TWI557081B - Manufacture of glass plates - Google Patents
Manufacture of glass plates Download PDFInfo
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- TWI557081B TWI557081B TW102109905A TW102109905A TWI557081B TW I557081 B TWI557081 B TW I557081B TW 102109905 A TW102109905 A TW 102109905A TW 102109905 A TW102109905 A TW 102109905A TW I557081 B TWI557081 B TW I557081B
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- glass
- groove portion
- molten glass
- molded body
- groove
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- 239000011521 glass Substances 0.000 claims description 215
- 239000006060 molten glass Substances 0.000 claims description 173
- 238000004519 manufacturing process Methods 0.000 claims description 39
- 238000012546 transfer Methods 0.000 claims description 31
- 238000002844 melting Methods 0.000 claims description 22
- 230000008018 melting Effects 0.000 claims description 22
- 239000005357 flat glass Substances 0.000 claims description 14
- 239000002994 raw material Substances 0.000 claims description 12
- 238000013459 approach Methods 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 10
- 238000000465 moulding Methods 0.000 claims description 10
- 238000004031 devitrification Methods 0.000 description 20
- 238000005352 clarification Methods 0.000 description 17
- 239000000463 material Substances 0.000 description 13
- 238000012986 modification Methods 0.000 description 13
- 230000004048 modification Effects 0.000 description 13
- 239000004065 semiconductor Substances 0.000 description 12
- 230000015572 biosynthetic process Effects 0.000 description 9
- 229910021420 polycrystalline silicon Inorganic materials 0.000 description 8
- 229920005591 polysilicon Polymers 0.000 description 8
- 239000008395 clarifying agent Substances 0.000 description 7
- 239000007791 liquid phase Substances 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- 229910006404 SnO 2 Inorganic materials 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 4
- 229910004298 SiO 2 Inorganic materials 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000007500 overflow downdraw method Methods 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 3
- 238000000265 homogenisation Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000006722 reduction reaction Methods 0.000 description 3
- 238000010583 slow cooling Methods 0.000 description 3
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 150000001340 alkali metals Chemical class 0.000 description 2
- 229910052788 barium Inorganic materials 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 229910052712 strontium Inorganic materials 0.000 description 2
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 2
- 229910001887 tin oxide Inorganic materials 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000006025 fining agent Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- VASIZKWUTCETSD-UHFFFAOYSA-N manganese(II) oxide Inorganic materials [Mn]=O VASIZKWUTCETSD-UHFFFAOYSA-N 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N zinc oxide Inorganic materials [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B17/00—Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
- C03B17/06—Forming glass sheets
- C03B17/064—Forming glass sheets by the overflow downdraw fusion process; Isopipes therefor
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B17/00—Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
- C03B17/06—Forming glass sheets
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B18/00—Shaping glass in contact with the surface of a liquid
- C03B18/02—Forming sheets
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Compositions (AREA)
Description
本發明係關於一種製造玻璃板之玻璃板之製造方法。 The present invention relates to a method of manufacturing a glass sheet for producing a glass sheet.
先前以來,於製造玻璃板時,進行有使用溢流下拉法而成形玻璃板。於溢流下拉法中,將玻璃原料在熔解槽中熔融而製作熔融玻璃,對該熔融玻璃實施澄清處理、均質化處理後,熔融玻璃通過輸送管而供給於長條狀之成形體。 Previously, in the production of glass sheets, glass sheets were formed using an overflow down-draw method. In the overflow down-draw method, the glass raw material is melted in a melting tank to prepare molten glass, and the molten glass is subjected to a clarification treatment and a homogenization treatment, and then the molten glass is supplied to the elongated molded body through a transfer pipe.
於長條狀之成形體中,在成形體之上部設有沿長度方向延伸之槽部,熔融玻璃供給至該槽部之一端。該槽部中,自熔融玻璃之供給側越向長度方向之相反側前進,槽深度越淺,因而熔融玻璃自成形體之槽部溢出,順著成形體兩側之側壁向下方流下。沿成形體兩側之側壁向下方流下之熔融玻璃於成形體之下端合流貼合為1體而成為平板玻璃。 In the elongated molded body, a groove portion extending in the longitudinal direction is provided on the upper portion of the molded body, and the molten glass is supplied to one end of the groove portion. In the groove portion, the supply side of the molten glass advances toward the opposite side in the longitudinal direction, and the shallower the groove depth, the molten glass overflows from the groove portion of the molded body, and flows downward along the side walls on both sides of the molded body. The molten glass which flows down along the side wall of the both sides of the molded body is joined to the lower end of the molded body to form a flat glass.
另外,將熔融玻璃供給至成形體之輸送管之流路剖面形狀通常為圓形狀,成形體之槽部之流路剖面形狀為矩形或者多邊形之形狀。將輸送管之流路剖面形狀設為圓形狀之原因在於,較佳為即使於輸送管內填充高溫之熔融玻璃,亦不會有產生彎曲之部分,可維持強度。另一方面,將成形體槽部之流路剖面形狀設為矩形或者多邊形之形狀係為了槽部之加工之容易性。 Further, the cross-sectional shape of the flow path for supplying the molten glass to the transfer tube of the molded body is generally a circular shape, and the cross-sectional shape of the flow path of the groove portion of the molded body is a rectangular or polygonal shape. The reason why the cross-sectional shape of the flow path of the transfer pipe is a circular shape is that it is preferable that even if the molten glass is filled with a high temperature in the transfer pipe, the bent portion is not formed and the strength can be maintained. On the other hand, the cross-sectional shape of the flow path of the molded body groove portion is a rectangular or polygonal shape for the ease of processing the groove portion.
例如,於下述專利文獻1之圖1、圖3中,揭示有具有流路剖面形狀為圓形狀之輸送管、及流路剖面形狀為矩形形狀之槽部之成形體。 於此情形時,自圓形形狀之輸送管向成形體之槽部供給熔融玻璃時,熔融玻璃之流路剖面具有階差而急遽擴大。 For example, in the following Patent Document 1 and FIG. 3, a molded body having a circular cross-sectional shape of a flow path and a groove having a rectangular cross-sectional shape is disclosed. In this case, when the molten glass is supplied from the circular-shaped conveying pipe to the groove part of the molded object, the flow path cross section of the molten glass has a step difference and is rapidly expanded.
[專利文獻1]日本專利特表2008-501609號公報 [Patent Document 1] Japanese Patent Laid-Open Publication No. 2008-501609
如此,一般而言,由於將熔融玻璃供給至成形體之輸送管之流路剖面形狀為圓形狀、成形體之槽部之流路剖面形狀為矩形或者多邊形之形狀,因而自輸送管向成形體之槽部供給熔融玻璃時,熔融玻璃之流路剖面具有階差而急遽擴大。因此,有藉由熔融玻璃之流路急遽擴大,而於成形體之槽部內熔融玻璃之流動容易部分性停留之情形。熔融玻璃之流動之停留容易導致熔融玻璃之失透。又,熔融玻璃之流動之停留容易產生異質坯料,容易導致波筋之產生。若更詳細地進行說明,則於熔融玻璃之流動停留時,與成形體接觸之時間與其它部分之熔融玻璃相比變長,因而成形體之成分自成形體之表面熔出,熔融玻璃之玻璃組成容易部分性地變化。又,受成形體溫度之影響,熔融玻璃之黏度容易部分性地變化。即,於熔融玻璃中容易產生異質坯料,其結果,於最終製品之玻璃板中容易產生波筋,並且玻璃板之厚度容易變得不均勻。 As described above, in general, the cross-sectional shape of the flow path in which the molten glass is supplied to the transfer tube of the molded body is a circular shape, and the cross-sectional shape of the flow path of the groove portion of the molded body is a rectangular or polygonal shape, and thus the transfer tube is formed into a molded body. When the molten glass is supplied to the groove portion, the flow path cross section of the molten glass has a step difference and is rapidly expanded. Therefore, the flow path of the molten glass is rapidly expanded, and the flow of the molten glass in the groove portion of the molded body is likely to partially stay. The residence of the flow of molten glass is liable to cause devitrification of the molten glass. Further, the residence of the flow of the molten glass tends to cause a foreign material to be generated, which tends to cause the generation of the ribs. More specifically, when the flow of the molten glass stays, the time of contact with the molded body becomes longer than that of the molten glass in other portions, and thus the components of the molded body are melted from the surface of the molded body, and the glass of the molten glass is melted. The composition is easily changed in part. Further, the viscosity of the molten glass is likely to partially change due to the influence of the temperature of the molded body. That is, a foreign material is likely to be generated in the molten glass, and as a result, a rib is easily generated in the glass plate of the final product, and the thickness of the glass plate tends to be uneven.
又,於平板顯示器用玻璃板中,TFT(Thin Film Transistor,薄膜電晶體)等半導體元件形成於玻璃基板上。近年來,為了實現顯示器顯示之進一步之高精細化,要求代替自先前一直使用之α-Si‧TFT而將p-Si(低溫多晶矽)‧TFT或氧化物半導體形成於玻璃板上。於p-Si‧TFT或氧化物半導體之形成步驟中,存在溫度高於α-Si‧TFT形成步驟之熱處理步驟。因此,對於形成有p-Si(低溫多晶矽)TFT或氧化物 半導體之玻璃板要求熱收縮率較小。為了減小熱收縮率,較佳為使玻璃之應變點增高,但應變點較高之玻璃存在液相溫度變高之傾向,且存在液相黏度(液相溫度下之黏度)變低之傾向。因此,亦有平板玻璃之成形所需之熔融玻璃之黏度(成形黏度)與液相黏度之差變小、或者成形黏度大於液相黏度之情形,其結果,玻璃容易失透。因而,於利用p-Si(低溫多晶矽)‧TFT形成用或者氧化物半導體形成用等液相黏度特別低之玻璃製造平板玻璃之情形時,必需極力避免熔融玻璃之一部分之流動容易於如有成形體成分自成形體之表面熔出、液相黏度之上升(失透之生成)之虞之成形體之槽部內停留。 Further, in a glass plate for a flat panel display, a semiconductor element such as a TFT (Thin Film Transistor) is formed on a glass substrate. In recent years, in order to achieve further high definition of display display, it is required to form a p-Si (low temperature polysilicon) ‧ TFT or an oxide semiconductor on a glass plate instead of the α-Si‧ TFT which has been used in the past. In the formation step of the p-Si‧TFT or the oxide semiconductor, there is a heat treatment step in which the temperature is higher than the α-Si‧ TFT formation step. Therefore, for the formation of p-Si (low temperature polysilicon) TFT or oxide Semiconductor glass sheets require a small heat shrinkage rate. In order to reduce the heat shrinkage rate, it is preferred to increase the strain point of the glass, but the glass having a higher strain point tends to have a higher liquidus temperature, and the liquidus viscosity (viscosity at the liquidus temperature) tends to be lower. . Therefore, there is also a case where the difference between the viscosity (forming viscosity) of the molten glass required for the formation of the flat glass and the liquidus viscosity is small, or the forming viscosity is larger than the liquidus viscosity, and as a result, the glass is easily devitrified. Therefore, in the case of producing flat glass using p-Si (low temperature polysilicon) ‧ TFT formation or glass having a particularly low liquid viscosity such as oxide semiconductor formation, it is necessary to prevent the flow of a part of the molten glass from being easily formed. The body component stays in the groove portion of the molded body after the surface of the molded body is melted and the liquidus viscosity is increased (the formation of devitrification is formed).
因此,為了解決先前之問題,本發明之目的在於提供一種玻璃板之製造方法,其係於使用成形體之熔融玻璃之成形時,通過成形體之槽部之熔融玻璃之流動不易停留,熔融玻璃不會產生失透及異質坯料,可製造無波筋、板厚均勻之高品質之玻璃板。 Therefore, in order to solve the problems of the prior art, an object of the present invention is to provide a method for producing a glass sheet which is characterized in that the flow of molten glass passing through the groove portion of the molded body is hard to stay when the molten glass using the molded body is formed, and the molten glass is used. It does not produce devitrified and heterogeneous billets, and can produce high-quality glass sheets with no corrugated and uniform thickness.
本發明之一態樣係製造玻璃板之玻璃板之製造方法。該製造方法包含:將玻璃原料熔解而製作熔融玻璃之步驟;供給步驟,其係將上述熔融玻璃通過輸送管供給至成形體;及成形步驟,其係使用上述成形體將上述熔融玻璃成形而製作平板玻璃。 One aspect of the present invention is a method of producing a glass sheet for producing a glass sheet. The production method includes a step of melting a glass raw material to produce molten glass, a supply step of supplying the molten glass to a molded body through a transfer pipe, and a molding step of molding the molten glass by using the molded body. plate glass.
於上述供給步驟中將上述熔融玻璃自上述輸送管供給至上述成形體之槽部時,上述熔融玻璃不會於上述槽部之底面停留而以具有朝向上述成形體之速度成分之方式使上述熔融玻璃流動。 In the supply step, when the molten glass is supplied from the transfer pipe to the groove portion of the molded body, the molten glass does not stay on the bottom surface of the groove portion and melts so as to have a velocity component toward the molded body. The glass flows.
因此,可使熔融玻璃自上述輸送管向上述成形體之上述槽部之流動順暢,能夠將熔融玻璃於上述槽部之滯留時間統一於固定範圍內而使熔融玻璃自上述槽部溢出。由此,可製造不易產生玻璃之失透或 異質坯料、無波筋且板厚均勻之高品質之玻璃板。 Therefore, the flow of the molten glass from the transport pipe to the groove portion of the molded body can be made smooth, and the residence time of the molten glass in the groove portion can be unified within a fixed range to cause the molten glass to overflow from the groove portion. Thereby, it is possible to manufacture a devitrification which is less likely to cause glass or A high quality glass plate with a heterogeneous billet, no corrugated and uniform thickness.
此時,可藉由以下之較佳之形態來實現上述供給步驟。 At this time, the above supply step can be realized by the following preferred embodiment.
即,較佳為,上述輸送管連接於上述槽部之開口端,於上述輸送管中流動之熔融玻璃之流路剖面之面積隨著接近於上述輸送管之開口端與上述成形體之上述槽部之開口端之連接位置而逐漸變寬。較佳為,於上述供給步驟中將上述熔融玻璃自上述輸送管供給至上述成形體之槽部時,於上述輸送管中流動之熔融玻璃之流路剖面之寬度隨著接近於上述輸送管之開口端與上述成形體之上述槽部之開口端之連接位置而逐漸變寬。藉由上述流路剖面之面積或寬度隨著接近於上述連接位置而逐漸變寬,上述熔融玻璃不會於上述槽部之底面停留而以具有朝向上述成形體之速度成分之方式流至上述成形體。 In other words, it is preferable that the transfer pipe is connected to the open end of the groove portion, and the cross-sectional area of the flow path of the molten glass flowing through the transfer pipe is close to the open end of the transfer pipe and the groove of the molded body. The connection position of the open end of the portion is gradually widened. Preferably, when the molten glass is supplied from the transfer pipe to the groove portion of the molded body in the supply step, the width of the cross section of the flow path of the molten glass flowing through the transfer pipe is close to the transfer pipe. The opening end is gradually widened at a position where it is connected to the opening end of the groove portion of the formed body. The area or width of the flow path cross section gradually becomes wider as it approaches the connection position, and the molten glass does not stay on the bottom surface of the groove portion and flows to the above-mentioned shape so as to have a velocity component toward the molded body. body.
於此情形時,較佳為,於上述連接位置達到槽部之槽寬,且於上述連接位置,上述輸送管之開口端之緣具有與上述成形體之上述槽部之開口端之至少底面之緣形狀一致之形狀,上述輸送管之壁面與上述槽部之上述底面無階差地連接。 In this case, it is preferable that the groove width of the groove portion is reached at the connection position, and at the connection position, the edge of the open end of the transfer tube has at least a bottom surface of the open end of the groove portion of the molded body. The shape of the edge shape is the same, and the wall surface of the conveying pipe is connected to the bottom surface of the groove portion without a step.
進而,較佳為,上述輸送管之開口端之緣具有與上述槽部之開口端之側面之緣形狀的一部分一致之形狀。 Furthermore, it is preferable that the edge of the opening end of the conveying pipe has a shape that matches a part of the shape of the edge of the side surface of the opening end of the groove portion.
上述輸送管之開口端之緣具有與上述成形體之上述槽部之開口端之至少底面之緣形狀一致之形狀,進而具有與上述槽部之開口端之側面之緣形狀的一部分一致之形狀,因而可使熔融玻璃自上述輸送管向上述成形體之上述槽部之流動更為順暢。 The edge of the opening end of the conveying pipe has a shape that matches the shape of at least the bottom surface of the opening end of the groove portion of the molded body, and further has a shape that matches a part of the shape of the side surface of the opening end of the groove portion. Therefore, the flow of the molten glass from the conveying pipe to the groove portion of the formed body can be made smoother.
上述輸送管較佳為具有上述流路剖面之寬度連續擴展至上述連接位置之端部。 Preferably, the conveying pipe has an end portion in which the width of the flow path cross section continuously extends to the connecting position.
由此,熔融玻璃之流動更不易停留。 Thereby, the flow of the molten glass is less likely to stay.
較佳為,上述成形體之上述槽部中之熔融玻璃之流路剖面隨著上述成形體之上述槽部接近於上述連接位置而逐漸變小。 Preferably, the flow path cross section of the molten glass in the groove portion of the molded body gradually decreases as the groove portion of the molded body approaches the connection position.
由此,即使於上述輸送管之流路剖面相比於上述成形體之上述槽部之流路剖面極小之情形時,亦可使熔融玻璃自上述輸送管向上述槽部之流動順暢。 Therefore, even when the flow path cross section of the transfer pipe is extremely smaller than the flow path cross section of the groove portion of the molded body, the flow of the molten glass from the transfer pipe to the groove portion can be made smooth.
較佳為,上述槽部於包含上述底面之槽下部具有如下部分,即,槽寬隨著向上述槽部之深度方向前進而變窄,隨著靠近於上述連接位置,上述槽寬變窄之上述深度方向之起始位置變淺。 Preferably, the groove portion has a portion at a lower portion of the groove including the bottom surface, that is, the groove width is narrowed as it advances in the depth direction of the groove portion, and the groove width is narrowed as it approaches the connection position. The starting position of the above depth direction becomes shallow.
由此,可使上述槽下部之熔融玻璃之流動更為順暢。 Thereby, the flow of the molten glass in the lower portion of the groove can be made smoother.
即使上述熔融玻璃之應變點為655℃以上,亦可適用於上述玻璃板之製造方法。 Even if the strain point of the molten glass is 655 ° C or more, it can be applied to the method for producing the above glass plate.
此種玻璃為應變點較高之玻璃,具有液相溫度(失透溫度)增高之傾向。於使用該應變點為655℃以上之玻璃之情形時,成形步驟中之熔融玻璃之適當黏度(例如40000 poise以上)與玻璃之液相黏度相近,因而容易失透。特別是若熔融玻璃於成形時停留,則成形體之成分會自成形體之表面熔出,更容易失透。於上述製造方法中,由於不易使熔融玻璃之流動停留於上述成形體之上述槽部,因而可抑制玻璃之失透。 Such a glass is a glass having a high strain point and has a tendency to increase the liquidus temperature (devitrification temperature). In the case where the glass having a strain point of 655 ° C or more is used, the appropriate viscosity (for example, 40,000 poise or more) of the molten glass in the forming step is similar to the liquid phase viscosity of the glass, and thus it is easy to devitrify. In particular, if the molten glass stays at the time of molding, the components of the molded body are melted from the surface of the molded body, and are more likely to devitrify. In the above production method, since the flow of the molten glass is less likely to stay in the groove portion of the molded body, devitrification of the glass can be suppressed.
即使為上述熔融玻璃之應變點為675℃以上之玻璃,亦可適用於上述玻璃板之製造方法,不易產生失透。又,即使為上述熔融玻璃之應變點為680℃以上之玻璃,亦可適用於上述玻璃板之製造方法,不易產生失透。進而,即使為上述熔融玻璃之應變點為690℃以上之玻璃,亦可適用於上述玻璃板之製造方法,不易產生失透。應變點之上限例如為750℃,較佳為730℃。 Even if the glass has a strain point of 675 ° C or higher, the glass sheet can be applied to the method for producing the glass sheet described above, and devitrification is less likely to occur. Further, even if the glass has a strain point of 680 ° C or higher, the glass sheet can be applied to the method for producing the glass sheet described above, and devitrification is less likely to occur. Further, even if the glass has a strain point of 690 ° C or higher, the glass sheet can be applied to the method for producing the glass sheet described above, and devitrification is less likely to occur. The upper limit of the strain point is, for example, 750 ° C, preferably 730 ° C.
上述熔融玻璃之液相黏度可設為60000 poise以下,亦可設為50000 poise以下。進而,液相黏度亦可設為45000 poise以下。此種玻璃由於接近於成形步驟中所需之熔融玻璃之黏度故為容易失透之玻璃。特別是若熔融玻璃於成形體中停留,則為更容易失透之玻璃。但 是,於上述玻璃板之製造方法中,由於不易使熔融玻璃之流動停留於上述成形體之上述槽部,因而即使液相黏度為60000 poise以下、50000 poise以下、進而45000 poise以下,亦可抑制玻璃之失透,可製造玻璃板。液相黏度之下限例如為40000 poise。 The liquid viscosity of the molten glass can be set to 60,000 poise or less, and can be set to 50,000 poise or less. Further, the liquidus viscosity may be set to 45,000 poise or less. Such a glass is a glass which is easily devitrified due to its close proximity to the viscosity of the molten glass required in the forming step. In particular, if the molten glass stays in the molded body, it is a glass which is more likely to devitrify. but In the method for producing a glass sheet, the flow of the molten glass is less likely to stay in the groove portion of the molded body, and therefore the liquid phase viscosity is 60,000 poise or less, 50,000 poise or less, and further 45,000 poise or less. The glass is devitrified and can be used to make glass sheets. The lower limit of the liquidus viscosity is, for example, 40,000 poise.
上述玻璃板例如為平板顯示器用玻璃板,例如為p-Si(低溫多晶矽)TFT形成用玻璃板或者氧化物半導體形成用玻璃板。 The glass plate is, for example, a glass plate for a flat panel display, and is, for example, a glass plate for forming a p-Si (low temperature polysilicon) TFT or a glass plate for forming an oxide semiconductor.
p-Si(低溫多晶矽)TFT形成用玻璃板或者氧化物半導體形成用玻璃板之應變點較高。若應變點較高,則具有液相溫度變高之傾向,且具有液相黏度(液相溫度下之黏度)變低之傾向。因此,亦有平板玻璃之成形所需之熔融玻璃之黏度(成形黏度)與液相黏度之差減小,或者成形黏度大於液相黏度之情形,其結果,玻璃容易失透。特別是若熔融玻璃於成形體中停留,則更容易失透。因而,即使將難以停留於成形體之槽部可使熔融玻璃順暢地流動之上述態樣之玻璃板之製造方法應用於平板顯示器用玻璃板、特別是p-Si(低溫多晶矽)TFT形成用玻璃板或者氧化物半導體形成用之玻璃板,亦不易產生失透。 The p-Si (low temperature polysilicon) glass plate for forming a TFT or the glass plate for forming an oxide semiconductor has a high strain point. When the strain point is high, the liquidus temperature tends to be high, and the liquidus viscosity (viscosity at the liquidus temperature) tends to be low. Therefore, there is also a case where the difference between the viscosity (forming viscosity) of the molten glass required for the formation of the flat glass and the liquidus viscosity is reduced, or the forming viscosity is greater than the liquidus viscosity, and as a result, the glass is easily devitrified. In particular, if the molten glass stays in the molded body, it is more likely to devitrify. Therefore, the method for producing a glass sheet of the above-described aspect in which the molten glass can smoothly flow even in the groove portion of the molded body is applied to a glass plate for a flat panel display, in particular, a glass for forming a p-Si (low-temperature polysilicon) TFT. A glass plate for forming a plate or an oxide semiconductor is also less likely to cause devitrification.
本發明之另一態樣係製造玻璃板之玻璃板之製造方法。該製造方法包含:將玻璃原料熔解而製作熔融玻璃之步驟;供給步驟,其係將上述熔融玻璃通過輸送管供給至成形體;及成形步驟,其係使用上述成形體將上述熔融玻璃成形而製作平板玻璃;於上述供給步驟中將上述熔融玻璃自上述輸送管供給至上述成形體之槽部時,於上述輸送管中流動之熔融玻璃之流路剖面之寬度隨著接近於上述輸送管之開口端與上述成形體之上述槽部之開口端之連接位置而逐漸變寬,於上述連接位置達到槽部之槽寬,且於上述連接位置,上述輸送管之開口端之緣具有與上述成形體之上述槽部之開口 端之至少底面之緣形狀一致之形狀,上述輸送管之壁面與上述槽部之上述底面無階差地連接。 Another aspect of the invention is a method of making a glass sheet for making a glass sheet. The production method includes a step of melting a glass raw material to produce molten glass, a supply step of supplying the molten glass to a molded body through a transfer pipe, and a molding step of molding the molten glass by using the molded body. In the above-described supplying step, when the molten glass is supplied from the conveying pipe to the groove portion of the molded body, the width of the cross section of the molten glass flowing in the conveying pipe is close to the opening of the conveying pipe The end portion is gradually widened at a position connecting the opening end of the groove portion of the molded body, and reaches a groove width of the groove portion at the connection position, and at the connection position, the edge of the open end of the conveying pipe has the molded body Opening of the above groove portion The shape of at least the bottom surface of the end is uniform, and the wall surface of the conveying pipe is connected to the bottom surface of the groove portion without a step.
因此,可使熔融玻璃自上述輸送管向上述成形體之上述槽部之流動順暢,可將熔融玻璃於上述槽部之滯留時間統一於固定範圍內而使熔融玻璃自上述槽部溢出。因此,可製造不易產生玻璃之失透或異質坯料、無波筋且板厚均勻之高品質之玻璃板。 Therefore, the flow of the molten glass from the transport pipe to the groove portion of the molded body can be made smooth, and the residence time of the molten glass in the groove portion can be unified within a fixed range to cause the molten glass to overflow from the groove portion. Therefore, it is possible to manufacture a high-quality glass plate which is less likely to cause devitrification of the glass or a foreign material, a corrugated material, and a uniform thickness.
根據上述態樣之玻璃板之製造方法,於使用成形體之熔融玻璃之成形時,通過成形體之槽部之熔融玻璃之流動不易停留,熔融玻璃不會產生失透及異質坯料,可製造無波筋且板厚均勻之高品質之玻璃板。 According to the method for producing a glass sheet according to the above aspect, when the molten glass using the molded body is molded, the flow of the molten glass passing through the groove portion of the molded body is less likely to stay, and the molten glass does not cause devitrification and a foreign material, and can be produced without A high-quality glass plate with a uniform thickness and uniform thickness.
100‧‧‧熔解裝置 100‧‧‧melting device
101‧‧‧熔解槽 101‧‧‧melting tank
101d‧‧‧料斗 101d‧‧‧ hopper
102‧‧‧澄清槽 102‧‧‧Clarification tank
103‧‧‧攪拌槽 103‧‧‧Stirring tank
103a‧‧‧攪拌器 103a‧‧‧Agitator
104、105、106‧‧‧玻璃供給管 104, 105, 106‧‧‧ glass supply tube
106a‧‧‧玻璃供給管本體 106a‧‧‧glass supply tube body
106b‧‧‧管擴張部 106b‧‧‧ Tube Expansion Department
200‧‧‧成形裝置 200‧‧‧Forming device
210‧‧‧成形體 210‧‧‧Formed body
210a‧‧‧槽部 210a‧‧‧Slots
210b‧‧‧側壁 210b‧‧‧ sidewall
210c‧‧‧下方前端 210c‧‧‧ bottom front
210d‧‧‧底面 210d‧‧‧ bottom
210e‧‧‧槽傾斜面 210e‧‧‧ slot slope
300‧‧‧切斷裝置切斷步驟 300‧‧‧cutting device cutting step
MG‧‧‧熔融玻璃 MG‧‧‧ molten glass
SG‧‧‧平板玻璃 SG‧‧ ‧ flat glass
ST1~ST7‧‧‧步驟 ST1~ST7‧‧‧Steps
W、W1、W2‧‧‧寬度 W, W 1 , W 2 ‧ ‧ width
Z1‧‧‧連接區域 Z 1 ‧‧‧Connected area
圖1係表示本實施形態之玻璃板之製造方法之步驟之一例的圖。 Fig. 1 is a view showing an example of a procedure of a method for producing a glass sheet of the embodiment.
圖2係模式性表示本實施形態中之進行熔解步驟~切斷步驟之裝置之一例的圖。 Fig. 2 is a view schematically showing an example of an apparatus for performing a melting step to a cutting step in the embodiment.
圖3(a)係表示本實施形態中之成形體與玻璃供給管之連接部分之分解立體圖,(b)係表示本實施形態之管擴張部與槽部連接時之連接區域與槽部之間的相對位置之圖。 Fig. 3 (a) is an exploded perspective view showing a connecting portion between the molded body and the glass supply pipe in the embodiment, and (b) is a view showing a connection between the connecting portion and the groove portion when the pipe expanding portion of the embodiment is connected to the groove portion. A map of the relative position.
圖4係說明自上方觀察本實施形態中之玻璃供給管及成形體之連接位置周邊時之熔融玻璃之流動之圖。 Fig. 4 is a view for explaining the flow of the molten glass when the vicinity of the connection position of the glass supply tube and the molded body in the embodiment is viewed from above.
圖5(a)、(b)係說明先前之成形體之槽部與玻璃供給管之連接狀態之圖。 Fig. 5 (a) and (b) are views showing a state in which the groove portion of the former molded body and the glass supply tube are connected.
圖6(a)係說明成形體之槽部與管擴張部之連接之變化例1之圖,(b)係說明成形體之槽部與管擴張部之連接之變化例2之圖。 Fig. 6(a) is a view showing a modification 1 of the connection between the groove portion of the molded body and the tube expansion portion, and Fig. 6(b) is a view showing a modification 2 of the connection between the groove portion of the molded body and the tube expansion portion.
圖7(a)、(b)係表示變化例3之形態之圖。 7(a) and 7(b) are views showing the form of the modification 3.
以下,對本實施形態之玻璃板之製造方法進行說明。圖1係表示本實施形態之玻璃板之製造方法之步驟之一例的圖。 Hereinafter, a method of producing the glass sheet of the present embodiment will be described. Fig. 1 is a view showing an example of a procedure of a method for producing a glass sheet of the embodiment.
玻璃板之製造方法主要具有熔解步驟(ST1)、澄清步驟(ST2)、均質化步驟(ST3)、供給步驟(ST4)、成形步驟(ST5)、緩冷步驟(ST6)、及切斷步驟(ST7)。此外具有研削步驟、研磨步驟、清洗步驟、檢査步驟、捆包步驟等,於捆包步驟中積層之複數個玻璃板被搬送至收貨方之業者。 The manufacturing method of a glass plate mainly has a melting step (ST1), a clarification step (ST2), a homogenization step (ST3), a supply step (ST4), a molding step (ST5), a slow cooling step (ST6), and a cutting step ( ST7). Further, there are a grinding step, a grinding step, a washing step, an inspection step, a packing step, and the like, and a plurality of glass sheets laminated in the packing step are conveyed to a supplier of the receiving side.
熔解步驟(ST1)係於熔解槽中進行。於熔解槽中,藉由將玻璃原料投入至蓄積在熔解槽內之熔融玻璃之液面處並進行加熱而製作熔融玻璃。進而,使熔融玻璃自設置於熔解槽內側側壁之一個底部之流出口向下游步驟流動。 The melting step (ST1) is carried out in a melting tank. In the melting tank, molten glass is produced by putting the glass raw material into the liquid surface of the molten glass accumulated in the melting tank and heating it. Further, the molten glass flows from the outlet opening provided at one bottom of the inner side wall of the melting tank to the downstream step.
關於熔解槽之熔融玻璃之加熱,除了對熔融玻璃本身通電而使其自身發熱來進行加熱之方法以外,亦可輔助性地提供由燃燒器產生之火焰而將玻璃原料熔解。再者,於玻璃原料中添加澄清劑。作為澄清劑,已知有SnO2、As2O3、Sb2O3等,並無特別限制。但是,自降低環境負擔之方面考慮,可使用SnO2(氧化錫)作為澄清劑。 In the heating of the molten glass of the melting tank, in addition to the method of heating the molten glass itself to heat itself and heating it, it is also possible to additionally provide a flame generated by the burner to melt the glass raw material. Further, a clarifying agent is added to the glass raw material. As the clarifying agent, SnO 2 , As 2 O 3 , Sb 2 O 3 and the like are known, and are not particularly limited. However, SnO 2 (tin oxide) can be used as a fining agent from the viewpoint of reducing the environmental burden.
澄清步驟(ST2)至少於澄清槽中進行。澄清步驟中,藉由將澄清槽內之熔融玻璃升溫,熔融玻璃中所含之含O2、CO2或者SO2之氣泡吸收由澄清劑之還原反應產生之O2而成長,氣泡上浮至熔融玻璃之液面而被釋放。進而,於澄清步驟中,藉由降低熔融玻璃之溫度而使由澄清劑之還原反應獲得之還原物質發生氧化反應。由此,殘存於熔融玻璃之氣泡中之O2等氣體成分被再次吸收至熔融玻璃中,氣泡消失。由澄清劑產生之氧化反應及還原反應係藉由控制熔融玻璃之溫度而進行。再者,澄清步驟亦可使用減壓脫泡方式,該減壓脫泡方式係於澄清槽中形成減壓環境之空間,使存在於熔融玻璃中之氣泡於減壓環境 中成長而脫泡。該情形於不使用澄清劑之方面為有效。再者,於澄清步驟中,使用將氧化錫用作澄清劑之澄清方法。 The clarification step (ST2) is carried out at least in the clarification tank. In the clarification step, by raising the temperature of the molten glass in the clarification tank, the bubbles containing O 2 , CO 2 or SO 2 contained in the molten glass absorb the O 2 generated by the reduction reaction of the clarifying agent, and the bubbles float up to the melting. The liquid level of the glass is released. Further, in the clarification step, the reducing substance obtained by the reduction reaction of the clarifying agent is oxidized by lowering the temperature of the molten glass. Thereby, the gas component such as O 2 remaining in the bubbles of the molten glass is again absorbed into the molten glass, and the bubbles disappear. The oxidation reaction and the reduction reaction by the clarifying agent are carried out by controlling the temperature of the molten glass. Further, in the clarification step, a vacuum degassing method may be employed in which a space for forming a reduced pressure environment is formed in the clarification tank, and bubbles existing in the molten glass are grown in a reduced pressure environment to be defoamed. This case is effective in that no clarifying agent is used. Further, in the clarification step, a clarification method using tin oxide as a clarifying agent is used.
於均質化步驟(ST3)中,使用攪拌器對通過自澄清槽延伸之配管供給之攪拌槽內之熔融玻璃進行攪拌,由此進行玻璃成分之均質化。由此,能夠降低作為波筋等之原因之玻璃之組成不均。 In the homogenization step (ST3), the molten glass in the stirring tank supplied through the pipe extending from the clarification tank is stirred by a stirrer to homogenize the glass component. Thereby, it is possible to reduce the compositional unevenness of the glass which is a cause of the ribs or the like.
於供給步驟(ST4)中,熔融玻璃通過自攪拌槽延伸之配管被供給至成形裝置。 In the supply step (ST4), the molten glass is supplied to the forming apparatus through a pipe extending from the stirring tank.
於成形裝置中進行成形步驟(ST5)及緩冷步驟(ST6)。 The forming step (ST5) and the slow cooling step (ST6) are performed in the molding apparatus.
於成形步驟(ST5)中,將熔融玻璃成形為平板玻璃,製作平板玻璃之流體。成形係使用溢流下拉法。 In the molding step (ST5), the molten glass is formed into a flat glass to prepare a fluid for the flat glass. The forming system uses an overflow down-draw method.
於緩冷步驟(ST6)中,以成形後流動之平板玻璃成為所期望之厚度,且不產生內部變形之方式、進而以不產生翹曲之方式進行冷卻。 In the slow cooling step (ST6), the flat glass which flows after molding has a desired thickness, and does not cause internal deformation, and further cools without causing warpage.
於切斷步驟(ST7)中,藉由在切斷裝置中將自成形裝置供給之平板玻璃切斷成特定長度,而獲得板狀之玻璃板。經切斷之玻璃板進而被切斷成特定尺寸,製作目標尺寸之玻璃板。之後,進行玻璃板端面之研削、研磨,進行玻璃板之清洗,進而檢查有無氣泡或波筋等異常缺陷之後,將檢査合格品之玻璃板作為最終製品進行捆包。 In the cutting step (ST7), the plate glass supplied from the forming device is cut into a specific length in the cutting device to obtain a plate-shaped glass plate. The cut glass sheet is further cut into a specific size to produce a glass sheet of a desired size. Thereafter, the glass plate end face is ground and polished, the glass plate is cleaned, and the presence or absence of abnormal defects such as bubbles or ribs is checked, and then the glass plate of the qualified product is packaged as a final product.
圖2係模式性表示進行本實施形態中之熔解步驟(ST1)~切斷步驟(ST7)之裝置之一例之圖。如圖2所示,該裝置主要具有熔解裝置100、成形裝置200、及切斷裝置300。熔解裝置100具有熔解槽101、澄清槽102、攪拌槽103、及玻璃供給管104、105、106。 Fig. 2 is a view schematically showing an example of an apparatus for performing the melting step (ST1) to the cutting step (ST7) in the present embodiment. As shown in FIG. 2, the apparatus mainly has a melting apparatus 100, a forming apparatus 200, and a cutting apparatus 300. The melting apparatus 100 has a melting tank 101, a clarification tank 102, a stirring tank 103, and glass supply pipes 104, 105, and 106.
圖2所示之熔解裝置101中,玻璃原料之投入係使用料斗101d進行。澄清槽102中,調整熔融玻璃MG之溫度,利用澄清劑之氧化還原反應來進行熔融玻璃MG之澄清。進而,於攪拌槽103中,利用攪拌器103a將熔融玻璃MG攪拌而使其均質化。於成形裝置200中,藉由使用成形體210之溢流下拉法自熔融玻璃MG成形平板玻璃SG。 In the melting apparatus 101 shown in Fig. 2, the input of the glass raw material is performed using the hopper 101d. In the clarification tank 102, the temperature of the molten glass MG is adjusted, and the clarification of the molten glass MG is performed by the oxidation-reduction reaction of a clarifier. Further, in the stirring tank 103, the molten glass MG is stirred and homogenized by the agitator 103a. In the forming apparatus 200, the sheet glass SG is formed from the molten glass MG by the overflow down-draw method using the formed body 210.
圖3(a)係表示成形體210與玻璃供給管106之連接部分之分解立體圖。 Fig. 3 (a) is an exploded perspective view showing a portion where the molded body 210 and the glass supply pipe 106 are connected.
成形體210係沿於其上部形成有槽部210a之一方向(圖中X方向)延伸之長條狀之構造體。槽部210a係隨著向X方向前進而槽深度變淺。因此,供給至槽部210a之熔融玻璃MG自槽部210a溢出,且沿設於成形體210之兩側之側壁210b向鉛垂下方流動。順著兩側之側壁210b流下之熔融玻璃MG於設於成形體210之鉛垂下方之下方前端210c合流,貼合為1體而成為平板玻璃SG。 The molded body 210 is formed in an elongated structure in which one of the groove portions 210a is formed in the upper direction (the X direction in the drawing). The groove portion 210a becomes shallower in the groove depth as it advances in the X direction. Therefore, the molten glass MG supplied to the groove portion 210a overflows from the groove portion 210a, and flows downward along the side wall 210b provided on both sides of the molded body 210. The molten glass MG which flows down the side wall 210b of both sides is merged by the lower end 210c provided in the vertical direction below the molded object 210, and is bonded together and becomes the sheet glass SG.
於此種成形體210之槽部210a中,自不會產生失透或波筋之方面考慮,較佳為流暢地供給熔融玻璃MG(熔融玻璃MG之流動不易停留)。特別是對於如液相溫度較高且液相黏度接近於成形步驟時之熔融玻璃之黏度(成形黏度)、或者液相黏度小於成形黏度之容易失透之玻璃而言,必需避免自玻璃供給管106供給至槽部210a之熔融玻璃MG之流動停留。 In the groove portion 210a of the molded body 210, it is preferable to smoothly supply the molten glass MG (the flow of the molten glass MG is not easily stopped) from the viewpoint that devitrification or ribs do not occur. Especially for glass which has a high liquidus temperature and a liquidus viscosity close to the viscosity of the molten glass at the forming step (forming viscosity) or a liquid phase viscosity which is less than the viscosity of the forming, it is necessary to avoid the glass supply tube. The flow of the molten glass MG supplied to the groove portion 210a is stopped.
成形體210之槽部210a之流路剖面呈矩形形狀。另一方面,與成形體210之槽部210a連接之玻璃供給管106為輸送管,其包括具有一定流路剖面之玻璃供給管本體106a、及設於玻璃供給管本體106a之端部之管擴張部106b。玻璃供給管本體106a之流路剖面呈圓形狀。又,作為玻璃供給管本體106a之流路剖面形狀之圓之直徑小於槽部210a之槽寬。 The flow path of the groove portion 210a of the molded body 210 has a rectangular cross section. On the other hand, the glass supply pipe 106 connected to the groove portion 210a of the molded body 210 is a transfer pipe including a glass supply pipe main body 106a having a constant flow path cross section, and a pipe expansion provided at the end of the glass supply pipe main body 106a. Part 106b. The flow path of the glass supply pipe main body 106a has a circular cross section. Moreover, the diameter of the circle which is the cross-sectional shape of the flow path of the glass supply pipe main body 106a is smaller than the groove width of the groove part 210a.
於將熔融玻璃MG自玻璃供給管本體106a通過管擴張部106b供給至成形體210之槽部210a時,流經玻璃供給管106之熔融玻璃MG之流路剖面之面積隨著接近於玻璃供給管106之開口端與成形體210之槽部210a之開口端之連接位置而逐漸擴大。又,流經玻璃供給管106之熔融玻璃MG之流路剖面之橫寬隨著接近於玻璃供給管106之開口端與成 形體210之槽部210a之開口端之連接位置而逐漸擴大。又,流路剖面之橫寬於連接位置達到槽部210a之槽寬。而且,於該連接位置,玻璃供給管106之開口端之緣具有與槽部210a之開口端之至少底面之緣形狀(圖3(a)之情形時為直線形狀)一致之形狀,玻璃供給管106(管擴張部106b)之壁面與槽部210a之底面無階差地連接。此處,熔融玻璃MG之流路剖面之橫寬係指槽部210a之槽寬方向上之寬度。 When the molten glass MG is supplied from the glass supply tube main body 106a to the groove portion 210a of the molded body 210 through the tube expansion portion 106b, the area of the flow path cross section of the molten glass MG flowing through the glass supply tube 106 is close to the glass supply tube. The open end of 106 is gradually enlarged at the position where it is connected to the open end of the groove portion 210a of the formed body 210. Further, the cross-sectional width of the flow path section of the molten glass MG flowing through the glass supply pipe 106 is close to the open end of the glass supply pipe 106. The connection position of the open end of the groove portion 210a of the body 210 is gradually enlarged. Further, the flow path cross section is wider than the connection position to the groove width of the groove portion 210a. Further, at the connection position, the edge of the open end of the glass supply tube 106 has a shape that matches the shape of at least the bottom surface of the open end of the groove portion 210a (the linear shape in the case of Fig. 3(a)), and the glass supply tube The wall surface of the 106 (tube expansion portion 106b) is connected to the bottom surface of the groove portion 210a without a step. Here, the lateral width of the flow path cross section of the molten glass MG means the width in the groove width direction of the groove portion 210a.
具體而言,管擴張部106b之剖面形狀係自玻璃供給管本體106a之圓形狀之流路剖面形狀變化為其剖面形狀之一部分與作為槽部210a底面之緣形狀之直線形狀一致之形狀。此處,所謂槽部210a之底面,除了於槽部210a之剖面形狀為矩形形狀之情形時相當於槽底之平面部分以外,亦包括較以一定槽寬沿深度方向延伸之部分更為下方且槽寬階段性或者連續性地變窄而槽終止之部分之面。於下述圖6(a)、(b)所示之例中,由傾斜面210b、210c形成之V字形狀或圓弧形狀之部分亦適合於底面之緣形狀。 Specifically, the cross-sectional shape of the tube expansion portion 106b is changed from the circular flow path cross-sectional shape of the glass supply tube main body 106a to a shape in which one of the cross-sectional shapes coincides with the linear shape of the edge shape of the bottom surface of the groove portion 210a. Here, the bottom surface of the groove portion 210a is not limited to the planar portion of the groove bottom when the cross-sectional shape of the groove portion 210a is a rectangular shape, but also includes a portion extending in the depth direction with a certain groove width and lower. The groove width is gradually or continuously narrowed to the face of the portion where the groove terminates. In the examples shown in Figs. 6(a) and 6(b) below, the V-shape or the arc-shaped portion formed by the inclined faces 210b and 210c is also suitable for the edge shape of the bottom face.
進而,管擴張部106b之開口端之剖面形狀具有與槽部210a之開口端之側面(側壁面)之緣形狀(直線形狀)之一部分一致之形狀。 Further, the cross-sectional shape of the open end of the tube-expanded portion 106b has a shape that matches one of the edge shapes (linear shapes) of the side surface (side wall surface) of the opening end of the groove portion 210a.
再者,玻璃供給管106中之熔融玻璃MG之流路剖面之寬度變化可連續地或者階段性地進行,但自儘可能地使熔融玻璃MG之流動不停留之方面考慮,較佳為連續性之寬度變化。 Further, the change in the width of the cross section of the flow path of the molten glass MG in the glass supply tube 106 may be continuously or stepwise, but from the viewpoint of not stopping the flow of the molten glass MG as much as possible, continuity is preferred. The width varies.
圖3(b)係表示管擴張部106b之開口端與槽部210a之開口端連接時之連接區域Z1與槽部210a之間的相對位置之圖。如上所述,管擴張部106b與槽210a連接時,係具有與槽部210a之槽寬相同之寬度與槽部210a連接。如圖3(b)所示,以管擴張部106b之開口端之緣與包括槽部210a之底面之槽下部之緣一致之方式設置管擴張部106b。由此,自管擴張部106b流入至槽部210a之熔融玻璃MG自管擴張部106b順暢地流至槽210a,因而熔融玻璃MG之流動不易滯留。於無管擴張部106b之 情形時,當自玻璃供給管本體進入至槽部時,流路剖面急遽擴大,因而有產生熔融玻璃MG之流動停留之情形。於此情形時,熔融玻璃MG特別容易停留於底面,容易導致失透、異質坯料之生成。因此,以玻璃供給管106之開口部之緣與包括槽部210a之底面之槽下部之緣的形狀一致之方式設置管擴張部106b。 FIG 3 (b) are diagrams showing the relative position between the opening end 210a of the connection portion 106b of the tube expansion and the open end of the groove portion 210a of the connecting region Z 1 and the groove portion. As described above, when the tube expansion portion 106b is connected to the groove 210a, it has a width equal to the groove width of the groove portion 210a and is connected to the groove portion 210a. As shown in Fig. 3 (b), the tube expansion portion 106b is provided so that the edge of the open end of the tube expansion portion 106b coincides with the edge of the groove portion including the bottom surface of the groove portion 210a. As a result, the molten glass MG that has flowed into the groove portion 210a from the tube expansion portion 106b smoothly flows into the groove 210a from the tube expansion portion 106b, so that the flow of the molten glass MG is less likely to stay. In the case of the tubeless expansion portion 106b, when the glass supply tube body enters the groove portion, the flow path section is rapidly enlarged, and thus the flow of the molten glass MG is stopped. In this case, the molten glass MG particularly tends to stay on the bottom surface, which tends to cause devitrification and generation of a foreign material. Therefore, the tube expansion portion 106b is provided such that the edge of the opening of the glass supply tube 106 coincides with the shape of the edge of the lower portion of the groove including the bottom surface of the groove portion 210a.
再者,如圖3(b)所示,於成形體210之槽部210a,熔融玻璃MG自包括槽部210a之底面之槽下部供給,於連接位置,槽部210a中之位於槽下部之上方之槽上部如圖3所示般使用板狀構件進行閉塞。因此,熔融玻璃MG自槽部210a之槽下部供給,而且熔融玻璃MG不會停留於底面而以具有朝向成形體210之速度成分之方式順暢地流動,因而熔融玻璃MG自槽部210a順暢地溢出。 Further, as shown in Fig. 3(b), in the groove portion 210a of the molded body 210, the molten glass MG is supplied from the lower portion of the groove including the bottom surface of the groove portion 210a, and at the connection position, the groove portion 210a is located above the lower portion of the groove. The upper part of the groove is closed by a plate-like member as shown in Fig. 3 . Therefore, the molten glass MG is supplied from the lower portion of the groove of the groove portion 210a, and the molten glass MG does not stay on the bottom surface and smoothly flows toward the speed component of the molded body 210, so that the molten glass MG smoothly overflows from the groove portion 210a. .
圖4係說明自上方觀察玻璃供給管106、管擴張部106b及成形體210之連接位置周邊時之熔融玻璃MG之流動之圖。如圖4所示,將熔融玻璃MG自玻璃供給管106供給至成形體210時,流經玻璃供給管106之熔融玻璃MG之流路剖面之寬度隨著接近於玻璃供給管106與成形體210而逐漸變化,玻璃供給管106中之流路剖面之橫寬自玻璃供給管本體106b之流路剖面之寬度W1向成形體210之槽部210a之流路剖面之寬度W2逐漸變化,因而熔融玻璃MG之滯留得到抑制,可順暢地流入至成形體210之槽部210a。 4 is a view for explaining the flow of the molten glass MG when the glass supply tube 106, the tube expansion portion 106b, and the molded body 210 are connected to each other from the top. As shown in FIG. 4, when the molten glass MG is supplied from the glass supply pipe 106 to the molded body 210, the width of the cross section of the flow path of the molten glass MG flowing through the glass supply pipe 106 is close to the glass supply pipe 106 and the formed body 210. changes gradually, the glass supply tube 106 cross-sectional view of the road ilk lateral width of the body from the glass supply tube 106b ilk path cross-sectional width of W 1 to W 210a to the passage cross section of the groove portion ilk article 210. 2 gradually changes, and therefore The retention of the molten glass MG is suppressed, and it can smoothly flow into the groove part 210a of the molded object 210.
圖5(a)、(b)係說明先前之成形體210之槽部210a與玻璃供給管106之連接狀態之圖。如圖5(a)、(b)所示,玻璃供給管106之連接位置之流路剖面與槽部210a之流路剖面相比較小,因而熔融玻璃MG之流路剖面於連接位置急遽擴大。因此,如圖5(b)所示,產生在相對於槽部210a之延伸方向(X方向)傾斜之方向上具有速度成分之熔融玻璃MG之流動,熔融玻璃MG於槽部210a內未能沿X方向順暢地流動。特別是由於槽部210a之底面與玻璃供給管106之壁面具有階差地連接,因而 流經底面附近之熔融玻璃MG之流動之停留之程度較大。 5(a) and 5(b) are views showing a state in which the groove portion 210a of the former molded body 210 is connected to the glass supply pipe 106. As shown in Figs. 5(a) and 5(b), the flow path cross section of the connection position of the glass supply pipe 106 is smaller than the flow path cross section of the groove portion 210a, so that the flow path cross section of the molten glass MG is rapidly expanded at the connection position. Therefore, as shown in Fig. 5 (b), a flow of the molten glass MG having a velocity component in a direction inclined with respect to the extending direction (X direction) of the groove portion 210a is generated, and the molten glass MG fails in the groove portion 210a. The X direction flows smoothly. In particular, since the bottom surface of the groove portion 210a is connected to the wall surface of the glass supply tube 106 in a stepped manner, The flow of the molten glass MG flowing near the bottom surface is largely maintained.
如此,於本實施形態中,玻璃供給管106於其端部包含管擴張部106b。此時,流經玻璃供給管106之熔融玻璃MG之流路剖面之寬度隨著接近於玻璃供給管106之開口端與成形體210之槽部210a之開口端之連接位置而逐漸擴大,於連接位置達到槽部210a之槽寬。於該連接位置,玻璃供給管106(管擴張部106b)之開口端之緣具有與成形體210之槽部210a之開口端之至少底面之緣形狀一致之形狀,玻璃供給管106之壁面與槽部210a之底面無階差地連接。因此,本實施形態中,可使熔融玻璃MG自玻璃供給管106向成形體210之槽部210a之流動順暢,能夠將熔融玻璃MG於槽部210a之滯留時間統一於相對固定之範圍內而使熔融玻璃MG自上述槽部210a溢出。即,於供給步驟中將熔融玻璃MG自玻璃供給管106供給至成形體210之槽部210a時,熔融玻璃MG不會於槽部210a之底部停留而以具有朝向成形體210之速度成分之方式使熔融玻璃MG流動。由此,可製造不易產生玻璃之失透或異質坯料、無波筋且板厚均勻之高品質之玻璃板。 As described above, in the present embodiment, the glass supply tube 106 includes the tube expansion portion 106b at its end portion. At this time, the width of the cross section of the flow path of the molten glass MG flowing through the glass supply pipe 106 gradually increases as it approaches the connection position between the open end of the glass supply pipe 106 and the open end of the groove portion 210a of the molded body 210. The position reaches the groove width of the groove portion 210a. At the connection position, the edge of the open end of the glass supply tube 106 (tube expansion portion 106b) has a shape conforming to the shape of the edge of at least the bottom surface of the open end of the groove portion 210a of the molded body 210, and the wall surface and the groove of the glass supply tube 106. The bottom surface of the portion 210a is connected without a step. Therefore, in the present embodiment, the flow of the molten glass MG from the glass supply tube 106 to the groove portion 210a of the molded body 210 can be made smooth, and the residence time of the molten glass MG in the groove portion 210a can be unified within a relatively fixed range. The molten glass MG overflows from the above-described groove portion 210a. In other words, when the molten glass MG is supplied from the glass supply tube 106 to the groove portion 210a of the molded body 210 in the supply step, the molten glass MG does not stay at the bottom of the groove portion 210a and has a velocity component toward the molded body 210. The molten glass MG is caused to flow. Thereby, it is possible to manufacture a high-quality glass plate which is less likely to cause devitrification of the glass, a foreign material, a corrugated material, and a uniform thickness.
圖6(a)係說明成形體210之槽部210a與管擴張部106b之連接之變化例1之圖。槽部210a之流路剖面係如圖所示般使用槽部210a之底面傾斜之2個槽底傾斜面210b、210c而形成。於此情形時,流經玻璃供給管106之熔融玻璃MG之流路剖面之寬度亦藉由管擴張部106b而隨著接近於玻璃供給管106之開口端與成形體210之槽部210a之開口端之連接位置而逐漸擴大,於連接位置達到槽部210a之槽寬。而且,於該連接位置,玻璃供給管106(管擴張部106b)之開口端之緣具有與成形體210之槽部210a之開口端之至少底面之緣形狀一致之形狀,玻璃供給管106之壁面與槽部210a之底面無階差地連接。進而,管擴張部106b之開口端之剖面形狀具有與槽部210a之開口端之側面(側壁面)之緣形狀 (直線形狀)之一部分一致之形狀。因此,可使熔融玻璃MG向成形體210之槽部210a之流動順暢,能夠將熔融玻璃MG於槽部210a中之滯留時間統一於相對固定之範圍內而使熔融玻璃MG自上述槽部210a溢出。由此,可製造不易產生玻璃之失透或異質坯料、無波筋且板厚均勻之高品質之玻璃板。 Fig. 6(a) is a view showing a modification 1 of the connection between the groove portion 210a of the molded body 210 and the tube expansion portion 106b. The flow path cross section of the groove portion 210a is formed by using two groove bottom inclined surfaces 210b and 210c which are inclined at the bottom surface of the groove portion 210a as shown in the drawing. In this case, the width of the cross section of the flow path of the molten glass MG flowing through the glass supply pipe 106 is also close to the opening end of the glass supply pipe 106 and the opening of the groove portion 210a of the formed body 210 by the pipe expansion portion 106b. The connection position of the end is gradually enlarged, and the groove width of the groove portion 210a is reached at the connection position. Further, at the connection position, the edge of the opening end of the glass supply tube 106 (tube expansion portion 106b) has a shape conforming to the shape of the edge of at least the bottom surface of the opening end of the groove portion 210a of the molded body 210, and the wall surface of the glass supply tube 106 It is connected to the bottom surface of the groove portion 210a without a step. Further, the cross-sectional shape of the open end of the tube expansion portion 106b has a shape of a side surface (side wall surface) of the open end of the groove portion 210a. One of the parts of the (straight line shape) has a uniform shape. Therefore, the flow of the molten glass MG to the groove portion 210a of the molded body 210 can be made smooth, and the residence time of the molten glass MG in the groove portion 210a can be unified within a relatively fixed range, and the molten glass MG can be overflowed from the groove portion 210a. . Thereby, it is possible to manufacture a high-quality glass plate which is less likely to cause devitrification of the glass, a foreign material, a corrugated material, and a uniform thickness.
圖6(b)係說明成形體210之槽部210a與管擴張部106b之連接之變化例2之圖。 Fig. 6(b) is a view showing a second modification of the connection between the groove portion 210a of the molded body 210 and the tube expansion portion 106b.
槽部210a之流路剖面係如圖所示般由槽底面呈圓形狀之曲面之底面210d形成。於此情形時,流經玻璃供給管106之熔融玻璃MG之流路剖面之寬度(直徑)亦藉由管擴張部106b而隨著接近於玻璃供給管106之開口端與成形體210之槽部210a之開口端之連接位置而逐漸擴大,於連接位置達到槽部210a之槽寬。而且,於該連接位置,玻璃供給管106(管擴張部106b)之開口端之緣具有與成形體210之槽部210a之開口端之至少半圓形狀之底面210d之緣形狀一致之形狀,玻璃供給管106之壁面與槽部210a之底面無階差地連接。即,管擴張部106b係一面自流路剖面形狀為圓形狀之玻璃供給管106維持圓形狀一面擴張流路剖面,於連接位置,成為對應於底面210d之大小之圓形狀。因此,可使熔融玻璃MG向成形體210之槽部210a之流動順暢,能夠將熔融玻璃MG於槽部210a中之滯留時間統一於相對固定之範圍內而使熔融玻璃MG自上述槽部210a溢出。因此,於變化例2中,可製造不易產生玻璃之失透或異質坯料、無波筋且板厚均勻之高品質之玻璃板。 The flow path section of the groove portion 210a is formed by the bottom surface 210d of the curved surface having a circular bottom surface as shown in the drawing. In this case, the width (diameter) of the cross section of the flow path of the molten glass MG flowing through the glass supply pipe 106 is also close to the open end of the glass supply pipe 106 and the groove portion of the formed body 210 by the pipe expansion portion 106b. The connection position of the open end of 210a is gradually enlarged, and the groove width of the groove portion 210a is reached at the connection position. Further, at the connection position, the edge of the opening end of the glass supply tube 106 (tube expansion portion 106b) has a shape conforming to the shape of the edge of at least the semicircular bottom surface 210d of the opening end of the groove portion 210a of the molded body 210, and the glass supply The wall surface of the tube 106 is connected to the bottom surface of the groove portion 210a without a step. In other words, the tube expansion portion 106b expands the flow path cross section while maintaining the circular shape of the glass supply tube 106 having a circular cross-sectional shape, and has a circular shape corresponding to the size of the bottom surface 210d at the connection position. Therefore, the flow of the molten glass MG to the groove portion 210a of the molded body 210 can be made smooth, and the residence time of the molten glass MG in the groove portion 210a can be unified within a relatively fixed range, and the molten glass MG can be overflowed from the groove portion 210a. . Therefore, in the second modification, it is possible to manufacture a high-quality glass plate which is less likely to cause devitrification of the glass, a foreign material, a corrugated material, and a uniform thickness.
圖7(a)、(b)係表示變化例3之形態之圖。變化例3構成為成形體210之槽部210a中之熔融玻璃MG之流路剖面隨著接近於成形體210之槽部210a與玻璃供給管106連接之連接位置而逐漸變小。即,以成形 體210之槽部210a中之熔融玻璃MG之流路剖面隨著接近於成形體210之槽部210a與玻璃供給管106連接之連接位置而逐漸變小之方式使熔融玻璃MG流動。 7(a) and 7(b) are views showing the form of the modification 3. In the modification 3, the flow path cross section of the molten glass MG in the groove portion 210a of the molded body 210 is gradually reduced as it approaches the connection position where the groove portion 210a of the molded body 210 is connected to the glass supply pipe 106. That is, to form The cross section of the flow path of the molten glass MG in the groove portion 210a of the body 210 flows toward the molten glass MG so as to gradually become smaller as the connection position between the groove portion 210a of the molded body 210 and the glass supply tube 106 is gradually decreased.
於槽部210a之下方設有槽傾斜面210e。於圖7(a)、(b)所示之例中,該槽傾斜面210e係較以一定槽寬沿深度方向延伸之部分更為下方且槽寬連續性地變窄而於槽底終止之面,且係底面之一部分。槽傾斜面210e之寬度W(參照圖7(b))隨著接近於槽部210a與玻璃供給管106連接之連接位置而變大(隨著自玻璃供給管106離開而變小)。即,槽部210a於包括底面之槽下部具有如下部分,即,槽寬隨著向槽部210a之深度方向前進而變窄,隨著接近於與玻璃供給管106之連接位置,槽寬變窄之槽部210a之深度方向之起始位置變淺。藉由該部分,槽部210a之流路剖面隨著接近於上述連接位置而逐漸變小。特別是由於槽部210a之槽下部之流路剖面越接近於連接位置越小,因而自玻璃供給管106供給熔融玻璃MG時,可抑制位於槽部210a之底面附近之熔融玻璃MG停留而使其順暢地流動。 A groove inclined surface 210e is provided below the groove portion 210a. In the example shown in FIGS. 7(a) and 7(b), the groove inclined surface 210e is lower than a portion extending in the depth direction with a certain groove width, and the groove width is continuously narrowed to terminate at the bottom of the groove. Face, and is a part of the bottom. The width W (see FIG. 7(b)) of the groove inclined surface 210e becomes larger as it approaches the connection position where the groove portion 210a is connected to the glass supply pipe 106 (it becomes smaller as it goes away from the glass supply pipe 106). That is, the groove portion 210a has a portion at the lower portion of the groove including the bottom surface, that is, the groove width is narrowed as it advances in the depth direction of the groove portion 210a, and the groove width is narrowed as it approaches the connection position with the glass supply pipe 106. The starting position of the groove portion 210a in the depth direction becomes shallow. With this portion, the flow path cross section of the groove portion 210a gradually becomes smaller as it approaches the above-described connection position. In particular, since the flow path cross section at the lower portion of the groove portion 210a is closer to the connection position, the molten glass MG located in the vicinity of the bottom surface of the groove portion 210a can be prevented from staying when the molten glass MG is supplied from the glass supply tube 106. Flow smoothly.
再者,於玻璃供給管本體106a中之流路剖面相比於槽部210a極小之情形時,管擴張部106b之流路剖面之擴張率變大。於此情形時,於擴張率較大之管擴張部106b,有無法保持熔融玻璃MG之順暢流動(熔融玻璃MG之流動不會停留之流動)之情形。因此,於變化例3中,為了保持熔融玻璃MG之順暢流動,而構成為於槽部210a之連接位置附近使流路剖面變小,隨著自該連接位置離開而逐漸擴大流路剖面。該槽部210a之流路剖面之擴大可為連續性之擴大,亦可為階段性之擴大。當然,於管擴張部106b與槽部210a之連接位置,管擴張部106b以具有與槽部210a之底面或槽傾斜面210e對應之緣之形狀與槽部210a連接。因而,於變化例3中,在槽部210a,熔融玻璃MG不易停留,從而可製造不易產生玻璃之失透或異質坯料、無波筋且板厚均勻之高品質 之玻璃板。 Further, when the flow path cross section in the glass supply tube main body 106a is extremely smaller than the groove portion 210a, the expansion ratio of the flow path cross section of the tube expansion portion 106b becomes large. In this case, in the pipe expansion portion 106b having a large expansion ratio, there is a case where the smooth flow of the molten glass MG (the flow in which the flow of the molten glass MG does not stay) cannot be maintained. Therefore, in the third modification, in order to keep the molten glass MG flowing smoothly, the flow path cross section is reduced in the vicinity of the connection position of the groove portion 210a, and the flow path cross section is gradually enlarged as it is separated from the connection position. The expansion of the flow path profile of the groove portion 210a may be an expansion of continuity or a stepwise expansion. Of course, the tube expansion portion 106b is connected to the groove portion 210a in a shape having a shape corresponding to the bottom surface of the groove portion 210a or the groove inclined surface 210e at the connection position between the tube expansion portion 106b and the groove portion 210a. Therefore, in the third modification, in the groove portion 210a, the molten glass MG is less likely to stay, and it is possible to produce a high quality which is less likely to cause devitrification of the glass or a foreign material, no corrugated, and uniform thickness. Glass plate.
如上所述,於本實施形態及變化例1~3中,玻璃供給管106於其端部包含管擴張部106b。此時,流經玻璃供給管106之熔融玻璃MG之流路剖面之寬度隨著接近於玻璃供給管106之開口端與成形體210之槽部210a之開口端之連接位置而逐漸擴大,於連接位置達到槽部210a之槽寬。而且,於該連接位置,玻璃供給管106(管擴張部106b)之開口端之緣具有與成形體210之槽部210a之開口端之至少底面之緣形狀一致之形狀,玻璃供給管106之壁面與槽部210a之底面無階差地連接。因此,本實施形態中,可使熔融玻璃MG自玻璃供給管106向成形體210之槽部210a之流動順暢,能夠將熔融玻璃MG於槽部210a中之滯留時間統一於相對固定之範圍內而使熔融玻璃MG自上述槽部210a溢出。因此,不易產生玻璃之失透或異質坯料。 As described above, in the present embodiment and the modifications 1 to 3, the glass supply tube 106 includes the tube expansion portion 106b at the end portion thereof. At this time, the width of the cross section of the flow path of the molten glass MG flowing through the glass supply pipe 106 gradually increases as it approaches the connection position between the open end of the glass supply pipe 106 and the open end of the groove portion 210a of the molded body 210. The position reaches the groove width of the groove portion 210a. Further, at the connection position, the edge of the opening end of the glass supply tube 106 (tube expansion portion 106b) has a shape conforming to the shape of the edge of at least the bottom surface of the opening end of the groove portion 210a of the molded body 210, and the wall surface of the glass supply tube 106 It is connected to the bottom surface of the groove portion 210a without a step. Therefore, in the present embodiment, the flow of the molten glass MG from the glass supply tube 106 to the groove portion 210a of the molded body 210 can be made smooth, and the residence time of the molten glass MG in the groove portion 210a can be unified within a relatively fixed range. The molten glass MG is allowed to overflow from the groove portion 210a. Therefore, it is difficult to produce a devitrified or heterogeneous blank of glass.
玻璃供給管106之流路剖面形狀係藉由作為玻璃供給管106之一部分之管擴張部106b而連續地變化,但該流路剖面形狀亦可階段性地變化。但是,自熔融玻璃MG順暢流動之方面考慮,較佳為熔融玻璃MG之流路剖面之橫寬自玻璃供給管106之橫寬連續地變化為槽部210a之槽寬。 The cross-sectional shape of the flow path of the glass supply pipe 106 is continuously changed by the pipe expansion portion 106b which is a part of the glass supply pipe 106, but the cross-sectional shape of the flow path may be changed stepwise. However, from the viewpoint of smooth flow of the molten glass MG, it is preferable that the lateral width of the flow path cross section of the molten glass MG continuously changes from the lateral width of the glass supply tube 106 to the groove width of the groove portion 210a.
於將本實施形態之玻璃板用於平板顯示器用玻璃板之情形時,例示以具有以下之玻璃組成之方式混合玻璃原料者。 In the case where the glass plate of the present embodiment is used for a glass plate for a flat panel display, it is exemplified that the glass raw material is mixed so as to have the following glass composition.
含有下述成分之無鹼玻璃:SiO2:50~70質量%、Al2O3:0~25質量%、B2O3:1~15質量%、MgO:0~10質量%、CaO:0~20質量%、 SrO:0~20質量%、BaO:0~10質量%、RO:5~30質量%(其中,R為Mg、Ca、Sr及Ba之總量)。 An alkali-free glass containing the following components: SiO 2 : 50 to 70% by mass, Al 2 O 3 : 0 to 25% by mass, B 2 O 3 : 1 to 15% by mass, MgO: 0 to 10% by mass, CaO: 0 to 20% by mass, SrO: 0 to 20% by mass, BaO: 0 to 10% by mass, and RO: 5 to 30% by mass (wherein R is the total amount of Mg, Ca, Sr, and Ba).
再者,本實施形態中為無鹼玻璃,但玻璃板亦可為含有微量鹼金屬之含微量鹼之玻璃。於含有鹼金屬之情形時,較佳為所含有之R'2O之合計為0.10質量%以上且0.5質量%以下、較佳為0.20質量%以上且0.5質量%以下(其中,R'為選自Li、Na及K中之至少一種,為玻璃板所含有之成分)。當然,R'2O之合計亦可低於0.10質量%。 Further, in the present embodiment, the alkali-free glass is used, but the glass plate may be a glass containing a trace amount of an alkali metal and containing a small amount of alkali. In the case of containing an alkali metal, the total amount of R' 2 O contained is preferably 0.10% by mass or more and 0.5% by mass or less, preferably 0.20% by mass or more and 0.5% by mass or less (wherein R' is selected At least one of Li, Na and K is a component contained in the glass plate). Of course, the total of R' 2 O may also be less than 0.10% by mass.
又,於應用本發明之玻璃板之製造方法之情形時,玻璃組合物中除上述各成分外,亦可含有SnO2:0.01~1質量%(較佳為0.01~0.5質量%)、Fe2O3:0~0.2質量%(較佳為0.01~0.08質量%),考慮到環境負擔,亦可以實質上不含As2O3、Sb2O3及PbO之方式製備玻璃原料。 Further, in the case of applying the method for producing a glass plate of the present invention, the glass composition may contain, in addition to the above components, SnO 2 : 0.01 to 1% by mass (preferably 0.01 to 0.5% by mass), Fe 2 . O 3 : 0 to 0.2% by mass (preferably 0.01 to 0.08% by mass), and a glass raw material may be prepared in such a manner that substantially no As 2 O 3 , Sb 2 O 3 or PbO is contained in consideration of environmental burden.
又,近年來為了實現平板顯示器之畫面顯示之進一步高精細化,要求不使用α-Si(非晶矽)‧TFT而使用p-Si(低溫多晶矽)‧TFT或氧化物半導體之顯示器。此處,於p-Si(低溫多晶矽)TFT或氧化物半導體之形成步驟中,存在溫度高於α-Si‧TFT之形成步驟之熱處理步驟。因此,對形成p-Si‧TFT或氧化物半導體之玻璃板要求熱收縮率要小。為了減小熱收縮率,較佳為使應變點增高,但應變點較高之玻璃具有如上所述般液相溫度變高、液相黏度變低之傾向。即,上述液相黏度接近於成形步驟中之熔融玻璃之適當之黏度。因此,為了抑制失透,更強烈地要求不使熔融玻璃MG之流動停留於成形體210之槽部210a。於本實施形態及變化例1~3中,熔融玻璃MG之流動不易停留。因而,本發明之玻璃板之製造方法亦可適用於使用了例如應變點為655℃以上之玻璃之玻璃板。特別是本發明之玻璃板之製造方法亦可適用於適於p-Si‧TFT或氧化物半導體之使用了應變點為655℃以 上、應變點為680℃以上、進而應變點為690℃以上之玻璃之玻璃板,不易產生失透。 Further, in recent years, in order to achieve further high definition of the screen display of a flat panel display, it is required to use a display of p-Si (low temperature polysilicon) ‧ TFT or an oxide semiconductor without using an α-Si (amorphous germanium) ‧ TFT. Here, in the step of forming a p-Si (low temperature polysilicon) TFT or an oxide semiconductor, there is a heat treatment step in which the temperature is higher than the formation step of the α-Si‧ TFT. Therefore, the glass plate forming the p-Si‧ TFT or the oxide semiconductor is required to have a small heat shrinkage rate. In order to reduce the heat shrinkage rate, it is preferable to increase the strain point, but the glass having a high strain point tends to have a high liquidus temperature and a low liquid phase viscosity as described above. That is, the liquid phase viscosity is close to the appropriate viscosity of the molten glass in the forming step. Therefore, in order to suppress devitrification, it is more strongly required not to cause the flow of the molten glass MG to stay in the groove portion 210a of the molded body 210. In the present embodiment and the modifications 1 to 3, the flow of the molten glass MG is less likely to stay. Therefore, the method for producing a glass sheet of the present invention can also be applied to a glass sheet using, for example, glass having a strain point of 655 ° C or higher. In particular, the method for producing a glass plate of the present invention can also be applied to a p-Si‧ TFT or an oxide semiconductor using a strain point of 655 ° C. A glass plate with a strain point of 680 ° C or higher and a strain point of 690 ° C or higher is less likely to cause devitrification.
又,對於使用了液相黏度為60000 poise以下之玻璃、進而液相黏度為50000 poise以下之玻璃、特別是液相黏度為45000 poise以下之玻璃之玻璃板亦可應用本發明之玻璃板之製造方法,不易產生失透。 Further, the glass sheet of the present invention can also be applied to a glass sheet using a glass having a liquidus viscosity of 60,000 poise or less and a glass having a liquidus viscosity of 50,000 poise or less, particularly a glass having a liquidus viscosity of 45,000 poise or less. The method is not easy to cause devitrification.
於將應變點為655℃以上或者液相黏度為45000 poise以下之玻璃用於玻璃板之情形時,作為玻璃組成,例如例示玻璃板以質量%表示含有以下之成分者。 In the case where the glass having a strain point of 655 ° C or higher or a liquid phase viscosity of 45,000 poise or less is used for the glass plate, for example, the glass plate is exemplified as containing the following components by mass%.
較佳為如下之無鹼玻璃或含微量鹼之玻璃,其含有:SiO2 52~78質量%、Al2O3 3~25質量%、B2O3 3~15質量%、RO(其中,R為選自Mg、Ca、Sr及Ba中之玻璃板所含有之全部成分,且為至少1種)3~20質量%;且質量比(SiO2+Al2O3)/B2O3處於7~20之範圍。 Preferably, the following alkali-free glass or glass containing a small amount of alkali contains: SiO 2 52 to 78% by mass, Al 2 O 3 3 to 25% by mass, B 2 O 3 3 to 15% by mass, RO (where R is all components contained in the glass plate selected from the group consisting of Mg, Ca, Sr, and Ba, and is at least one of 3 to 20% by mass; and mass ratio (SiO 2 + Al 2 O 3 ) / B 2 O 3 In the range of 7~20.
進而,為使應變點進一步上升,質量比(SiO2+Al2O3)/RO較佳為7.5以上。進而,為使應變點上升,較佳為將β-OH值設為0.1~0.3mm-1。進而,為了實現高應變點並且防止液相黏度之降低,較佳為將CaO/RO設為0.65以上。考慮到環境負擔,亦可以實質上不含As2O3、Sb2O3及PbO之方式製備玻璃原料。 Further, in order to further increase the strain point, the mass ratio (SiO 2 + Al 2 O 3 )/RO is preferably 7.5 or more. Further, in order to increase the strain point, it is preferable to set the β-OH value to 0.1 to 0.3 mm -1 . Further, in order to achieve a high strain point and prevent a decrease in liquid phase viscosity, it is preferred to set CaO/RO to 0.65 or more. The glass raw material can also be prepared in a manner that does not substantially contain As 2 O 3 , Sb 2 O 3 , and PbO in consideration of environmental burden.
進而,除上述成分外,本實施形態之玻璃板中所用之玻璃中,為了調節玻璃之各種物理、熔融、澄清、及成形之特性,亦可含有其它各種氧化物。作為如此之其他氧化物之例,雖不限定於以下,但可列舉SnO2、TiO2、MnO、ZnO、Nb2O5、MoO3、Ta2O5、WO3、Y2O3及La2O3。此處,由於液晶顯示器或有機EL顯示器等平板顯示器用玻璃板對於氣泡之要求特別嚴格,因而較佳為於上述氧化物中至少含有 澄清效果較大之SnO2。 Further, in addition to the above components, the glass used in the glass plate of the present embodiment may contain other various oxides in order to adjust various physical, melting, clarifying, and forming properties of the glass. Examples of such other oxides are not limited to the following, but examples thereof include SnO 2 , TiO 2 , MnO, ZnO, Nb 2 O 5 , MoO 3 , Ta 2 O 5 , WO 3 , Y 2 O 3 , and La. 2 O 3 . Here, since the glass plate for a flat panel display such as a liquid crystal display or an organic EL display is particularly strict with air bubbles, it is preferable that at least the above-mentioned oxide contains SnO 2 having a large clarification effect.
上述RO之供給源可使用硝酸鹽或碳酸鹽。再者,為了提高熔融玻璃之氧化性,更理想為以適於步驟之比例使用硝酸鹽作為RO之供給源。 A nitrate or a carbonate may be used as a supply source of the above RO. Further, in order to increase the oxidizing property of the molten glass, it is more preferable to use nitrate as a supply source of RO in a ratio suitable for the step.
以上,對本發明之玻璃板之製造方法進行了詳細說明,但本發明並不限於上述實施形態,當然亦可於不脫離本發明之主旨之範圍內進行各種改良或變更。 In the above, the method for producing the glass sheet of the present invention has been described in detail. However, the present invention is not limited to the above-described embodiments, and various modifications and changes can be made without departing from the spirit and scope of the invention.
106‧‧‧玻璃供給管 106‧‧‧Glass supply tube
106a‧‧‧玻璃供給管本體 106a‧‧‧glass supply tube body
106b‧‧‧管擴張部 106b‧‧‧ Tube Expansion Department
210‧‧‧成形體 210‧‧‧Formed body
210a‧‧‧槽部 210a‧‧‧Slots
210b‧‧‧側壁 210b‧‧‧ sidewall
210c‧‧‧下方前端 210c‧‧‧ bottom front
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| KR (1) | KR101559198B1 (en) |
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| JP6346461B2 (en) * | 2014-02-28 | 2018-06-20 | AvanStrate株式会社 | Glass plate manufacturing method and glass plate manufacturing apparatus |
| JP5921742B2 (en) * | 2014-03-29 | 2016-05-24 | AvanStrate株式会社 | Glass plate manufacturing method and glass plate manufacturing apparatus |
| CN104961327B (en) * | 2014-03-29 | 2017-09-22 | 安瀚视特控股株式会社 | Method for producing glass plate, and apparatus for producing glass plate |
| US11053153B2 (en) | 2016-04-07 | 2021-07-06 | Corning Incorporated | Forming bodies for forming continuous glass ribbons and glass forming apparatuses comprising the same |
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| JP2006248855A (en) * | 2005-03-11 | 2006-09-21 | Nippon Electric Glass Co Ltd | Formation apparatus for plate glass and method for forming plate glass |
| US20090013725A1 (en) * | 2004-12-28 | 2009-01-15 | Nippon Electric Glass Co., Ltd. | Device for Manufacturing Sheet Glass and Method for Manufacturing Sheet Glass |
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| JP5751439B2 (en) * | 2010-08-17 | 2015-07-22 | 日本電気硝子株式会社 | Alkali-free glass |
| JP5353963B2 (en) * | 2011-07-06 | 2013-11-27 | 日本電気硝子株式会社 | Sheet glass and method for forming the same |
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| JP2006248855A (en) * | 2005-03-11 | 2006-09-21 | Nippon Electric Glass Co Ltd | Formation apparatus for plate glass and method for forming plate glass |
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