so that the glass sheet can be manufactured to a quality (internal strain, small curvature). The manufacturing conditions at the time of initial setting and cold cooling are also not allowed to maintain a high-quality glass plate due to continuous operation for a long time. In particular, the conveyance of the contact with the glass ribbon causes a change in diameter, which has a large influence on the quality of the glass sheet. [Prior Art Document] [Patent Document 1] [Patent Document 1] Japanese Patent Application Publication No. 2008-501605 [Draft] [Problems to be Solved by the Invention] 163507.doc 201247566 Therefore, in order to solve the above problems, the present invention A first object of the invention is to provide a method for producing a glass sheet which can maintain the manufacture of a high quality glass sheet even if the manufacturing equipment is changed over time due to continuous production of the glass sheet. A second object of the present invention is to provide a circumferential speed distribution in which the circumferential speed of a conveying roller which is changed by the change in the diameter of the conveying roller is maintained, and the peripheral speed of the conveying roller and the conveying speed of the glass ribbon are prevented between the plurality of conveying roller pairs. A difference in the relative speed is produced, whereby a method for producing a glass sheet of a glass sheet excellent in surface quality and a glass sheet manufacturing apparatus can be produced. [Technical means for solving the problem] One aspect of the present invention is a method for producing a glass plate. The manufacturing method includes: a melting step of melting a glass raw material to form a molten glass; a forming step of “forming a molten glass to form a glass ribbon by a pulling method; and a cold cooling step of separating the glass ribbon The plurality of rolls provided in the conveying direction of the glass ribbon are sandwiched and guided downward by oxygen to be quenched. The forming step includes the step of cooling the both ends of the glass ribbon by holding the glass (four)-face held by the roll and depleting it downward. At least one of the above-mentioned pairs of the above-mentioned forming steps and the above-mentioned cold-pressing step, that is, the first pair of rollers, which are determined by the method of compensating for the change of the straightness of the roller It is driven by rotation according to the % turning speed. Another aspect of the invention is a method of making a glass sheet. The manufacturing method comprises: 163507.doc 201247566 a dazzling step, a forming step, a belt; and melting the glass raw material to produce a molten glass; and forming a molten glass using a down-draw method to form a glass 2 cold step, which comprises the glass ribbon The cold is carried out by a plurality of reconciliations along the conveyor side of the glass ribbon. In the above-described cold cooling step, at least any one of the pair of rolls, i.e., the first pair of rolls, is rotationally driven based on the rotational speed of the roll determined by compensating for the diameter change of the roll. In this case, preferably, the step of cooling includes: a detecting step of detecting a direct control change of each of the first pair of rollers by a detecting portion provided along a conveying direction of the glass ribbon; and The control step 'determines the rotation speed of each of the rolls of the i-th roll pair, determines the rotation speed of each of the rolls, and rotationally drives the respective rolls of the i-th roll pair. Preferably, each of the roll sets of the pair of rolls is disposed in a temperature range in which at least the glass transition point is equal to or higher than a glass transition point and a softening point or less in the cold rolling step, and in the above-described cold cooling step, The rotation speed of each of the first roller pairs is determined so as to compensate for the change in the diameter of each of the first roller pairs, and the rollers of the first roller pair are rotationally driven. Preferably, the forming step and the quenching step are performed by controlling the temperature of the glass ribbon as follows. The temperature in the central portion of the glass ribbon is in the region above the softening point of the glass. The end portion in the width direction of the glass ribbon is lower than the end portion. 163507.doc

S -6 · 201247566 之中央區域之溫度、且上述中央區域之溫度成為大致均一 之方式進行控制。 進而,於上述玻璃帶之中央部之溫度為未達軟化點且為 應變點附近以上之區域内,以搬送方向之拉伸應力作用於 上述玻璃帶之中央部之方式進行控制,以使上述玻璃帶之 寬度方向之溫度自上述玻璃帶之中央部朝向端部變低。 進而,上述成形步驟及上述徐冷步驟中,於上述玻璃帶 之玻璃應變點附近之溫度區域内,以上述玻璃帶之寬度方 向之端部與中央部之溫度梯度消失之方式,控制上述玻璃 帶之溫度分佈。 較佳為,上述徐冷步驟中,於上述玻璃帶之中央部之溫 度未達應變點附近之區域内,以搬送方向之拉伸應力作用 於上述玻璃帶之中央部之方式控制上述玻璃帶之溫度分 佈以使上述玻璃帶之溫度分佈自上I玻璃帶之寬度方向 之端部朝向中央部變低。 較佳為,上述徐冷步驟係包括: 第1冷部步驟,其以第1平均冷卻速度進行冷卻,直至上 述玻璃帶之中央部之溫度達到徐冷點為止; 第2冷々卩步驟’其以第2平均冷卻速度進行冷卻,直至上 述中央β之酿度自上述徐冷點達到應變點_5代為止;及 第7卻步驟’其以第3平均冷卻速度進行冷卻,直至上 v中央#之’皿度自上述應變點達到上述應變點-觸。。 為止。 時上述第1平均冷卻速度係5.0°C /秒以上,上述第1 163507.doc 201247566 平均冷卻速度快於上述第3平均冷卻速度,且上述第3平均 冷卻速度快於上述第2平均冷卻速度。 較佳為’以補償由上述第1輥對之各輥之熱膨脹引起之 上述第1輥之各輥之直徑變化而產生的圓周速度之偏差之 方式,決疋上述第1輥對之各報之旋轉速度,而使上述第i 輥對之各輥旋轉驅動。 又’同樣地較佳為,以補償由上述第1輥對之各輥之磨 損引起之上述第1輥對之各輥之直徑變化而產生的圓周速 度之偏差之方式,決定上述第1輥對之各輥之旋轉速度, 而使上述第1親對之各親旋轉驅動。 上述複數個輥對中之具有基於以補償輥之直徑變化之方 式決定之輥之旋轉速度予以旋轉驅動之輥的輥對,除上述 第1輥對以外並包含第2輥對。 於該情形時,上述製造方法係包括檢測步驟,該檢測步 驟藉由沿著上述玻璃帶之搬送方向設置之複數個檢測部而 檢測上述第1輥對及上述第2輥對之各輥之直徑變化。而 且,於上述第1輥對之各輥與上述第2輥對之各輥之間,以 輥之圓周速度與上述玻璃帶之搬送速度之相對速度成為固 定之方式’決定補償上述各輥之直徑變化之上述各輥之旋 轉速度。 較佳為’上述製造方法藉由沿著玻璃帶之搬送方向設置 之檢測上述玻璃帶之狀態之玻璃狀態檢測部,檢測上述玻 璃帶之溫度; 使用檢測出之上述玻璃帶之溫度中之玻璃熱膨脹係數, 163507.doc 201247566 檢測由上述玻璃帶之熱膨脹引起之上述玻璃帶之搬送速度 之文化,且以補償上述玻璃帶之搬送速度與輥之圓周速度 之偏差之方式,決定上述第丨輥對之各輥之旋轉速度。 使上述玻璃帶徐冷而成之玻璃板之厚度例如為0.5 mm以 下。 又’本發明之一態樣係一種玻璃板製造裝置。該裝置包 括: 成形裝置’其使用下拉法,自熔融玻璃將玻璃帶成 形;及 徐冷裝置’其將上述玻璃帶一面由複數個搬送輥對夾持 並朝向下方曳引,一面進行徐冷。 上述徐冷裝置包括上述複數個搬送輥對、檢測控制部、 及驅動部。 上述複數個搬送輥對係沿著上述玻璃帶之搬送方向設 置’且藉由朝向下方拉入上述玻璃帶而搬送玻璃帶。 上述檢測控制部包括沿著上述玻璃帶之搬送方向設置、 且檢測上述搬送輥對之搬送輥之直徑變化之複數個搬送輥 狀態檢測部。 上述驅動部於上述複數個搬送輥對間,以保持上述搬送 輥之圓周速度與上述玻璃帶之搬送速度之相對速度成為固 定時的上述複數個搬送報對間之圓周速度分佈之方式,基 於由檢測出之上述搬送輥之直徑變化而決定之各上述搬送 輥之旋轉速度,使上述搬送輥旋轉驅動。 較佳為,上述搬送輥狀態檢測部係基於上述搬送輥之溫 163507.doc -9· 201247566 度而檢測上述搬送報之直徑變化,且 上述驅動部以補償由上述搬送輥之熱膨脹引起之上述輥 之直徑變化而產生的上述搬送輥之圓周速度之與上述圓周 速度分佈之偏差之方式,基於利用檢測出之上述搬送輥之 /ja度中之觀熱膨服係數決定之上述各搬送輥之旋轉速度, 使上述搬送輥旋轉驅動。 較佳為’上述檢測部更包括沿著上述玻璃帶之搬送方向 設置'檢測上述玻璃帶之狀態的複數個玻璃狀態檢測部, 且上述驅動部基於由上述玻璃帶之狀態設定之上述圓周速 度分佈,使上述搬送輥旋轉驅動。 較佳為’上述玻璃狀態檢測部檢測上述玻璃帶之溫 度,且 上述驅動部基於利用檢測出之上述玻璃帶之溫度中之玻 璃熱膨脹係數且相應於上述玻璃帶之熱膨脹導致之上述玻 璃帶之搬送速度變化而設定之上述圓周速度分佈,使上述 搬送輥旋轉驅動。 較佳為’上述搬送輥狀態檢測部基於上述搬送輥之磨損 量’檢測上述搬送輥之直徑變化,且 上述驅動部基於以補償由檢測出之上述搬送輥之磨損引 起之上述搬送輥之直徑變化而產生的上述搬送輥之圓周速 度之與上述圓周速度分佈之偏差之方式決定的上述各搬送 報之旋轉速度,使上述搬送輥進行旋轉驅動。 將上述玻璃帶徐冷所得之玻璃板之厚度例 如為0.5 mm以 下。 163507.doc 201247566 [發明之效果] 上述玻璃板之製造方法係即便玻璃帶接觸之搬送親等製 造設備因長時間之玻璃板之連續製造而產生經時變化,亦 可維持高品質之玻璃板之製造。又,上述玻璃板之製造方 法及玻璃板製造裝置可將因搬送輥之直徑變化而變化之搬 送軺之圓周速度維持為所設定之圓周速度分佈,於複數個 搬送輥對間避免搬送輥之圓周速度與玻璃帶之搬送速度之 相對速度產生差值。藉此,可製造表面品質優異之玻璃 板。 【實施方式】 以下’對本發明之玻璃板之製造方法及玻璃板製造裝置 詳細地進行說明。 本實施形態或其變形例之玻璃板之製造方法及製造裝置 係作為玻璃板之製造法之一步驟的成形步驟及徐冷步驟中 使用之輥對(冷卻輥對、搬送輥對)令的至少任一個輥對(第 1輥對)之各輥基於以補償輥之直徑變化之方式決定之輥之 旋轉速度’受到旋轉驅動β x,徐冷步驟係複數個搬送報 對中之至少1個輥對(第丨輥對)之各輥基於以補償輥之直徑 變化之方式決定之輥之旋轉速度,受到旋轉驅動。如此之 輥之旋轉速度係藉由利用計測檢測第i報對之各輕之直徑 變化’而以補償直徑變化之方式決定。即,根據輥之直徑 變化之檢測結果,反饋控制輥之旋轉速度。或者,輥之旋 轉速度係基於第1親對之各輥之使用天數之資訊而決定。 即’基於各輥之使用#„之資訊,财地決定輥之旋轉速 163507.doc •11- 201247566 度。「使用天數之資訊」係用於基於第1輥對之磨損的輥 直徑之變化之換算,且基於該輥直徑之變化之換算值,決 定輥之旋轉速度。將如此之輥之旋轉速度決定之第1輥對 既可為單數,又,亦可為複數。所謂「補償輥之直徑變 化」係指即便第1輥對之各輥之直徑變化,亦顧及該直經 之變化’維持直徑變化前之輥之合理之圓周速度。 又,本說明書中之下述語句係規定如下。 所謂徐冷點附近係指關於玻璃之黏度η為logll=12.5〜13.5 之範圍。 所謂玻璃之徐冷點係指關於玻璃之黏度η達到1〇gr) = 1 3之 溫度。 所謂玻璃之應變點係指關於玻璃之黏度η達到1〇gT1==14 5 之溫度。 所謂玻璃之應變點附近係指關於玻璃之黏度η達到 logn = 14〜15之溫度之範圍。 所謂玻璃帶之中央區域係指玻璃帶之寬度方向之寬度中 與玻璃帶之寬度方向之中心相距寬度之85%以内之範圍。 所謂玻璃帶之中央部係指玻璃帶之寬度方向之中心。 所謂玻璃帶之中央區域之溫度大致均一係指溫度包含於 ±20°C之容許範圍内。 所謂玻璃帶之端部係指與玻璃帶之寬度方向之邊緣相距 200 mm以内之範圍。 (玻璃板之製造方法) 圖1係說明本實施形態之玻璃板之製造方法之流程之一 163507.docThe temperature in the central region of S -6 · 201247566 is controlled so that the temperature in the central region is substantially uniform. Further, in a region where the temperature of the central portion of the glass ribbon is not higher than the softening point and is higher than the strain point, the tensile stress in the transport direction is applied to the central portion of the glass ribbon to control the glass. The temperature in the width direction of the belt is lowered from the central portion of the glass ribbon toward the end portion. Further, in the forming step and the cooling step, the glass ribbon is controlled such that the temperature gradient between the end portion and the central portion in the width direction of the glass ribbon disappears in a temperature region near the glass strain point of the glass ribbon Temperature distribution. Preferably, in the step of cooling, the glass ribbon is controlled such that the tensile stress in the transport direction acts on the central portion of the glass ribbon in a region where the temperature in the central portion of the glass ribbon is not near the strain point. The temperature distribution is such that the temperature distribution of the glass ribbon becomes lower from the end portion in the width direction of the upper I glass ribbon toward the central portion. Preferably, the cold cooling step includes: a first cold portion step of cooling at a first average cooling rate until a temperature at a central portion of the glass ribbon reaches a cold point; and a second cold rolling step Cooling is performed at the second average cooling rate until the center β degree is reached from the above-mentioned cold point to the strain point _5 generations; and the seventh step is 'cooling at the third average cooling rate until the upper v center# 'The degree of the dish reaches the above strain point-touch from the above strain point. . until. The first average cooling rate is 5.0 ° C /sec or more, the first 163507.doc 201247566 average cooling rate is faster than the third average cooling rate, and the third average cooling rate is faster than the second average cooling rate. Preferably, the method of determining the deviation of the circumferential speed caused by the change in the diameter of each of the rolls of the first roll caused by the thermal expansion of each of the first roll pairs is determined by the first roll pair. The rotation speed is used to rotationally drive the respective rollers of the i-th roller pair. Further, it is preferable that the first roller pair is determined such that the circumferential speed difference caused by the change in the diameter of each of the first roller pairs caused by the abrasion of each of the first roller pairs is compensated. The rotation speed of each of the rolls is driven by the rotation of each of the first pair of parents. A pair of rollers having a roller that is rotationally driven based on a rotational speed of the roller determined by compensating for a change in the diameter of the roller among the plurality of roller pairs includes a second roller pair in addition to the first roller pair. In this case, the manufacturing method includes a detecting step of detecting a diameter of each of the first roller pair and the second roller pair by a plurality of detecting portions provided along a conveying direction of the glass ribbon Variety. Further, between the respective rolls of the first pair of rolls and the rolls of the second pair of rolls, the diameter of each of the rolls is determined to be fixed so that the relative speed of the peripheral speed of the rolls and the conveying speed of the glass ribbon are fixed. The rotational speed of each of the above rolls is varied. Preferably, the manufacturing method detects the temperature of the glass ribbon by detecting a state of the glass ribbon in a direction in which the glass ribbon is conveyed in the direction in which the glass ribbon is conveyed, and uses the detected thermal expansion of the glass in the temperature of the glass ribbon. Coefficient, 163507.doc 201247566 Detects the culture of the above-mentioned glass ribbon conveyance speed caused by the thermal expansion of the above-mentioned glass ribbon, and determines the above-mentioned nip roller pair by compensating for the deviation between the transport speed of the glass ribbon and the peripheral speed of the roller. The rotational speed of each roller. The thickness of the glass plate obtained by subjecting the glass ribbon to a cold is, for example, 0.5 mm or less. Further, an aspect of the present invention is a glass sheet manufacturing apparatus. The apparatus includes: a molding apparatus which uses a down-draw method to form a glass ribbon from molten glass; and a quenching apparatus which presses the glass ribbon by a plurality of conveying roller pairs and pulls it downward to perform cold cooling. The subcooling device includes the plurality of conveying roller pairs, the detection control unit, and the driving unit. The plurality of conveying roller pairs are disposed along the conveying direction of the glass ribbon, and the glass ribbon is conveyed by pulling the glass ribbon downward. The detection control unit includes a plurality of conveyance roller state detecting sections that are provided along the conveyance direction of the glass ribbon and that detect a change in the diameter of the conveyance roller of the conveyance roller pair. The driving unit is configured to maintain a circumferential speed distribution between the plurality of transporting pairs when the relative speed of the peripheral speed of the transport roller and the transport speed of the glass ribbon is fixed between the plurality of transport roller pairs The rotation speed of each of the conveyance rollers determined by the change in the diameter of the conveyance roller is detected, and the conveyance roller is rotationally driven. Preferably, the conveyance roller state detecting unit detects a change in diameter of the conveyance report based on a temperature of the conveyance roller of 163507.doc -9·201247566 degrees, and the drive unit compensates the roller caused by thermal expansion of the conveyance roller. The deviation of the peripheral speed of the transport roller caused by the change in diameter and the circumferential speed distribution is determined based on the rotation of each of the transport rollers determined by the detected thermal expansion coefficient in the /ja degree of the transport roller The speed is such that the conveying roller is rotationally driven. Preferably, the detecting unit further includes a plurality of glass state detecting portions that are provided along the conveying direction of the glass ribbon to detect the state of the glass ribbon, and the driving portion is configured based on the circumferential speed distribution set by the state of the glass ribbon. The rotation of the transport roller is driven. Preferably, the glass state detecting unit detects the temperature of the glass ribbon, and the driving unit transmits the glass ribbon based on a glass thermal expansion coefficient in the temperature of the glass ribbon detected and corresponding to thermal expansion of the glass ribbon. The circumferential speed distribution set by the speed change causes the conveyance roller to be rotationally driven. Preferably, the conveyance roller state detecting unit detects a change in the diameter of the conveyance roller based on the amount of wear of the conveyance roller, and the drive unit compensates for a change in the diameter of the conveyance roller caused by the detected abrasion of the conveyance roller. The conveyance roller is rotationally driven by the rotation speed of each of the conveyance reports determined by the deviation of the peripheral speed of the conveyance roller from the circumferential speed distribution. The thickness of the glass plate obtained by quenching the above glass ribbon is, for example, 0.5 mm or less. 163507.doc 201247566 [Effects of the Invention] The method for producing a glass sheet is to maintain a high-quality glass sheet even if the glass-belt-contacting production equipment is changed over time due to continuous production of the glass sheet for a long period of time. . Further, in the method for producing a glass sheet and the glass sheet manufacturing apparatus, the peripheral speed of the conveyance crucible which is changed by the change in the diameter of the conveyance roller can be maintained at the set circumferential speed distribution, and the circumference of the conveyance roller can be avoided between the plurality of conveyance roller pairs. The difference between the speed and the relative speed of the transport speed of the glass ribbon. Thereby, a glass plate excellent in surface quality can be produced. [Embodiment] Hereinafter, a method for producing a glass sheet and a glass sheet manufacturing apparatus of the present invention will be described in detail. The method and apparatus for producing a glass sheet according to the embodiment or its modification are at least one of a forming step of a method for producing a glass sheet and a pair of rolls (a pair of cooling rolls and a pair of conveying rolls) used in the step of cooling. Each of the rollers of the pair of rollers (the first pair of rollers) is driven to rotate by β x based on the rotational speed of the roller determined by the diameter of the compensation roller, and the cold cooling step is at least one of a plurality of conveying reports. Each of the rolls of the (second roll pair) is rotationally driven based on the rotational speed of the roll which is determined in such a manner as to compensate for the change in the diameter of the roll. The rotation speed of such a roller is determined by compensating for the change in diameter by detecting the change in the diameter of each of the ith reports. Namely, the rotation speed of the control roller is fed back based on the detection result of the change in the diameter of the roller. Alternatively, the rotational speed of the rolls is determined based on the information on the number of days of use of each of the first pair of rolls. That is, based on the information of the use of each roller, the rotation speed of the roller is determined by the financial position 163507.doc •11-201247566 degrees. The “Information on the number of days of use” is used to change the diameter of the roller based on the wear of the first roller pair. The conversion speed is determined based on the converted value of the change in the diameter of the roll. The first roller pair which determines the rotation speed of such a roller may be singular or plural. The "diameter change of the compensation roller" means a reasonable circumferential speed of the roller before the change in diameter is maintained in consideration of the change in the diameter of each roller of the first roller pair. In addition, the following statements in this specification are as follows. The term "cold cold point" refers to a range in which the viscosity η of the glass is logll=12.5 to 13.5. The so-called cold spot of glass refers to the temperature at which the viscosity η of the glass reaches 1〇gr) = 1 3 . The strain point of the glass refers to a temperature at which the viscosity η of the glass reaches 1〇gT1==14 5 . The vicinity of the strain point of the glass refers to a range in which the viscosity η of the glass reaches a temperature of logn = 14 to 15. The central region of the glass ribbon refers to a range within 85% of the width of the width direction of the glass ribbon in the width direction of the glass ribbon. The central portion of the glass ribbon refers to the center of the width direction of the glass ribbon. The fact that the temperature in the central portion of the glass ribbon is substantially uniform means that the temperature is within the allowable range of ±20 °C. The end portion of the glass ribbon refers to a range within 200 mm from the edge in the width direction of the glass ribbon. (Manufacturing Method of Glass Plate) FIG. 1 is a flow chart showing the method of manufacturing the glass plate of the present embodiment. 163507.doc

•12· S 201247566 圖玻璃板之製造方法主要包括熔解步驟(步驟 si〇)、澄清步驟(步驟S20)、攪拌步驟(步驟s3〇)、成形步 驟(步驟S40)、徐冷步驟(步驟S5〇)、裁板步驟(步驟㈣)、 及形狀加工步驟(步驟S70)。 在熔解步驟(步驟sl〇)中’於未圖示之熔解爐中,將玻 璃原料ί]用來自其上方之間接加熱、及利用使電流流入玻 璃中的直接加熱而加熱至高溫,製作溶融玻璃。玻璃之溶 解亦可由除此以外之方法進行。 其次,進行澄清步驟(步驟S2〇)。澄清步驟係於熔融玻 璃蓄積於未圖示之液槽中之狀態下,例如與熔解步驟中之 加熱時相比更使熔融玻璃之溫度上升,藉此,促進熔融玻 璃中之氣泡之消泡。藉此,可降低最終所得之玻璃板中之 氣泡含有率,從而可使良率提昇。 澄清步驟亦可藉由其他方法進行,例如亦可於熔融玻璃 蓄積於液槽中之狀態下,使用澄清劑去除熔融玻璃中之氣 泡。作為澄清劑無特別限制’例如使用氧化錫、氧化鐵等 金屬氧化物。具體而言,該情形時之澄清步驟係藉由於熔 融玻璃中價數變動之金屬氧化物之氧化還原反應而進行。 於高溫時之熔融玻璃中,金屬氧化物藉由還原反應而釋放 氧’該氧變成氣體’使熔融玻璃中之氣泡成長而浮上液 面。藉此,熔融玻璃中之氣泡被消泡。或者,使氧氣之氣 泡吸取熔融玻璃中之其他氣泡中之氣體而成長,從而浮上 溶融玻璃之液面。藉此,炫融玻璃中之氣泡被消泡。進 而’若熔融玻璃之溫度降低’則金屬氧化物藉由氧化反應 163507.doc -13- 201247566 而吸收熔融玻璃中殘存之氧,使熔融玻璃中之氣泡減少。 其次’進行攪拌步驟(步驟S30)。攪拌步驟係藉由搜摔 裝置而機械性攪拌熔融玻璃,以保持玻璃之化學及熱均一 性。藉此,可抑制脈理等之玻璃之不均一性。 其次,進行成形步驟(步驟S40)。成形步驟係採用下拉 法。包括溢流下拉法或流孔下引法等之下拉法係例如專利 第3586142號公報或使用圖3及圖4所示之裝置的公知之方 法。對下拉法中之成形步驟將於下文敍述。藉此,將具有 特定之厚度、寬度之板狀之玻璃帶成形。作為成形方法, 於下拉法中,最佳為溢流下拉法’但亦可為流孔下引法。 成形步驟包括將藉由成形而形成之玻璃帶一面由辕對夾持 並朝搬送方向之下方(下游側之方向)曳引,一面冷卻玻璃 帶之兩端部之步驟。 其次’進行徐冷步驟(步驟S50)。徐冷步驟係將成形為 板狀之玻璃帶以不產生應變或降低應變之方式控制冷卻速 度,於圖3及圖4所示之徐冷爐中冷卻至徐冷點以下。具體 而言’於玻璃帶之寬度方向端部將在寬度方向上鄰接之附 近區域’ 一面由沿著玻璃帶之搬送方向至少設置有2個以 上之複數個搬送輥對夾持並以預先設定之搬送速度朝向下 方曳引’一面進行徐冷。 圖2係說明徐冷步驟之流程之一例之圖。徐冷步驟包括 檢測步驟(步驟S51)、速度決定步驟(步驟S52) '及速度控 制步驟(步驟S53)。再者,本實施形態之玻璃板之製造方 法雖包括檢測步驟(步驟S51),但亦可如下述變形例所述• 12· S 201247566 The manufacturing method of the glass plate mainly includes a melting step (step si〇), a clarification step (step S20), a stirring step (step s3〇), a forming step (step S40), and a cold cooling step (step S5〇). ), a paneling step (step (4)), and a shape processing step (step S70). In the melting step (step sl), in the melting furnace (not shown), the glass raw material is heated to a high temperature by direct heating from above, and direct heating by flowing a current into the glass to produce a molten glass. . The dissolution of the glass can also be carried out by other methods. Next, a clarification step (step S2 〇) is performed. The clarification step is carried out in a state where the molten glass is accumulated in a liquid tank (not shown), for example, the temperature of the molten glass is increased as compared with the heating in the melting step, whereby the defoaming of the bubbles in the molten glass is promoted. Thereby, the bubble content in the finally obtained glass plate can be lowered, and the yield can be improved. The clarification step can also be carried out by other methods, for example, by using a clarifying agent to remove the bubbles in the molten glass while the molten glass is accumulated in the liquid tank. The clarifying agent is not particularly limited. For example, a metal oxide such as tin oxide or iron oxide is used. Specifically, the clarification step in this case is carried out by a redox reaction of a metal oxide whose valence is varied in the molten glass. In the molten glass at a high temperature, the metal oxide releases oxygen by the reduction reaction, and the oxygen becomes a gas, and the bubbles in the molten glass grow to float on the liquid surface. Thereby, the bubbles in the molten glass are defoamed. Alternatively, the bubble of oxygen is sucked up by the gas in the other bubbles in the molten glass to grow, thereby floating on the liquid surface of the molten glass. Thereby, the bubbles in the glazed glass are defoamed. Further, if the temperature of the molten glass is lowered, the metal oxide absorbs oxygen remaining in the molten glass by the oxidation reaction 163507.doc -13 - 201247566 to reduce the bubbles in the molten glass. Next, the stirring step is performed (step S30). The agitation step mechanically agitates the molten glass by means of a search device to maintain the chemical and thermal uniformity of the glass. Thereby, the unevenness of the glass such as the pulse can be suppressed. Next, a forming step (step S40) is performed. The forming step is a pull-down method. The following methods include an overflow down-draw method or a flow-down method, such as Patent No. 3586142, or a known method using the apparatus shown in Figs. 3 and 4. The forming steps in the downdraw method will be described below. Thereby, a glass ribbon having a plate thickness of a specific thickness and width is formed. As the forming method, in the down-draw method, the overflow down method is preferable, but the orifice down method can also be used. The forming step includes a step of cooling the both ends of the glass ribbon while the glass ribbon formed by molding is pulled by the crucible pair and pulled downward in the conveying direction (the direction of the downstream side). Next, the step of cooling is performed (step S50). The Xu cold step is to form a glass ribbon which is formed into a plate shape to control the cooling rate without strain or strain reduction, and is cooled to below the freezing point in the quench furnace shown in Figs. 3 and 4 . Specifically, 'the vicinity of the width direction of the end portion in the width direction of the glass ribbon' is held by at least two or more transport roller pairs provided along the direction in which the glass ribbon is conveyed, and is set in advance. The conveying speed is pulled downwards and the side is cold. Fig. 2 is a view showing an example of the flow of the step of cooling. The cold step includes a detecting step (step S51), a speed determining step (step S52)', and a speed controlling step (step S53). Further, although the method of manufacturing the glass sheet of the present embodiment includes the detecting step (step S51), it may be as described in the following modification.

163507.doc •14- S 201247566 不進行檢測步驟,而於徐冷步驟中包括速度決定步驟(步 驟S52)、及速度控制步驟(步驟S53)。 檢測步驟(步驟S51)係藉由沿著玻璃帶之搬送方向分別 與上述複數個搬送輥對對應地設置之複數個檢測部,檢測 複數個搬送輥對之各搬送輥之直徑變化。作為搬送輥之直 徑變化,例如可列舉基於搬送輥之溫度或搬送輥之磨損量 算出之搬送輥之直徑變化量。該情形時之檢測部例如包括 下述溫度感測器或距離測定感測器、及與該等感測器連接 之電腦。作為徑’可列舉搬送輥之直徑或半徑。 速度決疋步驟(步驟S52)係設定在複數個搬送報對間搬 送輥之圓周速度與玻璃帶之搬送速度之相對速度固定、即 相對速度中不產生差值時的複數個搬送輥對間之圓周速度 分佈’且基於檢測出之搬送輥之直徑變化,以保持設定之 圓周速度分佈之方式,決定各搬送輥之旋轉速度。作為圓 周速度分佈’例如可利用複數個搬送輥對間之圓周速度 比、各搬送觀之具體之圓周速度。此處,由於玻璃帶不產 生損傷或形狀變形時之相對速度為〇,故所謂相對速度中 產生差值係指於複數個搬送輥對中某對之相對速度為〇, 而其他對之相對速度不為〇之類的相對速度具有分佈β 例如於搬送輥之直徑變化係基於溫度算出之搬送輥之熱 膨脹量(直徑之變化量)之情形時,具體而言,如同藉由下 述檢測部37及速度決定部38進行般,利用檢測出之搬送輥 之溫度中之輥熱膨脹係數,以補償因搬送輥之熱膨脹導致 之輥直徑之變化而產生的搬送輥之圓周速度之與圓周速度 163507.doc 15 201247566 分佈之偏差之方式,即以將各搬送輥之圓周速度維持為設 定之圓周速度分佈之方式,決定搬送輥之旋轉速度。搬送 輥之熱膨脹係數係預先記憶於速度決定部3 8中。再者,搬 送輥之圓周速度係例如藉由以形成之玻璃帶達到製造之玻 璃板之板厚之方式進行調整而決定。 又’例如於搬送輥之直徑變化係基於其磨損量算出之搬 送報之半徑之變化量之情形時,具體而言,如同按照下述 第2實施形態進行般,以補償因檢測出之搬送輥之磨損導 致之搬送報之半徑之變化而產生的搬送報之圓周速度之與 圓周速度分佈之偏差之方式,即將各搬送輥之圓周速度維 持為設定之圓周速度分佈之方式,決定搬送輥之旋轉速 度。 再者,速度決定部38亦可基於操作人員輸入之内容,決 定各搬送輥之旋轉速度。於該情形時,操作人員亦可基於 檢測出之搬送報之直徑變化’算出各搬送輥之旋轉速度, 以保持設定之圓周速度分佈。例如於搬送報之直徑變化係 上述熱膨脹量之情形時,操作人員可基於檢測出之搬送輥 之溫度’以補償因搬送輥之熱膨脹導致之輥直徑之變化而 產生的搬送輥之圓周速度之與圓周速度分佈之偏差之方 式’即將各搬送輥之圓周速度維持為設定之圓周速度分佈 之方式’算出搬送輥之旋轉速度。算出後經輸入之各搬送 親之旋轉速度係藉由速度決定部38而決定,且於速度控制 步驟(步驟S53)中控制搬送輥之旋轉。 速度控制步驟(步驟S53)係基於在速度決定步驟中決定163507.doc • 14- S 201247566 The detection step is not performed, and the speed determination step (step S52) and the speed control step (step S53) are included in the cold step. In the detecting step (step S51), the diameters of the respective conveying rollers of the plurality of conveying roller pairs are detected by a plurality of detecting portions provided corresponding to the plurality of conveying roller pairs in the conveying direction of the glass ribbon. The change in the diameter of the conveying roller is, for example, the amount of change in the diameter of the conveying roller calculated based on the temperature of the conveying roller or the amount of wear of the conveying roller. The detecting portion in this case includes, for example, a temperature sensor or a distance measuring sensor described below, and a computer connected to the sensors. The diameter 'is a diameter or a radius of a conveyance roller. The speed determination step (step S52) sets a plurality of conveying roller pairs when the relative speed of the peripheral speed of the plurality of conveying inter-feeding conveying rollers and the conveying speed of the glass ribbon is fixed, that is, when no difference occurs in the relative speed. The circumferential speed distribution 'and the rotation speed of each conveying roller is determined so as to maintain the set circumferential speed distribution based on the detected change in the diameter of the conveying roller. As the circumferential speed distribution ', for example, a peripheral speed ratio between a plurality of conveying roller pairs and a specific peripheral speed of each conveying view can be used. Here, since the relative speed of the glass ribbon is not damaged or the shape is deformed, the difference in the relative speed means that the relative speed of a pair of the plurality of conveying roller pairs is 〇, and the other relative speeds The relative velocity such as the enthalpy has a distribution β. For example, when the diameter change of the conveying roller is based on the temperature-calculated amount of the thermal expansion of the conveying roller (the amount of change in the diameter), specifically, the following detecting portion 37 is used. In the same manner as the speed determining unit 38, the circumferential speed of the conveying roller caused by the change in the diameter of the roller due to the thermal expansion of the conveying roller is compensated by the detected coefficient of thermal expansion of the roller in the temperature of the conveying roller. 15 201247566 The deviation of the distribution is such that the rotation speed of the conveyance roller is determined such that the circumferential speed of each conveyance roller is maintained at the set circumferential speed distribution. The thermal expansion coefficient of the transfer roller is previously stored in the speed determining unit 38. Further, the peripheral speed of the conveying roller is determined, for example, by adjusting the thickness of the glass plate to be produced by the formed glass ribbon. Further, for example, when the change in the diameter of the transfer roller is based on the amount of change in the radius of the conveyance report calculated based on the wear amount, specifically, the conveyance roller is compensated for as described in the second embodiment described below. The deviation of the circumferential speed of the conveyance report caused by the change in the radius of the conveyance report due to the wear and tear, that is, the circumferential speed of each conveyance roller is maintained at the set circumferential speed distribution, and the rotation of the conveyance roller is determined. speed. Further, the speed determining unit 38 may determine the rotational speed of each of the transport rollers based on the contents input by the operator. In this case, the operator can calculate the rotational speed of each transport roller based on the detected diameter change of the transport report to maintain the set circumferential speed distribution. For example, when the diameter change of the conveyance report is the above-described thermal expansion amount, the operator can compensate the circumferential speed of the conveyance roller caused by the change in the diameter of the roller due to the thermal expansion of the conveyance roller based on the detected temperature of the conveyance roller. The method of calculating the deviation of the circumferential speed distribution 'calculates the circumferential speed of each of the conveying rollers to the set circumferential speed distribution' is calculated as the rotational speed of the conveying roller. The rotation speed of each of the transports that have been input after the calculation is determined by the speed determining unit 38, and the rotation of the transport roller is controlled in the speed control step (step S53). The speed control step (step S53) is based on determining in the speed decision step

163507.doc Μ S 201247566 之旋轉速度,控制搬送輥之旋轉。 具體而 裁板得 丄於上述徐冷”後,進行裁板步驟(步驟⑽)。 5 ’將連續生成之玻璃帶切斷為每—個固定長产, 到玻璃板。 < & 其後,進行形狀加工步驟(步驟㈣)。形狀加工 不僅切取特定之玻璃板之尺寸或形一 之研s,丨' 裔y 一 且進行玻璃端面 物理性;^ °形狀加工既可制制有切割機或雷射之 物理性方法,亦可利用㈣等化學性方法。 又’較佳為’成形步驟及徐冷㈣係於麵帶之中 之溫度為玻璃軟化點以上之區域内,以破璃帶之寬度二 之端部低於由上述端部夾隔之中央區域之溫度、且=央區 域之溫度達到大致均-之方式控制玻㈣之溫度,以抑: 玻璃帶之寬度方向之收縮。此時,於抑制玻璃板之翹曲之 方面’較佳為,於玻璃帶之令央部之溫度未達軟化點且為 應變點附近以上之區域内’以搬送方向之拉伸應力作用於 玻璃帶之中央部之方式,控制玻璃帶之溫度,以使玻璃帶 之寬度方向之溫度自玻璃帶之中央部朝向端部下降。進 而,於抑制玻璃板之内部應變之方面’較佳為,於玻璃帶 之溫度達到應變點之附近之溫度區域内,以玻璃帶之寬度 方向之端部與中央部之溫度梯度消失之方式,控制玻璃= 之溫度分佈。 進而’於抑制玻璃帶之搬送方向之翹曲之方面,較佳 為,於玻璃帶之中央部之溫度未達應變點附近之區域内, 以搬送方向之拉伸應力作用於玻璃帶之中央部之方式,控 163507.doc •17· 201247566 制玻璃帶之溫度分佈,以使該玻璃帶之溫度分佈自玻璃帶 之寬度方向之端部朝向中央部降低。 進而,較佳為,徐冷步驟包括第丄冷卻步驟其以^平 均冷卻速度進行冷卻’直至玻璃帶之中央部之溫度達到徐 冷點為止;第2冷卻步驟’其以第2平均冷卻速度進行冷 卻’直至玻璃帶之中央部之溫度自徐冷點達到應變點-贼 為止;及第3冷卻步驟,其以第3平均冷卻速度進行冷卻, 直至玻璃帶之中央部之溫度自應變點·5(rc達到應變點· 為止。於該情形時’第i平均冷卻速度係5〇口秒以上,且 第1平均冷卻速度快於第3平均冷卻速度,第3平均冷卻速 度快於第2平均冷卻逮度。肖卩,平均冷卻速度由高至低依 序為第1平均冷卻速度、第3平均冷卻速度 '第2平均冷卻 速度。玻璃帶之搬送方向之冷卻速度對製造之玻璃板之熱 收縮迈成影響。然而,如上所述,於徐冷步驟中可藉由 »又疋冷卻速度,而一面提昇玻璃板之製造量,一面獲得具 有較佳之熱收縮率之玻璃板。 此外,玻璃板之製造方法包括清洗步驟及檢查步驟但 省略該等步驟之說明。再者,澄清步驟及攪拌步驟可分別 省略。 (玻璃板製造裝置) 圖3及圖4係作為本發明之第丨實施形態的玻璃板製造裝 置1之概略構成圖。本實施形態之玻璃板製造裝置1及使用 有玻璃板製造裝置1之玻璃板之製造方法可較佳地應用於 液b日顯示裝置或有機EL(Electro Luminescence,電致發光) 163507.doc 201247566 顯示裝置等平板顯示器之玻璃基板或便攜式終端設備之顯 示面之防護玻璃之製造。其原因在於液晶顯示裝置或有機 EL顯示裝置等近年來要求高精度、高晝質,故對於用於其 之玻璃基板要求較高之表面品質。又,其原因在於,由於 防護玻璃應用於裝置之顯示面等,故對於用於其之玻璃基 板要求極南之表面品質。 玻璃板製造裝置1係利用下拉法由熔融玻璃A製造玻璃板 玻璃板製造裝置1係包括由配置於上下方向之3個部位 的隔熱板21、22 '23隔離而成之爐室11、第1徐冷爐12、 第2徐冷爐13、及未圖示之裁板室。隔熱板21〜23係包含陶 莞纖維等隔熱材料之板狀構件。於隔熱板21〜23中分別形 成有搬送孔16,以使下述玻璃帶b朝向下方通過^隔熱板 21〜23分別於圖3中,為易於理解而將與下述爐壁15接觸之 水平方向之2個部位去除,且省略圖示,但對於玻璃帶B, 於紙面前面側及背面側,—體地連接有水平方向之2個部 位彼此。再者,於圖3及圖4中表示有藉由隔熱板而於3個 邛位進行隔離之例,但隔熱板之個數及設置位置並無特別 :定,隔熱板設置i個以上即可。再纟,由於隔熱板之數 1越多’則可獨立地控制環境溫度之空間越多,環境温度 之調整(徐冷條件之調整)變得越容易,故而,較佳為,徐 冷裝置3 &置複數個隔熱板而隔離成複數個空間。換古 之,徐冷爐雖設置㈣以上即可,但更佳為設置3個以上f 玻璃板製造裝置丨係包括成形裝置2、徐冷裝置3、及裁 板裝置4。 163507.doc .19· 201247566 成形裝置2係自熔融玻璃A利用下拉法使玻璃帶B成形之 裝置。成形裝置2係包括以由耐火磚或塊狀之電鑄耐火物 等組裝而成之爐壁15包圍之爐室u。於爐室丨丨内設置有成 形體10、及輥對(冷卻輥對)17。成形體1〇係包括朝上方開 放之槽10a(參照圖4),且熔融玻璃A於槽1〇a内流動。成形 體10係包括例如煉磚。輥對17係於與在成形體1〇之下端融 合之熔融玻璃A之寬度方向兩側之端部對應之位置分別設 置1對,且一面將熔融玻璃A夾持著朝向下方曳引,一面將 玻璃帶B之兩端部冷卻之冷卻輥之對。再者,圖3中紙面内 之左右方向及圖4中之垂直於紙面之方向係玻璃帶B之寬度 方向。圖3及圖4中紙面内之上下方向係玻璃帶8之搬送方 向。再者,於圖3及圖4中,成形體1〇與輥對17係未隔離地 設置’但為使徐冷條件之調整變得容易,亦可於該等之間 設置隔熱板進行隔離。又,報對17亦可設置2對以上。 此時,於成形步驟令,玻璃帶3之溫度位於自高於軟化 點之溫度至達到徐冷點附近為止之溫度區域時,較佳為, 以一面朝向玻璃帶之兩端部施加張力,一面以關於兩端部 之黏度11達到1叫11=9.0〜14.5之方式進行冷卻。該冷卻例如 藉由輥對17夾持玻璃帶b之兩端部而進行β 藉由利用作為冷卻輥的輥對17之各輥對玻璃帶17之兩端 部進行冷卻,而使兩端部之黏度上升,因此,可抑制玻璃 帶Β之寬度之收縮。 (徐冷裝置) 徐冷裝置3係將玻璃帶β—面由複數個搬送挺對Μ、β夾 163507.doc • 20- 201247566 持者朝向下方曳引,一面進行徐冷。徐冷裝置3係包括鄰 接地設置於爐室丨丨之下方之第丨徐冷爐12及第2徐冷爐13。 第1徐冷爐12及第2徐冷爐13係由亦構成爐室丨丨之上述爐壁 15包圍而成。徐冷裝置3係於第丨徐冷爐12及第2徐冷爐13 内設置有沿著玻璃帶B之搬送方向配置之由下述電腦自動 控制之加熱機構。加熱機構並無特別限制,例如可使用電 加熱器。於第1徐冷爐12内設置有沿玻璃帶B之搬送方向配 置之3個搬送親對18。於第2徐冷爐丨3内設置有沿玻璃帶B 之搬送方向配置之4個搬送輥對19 ^進而,徐冷裝置3係包 括檢測控制部30及驅動部32(參照圖5)。再者,徐冷爐12、 13内之搬送輥對18、19之設置數並無限制,設置至少“固 以上即可。 搬送輥對18、19係藉由朝向下方拉入玻璃帶b而搬送玻 璃帶B。各搬送輥對18係包括以夾持與玻璃帶b之寬度方 向兩端部鄰接之附近區域之方式配置於玻璃帶B之兩側的4 個搬送輥18a、及將位於與玻璃帶b相同側之2個搬送輥18a 連結且配置於玻璃帶B之兩側之2根驅動用轴18b。各搬送 輥對19係包括以夾持與玻璃帶B之寬度方向兩端部鄰接之 附近區域之方式配置於玻璃帶B之兩側的4個搬送輥19a、 及將位於與玻璃帶B相同側之2個搬送輥19a連結且配置於 玻璃帶B之兩側之2根驅動用轴19b。於圖3中,驅動用轴 18b、19b之兩端部省略圖示。再者,於圖3中,搬送輥 18a、19a並不限定於上述者。例如搬送輥i8a、19a亦可為 位於與玻璃帶B相同面側者彼此未由驅動用轴連結,而與 163507.doc •21- 201247566 輥對17之輥同樣地獨立配置於玻璃帶3之寬度方向兩端部 者。 於進行徐冷步驟之徐冷裝置3中,較佳為使玻璃帶B之溫 度分佈於寬度方向上成為山峰之分佈,其後,以使山峰之 分佈伴隨進入搬送方向下游側而逐漸減小之方式,進行配 置於玻璃帶B之周圍之加熱器等之控制。此時,於玻璃帶 B之應變點附近之溫度區域内,較佳為以山峰之分佈成為 平坦之直線狀之分佈、即寬度方向之溫度分佈成為固定之 方式,進行未圖示之加熱器等之控制。換言之,於自玻璃 帶B之徐冷點加上15〇t之溫度起直至應變點為止之溫度區 域内,較佳為,以使玻璃帶之寬度方向上之中央部之冷卻 速度快於寬度方向之兩端部之冷卻速度,且玻璃帶B之寬 度方向上之中央部之溫度自高於兩端部之狀態起,於應變 點附近之溫度區域内成為相同之方式,使溫度分佈成為固 疋。可藉由成為如此之溫度分佈,使拉伸應力朝向玻璃帶 之搬送方向之下游側作用。因此,玻璃帶B可抑制搬送方 向之翹曲。又,由於在應變點附近之溫度區域成為均一之 溫度分佈,故而可於玻璃板中降低内部應變。 進而,於玻璃帶B之溫度自徐冷點成為(應變點_5〇t>c )之 溫度内,較佳為,與其他溫度區域相比,緩慢地將玻璃帶 B徐冷。藉此,可降低玻璃帶8之熱收縮率。 進而,於玻璃帶B之溫度自應變點成為將應變點減去 200 ^所得之溫度的溫度區域内,較佳為,以使玻璃帶B之 溫度分佈沿寬度方向成為山谷、且該山谷之深度伴隨進入 163507.doc -22· 201247566 搬送方向下游側而變大之古4 變大之方式,即以中央部之溫度與兩端 部相比逐漸降低之方式,進行未圖示之加熱器等之控制。 可糟由以此方式,於溫度分佈中逐漸使山谷變深,而使拉 伸應力朝向搬送方向下游側作 1〗作用因此,可抑制搬送方向 之魅曲。 如圖5所示,檢測控制部3〇包括作為搬送輥狀態檢測部 (以下’亦簡稱為檢測部)37及速度決定部38發揮功能之未 圖示之電腦。圖5係說明控·送輥對18、19之旋轉驅動 的控制系統之構成之方塊圖。檢測部37具有與搬送輥對 18、19對應地配置之溫度感測器(玻璃狀態檢測部)3卜速 度決疋部38經由驅動部32而連接於搬送輥對丨8、丨9。檢測 控制部3 0之詳細情況將於下文敍述。 驅動部32係基於由速度決定部38決定之各搬送輥18&、 19a之旋轉速度,使搬送輥18a、i9a旋轉驅動。驅動部w 具有與各搬送輥對18、19對應地設置之未圖示之馬達。再 者’馬達亦可不對應於各搬送輥對18、19設置,且其數量 例如亦可少於各搬送輥對18、19之數量。於該情形時,可 使用具備可於各搬送輥18a、19a間變更速度比之齒輪者, 以利用1個馬達驅動複數個搬送輥18a、19a。於該情形 時,來自馬達之驅動力係例如經由萬向接頭等傳遞至搬送 輞il8a、19a〇 (檢測控制部) 此處,對檢測控制部30進一步詳細地進行說明。再者, 由檢測控制部30進行之檢測步驟(步驟S5 1)係如上所述於 163507.doc -23- 201247566 本實施形態中進行,但亦可如下述變形例所述不進行檢測 步驟’且徐冷步驟包括速度決定步驟及速度控制步驟。於 該情形時’不使用檢測控制部3 0。 溫度感測器3 4係檢測搬送輥18 a、19 a之溫度。作為溫度 感測器34,例如使用接觸式或非接觸式者。此處,檢測搬 送輥18a、19a之溫度亦包括算出搬送輥18a、19a之溫度。 具體而言’各溫度感測器34分別檢測第1徐冷爐12及第2徐 冷爐13内之配置位置之環境溫度。而且,參照檢測出之環 境溫度中的記憶於速度決定部38之下述記憶部36中之溫度 差資料’算出搬送輥18a、19a之溫度。檢測部37係基於檢 測出之搬送梃18a、19a之溫度,如下所述,算出搬送親 18a、19a之熱膨脹量作為直徑之變化。 速度決定部3 8係包括記憶部3 6。記憶部3 6係記憶溫度差 資料。溫度差資料係包括於徐冷爐丨2、丨3之設置時預先測 定的徐冷爐12、13之環境溫度與各環境溫度中之搬送輥 18a、19a之溫度(表面溫度)之差之資料。溫度差資料係因 你冷爐12、13之構造而不同地記憶。記憶部3 6中更記憶有 搬送輥18a、19a之熱膨脹係數(以下,亦稱為輥熱膨脹係 數)。輥熱膨脹係數係由搬送輥18a、19a之材質決定。 又’記憶部36中更記憶由速度決定部38決定之各搬送輥 18a、19a之旋轉速度、於複數個搬送親對18、19間設定之 作為基準之圓周速度分佈、及各搬送輥18a、19a之直徑之 基準值。各搬送輥18a、19a之直徑之基準值分別為常溫 (例如25度)下之新製品時之直徑。又,記憶部36係記憶達 163507.doc •24·163507.doc Μ S 201247566 The rotation speed controls the rotation of the conveying roller. Specifically, after the cutting is performed, the cutting step (step (10)) is performed. 5 ' Cut the continuously formed glass ribbon into a fixed length per glass to the glass plate. <& , the shape processing step (step (4)). The shape processing not only cuts the size or shape of the specific glass plate, but also performs the physical properties of the glass end face; ^ ° shape processing can be used to manufacture a cutting machine Or the physical method of laser, you can also use (4) and other chemical methods. Also 'preferably' the forming step and the cold (4) is in the zone where the temperature is above the softening point of the glass, The end of the width 2 is lower than the temperature of the central region sandwiched by the end portion, and the temperature of the central region is substantially uniform - to control the temperature of the glass (4) to suppress the shrinkage of the width direction of the glass ribbon. In the aspect of suppressing the warpage of the glass sheet, it is preferable that the tensile stress in the conveying direction acts on the glass ribbon in the region where the temperature of the central portion of the glass ribbon does not reach the softening point and is higher than the strain point. Central way, control The temperature of the glass ribbon is such that the temperature in the width direction of the glass ribbon descends from the central portion of the glass ribbon toward the end portion. Further, in terms of suppressing the internal strain of the glass ribbon, it is preferable that the temperature of the glass ribbon reaches the strain point. In the temperature region in the vicinity, the temperature distribution of the glass is controlled such that the temperature gradient between the end portion and the central portion in the width direction of the glass ribbon disappears. Further, it is preferable to suppress the warpage of the glass ribbon in the conveying direction. In the region where the temperature in the central portion of the glass ribbon is not near the strain point, and the tensile stress in the transport direction acts on the central portion of the glass ribbon to control the temperature distribution of the glass ribbon of 163507.doc •17·201247566, The temperature distribution of the glass ribbon is decreased from the end portion in the width direction of the glass ribbon toward the central portion. Further, preferably, the cold cooling step includes a second cooling step of cooling at an average cooling rate until the center of the glass ribbon The temperature of the part reaches the cold point; the second cooling step 'cools it at the second average cooling rate' until the temperature in the central part of the glass ribbon is from the cold The strain point is reached until the thief; and the third cooling step is performed at the third average cooling rate until the temperature in the central portion of the glass ribbon is from the strain point of 5 (rc reaches the strain point. In this case) i The average cooling rate is 5 〇 or more, and the 1st average cooling rate is faster than the 3rd average cooling rate, and the 3rd average cooling rate is faster than the 2nd average cooling catch. Xiao Wei, the average cooling rate is high to low. The order is the first average cooling rate and the third average cooling rate 'the second average cooling rate. The cooling rate in the direction in which the glass ribbon is conveyed affects the heat shrinkage of the produced glass sheet. However, as described above, in the cold step The glass sheet having a better heat shrinkage rate can be obtained by increasing the glass sheet by increasing the cooling rate. Further, the method for manufacturing the glass sheet includes a washing step and an inspection step, but the steps are omitted. Description. Further, the clarification step and the stirring step can be omitted, respectively. (Glass plate manufacturing apparatus) Fig. 3 and Fig. 4 are schematic configuration diagrams of a glass sheet manufacturing apparatus 1 according to a third embodiment of the present invention. The glass sheet manufacturing apparatus 1 of the present embodiment and the method of manufacturing the glass sheet using the glass sheet manufacturing apparatus 1 can be preferably applied to a liquid b day display device or an organic EL (Electro Luminescence) 163507.doc 201247566 display. The manufacture of a cover glass for a glass substrate of a flat panel display or a display surface of a portable terminal device. The reason for this is that liquid crystal display devices or organic EL display devices have required high precision and high quality in recent years, and therefore high surface quality is required for the glass substrates used therefor. Further, the reason is that since the cover glass is applied to the display surface of the device, etc., the surface quality of the glass substrate for the glass substrate is required. In the glass plate manufacturing apparatus 1 , the glass plate glass plate manufacturing apparatus 1 is manufactured by the molten glass A by the down-draw method, and the furnace chamber 11 which isolate|separates the heat insulation board 21 and 22 '23 arrange|positioned by the three positions of the up-down direction. 1 Xu cold furnace 12, second Xu cold furnace 13, and a panel chamber (not shown). The heat insulating panels 21 to 23 are plate-shaped members including heat insulating materials such as ceramic fibers. The transfer holes 16 are formed in the heat insulating plates 21 to 23, respectively, so that the glass ribbons b described below are directed downward through the heat insulating plates 21 to 23, respectively, in Fig. 3, and are in contact with the furnace wall 15 described below for easy understanding. The two portions in the horizontal direction are removed, and the illustration is omitted. However, in the glass ribbon B, two portions in the horizontal direction are integrally connected to the front side and the back side of the paper. In addition, in FIGS. 3 and 4, there is an example in which the insulation is used to separate the three clamps. However, the number of the heat shields and the installation position are not particularly limited. More than that. Furthermore, since the number of the heat shields is more than one, the more space that can independently control the ambient temperature, the easier the adjustment of the ambient temperature (the adjustment of the cold condition) becomes, and therefore, preferably, the cold storage device 3 & A number of insulation panels are placed to isolate multiple spaces. In other words, the Xu cold furnace may be provided with four or more, but it is more preferable to provide three or more f glass plate manufacturing apparatuses including a forming device 2, a cold cooling device 3, and a cutting device 4. 163507.doc .19· 201247566 The forming apparatus 2 is a device for forming the glass ribbon B from the molten glass A by a down-draw method. The forming apparatus 2 includes a furnace chamber u surrounded by a furnace wall 15 assembled of refractory bricks or block-shaped electroformed refractories. A forming body 10 and a pair of rolls (cooling roll pairs) 17 are provided in the furnace chamber. The molded body 1 includes a groove 10a (see Fig. 4) opened upward, and the molten glass A flows in the groove 1A. The formed body 10 includes, for example, a brick. The roller pair 17 is provided in a pair at a position corresponding to the end portions on both sides in the width direction of the molten glass A fused to the lower end of the molded body 1 ,, and the molten glass A is pulled downward while being pulled downward. A pair of cooling rolls cooled at both ends of the glass ribbon B. Further, the left-right direction in the paper surface in Fig. 3 and the direction perpendicular to the paper surface in Fig. 4 are the width directions of the glass ribbon B. In Fig. 3 and Fig. 4, the direction of conveyance of the glass ribbon 8 is in the upper and lower directions in the plane of the paper. In addition, in FIGS. 3 and 4, the molded body 1 is not provided in isolation from the roller pair 17 but it is easy to adjust the cold conditions, and a heat insulating plate may be provided for isolation therebetween. . Also, the report 17 can be set to two or more pairs. In this case, in the forming step, when the temperature of the glass ribbon 3 is in a temperature range from a temperature higher than the softening point to a vicinity of the near-cold point, it is preferable to apply tension to both end portions of the glass ribbon. Cooling is performed in such a manner that the viscosity 11 at both end portions reaches 1 = 11 = 9.0 to 14.5. This cooling is performed by, for example, holding the both end portions of the glass ribbon b by the pair of rollers 17 to perform β by cooling the both ends of the glass ribbon 17 by the respective rollers of the roller pair 17 as the cooling roller. The viscosity rises, so that the shrinkage of the width of the glass ribbon can be suppressed. (Xu cold device) The X-cooling device 3 system transports the β-face of the glass belt from a plurality of pairs to the Μ, β clip 163507.doc • 20- 201247566 The holder is dragged downwards while performing a cold. The X-cooling device 3 includes a second cooling furnace 12 and a second quenching furnace 13 which are disposed adjacent to the furnace chamber. The first Xu cold furnace 12 and the second quench furnace 13 are surrounded by the furnace wall 15 which also constitutes a furnace chamber. The chilling device 3 is provided with a heating mechanism that is automatically controlled by the following computer, which is disposed along the conveying direction of the glass ribbon B, in the second cooling furnace 12 and the second chill furnace 13. The heating mechanism is not particularly limited, and for example, an electric heater can be used. In the first Xu-cooling furnace 12, three transporting pairs 18 arranged along the transport direction of the glass ribbon B are provided. In the second cooling furnace 3, four conveying roller pairs 19 disposed along the conveying direction of the glass ribbon B are provided. Further, the rapid cooling device 3 includes the detection control unit 30 and the driving unit 32 (see Fig. 5). Further, the number of the transport roller pairs 18 and 19 in the cold furnaces 12 and 13 is not limited, and it is sufficient to provide at least "solid." The transport roller pairs 18 and 19 are carried by pulling the glass ribbon b downward to convey the glass ribbon. B. Each of the transport roller pairs 18 includes four transport rollers 18a disposed on both sides of the glass ribbon B so as to sandwich a region adjacent to both end portions in the width direction of the glass ribbon b, and will be located at the glass ribbon b The two transport rollers 18a on the same side are connected to the two drive shafts 18b disposed on both sides of the glass ribbon B. Each of the transport roller pairs 19 includes a region adjacent to both end portions in the width direction of the glass ribbon B. The four conveying rollers 19a disposed on both sides of the glass ribbon B and the two driving rollers 19b that are disposed on the both sides of the glass ribbon B are connected to the four conveying rollers 19a on the both sides of the glass ribbon B. In Fig. 3, the both ends of the drive shafts 18b and 19b are not shown. In Fig. 3, the conveyance rollers 18a and 19a are not limited to the above. For example, the conveyance rollers i8a and 19a may be located in the same manner. The same side of the glass ribbon B is not connected to each other by the drive shaft, but with 163507.doc •21-201247566 Similarly, the rolls of 17 are independently disposed at both end portions in the width direction of the glass ribbon 3. In the rapid cooling device 3 for performing the cold cooling step, it is preferable that the temperature of the glass ribbon B is distributed in the width direction to become a mountain peak. Then, the heater or the like disposed around the glass ribbon B is controlled so that the distribution of the mountain peak gradually decreases toward the downstream side in the transport direction. At this time, the temperature near the strain point of the glass ribbon B In the region, it is preferable to control the heater or the like (not shown) so that the distribution of the peaks becomes a flat linear shape, that is, the temperature distribution in the width direction is fixed. In other words, it is cooled from the glass ribbon B. Preferably, the cooling rate of the central portion in the width direction of the glass ribbon is faster than the cooling speed of both ends in the width direction, and the glass is added to the temperature region up to the strain point from the temperature of 15 〇t. The temperature in the central portion in the width direction of the belt B is higher than the temperature at the end portion in the vicinity of the strain point, and the temperature distribution becomes solid. Such a temperature distribution causes the tensile stress to act toward the downstream side in the conveying direction of the glass ribbon. Therefore, the glass ribbon B can suppress the warpage in the conveying direction. Further, since the temperature region in the vicinity of the strain point becomes a uniform temperature distribution, The internal strain can be reduced in the glass sheet. Further, in the temperature at which the temperature of the glass ribbon B becomes (strain point _5〇t > c) from the cold point, it is preferable to slowly compare with other temperature regions. The glass ribbon B is cooled, whereby the heat shrinkage rate of the glass ribbon 8 can be lowered. Further, in the temperature region where the temperature of the glass ribbon B is from the strain point to a temperature obtained by subtracting 200 cm from the strain point, it is preferable that In such a manner that the temperature distribution of the glass ribbon B becomes a valley in the width direction, and the depth of the valley becomes larger as the depth of the valley 163507.doc -22·201247566 is shifted to the downstream side, that is, the temperature of the central portion is increased. The heaters and the like (not shown) are controlled so that the end portions are gradually lowered. In this way, the valley is gradually deepened in the temperature distribution, and the tensile stress is applied to the downstream side in the transport direction. Therefore, the charm of the transport direction can be suppressed. As shown in Fig. 5, the detection control unit 3 includes a computer (not shown) that functions as a conveyance roller state detection unit (hereinafter also referred to as a detection unit) 37 and a speed determination unit 38. Fig. 5 is a block diagram showing the construction of a control system for rotational driving of the pair of feed rollers 18, 19. The detecting unit 37 has a temperature sensor (glass state detecting unit) 3 corresponding to the pair of conveying rollers 18 and 19, and the speed determining unit 38 is connected to the conveying roller pair 8 and the weir 9 via the driving unit 32. The details of the detection control unit 30 will be described later. The drive unit 32 rotationally drives the transport rollers 18a and i9a based on the rotational speeds of the transport rollers 18&, 19a determined by the speed determining unit 38. The drive unit w has a motor (not shown) provided corresponding to each of the transport roller pairs 18 and 19. Further, the motor may not be provided corresponding to each of the pair of conveying rollers 18, 19, and the number thereof may be, for example, less than the number of the pair of conveying rollers 18, 19. In this case, a plurality of conveying rollers 18a and 19a can be driven by one motor by using a gear having a speed ratio change between the respective conveying rollers 18a and 19a. In this case, the driving force from the motor is transmitted to the transport 辋 il 8a, 19a 〇 (detection control unit) via a universal joint or the like, for example, and the detection control unit 30 will be described in further detail. The detection step (step S5 1) performed by the detection control unit 30 is performed as described above in 163507.doc -23-201247566, but the detection step 'may not be performed as described in the following modification. The Xu cold step includes a speed determining step and a speed control step. In this case, the detection control unit 30 is not used. The temperature sensor 34 detects the temperatures of the conveying rollers 18a, 19a. As the temperature sensor 34, for example, a contact type or a non-contact type is used. Here, the detection of the temperatures of the conveyance rollers 18a and 19a also includes calculating the temperatures of the conveyance rollers 18a and 19a. Specifically, each temperature sensor 34 detects the ambient temperature of the arrangement position in the first quenching furnace 12 and the second quenching furnace 13, respectively. Then, the temperatures of the transport rollers 18a and 19a are calculated with reference to the temperature difference data ' stored in the memory unit 36 of the speed determining unit 38 in the detected environmental temperature. The detecting unit 37 calculates the amount of thermal expansion of the transporting members 18a and 19a as a change in diameter based on the detected temperatures of the transporting ports 18a and 19a. The speed determining unit 38 includes a storage unit 36. The memory unit 36 is a memory temperature difference data. The temperature difference data includes data of the difference between the ambient temperature of the quenching furnaces 12 and 13 and the temperature (surface temperature) of the conveying rollers 18a and 19a in each of the environmental temperatures measured in the setting of the cold furnaces 2 and 3. The temperature difference data is memorized differently due to the structure of your furnaces 12, 13. The thermal expansion coefficient of the conveying rollers 18a and 19a (hereinafter also referred to as the coefficient of thermal expansion of the roller) is more stored in the memory unit 36. The coefficient of thermal expansion of the roller is determined by the material of the conveying rollers 18a and 19a. Further, in the memory unit 36, the rotational speed of each of the transport rollers 18a and 19a determined by the speed determining unit 38, the peripheral speed distribution set as a reference between the plurality of transport pro-pairs 18 and 19, and the transport rollers 18a and The reference value of the diameter of 19a. The reference values of the diameters of the respective conveying rollers 18a and 19a are the diameters of the new products at normal temperature (e.g., 25 degrees). In addition, the memory department 36 memory reaches 163507.doc •24·

S 201247566 成作為基準之圓周速度分佈時之條件(搬送輥之溫度、玻 璃帶之溫度、玻璃帶之熱膨脹係數、玻璃帶之厚度、寬 度、玻璃帶之流量等)。 速度決定部38係設定於複數個搬送輥對18、19間搬送輥 18a、19a之圓周速度與玻璃帶B之搬送速度之相對速度為 固定時的複數個搬送輥對18、19間之圓周速度比(圓周速 度分佈)。其次,速度決定部38基於藉由檢測部37算出之 搬送輥18a、19a之直徑之變化,以保持複數個搬送輥對 18、19間之圓周速度比之方式,決定各搬送輥i8a、19a之 旋轉速度。 ((圓周速度比之設定)) 複數個搬送輥對18、19間之圓周速度比係例如以所有搬 送輥18a、19a成為相同之圓周速度之方式均設定為1()。以 此方式設定為基準之圓周速度比係以先前玻璃帶B不會產 生損傷或形狀變形之問題之方式進行徐冷時之圓周速度 比°作為該基準之圓周速度分佈係與玻璃帶B之溫度、熱 膨脹係數、厚度、寬度、玻璃流量等條件一併記憶保持於 速度決定部38。該圓周速度比係如下所述於玻璃帶b之溫 度變化等徐冷時之條件變化之情形時,修正並設定作為基 準之圓周速度分佈。 就進一步確實地防止玻璃帶B與搬送輥18&、l9a之間之 ’月移之觀點而言’較佳為,於複數個搬送輥對丨8、丨9間, 玻璃帶B之槪送速度與搬送輥18a' 19a之圓周速度之相對 速度為〇。 163507.doc -25- 201247566 又,速度決定部38係藉由玻璃帶B之溫度、熱膨脹係 數、厚度、玻璃流量等來修正設定基準之圓周速度比。 具體而言,於設定為基準之圓周速度分佈的圓周速度 比,設定有各搬送輥對之作為基準之溫度作為此時之條 件。因此,於當前之玻璃帶B之溫度相對作為該基準之溫 度變化之情形時,例如於溫度Τι變化成丁2之情形時,速度 決定部38利用丁2與丁1之溫度差中之熱膨脹率之差,修正設 定為基準之圓周速度分佈的圓周速度比。其原因在於,玻 璃帶B之搬送速度係因由玻璃帶3之溫度及熱膨脹係數決 定的熱膨脹率而變化。於該情形時,由於熱膨脹係數因玻 璃帶B之種類不同而不同’故而,亦可利用兼顧玻璃帶b 之熱膨脹係數與溫度的熱膨脹率之差異,更普通化地修正 圓周速度比。如此之圓周速度比係不僅根據玻璃帶B之温 度及熱膨脹係數之溫度依存性’而且根據玻璃帶B之厚 度、寬度、玻璃流重等條件之變化進行修正及設定。因 此’玻璃帶B之溫度、熱膨脹係數之溫度依存性之特性、 厚度、寬度、玻璃流量等基準之圓周速度比中之條件係預 先記憶保持於速度決定部38中。玻璃熱膨脹係數係由熔融 玻璃之組成所決定。根據設定之圓周速度比,以最上游侧 之搬送輥對之當前之圓周速度為基準,算出下游側之各搬 送輥對之圓周速度。 可藉由以此方式,相應於包括玻璃帶B之溫度的狀態之 變化’修正圓周速度比,而決定更適當之搬送輥l8a、19a 之旋轉速度。 163507.doc *26· 201247566 ((搬送輥之旋轉速度之決定)) 速度決定邹38係基於算出之各搬送輥 18a、19a之圓周速 度,按照下式決定各搬送輥18a、19a之旋轉速度。 旋轉速度=圓周速度/(熱膨脹後之搬送輥之直徑χπ) 此處,於在徐冷爐12、13内之各搬送輥對18、19之配置 位置檢測出之環境溫度相對於上述作為基準之圓周速度比 中之搬送輥對之溫度變化之情形時,以保持上述圓周速度 比之方式決定搬送輥18a、i9a之旋轉速度。 具體而言’對於由溫度感測器34探測之溫度變化之搬送 輥18a、19a’檢測部37參照搬送輥18a、19a之溫度中之輥 熱膨脹係數、及各搬送輥18a、19a之直徑之基準值,按照 下式算出該搬送輥18a之膨服量(直徑之變化量)。 dD=p-DAT dD :膨脹量 β :熱膨脹係數 D:搬送輥之直徑之基準值 AT:與基準之圓周速度比中設定之搬送輥之溫度的溫 度差 速度決定部38係根據由檢測部37算出之搬送輥18a之直 • 徑之變化量,按照下式,為圓周速度之變化量為1,算出 新的旋轉速度,從而變更搬送輥18a、19a之旋轉速度。 新的旋轉速度=(圓周速度+圓周速度之變化量)/((搬送輥 之直徑+搬送輕之直徑之變化量)χπ) 由速度決定部38決定之旋轉速度係搬送至驅動部32,控 163507.doc -27- 201247566 制搬送輥18a、19a之旋轉。 又,未圖示之電腦係基於由溫度感測器3 4檢測之環境溫 度,以將徐冷爐12、13内之環境溫度分別維持於特定之溫 度範圍内之方式,自動控制徐冷爐12、13内之加熱機構。 第1徐冷爐12之特定之溫度範圍係設定為例如5〇〇〜8〇〇度。 第2徐冷爐13之特定之溫度範圍係設定為例如2〇〇〜5〇〇度。 即便以此方式控制徐冷爐12、13内之環境溫度,亦如上所 述’玻璃帶B之溫度或搬送輥183、19a之溫度產生變化。 然而,由於該變化相對較小,故而’即便相應於溫度,修 正上述作為基準之圓周速度比,其修正量亦較小,不會較 大地改變作為設定之基準之圓周速度比之分佈。 再者,速度決定部38亦可基於操作人員輸入之内容,決 定搬送輥18a、19a之旋轉速度。於該情形時,玻璃板製造 裝置1更包括受理操作人員之輸入操作之未圖示之輸入 部,且該輸入部受理操作人員所輸入之搬送輥18&、19&之 旋轉速度。記憶部36亦可不記憶溫度差資料、輥熱膨脹係 數、圓周速度分佈、各搬送輥18a、19a之直徑之基準值、 達成作為基準之圓周速度分佈時之條件等,只要記憶由操 作人員基於溫度差資料、輥熱膨脹係數、圓周速度分佈、 各搬送輥18a、19a之直徑之基準值、達成作為基準之圓周 速度分佈時之條件等算出且輸入之旋轉速度即可。該等溫 度差資料、輥熱膨脹係數、圓周速度分佈 '各搬送輥 18a、19a之直徑之基準值、作為基準之圓周速度分佈可由 操作人員算出,且算出之值可記憶於記憶部36中。 163507.doc •28- 201247566 裁板裝置4係包括配置於第2徐冷爐13之下游側的未圖示 之裁板至。裁板室係將玻璃帶B切斷為每一個固定之長 度,裁板得到玻璃板c。玻璃板c之厚度係例如〇 7 mmW 下、或0.5 mm以下。又,由於近年來要求平板顯示器之纖 細化,故而液晶顯示器或有機EL顯示器等平板顯示器用玻 璃基板亦要求薄板化。另一方面,由於玻璃板之厚度越 薄,則玻璃板之強度越低下,故容易產生破損。若考慮上 述情況,則平板顯示器用之玻璃板之厚度較佳為〇〇1〜1〇 mm,更佳為〇.05〜0 7 mm,進而較佳為〇 〇5~〇 5爪爪。再 者,由於越薄之玻璃板,強度越低下,故而,存在因搬送 玻璃帶之輥與玻璃帶之間之滑移造成之損傷等而變得容易 破碎之虞。即,如上所述,可抑制輥與玻璃帶之間之滑移 之本實把形態例如適於〇.〇5〜0.7 mm之玻璃板之製造,尤 其適於0.05〜0.5 mm之薄板玻璃之製造。 又’例如破璃板C之寬度方向長度亦可為1000 mm以 上、1500 mm以上、2000 mm以上、2500 mm以上,且長度 方向長度亦可為1000 mm以上、15〇〇 mm以上、2000 mm以 上、2500 mm以上。玻璃板c係越大型化,則越容易因玻 璃帶之自重而於其與各搬送輕18a、19a之間產生相對速度 差(滑移)。因此,於玻璃板C之寬度方向長度為1000 mm以 上之情形時’存在上述相對速度差變得容易產生之傾向, 但防止上述相對速度差之產生之效果變得明顯^再者,隨 著玻璃板C之寬度方向長度為1500 mm以上、2000 mm以 上、2500 mm以上’本發明之效果越為有益。 163507.doc •29· 201247566 (玻璃板之組成) 利用上述玻璃板製造方法及玻璃板製造裝置製造之玻璃 板例如可較佳地列舉液晶顯示器用玻璃基板。 液晶顯示器用玻璃基板之玻璃組成可例示以下之玻璃組 成。 較佳為含有:S 201247566 The conditions for the circumferential speed distribution as the reference (temperature of the conveying roller, temperature of the glass ribbon, thermal expansion coefficient of the glass ribbon, thickness of the glass ribbon, width, flow rate of the glass ribbon, etc.). The speed determining unit 38 sets the peripheral speed between the plurality of conveying roller pairs 18 and 19 when the relative speeds of the peripheral speeds of the conveying rollers 18a and 19a between the plurality of conveying roller pairs 18 and 19 and the conveying speed of the glass ribbon B are fixed. Ratio (circumferential velocity distribution). Next, the speed determining unit 38 determines the respective conveying rollers i8a and 19a so as to maintain the peripheral speed ratio between the plurality of conveying roller pairs 18 and 19 based on the change in the diameter of the conveying rollers 18a and 19a calculated by the detecting unit 37. spinning speed. ((circumferential speed ratio setting)) The peripheral speed ratio between the plurality of conveying roller pairs 18 and 19 is set to 1 (), for example, in such a manner that all of the conveying rollers 18a and 19a have the same circumferential speed. The circumferential speed ratio set as the reference in this manner is the circumferential speed ratio when the cold glass ribbon B is not damaged or the shape is deformed as the circumferential speed distribution of the reference and the temperature of the glass ribbon B. Conditions such as the coefficient of thermal expansion, the thickness, the width, and the flow rate of the glass are collectively stored in the speed determining unit 38. When the circumferential speed ratio is changed as follows when the temperature of the glass ribbon b changes, such as when the temperature changes, the circumferential speed distribution is corrected and set. Further, it is preferable to prevent the "transition of the glass ribbon B" from the transfer rollers 18 & and l9a from the viewpoint of the monthly shift, and the transfer speed of the glass ribbon B between the plurality of transport roller pairs 丨8 and 丨9. The relative speed to the peripheral speed of the conveying roller 18a' 19a is 〇. 163507.doc -25- 201247566 Further, the speed determining unit 38 corrects the circumferential speed ratio of the setting reference by the temperature of the glass ribbon B, the coefficient of thermal expansion, the thickness, the flow rate of the glass, and the like. Specifically, the temperature as a reference for each of the transport roller pairs is set as the condition at the circumferential speed ratio set as the reference circumferential speed distribution. Therefore, when the temperature of the current glass ribbon B changes with respect to the temperature as the reference, for example, when the temperature is changed to the temperature of 2, the speed determining unit 38 uses the thermal expansion coefficient in the temperature difference between the butyl 2 and the dicing The difference is corrected by the circumferential speed ratio set as the reference circumferential speed distribution. The reason for this is that the conveying speed of the glass ribbon B changes due to the thermal expansion coefficient determined by the temperature of the glass ribbon 3 and the coefficient of thermal expansion. In this case, since the coefficient of thermal expansion differs depending on the type of the glass ribbon B, the circumferential speed ratio can be more commonly corrected by taking into consideration the difference between the thermal expansion coefficient of the glass ribbon b and the thermal expansion coefficient of the temperature. Such a peripheral speed ratio is corrected and set not only according to the temperature dependence of the temperature and thermal expansion coefficient of the glass ribbon B but also by changes in the thickness, width, and glass flow weight of the glass ribbon B. Therefore, the conditions of the temperature dependence of the temperature of the glass ribbon B, the temperature dependence of the thermal expansion coefficient, the thickness ratio of the thickness, the width, and the glass flow rate are preliminarily stored in the speed determining unit 38. The coefficient of thermal expansion of the glass is determined by the composition of the molten glass. Based on the set peripheral speed ratio, the peripheral speed of each pair of transport rollers on the downstream side is calculated based on the current peripheral speed of the most upstream transport roller pair. In this manner, the rotational speed of the more appropriate transport rollers 18a, 19a can be determined by correcting the peripheral speed ratio corresponding to the change in the state including the temperature of the glass ribbon B. 163507.doc *26·201247566 (Determining the rotation speed of the conveyance roller) The speed determination determines the rotation speed of each of the conveyance rollers 18a and 19a based on the calculated circumferential speed of each of the conveyance rollers 18a and 19a. Rotation speed = circumferential speed / (diameter of the conveyance roller after thermal expansion χ π) Here, the ambient temperature detected at the arrangement position of each of the conveyance roller pairs 18 and 19 in the cold furnaces 12 and 13 is relative to the above-mentioned peripheral speed as a reference When the temperature of the pair of conveyance rollers is changed, the rotation speeds of the conveyance rollers 18a and i9a are determined so as to maintain the circumferential speed ratio. Specifically, the detecting unit 37 of the conveying rollers 18a and 19a' detecting the temperature change detected by the temperature sensor 34 refers to the thermal expansion coefficient of the rollers in the temperatures of the conveying rollers 18a and 19a, and the reference of the diameters of the respective conveying rollers 18a and 19a. The value of the amount of expansion (the amount of change in diameter) of the conveying roller 18a was calculated according to the following formula. dD=p-DAT dD : expansion amount β : thermal expansion coefficient D: reference value of the diameter of the conveyance roller AT: temperature difference speed determination unit 38 based on the temperature of the conveyance roller set in the reference peripheral speed ratio is based on the detection unit 37 The amount of change in the straight diameter of the conveyance roller 18a is calculated by the following equation, and the amount of change in the circumferential speed is 1, and a new rotation speed is calculated to change the rotation speed of the conveyance rollers 18a and 19a. The new rotation speed = (circumference speed + change amount of the peripheral speed) / ((the diameter of the conveyance roller + the amount of change in the diameter of the conveyance light) χ π) The rotation speed determined by the speed determination unit 38 is conveyed to the drive unit 32, and is controlled. 163507.doc -27- 201247566 The rotation of the conveying rollers 18a, 19a. Further, the computer (not shown) automatically controls the inside of the quenching furnaces 12 and 13 in such a manner that the ambient temperatures in the quenching furnaces 12 and 13 are maintained within a specific temperature range based on the ambient temperature detected by the temperature sensor 34. Heating mechanism. The specific temperature range of the first quenching furnace 12 is set to, for example, 5 〇〇 to 8 〇〇. The specific temperature range of the second quenching furnace 13 is set to, for example, 2 〇〇 to 5 〇〇. Even if the ambient temperature in the quench ovens 12, 13 is controlled in this manner, the temperature of the glass ribbon B or the temperature of the conveying rollers 183, 19a changes as described above. However, since the change is relatively small, even if the peripheral speed ratio as the reference is corrected corresponding to the temperature, the correction amount is small, and the distribution of the peripheral speed ratio as the reference for setting is not largely changed. Further, the speed determining unit 38 can determine the rotational speed of the transport rollers 18a and 19a based on the contents input by the operator. In this case, the glass sheet manufacturing apparatus 1 further includes an input unit (not shown) that accepts an input operation by an operator, and the input unit receives the rotational speeds of the transport rollers 18 & 19 & The memory unit 36 may not memorize the temperature difference data, the roller thermal expansion coefficient, the circumferential speed distribution, the reference value of the diameters of the respective conveying rollers 18a and 19a, the conditions at which the circumferential speed distribution as the reference is obtained, and the like, as long as the memory is based on the temperature difference by the operator. The data, the coefficient of thermal expansion of the roll, the circumferential speed distribution, the reference value of the diameter of each of the transport rollers 18a and 19a, the condition at which the circumferential speed distribution is determined as a reference, and the like may be calculated and input. The isothermal temperature data, the roller thermal expansion coefficient, and the circumferential speed distribution 'the reference values of the diameters of the respective conveying rollers 18a and 19a, and the circumferential velocity distribution as the reference can be calculated by the operator, and the calculated values can be stored in the memory unit 36. 163507.doc • 28-201247566 The panel device 4 includes a panel (not shown) disposed on the downstream side of the second quenching furnace 13. In the paneling room, the glass ribbon B is cut into each fixed length, and the panel is obtained to obtain a glass plate c. The thickness of the glass plate c is, for example, 〇 7 mmW or less than 0.5 mm. Further, since the flat panel display has been required to be thinner in recent years, a glass substrate for a flat panel display such as a liquid crystal display or an organic EL display is required to be thinned. On the other hand, since the thickness of the glass sheet is thinner, the strength of the glass sheet is lowered, so that damage is likely to occur. In consideration of the above, the thickness of the glass plate for a flat panel display is preferably 〇〇1 to 1 mm, more preferably 〇.05 to 0 7 mm, and further preferably 〇5 to 〇5 claws. Further, since the thinner glass plate is used, the strength is lowered, so that it is easily broken due to damage caused by slippage between the roll of the glass ribbon and the glass ribbon. That is, as described above, the actual shape of the slip between the roll and the glass ribbon can be suppressed, for example, it is suitable for the manufacture of a glass plate of 5 to 0.7 mm, and is particularly suitable for the manufacture of a thin plate glass of 0.05 to 0.5 mm. . Further, for example, the length of the glass plate C in the width direction may be 1000 mm or more, 1500 mm or more, 2000 mm or more, 2500 mm or more, and the length in the longitudinal direction may be 1000 mm or more, 15 mm or more, or 2000 mm or more. , 2500 mm or more. As the glass plate c is increased in size, it is easier to cause a relative speed difference (slip) between the glass sheets c and the respective conveyance lamps 18a and 19a due to the weight of the glass ribbon. Therefore, when the length of the glass sheet C in the width direction is 1000 mm or more, the above-mentioned relative speed difference tends to occur, but the effect of preventing the above-described relative speed difference becomes apparent. The length of the sheet C in the width direction is 1500 mm or more, 2000 mm or more, and 2500 mm or more. The effect of the present invention is more advantageous. 163507.doc •29·201247566 (Composition of a glass plate) The glass plate manufactured by the glass plate manufacturing method and the glass plate manufacturing apparatus is preferably a glass substrate for liquid crystal displays, for example. The glass composition of the glass substrate for a liquid crystal display can exemplify the following glass composition. Preferably, it contains:

Si02 50〜70 質量。/〇、 b2〇3 〇〜15質量%、Si02 50~70 quality. /〇, b2〇3 〇~15% by mass,

Al2〇3 5 〜25質量%、Al2〇3 5 to 25% by mass,

MgO 0〜1〇質量%、MgO 0~1〇% by mass,

CaO 〇〜2〇質量%、CaO 〇~2〇% by mass,

SrO 〇〜2〇質量%、SrO 〇~2〇% by mass,

BaO 〇〜1〇質量%、 R0 5〜2〇質量%(其中R係選自Mg、Ca、Sr及Ba中之玻璃 板中所含之總成分且為至少1種)。 進而’就抑制形成於液晶顯示器用玻璃基板之TFT(Thin Film Transistor’薄膜電晶體)之破壞之觀點而言,較佳為 無驗玻璃(實質上不含鹼成分之玻璃)。另一方面,為使熔 融玻璃之炼解性及澄清性提昇,可反而使其含有微量驗成 分。於該情形時,較佳為R'O超過〇.〇5質量❶/❶且為2.0質量 0/〇以下,更佳為Rio超過〇 1質量%且為2 〇質量%以下(其中 R·係選自Li、Na及Κ中之玻璃板中所含之總成分且為至少i 種)。 根據以上述方式構成之玻璃板製造裝置1,考慮到產生 163507.doc •30-BaO 〇~1〇% by mass, R0 5~2〇% by mass (wherein R is at least one selected from the total components contained in the glass sheets of Mg, Ca, Sr and Ba). Further, from the viewpoint of suppressing the destruction of a TFT (Thin Film Transistor') formed on a glass substrate for a liquid crystal display, it is preferable to have no glass (substantially free of alkali-containing glass). On the other hand, in order to improve the refining property and the clarification property of the molten glass, it may be made to contain a minute amount of the component. In this case, it is preferred that R'O exceeds 〇.〇5 mass ❶/❶ and is 2.0 mass%/〇 or less, more preferably Rio exceeds 〇1 mass% and is 2% by mass or less (wherein R· is The total composition contained in the glass plate selected from the group consisting of Li, Na, and lanthanum is at least i). According to the glass sheet manufacturing apparatus 1 constructed as described above, it is considered to generate 163507.doc • 30-

S 201247566 於搬送輥18a、19a之直徑變化,而以補償該直徑變化之方 式,控制各搬送輥18a、19a之旋轉速度,故而,可以更高 之精度抑制各搬送輥18a、19a之圓周速度與玻璃帶B之搬 送速度之相對速度於複數個搬送輥對18、19中產生差值。 藉此’可防止玻璃帶B與搬送輥18a、19a之間之滑移,從 而使玻璃板表面之品質提昇。 • 又,由於根據玻璃帶之溫度’修正及設定用以搬送玻璃 帶之複數個搬送輥對之圓周速度分佈,故而可防止玻璃帶 殘餘’導致玻璃帶變形,又,可藉由變得比要求快,而防 止玻璃帶受到拉伸,導致玻璃帶破碎。如此之效果係於玻 璃之搬送速度較快之情形時(例如搬送速度為2〇〇 m/以上之 情形時)、或者玻璃帶之強度較小容易變形之厚度為〇5 mm以下、較佳為〇.〇5〜〇.5 mm之薄板玻璃之製造中更為明 顯。 再者’複數個搬送輥對之數量為至少2個即可,並無特 別限制。 又’上述例係於溫度感測器中檢測徐冷爐12、13内之環 . 境溫度’並利用該環境溫度算出玻璃帶溫度及搬送輥溫 度,但亦可直接測定玻璃帶溫度及搬送輥溫度。因此,例 如可使用用以連續地測定玻璃帶之溫度之放射溫度計作為 玻璃狀態檢測部,且可使用用以連續地測定搬送輥之溫度 之溫度計作為搬送輥狀態檢測部。 圓周速度比並不限制於上述者。又,速度決定部38亦可 算出各搬送輥18a、19a之具體之圓周速度作為圓周速度分 I63507,doc -31 - 201247566 佈而取代ai周速纽。於該情形時,料基準之圓周速度 分佈及修正後之圓周速度亦設定為具體之速度值。 本實施形態係不僅根據搬送輥之直徑之變化以達到設 定之圓周速度分佈之方式調整旋轉速度,而且對於圓周速 度分佈,根據玻璃帶之溫度,修正設定作為基準之圓周速 度分佈。然而,亦可不根據玻璃帶之當前之溫度修正作為 基準之圓周速度分佈。然而,就製造表面品質優異之玻璃 板之方面而言,較佳為,根據玻璃帶之當前之溫度修正作 為基準之圓周速度分佈。 (第1實施形態之變形例) 第1實施形態係以補償產生於搬送輥對18、19之各輥中 之搬送輥之直徑變化之方式,決定搬送輥18a、19a之旋轉 速度’但除了搬送㈣、19a以外,亦可以補償成形步驟 中用作冷卻輥對的輥對17之各輥之直徑變化之方式,決定 輕對17之各輥之旋轉速度。對於輥對17之純係利用上述 搬送輥狀態檢測部37之類的檢測部,檢測輥對丨7之各輥之 狀態,且基於檢測結果,以補償輥對17之各輥之直徑變化 之方式,決定輥對17之各輥之旋轉速度。 一般而言,由於輥對丨7之各輥之圓周速度以玻璃板之厚 度分佈或玻璃表面之凹凸變得最小之方式設定為適當之 值,故而,與該值偏差會使玻璃板之厚度分佈或玻璃表面 之凹凸劣化。 即,若輥對17之圓周速度變化,則自成形體1〇之下端於 輥對17之間進行之玻璃帶B之拉伸之量、及自輥對17於搬S 201247566, the diameters of the conveying rollers 18a and 19a are changed, and the rotation speed of each of the conveying rollers 18a and 19a is controlled so as to compensate for the change in the diameter. Therefore, the peripheral speed of each of the conveying rollers 18a and 19a can be suppressed with higher accuracy. The relative speed of the transport speed of the glass ribbon B is different between the plurality of transport roller pairs 18, 19. Thereby, the slip between the glass ribbon B and the conveying rollers 18a and 19a can be prevented, thereby improving the quality of the surface of the glass sheet. • Moreover, since the circumferential speed distribution of the plurality of conveying roller pairs for conveying the glass ribbon is corrected and set according to the temperature of the glass ribbon, the glass ribbon residual can be prevented from causing deformation of the glass ribbon, and can be made more demanding Fast, and prevent the glass ribbon from being stretched, causing the glass ribbon to break. The effect is such that when the conveying speed of the glass is fast (for example, when the conveying speed is 2 〇〇m/above), or the strength of the glass ribbon is small, the thickness is easily 变形5 mm or less, preferably 〇.〇5~〇.5 mm of thin sheet glass is more obvious in the manufacture. Further, the number of the plurality of conveying roller pairs is at least two, and there is no particular limitation. Further, the above example is for detecting the temperature of the glass ribbon and the temperature of the conveying roller by using the ambient temperature in the temperature sensor of the quenching furnaces 12 and 13, but the glass ribbon temperature and the conveying roller temperature can be directly measured. For this reason, for example, a radiation thermometer for continuously measuring the temperature of the glass ribbon can be used as the glass state detecting portion, and a thermometer for continuously measuring the temperature of the conveying roller can be used as the conveying roller state detecting portion. The peripheral speed ratio is not limited to the above. Further, the speed determining unit 38 can calculate the specific peripheral speed of each of the transport rollers 18a and 19a as the peripheral speed score I63507, doc -31 - 201247566, and replace the ai weekly speed. In this case, the circumferential speed distribution of the material reference and the corrected circumferential speed are also set to specific speed values. In the present embodiment, the rotational speed is adjusted not only in accordance with the change in the diameter of the transport roller so as to reach the set circumferential velocity distribution, but also in the circumferential speed distribution, the circumferential speed distribution as the reference is corrected based on the temperature of the glass ribbon. However, it is also possible to correct the circumferential speed distribution as a reference without depending on the current temperature of the glass ribbon. However, in terms of producing a glass sheet excellent in surface quality, it is preferred to adjust the circumferential speed as a reference based on the current temperature correction of the glass ribbon. (Modification of the first embodiment) In the first embodiment, the rotation speed of the conveyance rollers 18a and 19a is determined so as to compensate for the change in the diameter of the conveyance rollers generated in the respective rollers of the conveyance roller pairs 18 and 19. (4) In addition to 19a, it is also possible to compensate for the change in the diameter of each of the rolls of the pair of rolls 17 used as the pair of cooling rolls in the forming step, and determine the rotational speed of each of the rolls of the light pair 17. The detection unit such as the conveyance roller state detecting unit 37 is used to detect the state of each roller of the roller pair 7 and the diameter of each roller of the roller pair 17 is changed based on the detection result. The rotation speed of each roller of the pair of rollers 17 is determined. In general, since the circumferential speed of each roller of the pair of rollers 7 is set to an appropriate value such that the thickness distribution of the glass sheet or the unevenness of the glass surface is minimized, the deviation from the value causes the thickness distribution of the glass sheet. Or the unevenness of the surface of the glass is deteriorated. That is, if the peripheral speed of the pair of rolls 17 is changed, the amount of stretching of the glass ribbon B between the lower end of the formed body 1〇 between the pair of rolls 17 and the self-rolling pair 17 are moved.

163507.doc ^2 S 201247566 送輥對18之間進行之玻璃帶B之拉伸之量產生變換,(由於 成形體1〇之下端,對17間之破璃帶B之寬度方向之溫度分 佈與輕對17〜搬送輥對18、19之玻璃帶之寬度方向溫度 分佈之形態不同)’故導致製造之玻璃板之寬度方向之厚 度分佈或玻璃表面之凹凸之大小產生變化。因此,較佳 為,以補償輥對17之各輥之直徑變化之方式,決定輕對17 之各輥之旋轉速度。 再者,本變形例係除了搬送報對18、19之各輕以外,亦 以補償成形步驟中用作冷卻輥對的輥對17之各輥之直徑變 化之方式,決定旋轉速度,但亦可對於搬送輥對丨8、Μ及 輥對17之各輥中之至少任—個各輥,以補償各輥之直徑變 化之方式’決定旋轉速度。 即,以補償冷卻輥或.搬送輥之直徑變化之方式,決定輥 之旋轉速度亦可僅對有效之輥進行而無需於所有輥(冷卻 輥、搬送輥)中進行。 例如可藉由以補償設置於玻璃帶B之中央部成為軟化點 (黏度η成為l〇gT1==7.65之溫度)以下之區域内的搬送輥之直 徑變化之方式,決定搬送輥之旋轉速度,且使搬送輥進行 旋轉驅動’而抑制玻璃帶B之滑移等,從而可抑制於玻璃 帶B之表面產生損傷。 若玻璃為軟化點以上,則玻璃帶B並未充分地固化,故 不易產生滑移。另一方面,軟化點以下之玻璃帶3變得容 易產生滑移。因此,較佳為,以補償設置於玻璃帶B之中 央部為軟化點以下之區域内的搬送輥之直徑變化之方式, 163507.doc •33- 201247566 決定搬送輥之旋轉速度。 又,於上述徐冷步驟中,由於以補償至少設置於玻璃帶 B之中央部之溫度達到玻璃轉移點以上且軟化點以下之溫 度區域内的搬送輥之直徑變化之方式,決定搬送輥之旋轉 速度,故而,玻璃帶B之塑性變形之抑制效果變大。因 此,較佳為,以補償至少設置於玻璃帶]5之中央部之溫度 達到玻璃轉移點以上且軟化點以下之溫度區域内的搬送輥 之直徑變化之方式’決定搬送輥之旋轉速度。 又’由於設置於玻璃帶B之中央部之溫度達到玻璃轉移 點以上且軟化點以下之溫度區域内的搬送輥容易產生直徑 變化,故而,較佳為,以補償設置於該區域内之搬送輥之 直徑變化之方式’決定搬送輥之旋轉速度。 於玻璃溫度相較軟化點為高溫之情形時,由於作用於玻 璃之壓縮應力瞬間得到緩和,故而於玻璃帶B中,不易產 生波形之塑性變形。另一方面,於玻璃溫度相較玻璃轉移 點為低溫之情形時,由於玻璃帶3之黏度充分上升,故而 不易產生波形之塑性變形。 又’越為上游侧之搬送輥,則越容易產生因磨損或熱膨 脹引起之輥徑變化。即,較佳為,以補償至少設置於溫度 達到玻璃轉移點以上且軟化點以下之溫度區域内的搬送輥 之直徑變化之方式,決定搬送輥之旋轉速度。 又’可藉由以補償設置於玻璃帶B之中央部之溫度自徐 冷點達到(應變點_5〇t )之溫度區域内的搬送輥之直徑變化 之方式’決定搬送親之旋轉速度,且使上述搬送親進行旋 163507.doc -34·163507.doc ^2 S 201247566 The amount of stretching of the glass ribbon B between the pair of rollers 18 is changed. (Because of the lower end of the formed body 1 , the temperature distribution in the width direction of the 17 strips B is The thickness of the glass ribbon of the pair of conveying rollers 18 and 19 is different in the width direction of the conveying belt). Therefore, the thickness distribution in the width direction of the glass sheet to be produced or the size of the unevenness of the glass surface is changed. Therefore, it is preferable to determine the rotational speed of each of the rollers of the light pair 17 in such a manner as to compensate for the change in the diameter of each of the rollers of the pair of rollers 17. Further, in the present modification, in addition to the lightness of the conveyance reports 18 and 19, the rotation speed is determined by compensating for the diameter change of each of the rollers 17 serving as the pair of cooling rollers in the forming step, but it is also possible At least one of the rollers of the transport roller pair 丨8, Μ and the pair of rollers 17 determines the rotational speed in such a manner as to compensate for the change in the diameter of each roller. In other words, the rotation speed of the roller can be determined so as to compensate for the change in the diameter of the cooling roller or the conveying roller, and it is not necessary to perform the roller only for all the rollers (cooling roller, conveying roller). For example, the rotation speed of the conveyance roller can be determined by compensating for the change in the diameter of the conveyance roller in the region where the center portion of the glass ribbon B is at a softening point (the temperature at which the viscosity η becomes l〇gT1==7.65). Further, the conveyance roller is rotationally driven to suppress the slip of the glass ribbon B or the like, thereby suppressing damage on the surface of the glass ribbon B. If the glass is at least the softening point, the glass ribbon B is not sufficiently cured, so that slippage is less likely to occur. On the other hand, the glass ribbon 3 below the softening point becomes liable to cause slippage. Therefore, it is preferable to determine the rotation speed of the conveyance roller so as to compensate for the change in the diameter of the conveyance roller provided in the region where the center portion of the glass ribbon B is below the softening point, 163507.doc • 33 - 201247566. Further, in the above-described cold cooling step, the rotation of the conveying roller is determined so as to compensate for the change in the diameter of the conveying roller in the temperature region at least the glass transition point and the softening point or lower in the central portion of the glass ribbon B. The speed, therefore, the effect of suppressing the plastic deformation of the glass ribbon B becomes large. Therefore, it is preferable to determine the rotational speed of the transport roller by compensating for the change in the diameter of the transport roller in the temperature region where the temperature at the central portion of the glass ribbon 5 is equal to or higher than the glass transition point and below the softening point. Further, since the conveying roller provided in the central portion of the glass ribbon B reaches a temperature higher than the glass transition point and below the softening point, the diameter of the conveying roller is likely to change. Therefore, it is preferable to compensate the conveying roller provided in the region. The way in which the diameter changes 'determines the rotation speed of the conveying roller. When the glass temperature is higher than the softening point, since the compressive stress acting on the glass is instantaneously relieved, the plastic deformation of the waveform is less likely to occur in the glass ribbon B. On the other hand, when the glass temperature is lower than the glass transition point, since the viscosity of the glass ribbon 3 is sufficiently increased, plastic deformation of the waveform is less likely to occur. Further, the more the transfer roller on the upstream side, the more likely the roll diameter changes due to abrasion or thermal expansion. That is, it is preferable to determine the rotation speed of the conveyance roller so as to compensate for the change in the diameter of the conveyance roller provided in at least the temperature range of the glass transition point or more and the softening point or less. In addition, the rotational speed of the transporting parent can be determined by compensating for the change in the diameter of the transport roller in the temperature region where the temperature at the central portion of the glass ribbon B is reached from the cold point (strain point _5 〇t). And the above-mentioned transfer pro is rotated 163507.doc -34·

S 201247566 轉驅動,而抑制玻璃帶之塑性變形。 如上所述’以補償輥之直徑變化之方式決定旋轉速度之 搬送輥之部位因改善玻璃帶B之哪一特徵而不同。 (第2實施形態) 其次’對作為本發明之第2實施形態的玻璃板製造裝置 進行說明。 此處’著目艮於與上述第1實施形態不同之處進行說明。 第1實施形態之搬送輥狀態檢測部37係包括檢測搬送報 之溫度的溫度感測器3 4 ’但如圖6所示,第2實施形態之搬 送輥狀態檢測部(以下,亦簡稱為檢測部)47係包括用以檢 測搬送輥之磨損量之距離測定感測器44。圖6係說明第2實 施形態之控制搬送輥對1 8、19之旋轉驅動的控制系統之構 成之方塊圖。再者,於圖6中,由與第1實施形態同一之符 號表示之要素係與第1實施形態中說明之構成無不同之 處。 距離測定感測器44係對應於各搬送輥對1 8、19設置有複 數個。距離測定感測器44係檢測驅動用軸間隔。驅動用軸 間隔係指將位於與玻璃帶B相同側之搬送輥18a、19a彼此 連結之驅動用軸18b、19b、及與該驅動用轴18b、19b對向 配置之驅動用軸18b、19b之距離。搬送輥對18、19係於成 對之搬送輥1 8a、19a間相互受到偏壓之狀態下夾持玻璃帶 B。因此,各搬送輥18a、19a之磨損量係作為按照下式算 出之輥半徑之與新製品時之輥半徑相比的變化量因搬送輥 18a、19a之磨損所產生,由檢測部47檢測。於該式中,由 163507.doc -35- 201247566 於玻璃帶B之厚度於各搬送輥18a、19a之位置固 M弋,故而 藉由測定驅動用軸18b、19b彼此之間隔而算出親半柄。 輥半徑=(驅動用軸間隔-玻璃帶厚度)/2 檢測控制部40之速度決定部48以補償因起因於檢測之搬 送輥18a、19a之磨損的搬送輥18a、19a之半徑之變化而產 生之搬送輥18a、19a之圓周速度之與圓周速度比之偏差之 方式,決定搬送輥18a、19a之旋轉速度。 再者,第2實施形態係利用基於磨損之狀態算出之半徑 之變化,作為搬送輥18a、19a之直徑變化,但亦可與第i 實施形態中使用之搬送輥18a、19a之溫度一併综合地應用 該磨損之狀態。於該情形時,搬送輥18a、19a之直徑因磨 損量而變化,並且因熱膨脹而變化。可以將伴隨該直徑變 化而變化之搬送輥之圓周速度維持為圓周速度比之方式, 算出搬送輥18a、19a之旋轉速度。. 進而,除搬送報18a、19a之直徑變化以外,亦可綜合地 應用根據由玻璃帶B之熱膨脹引起之玻璃帶B之溫度變化 之玻璃帶B之搬送速度變化,作為玻璃帶之狀態。 根據以上之第2實施形態,可補償因搬送輥18a、19a之 磨損引起之直徑變化而導致的搬送輥之圓周速度之與圓周 速度比之偏差。 再者,於該玻璃板製造裝置中,可構成為距離測定感測 器44讀取搬送輥對18、19之驅動用軸18b、19b之與原點位 置之偏差,而取代搬送輥對18、19之驅動用轴18b、19b彼 此之距離,以檢測磨損量。原點位置係搬送輥18a、19a為S 201247566 turns to drive and inhibits the plastic deformation of the glass ribbon. As described above, the position of the conveying roller which determines the rotation speed in such a manner that the diameter of the compensation roller changes is different depending on which characteristic of the glass ribbon B is improved. (Second Embodiment) Next, a glass sheet manufacturing apparatus according to a second embodiment of the present invention will be described. Here, the description will be made focusing on differences from the above-described first embodiment. The conveyance roller state detecting unit 37 of the first embodiment includes a temperature sensor 34 that detects the temperature of the conveyance report. However, as shown in FIG. 6, the conveyance roller state detection unit of the second embodiment (hereinafter also referred to simply as detection) The portion 47 includes a distance measuring sensor 44 for detecting the amount of wear of the conveying roller. Fig. 6 is a block diagram showing the configuration of a control system for controlling the rotational driving of the transport roller pair 18, 19 in the second embodiment. Further, in Fig. 6, the elements indicated by the same symbols as in the first embodiment are different from the configurations described in the first embodiment. The distance measuring sensor 44 is provided in plural for each of the conveying roller pairs 18, 19. The distance measuring sensor 44 detects the shaft spacing for driving. The drive shaft spacing means the drive shafts 18b and 19b that connect the conveyance rollers 18a and 19a on the same side as the glass ribbon B, and the drive shafts 18b and 19b that are disposed opposite to the drive shafts 18b and 19b. distance. The pair of conveying rollers 18 and 19 hold the glass ribbon B while the pair of conveying rollers 18a and 19a are biased to each other. Therefore, the amount of wear of each of the transport rollers 18a and 19a is detected by the detecting unit 47 as a result of the amount of change in the roll radius calculated by the following formula as compared with the roll radius of the new product due to the abrasion of the transport rollers 18a and 19a. In this formula, 163507.doc -35 - 201247566 is used to fix the thickness of the glass ribbon B at the position of each of the transport rollers 18a and 19a. Therefore, by measuring the distance between the drive shafts 18b and 19b, the proximate handle is calculated. . Roller radius = (drive shaft interval - glass ribbon thickness) / 2 The speed determining portion 48 of the detection control portion 40 generates compensation for the change in the radius of the transport rollers 18a, 19a due to the abrasion of the detected transport rollers 18a, 19a. The rotational speeds of the transport rollers 18a and 19a are determined such that the circumferential speeds of the transport rollers 18a and 19a deviate from the peripheral speed ratio. In addition, in the second embodiment, the diameters of the conveyance rollers 18a and 19a are changed by the change in the radius calculated based on the state of wear, but they may be combined with the temperatures of the conveyance rollers 18a and 19a used in the i-th embodiment. The state of wear is applied. In this case, the diameters of the conveying rollers 18a and 19a vary depending on the amount of wear and change due to thermal expansion. The rotational speed of the transport rollers 18a and 19a can be calculated by maintaining the peripheral speed of the transport roller that changes in accordance with the diameter change to the peripheral speed ratio. Further, in addition to the change in the diameter of the conveyance marks 18a and 19a, the change in the conveyance speed of the glass ribbon B in accordance with the temperature change of the glass ribbon B caused by the thermal expansion of the glass ribbon B can be comprehensively applied as the state of the glass ribbon. According to the second embodiment described above, it is possible to compensate for the deviation of the circumferential speed of the conveying roller from the circumferential speed ratio caused by the change in the diameter caused by the abrasion of the conveying rollers 18a and 19a. Further, in the glass sheet manufacturing apparatus, the distance measuring sensor 44 may read the deviation of the driving shafts 18b and 19b of the pair of conveying rollers 18 and 19 from the origin position, instead of the pair of conveying rollers 18, The driving shafts 18b, 19b of 19 are spaced apart from each other to detect the amount of wear. The origin position conveyance rollers 18a and 19a are

163507.doc -36- S 201247566 新製品時驅動用轴18b、19b所在之中心位置,且記憶於記 憶部46中。利用搬送輥對18、19之驅動用軸i8b、i9b之與 原點位置之偏差,檢測搬送輥l8a、19a之磨損量,藉此, 可算出經磨損之搬送輥之輥徑。 再者,搬送輥18a、19a之直徑並不限定於檢測部47算 出,例如亦可基於磨損量由操作人員算出。於該情形時, 基於由操作人員算出且輸入至速度決定部48之搬送輥 18a、19a之直徑,藉由速度決定部48而算出搬送輥18还、 19a之旋轉速度。或者,亦可基於操作人員算出之搬送輥 18a、19a之直徑,進一步算出搬送輥18a、19a之旋轉速 度’且將該算出結果輸入至速度決定部48。速度決定部48 中鼻出或輸入之方疋轉速度係由速度決定部48決定,且傳遞 至驅動部32。又,搬送輥18a、19a之磨損量、原點位置亦 可由操作人員算出,且可將算出之值記憶於記憶部46中。 (第2實施形態之變形例) 亦可使用將基於搬送輥18a、19a之使用天數算出之搬送 輥之直徑之變化作為搬送輥18a、19a之直徑變化進行計數 之裝置’而取代第2實施形態之玻璃板製造裝置之距離測 定感測器44。例如對該直徑變化進行計數之裝置係將搬送 輥18a、19a之使用天數搬送至速度決定部48。速度決定部 48係參照記憶於速度決定部48之記憶部46中且關於各搬送 輥18a、19a作為以往之更換實績以往更換時輥直徑與其新 製品時相比之磨相量、及直至更換為止之使用天數,並基 於該等,算出每1天之磨損量。其次,參照記憶於記憶部 163507.doc •37- 201247566 46中之新製品時之親直徑’按照下式算出報直徑。此時, 利用自對上述直徑變化進行計數之裝置搬送之使用天數, 如下式所不,作為每1天之磨損量\使用天數之積相當於搬 送輥18a、19a之磨損量進行檢測。 輥直徑=新製品時之直徑_(每丨天之磨損量乂使用天數) 速度決定部48係於記憶部46中,對於各搬送輥丨仏、19& 記憶以往之更換實績、新製品時之輥直徑。 根據該變形例,可以更簡單之方法’補償因搬送輥 18a 1知之直徑變化而產生之搬送輥18a、19a之圓周速度 之與圓周速度比之偏差》再者,每丨天之磨損量亦可由操 作人員算出且記憶於記憶部46中。又,由上述磨損量引起 之搬送輥18a、19a之直徑變化亦可由操作人員算出,且傳 遞至檢測控制部40或驅動部32。進而,以往更換時之親直 徑之與其新製品時相比之磨損量、及直至更換為止之使用 天數亦可由操作人員异出’且算出之值可記憶於記憶部46 中。 如上所述’本變形例中’搬送輥18a、19a係基於以補償 輥之直徑變化之方式基於搬送輥18a、19a之使用天數決定 之報之旋轉速度進行紅轉驅動。本變形例係於以下方面斑 第1實施形態及第2實施形態不同,即基於搬送親iga、i9a 之使用天數循序地決定報旋轉速度’而並非如第1實施形 態及第2實施形態所述’利用搬送輥狀態檢測部檢測搬送 輥之狀態,且基於該檢測結果’決定輥旋轉速度。 再者,第1實施形態或第1實施形態之變形例、與第2實 163507.doc163507.doc -36- S 201247566 The center position of the drive shafts 18b, 19b at the time of the new product, and is stored in the memory unit 46. The deviation between the driving axes i8b and i9b of the pair of conveying rollers 18 and 19 and the origin position is detected, and the amount of wear of the conveying rollers 18a and 19a is detected, whereby the diameter of the worn conveying roller can be calculated. Further, the diameters of the conveying rollers 18a and 19a are not limited to the detection unit 47, and may be calculated by the operator based on, for example, the amount of wear. In this case, the rotation speed of the conveyance rollers 18 and 19a is calculated by the speed determination unit 48 based on the diameters of the conveyance rollers 18a and 19a which are calculated by the operator and input to the speed determination unit 48. Alternatively, the rotation speeds of the conveyance rollers 18a and 19a can be further calculated based on the diameters of the conveyance rollers 18a and 19a calculated by the operator, and the calculation result can be input to the speed determination unit 48. The speed of the nose or the input of the speed determining unit 48 is determined by the speed determining unit 48 and transmitted to the driving unit 32. Further, the amount of wear and the position of the origin of the transport rollers 18a and 19a can be calculated by the operator, and the calculated value can be stored in the memory unit 46. (Variation of the second embodiment) Instead of the second embodiment, a device for counting the change in the diameter of the transport roller calculated based on the number of days of use of the transport rollers 18a and 19a as the change in the diameter of the transport rollers 18a and 19a may be used. The distance measuring sensor 44 of the glass plate manufacturing apparatus. For example, the device for counting the change in diameter conveys the number of days of use of the transport rollers 18a and 19a to the speed determining portion 48. The speed determining unit 48 refers to the memory unit 46 stored in the speed determining unit 48, and the respective conveying rollers 18a and 19a are used as the grinding amount of the conventional replacement performance when the roller diameter is replaced with the new product, and until the replacement. The number of days of use is used, and based on these, the amount of wear per day is calculated. Next, referring to the pro-diameter of the new product in the memory section 163507.doc • 37- 201247566 46, the diameter is calculated according to the following formula. In this case, the number of days of use of the apparatus for counting the change in diameter is not as follows, and the product of the amount of wear per day/the number of days of use corresponds to the amount of wear of the conveyance rollers 18a and 19a. Roll diameter = diameter at the time of the new product _ (the amount of wear per day 乂 the number of days of use) The speed determining unit 48 is attached to the storage unit 46, and remembers the previous transfer performance and new products for each of the transfer rollers 19, 19& Roll diameter. According to this modification, it is possible to compensate for the deviation of the circumferential speed of the conveying rollers 18a and 19a caused by the change in the diameter of the conveying roller 18a1 by the simpler method. Further, the amount of wear per day can also be The operator calculates and memorizes it in the memory unit 46. Further, the diameter change of the conveyance rollers 18a and 19a caused by the above-described wear amount can be calculated by the operator and transmitted to the detection control unit 40 or the drive unit 32. Further, the amount of wear of the intimate diameter in the conventional replacement and the number of days until the replacement of the new product can be changed by the operator, and the calculated value can be stored in the memory unit 46. As described above, in the present modification, the conveyance rollers 18a and 19a are red-rotated based on the rotation speed determined based on the number of days of use of the conveyance rollers 18a and 19a so as to compensate for the change in the diameter of the compensation roller. The present modification is different from the first embodiment in that the first embodiment and the second embodiment are different in that the number of days of use of the transport pro iga and i9a is determined sequentially, and the rotation speed is not determined as described in the first embodiment and the second embodiment. 'The conveyance roller state detecting unit detects the state of the conveyance roller, and determines the roller rotation speed based on the detection result'. Furthermore, the first embodiment or the modification of the first embodiment and the second embodiment 163507.doc

S -38- 201247566 施形態或諫2實施形態之變形例亦可進行組合。可藉由組 合第1實施形態或第1實施形態之變形例、與第2實施形態 或第2實施形態之變形例,而與單獨地應用第丨實施形態或 第1實施形態之變形例或者第2實施形態或第2實施形態之 變形例之情形相比,以更高之精度補償與圓周速度比之偏 差。 (實施例) 為研究本發明之效果,使用先前之玻璃板製造裝置與本 實施形態之玻璃板製造裝置,分別按照下述方法製造玻璃 帶’並測定產生於玻璃帶中之波狀之凹凸變形。再者,所 用之玻璃板製造裝置均為圖3及圖4所示之下拉法之玻璃板 製造裝置1 ’玻璃係使用含有下述所示成分之鋁矽酸鹽玻 璃。The modification of the S-38-201247566 embodiment or the 谏2 embodiment may be combined. By combining the modification of the first embodiment or the first embodiment with the modification of the second embodiment or the second embodiment, the modification of the third embodiment or the first embodiment or the 2 Compared with the case of the modification of the second embodiment, the deviation from the peripheral speed ratio is compensated with higher accuracy. (Examples) In order to investigate the effects of the present invention, the glass ribbon manufacturing apparatus of the present embodiment and the glass sheet manufacturing apparatus of the present embodiment were used to produce a glass ribbon ′ according to the following method, and the undulation of the undulations generated in the glass ribbon was measured. . Further, the glass plate manufacturing apparatus used is a glass plate manufacturing apparatus 1 of the lower drawing method shown in Figs. 3 and 4, and an aluminosilicate glass containing the components shown below is used.

Si02 60質量%、Si02 60% by mass,

Al2〇3 19.5質量%、 b2o3 10質量%、Al2〇3 19.5 mass%, b2o3 10 mass%,

CaO 5質量%、CaO 5 mass%,

SrO 5質量%、SrO 5 mass%,

Sn02 0.5質量%。 實施例1係按照上述第1實施形態,藉由速度決定部3 8而 決定各搬送輥18a、19a之旋轉速度,且基於決定後之旋轉 速度,控制各搬送輥18a、19a之旋轉驅動,以〇.7 mm厚度 製造寬度方向長2000 mm X長度方向長2500 mm之大小之液 晶顯示器用玻璃基板。作為圓周速度比的各搬送輥18a、 163507.doc -39- 201247566 19a之圓周速度均為相同。玻璃帶之溫度及搬送輥之溫度 係利用接觸式之溫度感測器測定。 實施例2係除了按照上述第2實施形態,藉由速度決定部 48而決定各搬送報iga、i9a之旋轉速度之方面以外,與實 施例1同樣地製造液晶顯示器用玻璃基板。具體而言,搬 送輥18a、19a之磨損量係利用由距離測定感測器44測定之 驅動用軸間隔算出。又,不僅考慮由搬送輥18a、19a之磨 損量引起之輥之直徑之變化量,而且考慮由搬送輥18a、 19a之溫度引起之輥直徑之變化量,算出搬送輥18a、i9a 之旋轉速度。 實施例3係於搬送輥18a、19a之旋轉速度之決定過程 中’將各搬送輥18a、19a之圓周速度均變更為實施例1之 1·1倍,進而製造0.5 mm厚度之液晶顯示器用玻璃基板, 除此以外’以與實施例1相同之方法,製造液晶顯示器用 玻璃基板。 比較例1、2係於速度決定部中不進行基於玻璃帶之狀態 及搬送輥18a、19a之直徑變化的旋轉速度之控制,除此之 外’分別以與實施例1、2相同之條件進行。 對於所得之實施例1〜3、比較例1、2之液晶顯示器用玻 璃基板’以目視確認液晶顯示器用玻璃基板表面有無損 傷’並利用厚度規計測波形之變形。波形之變形係於厚度 為0.7 mm之液晶顯示器用玻璃基板中,將厚度方向上為 0.4 mm以内者設為滿足表面品質。於厚度為〇 5 mm之液晶 顯示器用玻璃基板中’將厚度方向上為〇2 mm以内者設為 163507.doc •40-Sn02 0.5% by mass. In the first embodiment, the speed determining unit 38 determines the rotational speed of each of the transport rollers 18a and 19a, and controls the rotational driving of the transport rollers 18a and 19a based on the determined rotational speed. 7.7 mm thickness Manufacture of a glass substrate for a liquid crystal display having a length of 2000 mm in the width direction and a length of 2500 mm in the longitudinal direction. The circumferential speeds of the respective conveying rollers 18a, 163507.doc - 39 - 201247566 19a which are circumferential speed ratios are the same. The temperature of the glass ribbon and the temperature of the transfer roller were measured using a contact type temperature sensor. In the second embodiment, a glass substrate for a liquid crystal display is produced in the same manner as in the first embodiment except that the rotation speed of each of the conveyance marks iga and i9a is determined by the speed determining unit 48. Specifically, the amount of wear of the conveyance rollers 18a and 19a is calculated by the drive shaft interval measured by the distance measuring sensor 44. In addition, the amount of change in the diameter of the roller caused by the amount of wear of the conveying rollers 18a and 19a is considered, and the rotational speed of the conveying rollers 18a and i9a is calculated in consideration of the amount of change in the diameter of the roller caused by the temperatures of the conveying rollers 18a and 19a. In the third embodiment, the circumferential speeds of the respective transfer rollers 18a and 19a are changed to one-to-one times that of the first embodiment, and the glass for a liquid crystal display having a thickness of 0.5 mm is produced in the process of determining the rotational speed of the transport rollers 18a and 19a. A glass substrate for a liquid crystal display was produced in the same manner as in Example 1 except for the substrate. In Comparative Examples 1 and 2, the control of the rotation speed of the state of the glass ribbon and the change of the diameter of the conveyance rollers 18a and 19a was not performed in the speed determination unit, and the conditions were the same as those of the first and second examples. . With respect to the obtained glass substrates for liquid crystal displays of Examples 1 to 3 and Comparative Examples 1 and 2, the surface of the glass substrate for liquid crystal display was visually observed to have no damage, and the waveform was measured by a thickness gauge. The waveform was deformed in a glass substrate for a liquid crystal display having a thickness of 0.7 mm, and the surface quality was set to be within 0.4 mm in the thickness direction. For glass substrates for liquid crystal displays with a thickness of 〇 5 mm, set 〇2 mm in the thickness direction to 163507.doc •40-

S 201247566 滿足表面品質。 利用先别之製造裝置所得之比較例丨、2之液晶顯示器用 玻璃基板均於玻璃表面上目視確認到損傷。又,均產生厚 度方向上0.5 mm之波形之變形。 與此相對,利用本實施形態之製造裝置丨所得之實施例 1 3之液B曰顯示器用玻璃基板均未能於玻璃表面目視確認 到損傷。又’關於波形之變形’實施例1係產生厚度方向 上為〇_2 mm左右之變形。實施例2係產生厚度方向上為〇1 mm左右之變形。實施例3係產生厚度方向上為〇 〇2瓜山以 下之變形。實施例1〜3均滿足上述表面品質。 以上’對本發明之玻璃板之製造方法及玻璃板製造裝置 詳細地進行了說明,但本發明並不限定於上述實施形態, 勿庸置疑’於不脫離本發明之精神之範圍内,亦可進行各 種改良或變更。 【圖式簡單說明】 圖1係表示本實施形態之玻璃板之製造方法之流程之一 例之圖。 圖2係表示徐冷步驟之流程之一例之圖。 圖3係說明本發明之第1實施形態之玻璃板製造裝置之内 部之平面圖。 圖4係圖3之IV線箭線剖面圖。 圖5係說明控制搬送輥對之旋轉驅動的控制系統之構成 之方塊圖。 圖6係說明本發明之第2實施形態之玻璃板製造裝置之控 163507.doc • 41 · 201247566 制搬送輥對之旋轉驅動的控制系統之構成之方塊圖。 【主要元件符號說明】 1 玻璃板製造裝置 2 成形裝置 3 徐冷裝置 4 裁板裝置 10 成形體 10a 槽 11 爐室 12 第1徐冷爐 13 第2徐冷爐 15 爐壁 16 搬送孔 17 輥對 18、19 搬送輥對 18a、19a 搬送輥 18b 、 19b 驅動用轴 21 〜23 隔熱板 30 檢測控制部 32 驅動部 34 溫度感測器(玻璃狀態檢測部) 36 記憶部 37 搬送輥狀態檢測部 38 速度決定部 163507.doc •42- 201247566 40 檢測控制部 44 距離測定感測器 46 記憶部 47 搬送輥狀態檢測部 48 速度決定部 A 熔融玻璃 B 玻璃帶 C 玻璃板 IV 線 S10 熔解步驟 S20 澄清步驟 S30 攪拌步驟 S40 成形步驟 S50 徐冷步驟 S51 檢測步驟 S52 速度決定步驟 S53 速度控制步驟 S60 裁板步驟 S70 形狀加工步驟 163507.doc -43-S 201247566 Meets surface quality. The glass substrates for liquid crystal displays of Comparative Examples 2 and 2 obtained by the prior art manufacturing apparatus were visually confirmed to have damage on the glass surface. Further, deformation of a waveform of 0.5 mm in the thickness direction is generated. On the other hand, in the glass substrate for liquid B 曰 display of Example 13 obtained by the production apparatus of the present embodiment, the damage was not visually observed on the surface of the glass. Further, in the case of "deformation of the waveform", the first embodiment produced a deformation of about 〇 2 mm in the thickness direction. In the second embodiment, deformation in the thickness direction of about 1 mm was produced. In the third embodiment, the deformation in the thickness direction is 〇 〇 2 瓜山. Each of Examples 1 to 3 satisfies the above surface quality. In the above, the glass sheet manufacturing method and the glass sheet manufacturing apparatus of the present invention have been described in detail. However, the present invention is not limited to the above-described embodiments, and it is needless to say that it can be carried out without departing from the spirit of the invention. Various improvements or changes. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a view showing an example of a flow of a method for producing a glass sheet according to the present embodiment. Fig. 2 is a view showing an example of the flow of the cold step. Fig. 3 is a plan view showing the inside of a glass sheet manufacturing apparatus according to a first embodiment of the present invention. Figure 4 is a cross-sectional view of the arrow line of the IV line of Figure 3. Fig. 5 is a block diagram showing the configuration of a control system for controlling the rotational driving of the pair of conveying rollers. Fig. 6 is a block diagram showing the configuration of a control system for rotational driving of a transport roller pair according to a control unit of a glass sheet manufacturing apparatus according to a second embodiment of the present invention. 163507.doc • 41 · 201247566. [Description of main component symbols] 1 Glass plate manufacturing apparatus 2 Forming device 3 Pressing device 4 Cutting device 10 Molded body 10a Groove 11 Furnace chamber 12 First cold furnace 13 Second cold furnace 15 Furnace wall 16 Transfer hole 17 Roll pair 18, 19 Transfer roller pair 18a, 19a Transport roller 18b, 19b Drive shaft 21 to 23 Heat shield 30 Detection control unit 32 Drive unit 34 Temperature sensor (glass state detecting unit) 36 Memory unit 37 Transport roller state detecting unit 38 Speed determination 163507.doc •42- 201247566 40 Detection control unit 44 Distance measurement sensor 46 Memory unit 47 Transport roller state detection unit 48 Speed determination unit A Molten glass B Glass ribbon C Glass plate IV line S10 Melting step S20 Clarification step S30 Stirring Step S40 Forming Step S50 Thawing Step S51 Detection Step S52 Speed Determination Step S53 Speed Control Step S60 Panel Step S70 Shape Processing Step 163507.doc -43-

Claims (1)

201247566 七、申請專利範圍: ι_ —種玻璃板之製造方法’其特徵在於包括: 熔解步驟’其將玻璃原料熔解而製作熔融玻璃; 成形步驟,其使用下拉法將熔融玻璃成形,而形成玻 璃帶;及 徐冷步驟,其將上述玻璃帶由沿著上述玻璃帶之搬送 方向設置之複數個輥夾持並朝向下方曳引而進行徐冷;且 上述成形步驟包括將上述玻璃帶一面由輥對夾持並朝 向下方良引,一面冷卻上述玻璃帶之兩端部之步驟, 上述成形步驟及上述徐冷步驟之任一者所使用之上述 輥對中之至少任-個輥對即^輥對之各輕,係基於以 補償輥之直徑變化之方式衫之輥之旋轉速度予以旋轉 驅動。 2. 一 種玻璃板之製造方法,其特徵在於包括: 熔解步驟,其將玻璃原料熔解而製作熔融玻璃; 成形步驟,其使用下拉法將忮 祖次肘尨岫玻璃成形,而形成玻 璃帶;及 徐冷步驟’其將上述玻璃帶由々丄 坡,帝由/〇者上述玻璃帶之搬送 方向設置之複數個輥對夾持 穴付亚朝向下方曳引而進行徐 冷;且 上述徐冷步驟中,上述輥對中 親對中之至少任一個輥對即第 1輥對之各輥,係基於 .^ 補慣輥之直徑變化之方式決定 之輥之旋轉速度予以旋轉驅動。 3.如請求項1或2之玻璃板之製 衣以万法’其中上述徐冷步驟 163507.doc 201247566 包括: 檢測步驟,其藉由沿著上述玻璃帶 檢測部而檢測上述第 、向設置之 、去“ 疋第1輥對之各輥之直徑變化;及 々& /、基於檢測出之上述第1輥對之上,十. 各輥之直徑變化,也— ί之上述 第_之上述各親旋=各報之旋轉速度,而使上述 4.如請求項1或2之破璃 ’饥Ilk方法’其中上述第1輥 之各輥係設置於上述徐冷 4你冷步驟之至少上述玻璃帶中央 之溫度成為玻璃轉移點 點以上且軟化點以下之溫度區域 内,且 在上述徐冷步驟中,以補償上述第旧對之各輕之直 «化之方式’決定上述第i輕對之各輕之旋轉速度, 而使上述第1輥對之各輥旋轉驅動。 5.如請求項【或2之玻璃板之製造方法,其中在上述成形步 驟及上述徐冷步驟中, 於上述玻璃帶之中央部之溫度為玻璃軟化點以上之區 域内,以上述玻璃帶之寬度方向之端部低於由上述端部 所夾之中央區域之溫度、且上述中央區域之溫度成為大 致均一之方式進行控制, 於上述玻璃帶之中央部之溫度為未達軟化點且為應變 點附近以上之區域内,以搬送方向之拉伸應力作用於上 述玻璃帶之中央部之方式進行控制,以使上述玻璃帶之 寬度方向之溫度自上述玻璃帶之中央部朝向端部變低,且 於上述玻璃帶之玻璃應變點附近之溫度區域内,以上 I63507.doc * S 201247566 述玻璃帶之寬度方向之端部與中央部之溫度梯度消失之 方式,控制上述玻璃帶之溫度分佈。 6. 如請求項1或2之玻璃板之製造方法,其中在上述徐冷步 驟中,於上述玻璃帶之中央部之溫度未達應變點附近之 區域内,以搬送方向之拉伸應力作用於上述玻璃帶之中 央部之方式控制上述玻璃帶之溫度分佈,以使上述玻璃 帶之溫度分佈自上述玻璃帶之寬度方向之端部朝向中央 部變低。 ' 7. 如請求項1或2之玻璃板之製造方法,其中上述徐冷步驟 包括: 第1冷卻步驟,其以第丨平均冷卻速度進行冷卻直至 上述玻璃帶之中央部之溫度達到徐冷點為止; 第2冷卻步驟,其以第2平均冷卻速度進行冷卻直至 上述中央部之溫度自上述徐冷點達到應變點·5〇。〇為 止;及 第3冷卻步驟,其以第3平均冷卻速度進行冷卻直至 上述中央邹之溫度自上述應變點·机達到上述應變點_ 2〇〇°C 為止; ’ 上述第1平均冷卻速度係5 〇〇c/秒 — 8. 上述第1平均冷卻速度快於上述第3平均冷卻速度, 上述第3平均冷卻速度快於上述第2平均冷卻速度。 如請求項1或2之玻璃板之製造方法,其中以補償:上述 第1輕對之各輥之熱膨脹引起之上述第旧之各輕之直和 變化而產生的圓周速度之偏差之方式,決定上述第W 163507.doc 201247566 對之各輥之旋轉速度, 動0 而使上述第1輥對 之各軺•旋轉驅 9.如請求項丨或2之玻璃板之製造方法,其中以補償由上述 第1輥對之各報之磨損引起之上述第1輥對之各輥之直徑 變化而產生的圓周速度之偏差之方式,決定上述第1 = 對之各親之旋轉速度’而使上述第i輥對之各輥旋轉驅 動。 10.如請求項1或2之玻璃板之製造方法,其令上述複數個輥 對中之具有基於以補償輥之直徑變化之方式決定之棍之 旋轉速度予以旋轉驅動之輥的輥對,除上述第1輥對以 外並包含第2輥對; 該玻璃板之製造方法包括藉由沿著上述玻璃帶之搬送 方向設置之複數個檢測部而檢測上述第1輥對及上述第2 輥對之各親之直徑變化之檢測步驟,且 於上述第1輥對之各輥與上述第2輥對之各輥之間,以 輥之圓周速度與上述玻璃帶之搬送速度之相對速度成為 固定之方式,決定補償上述各軺•之直徑變化之上述各報 之旋轉速度。 11·如請求項1或2之玻璃板之製造方法,其中藉由沿著玻璃 帶之搬送方向設置且檢測上述玻璃帶之狀態之玻璃狀態 檢測部,檢測上述玻璃帶之溫度; 使用檢測出之上述玻璃帶之溫度中之玻璃熱膨脹係 數’檢測由上述玻璃帶之熱膨脹引起之上述玻璃帶之搬 送速度之變化’且以補償上述玻璃帶之搬送速度與輥之 163507.doc S 201247566 圓周速度之偏差之方式’決定上述第1輥對之各報之旋 轉速度。 12. 如請求項1或2之玻璃板之製造方法,其中使上述玻璃帶 徐冷而成之玻璃板之厚度係為0.5 mm以下。 13. —種玻璃板製造裝置’其特徵在於包括: 成形裝置’其使用下拉法’自溶融玻璃將玻璃帶成 形;及 徐冷裝置’其將上述玻璃帶一面由複數個搬送報對夾 持並朝向下方曳引,一面進行徐冷;且 上述徐冷裝置包括上述複數個搬送輥對、檢測控制 部、及驅動部; 上述複數個搬送輥對係沿著上述玻璃帶之搬送方向設 置,且藉由朝向下方拉入上述玻璃帶而搬送玻璃帶; 上述檢測控制部包括沿著上述玻璃帶之搬送方向設 置、且檢測上述搬送輥對之搬送輥之直徑變化之複數個 搬送輥狀態檢測部; 上述驅動部於上述複數個搬送輕對間,以保持上述搬 送輥之圓周速度與上述玻璃帶之搬送速度之相對速度成 為固定時的上述複數個搬送輥對間之圓周速度分佈之方 式,基於由檢測出之上述搬送輥之直徑變化而決定之各 上述搬送輥之旋轉速度’使上述搬送輥旋轉驅動。 163507.doc201247566 VII. Patent application scope: ι_ - A method for manufacturing a glass plate, characterized by comprising: a melting step of melting a glass raw material to produce molten glass; and a forming step of forming a molten glass by using a down-draw method to form a glass ribbon And a cold step of tempering the glass ribbon by a plurality of rollers disposed along a direction in which the glass ribbon is conveyed and dragging downward; and the forming step comprises: arranging the glass ribbon on one side by a roller pair a step of cooling the both ends of the glass ribbon while holding it downward, and at least one of the pair of rollers used in any one of the forming step and the quenching step is a pair of rollers Each of them is lightly driven based on the rotational speed of the roller of the shirt in such a manner as to compensate for the change in the diameter of the roller. A method for producing a glass sheet, comprising: a melting step of melting a glass raw material to produce a molten glass; and a forming step of forming a glass ribbon by using a down-draw method to form a glass ribbon; and "Xu cold step", which uses the plurality of rollers disposed in the direction in which the glass ribbon is transported by the sloping slope, and the locating hole is pulled downward to perform the cold cooling; and the above-mentioned cold cooling step In the above roller pair, at least one of the pair of rollers, that is, each roller of the first roller pair, is rotationally driven based on the rotation speed of the roller determined by the diameter change of the complementary roller. 3. The garment of the glass sheet of claim 1 or 2, wherein the above-mentioned cold cooling step 163507.doc 201247566 includes: a detecting step of detecting the above-mentioned first and second directions by the glass ribbon detecting portion Going to "the diameter change of each roller of the first roller pair; and 々 & /, based on the detected first roller pair, ten. the diameter change of each roller, also - the above-mentioned _th Each of the rotation speeds of the respective rotations, and the above-mentioned 4. The broken glass 'Hungry Ilk method' of the claim 1 or 2, wherein each of the roller systems of the first roller is disposed at least the above-mentioned cold step The temperature in the center of the glass ribbon is in the temperature region above the glass transition point and below the softening point, and in the above-mentioned cold cooling step, the above-mentioned i-th light pair is determined by compensating for the lightness of the above-mentioned old pair. The light-rotating speed of each of the first roller pairs is rotatably driven. 5. The method of manufacturing the glass sheet of claim 2, wherein in the forming step and the quenching step, the glass is The temperature in the center of the belt is glass In the region above the softening point of the glass, the end portion of the glass ribbon in the width direction is controlled to be lower than the temperature of the central region sandwiched by the end portion, and the temperature of the central region is substantially uniform, and the glass ribbon is controlled. The temperature in the central portion is controlled in a region where the softening point is not higher than the strain point, and the tensile stress in the transport direction acts on the central portion of the glass ribbon to control the temperature in the width direction of the glass ribbon. From the central portion of the glass ribbon toward the end portion, and in the temperature region near the glass strain point of the glass ribbon, the temperature gradient between the end portion and the central portion of the width direction of the glass ribbon is described above. 6. The method of manufacturing the glass sheet according to claim 1 or 2, wherein in the step of cooling, the temperature in the central portion of the glass ribbon is not near the strain point. In the region, the temperature distribution of the glass ribbon is controlled such that the tensile stress in the conveying direction acts on the central portion of the glass ribbon. The temperature distribution of the glass ribbon is lowered from the end portion in the width direction of the glass ribbon toward the central portion. The method of manufacturing the glass sheet according to claim 1 or 2, wherein the step of cooling comprises: a first cooling step Cooling at the second average cooling rate until the temperature in the central portion of the glass ribbon reaches the freezing point; and in the second cooling step, cooling at the second average cooling rate until the temperature in the central portion is from the above-mentioned cold point Achieving a strain point of 5 〇. 及; and a third cooling step, which is cooled at a third average cooling rate until the temperature of the center Zou reaches the strain point _ 2 〇〇 ° C from the strain point machine; The first average cooling rate is 5 〇〇 c / sec - 8. The first average cooling rate is faster than the third average cooling rate, and the third average cooling rate is faster than the second average cooling rate. The method for producing a glass sheet according to claim 1 or 2, wherein the method of compensating for the deviation of the circumferential speed caused by the change of the lightness of the first and the first light caused by the thermal expansion of each of the first pair of rollers is determined In the above-mentioned W 163507.doc 201247566, the rotation speed of each roller is changed to 0, and the first roller pair is rotated. 9. The manufacturing method of the glass plate of claim 2 or 2, wherein the compensation is made by the above The first i = the rotational speed of each of the first pair of pairs is determined by the difference in the circumferential speed caused by the change in the diameter of each of the first roller pairs caused by the abrasion of each of the first roller pairs Each roller of the roller pair is rotationally driven. 10. The method of producing a glass sheet according to claim 1 or 2, wherein the plurality of pairs of rolls have a pair of rolls that are rotationally driven based on a rotation speed of the stick determined by compensating for a change in diameter of the roll, The second roller pair is included in addition to the first roller pair; the method for manufacturing the glass plate includes detecting the first roller pair and the second roller pair by a plurality of detecting portions provided along a conveying direction of the glass ribbon a step of detecting a diameter change of each of the members, wherein a speed at which the circumferential speed of the roller and the conveying speed of the glass ribbon are fixed between the rollers of the first roller pair and the rollers of the second roller pair is fixed It is decided to compensate for the above-mentioned respective rotation speeds of the respective diameter changes. The method for producing a glass sheet according to claim 1 or 2, wherein the temperature of the glass ribbon is detected by a glass state detecting portion which is disposed along a conveying direction of the glass ribbon and detects the state of the glass ribbon; The coefficient of thermal expansion of the glass in the temperature of the glass ribbon 'detects the change in the conveying speed of the glass ribbon caused by the thermal expansion of the glass ribbon' and compensates for the deviation of the conveying speed of the glass ribbon from the circumferential speed of the roller 163507.doc S 201247566 The method 'determines the rotation speed of each of the first roller pairs. 12. The method of producing a glass sheet according to claim 1 or 2, wherein the thickness of the glass sheet obtained by quenching the glass ribbon is 0.5 mm or less. 13. A glass sheet manufacturing apparatus characterized by comprising: a forming apparatus that shapes a glass ribbon from a molten glass using a down-draw method; and a "cold cooling apparatus" that holds the glass ribbon by a plurality of conveyance reports The cold cooling device includes a plurality of conveying roller pairs, a detection control unit, and a driving unit, and the plurality of conveying roller pairs are disposed along the conveying direction of the glass ribbon, and are borrowed The glass ribbon is conveyed by pulling the glass ribbon downward; the detection control unit includes a plurality of conveyance roller state detecting sections that are provided along the conveyance direction of the glass ribbon and that detect a change in the diameter of the conveyance roller of the conveyance roller pair; The driving unit is configured to detect the circumferential speed distribution between the plurality of conveying roller pairs when the relative speed between the peripheral speed of the conveying roller and the conveying speed of the glass ribbon is fixed between the plurality of conveying pairs The rotation speed of each of the conveyance rollers determined by the change in the diameter of the conveyance roller is made to convey the conveyance Rotary drive. 163507.doc
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