JP5454535B2 - Sheet glass manufacturing method and manufacturing apparatus - Google Patents

Description

  The present invention relates to a plate glass manufacturing method and a manufacturing apparatus, and more particularly to an improvement in a supply flow path for supplying molten glass flowing out of a melting chamber to a molded body.

  In recent years, with the widespread use of various flat panel displays, in particular, the spread of liquid crystal displays, for example, a large amount of thin liquid crystal plate glass having a thickness of about 0.3 to 1.2 mm has been produced. This liquid crystal plate glass is actually formed by various methods typified by the overflow down draw method and the slot down draw method, but the plate glass obtained by the forming has a small surface undulation and roughness. It is required that not only the surface accuracy is excellent but also foreign matters such as bubbles are not mixed.

  For example, in the overflow downdraw method described above, molten glass is continuously supplied to an overflow tank formed on the upper part of a substantially wedge-shaped cross section, and the molten glass is allowed to overflow from the overflow tank so that both sides of the molded body After flowing down along the side wall surface of the sheet, it is fused at the lower top part of the molded body to form a single sheet, and when the sheet-shaped glass molded body of this form is solidified, the pulling roller holds it. This is a method for obtaining a liquid crystal plate glass to be finally produced by pulling downward.

In this case, the molten glass obtained by melting the glass raw material in the melting chamber is supplied to the above-described molded body by continuously flowing down the supply channel, and is provided with this supply channel. It is customary that the plate glass manufacturing apparatus is configured as follows. That is, as shown in FIG. 7, the plate glass manufacturing apparatus 1 is connected to the downstream side of the dissolution chamber 2 disposed at the upstream end through the clarification chamber 3, and the stirring tank 4 A pot 6, which is a volume portion that mainly adjusts the viscosity of the molten glass, is connected via a connecting pipe 5 on the downstream side. Furthermore,
A flow passage area restricting portion 7 whose diameter gradually decreases as it moves downward is formed at the lower portion of the pot 6, and a small diameter pipe 8 is connected to the downstream end of the flow passage area restricting portion 7. A large-diameter pipe 10 having a bent portion 9 is provided on the downstream side of the small-diameter pipe 8. And molten glass is supplied to the molded object 12 from the downstream end part 11 of this large diameter pipe 10, and the molten glass G is made into a plate-like form in this molded object 12 (for example, patent document 1, 2, 3). reference).

US Patent Application Publication No. 2004/0177649 JP 2005-512926 gazette Japanese Patent Publication No.42-23356

By the way, in the melting chamber 2 and the fining chamber 3, in addition to melting the glass raw material, a fining agent is introduced or the temperature distribution of the molten glass is made uniform. When the molten glass flows down in the surrounding pipe 3a, the probability that bubbles are generated in the molten glass is extremely low, and problems due to this hardly occur. However, the oxygen concentration in the molten glass in the vicinity of the peripheral surface of the molten glass is higher on the downstream side than the periphery of the clarification chamber 3 of the molten glass supply flow channel, while the central portion of the flow channel (the central axis of the flow channel) The phenomenon that the oxygen concentration in the molten glass becomes low in the vicinity) occurs. In such a phenomenon, in the vicinity (especially at the interface) of the peripheral surface of the flow channel, hydrogen in the water contained in the molten glass is released into the outside air through the peripheral surface of the flow channel, and only oxygen is present in the flow channel (the flow channel). Residue in the vicinity of the peripheral surface is caused by one factor.

  In addition, since the flow rate of the molten glass is low in the vicinity of the flow path peripheral surface, the oxygen tends to accumulate, so that the oxygen concentration in the molten glass in the vicinity of the flow path peripheral surface is further increased. And when this oxygen concentration reaches a saturated state, bubbles are generated and bubbles are mixed in the molten glass. If such molten glass is supplied to the molded body, it is finally obtained. The quality of the plate glass is lowered and the probability of occurrence of defective products increases.

  In consideration of such matters, bubbles may be generated in the entire region of the supply flow channel downstream from the periphery of the clarification chamber 3, but the present inventors invite the above problems. It has been inferred that the part where bubbles are generated to such an extent is only a part of the supply flow channel downstream from the periphery of the clarification chamber 3. However, as is clear from FIG. 7, the supply flow path downstream from the periphery of the clarification chamber 3 has a complicated structure or shape, so that it is possible to accurately determine at which site the generation of bubbles becomes a problem. In fact, it is extremely difficult to find them, and no measures are taken against the generation of such bubbles.

  In view of the above circumstances, an object of the present invention is to improve the part that is really necessary in the supply flow channel downstream from the periphery of the clarification chamber to avoid the problem due to the generation of bubbles.

  As a result of intensive research, the present inventors, among the supply channels of molten glass from the melting chamber to the molded body, have problems due to the generation of bubbles at specific sites in the supply channel downstream from the periphery of the clarification chamber. As a result, the present invention has been completed.

That is, the method according to the present invention, which has been made to solve the above technical problem, allows the molten glass flowing out of the melting chamber to pass through the clarification chamber and flow down from the stirring tank to the pot via the connecting pipe. The flow path area of the pot whose molten glass flow direction is downward is flowed down, and a small-diameter pipe connected to the downstream side is further flowed down, and then the downstream side of the molten glass flows in the molten glass flow direction. In the method for producing plate glass, a large-diameter pipe having a bent portion which is a portion that converts the material from the downward direction to the lateral direction is caused to flow down and supplied to the formed body, and the molten glass is formed into a plate shape with the formed body. On the downstream side of the periphery of the clarification chamber, at least the flow passage area restriction portion of the pot is bent with a restriction angle of 30 degrees or less or smoothly with a curvature radius of 50 mm or more in a cross section including the flow path center axis. bay In the shape of, adjusting the flow of the molten glass, the oxygen concentration in the vicinity of the flow path peripheral surface of the molten glass flowing down the flow path area narrowed portion of the pot is marked especially wherein suppress to reach saturation .

  Prior to the description of the method according to the present invention, conventional problems will be described. That is, the flow path area restricting portion of the pot has a bent portion 7a having a large degree of bending at the starting end of the restricting portion as shown in FIG. 7 (described in FIG. 1 of the aforementioned Patent Document 1). And the stagnation (stagnation) in the flow of the molten glass due to the presence of the bent portion 7a, and oxygen accumulates in the vicinity of the flow path peripheral surface, so that the oxygen concentration reaches a saturated state, and bubbles are formed in the molten glass. It was a mixed situation.

  Therefore, in the present invention, attention is paid to the flow passage area restricting portion of the pot in the supply passage having a complicated form in which bent portions and the like exist in many places. Then, the flow path area throttle portion of the pot is bent in a cross section including the flow path center axis at a throttle angle of 30 degrees or less, or smoothly curved with a curvature radius of 50 mm or more. The degree of bending of the bent portion at the start end of the path area throttle portion is reduced, or it will be gently curved without bending, so that no unreasonable stagnation occurs in the molten glass flowing down the flow path area throttle portion of the pot, The bubble generation probability at this site is reduced as much as possible. Therefore, the flow channel shape of the flow channel area restricting portion of the pot is a flow channel shape that suppresses the saturation of the oxygen concentration in the vicinity of the flow channel peripheral surface of the molten glass flowing down that portion. Will be. In addition, as a molten glass, if it has the characteristic that the temperature corresponding to the viscosity of 1000 poise becomes 1350 degreeC or more (henceforth a highly viscous glass), it is suitable when enjoying said advantage.

  In this case, it is preferable that the flow path peripheral surface of the connection pipe does not have a recess or a protrusion having a depth exceeding 3 mm in a cross section including the flow path center axis.

  In this way, unreasonable stagnation due to the formation of the circumferential groove does not occur in the molten glass that flows in the vicinity of the flow path peripheral surface of the connection pipe, and the probability of occurrence of bubbles in this connection pipe is as much as possible. Will be reduced.

  Furthermore, it is preferable that the bent portion of the large-diameter pipe does not have a bent portion in a cross section including the flow path center axis.

  In this way, unreasonable stagnation does not occur in the molten glass flowing while changing the direction in the large-diameter pipe, and the occurrence probability of bubbles at the bent portion of the large-diameter pipe is reduced as much as possible. .

  And at least the flow path peripheral surface of the pot is preferably formed of platinum or a platinum alloy.

  If it does in this way, when supplying the above-mentioned high-viscosity glass as a molten glass, the flow path surrounding surface which has sufficient heat resistance and by extension durability can be obtained.

  The forming method having the above-described configuration is suitable for forming a plate glass by, for example, either the overflow down draw method or the slot down draw method.

  Moreover, when shape | molding plate glass only by the overflow down draw method, it is preferable to further provide the structure as shown below.

  That is, when the molten glass flows down from the downstream end of the large-diameter pipe to the molded body, the oxygen concentration in the molten glass existing in the vicinity of the circumferential surface of the channel reaches a saturated state. In order to suppress, it is preferable to adjust the flow of the molten glass.

  In this way, when the overflow downdraw method is adopted, the part where the bubble generation probability is high other than the part described above, that is, the flow path from the downstream end of the large-diameter pipe to the molded body, In order to prevent the oxygen concentration in the molten glass in the vicinity of the flow channel surface from reaching saturation, the flow of the molten glass will be adjusted, and the problem of foam generation after selecting the appropriate part Can be avoided. Specifically, the flow path leading from the downstream end portion of the large-diameter pipe to the molded body has an upper surface portion 11a that is inclined while rising at an angle of about 45 degrees toward the molded body side as shown in FIG. (It is also described in FIG. 1 of Patent Document 1 described above and FIG. 2 of Patent Document 2), and the presence of the upper surface portion 11a causes stagnation in the flow of the molten glass. There was a risk of causing problems due to the occurrence of Therefore, paying attention also to the upper surface portion 11a, a simple method of adjusting the flow in order to suppress the saturation of the oxygen concentration in the molten glass in the vicinity of the peripheral surface, a wide area as described above. Thus, the problem of the generation of bubbles, which has been regarded as a problem, can be easily avoided at low cost.

  In this case, with respect to the flow path leading from the downstream end portion of the large-diameter pipe to the molded body, the upper surface portion is rising at an angle of 30 degrees or less toward the molded body side in the vertical cross section including the flow path center axis. It is preferable that the surface is inclined or curved while smoothly rising at a radius of curvature of 30 mm or more.

  In this way, the degree of inclination (bending degree) at the upper surface portion of the flow path leading to the molded body is reduced or gently curved without bending, so the molten glass flowing along the upper surface portion. No unreasonable stagnation occurs, and the occurrence probability of bubbles at this site is reduced as much as possible.

On the other hand, an apparatus according to the present invention, which has been made to solve the above technical problem, includes a stirring tank and a downstream side thereof in a supply channel that supplies molten glass that has flowed out of the melting chamber to the formed body through the clarification chamber. A connecting pipe that communicates with the pot, a flow passage area restricting portion of the pot in which the molten glass flow direction is downward, a small-diameter pipe connected to the downstream side thereof, and a downstream side of the small-diameter pipe and on the way And a large-diameter pipe having a bent portion which is a part for converting the molten glass flow direction from the lower side to the horizontal direction, and the molten glass supplied through the downstream end portion of the large-diameter pipe is plated by the molded body. In the sheet glass manufacturing apparatus configured to be formed into a shape, at least the flow path area throttle part of the pot is downstream of the periphery of the clarification chamber, and the throttle angle is 30 in the cross section including the flow path center axis. Below Bent, or radius of curvature in the shape of smoothly curved in at least 50mm, as well as configured to regulate the flow of molten glass, a flow passage area narrowed portion of the channel shape of the pot, the molten glass flows down It is characterized in that the flow of molten glass is adjusted to have a flow path shape that suppresses the oxygen concentration in the molten glass existing in the vicinity of the flow path peripheral surface from reaching a saturated state .

  Since this apparatus is substantially the same as the basic configuration of the above-described method, and its operation and effect are also substantially the same, the description thereof is omitted here for convenience.

  In this apparatus, when the molten glass flows down the flow path leading from the downstream end portion of the large-diameter pipe to the molded body, the oxygen concentration in the molten glass existing in the vicinity of the peripheral surface of the flow path reaches a saturated state. In order to suppress this, it is preferable to adjust the flow of the molten glass.

  This configuration is also substantially the same as the configuration according to the corresponding method already described, and the operation and effect thereof are also substantially the same, and therefore the description thereof is omitted here for convenience.

  As described above, according to the present invention, at least on the downstream side of the clarification chamber periphery, the flow channel shape of the flow channel area restricting portion of the pot is specified as the above-described shape, so that the molten glass flows down that portion. The flow of the molten glass is adjusted so as to suppress the oxygen concentration in the vicinity of the flow path peripheral surface from reaching a saturated state. As a result, it is possible to efficiently avoid problems caused by the generation of bubbles in the supply flow path.

It is the schematic which shows the manufacturing apparatus of the plate glass which concerns on embodiment of this invention. FIG. 2A is an enlarged front view of a main part showing a connecting pipe that is a component of the manufacturing apparatus, and FIG. 2B is a main part that shows another example of the connecting pipe that is a component of the manufacturing apparatus. FIG. It is a principal part expansion vertical front view which shows the pot which is a component of the said manufacturing apparatus. It is a principal part expansion vertical front view which shows the other example of the pot which is a component of the said manufacturing apparatus. It is a principal part expansion vertical front view which shows the bending part of the large diameter pipe which is a component of the said manufacturing apparatus. FIG. 6A is an enlarged front view of a main part showing a downstream end portion of a large-diameter pipe that is a component of the manufacturing apparatus, and FIG. 6B is a diagram of a large-diameter pipe that is a component of the manufacturing apparatus. It is a principal part expansion vertical front view which shows the other example of a downstream end part. It is the schematic which shows the manufacturing apparatus of the conventional plate glass. It is a principal part expansion vertical front view which shows the connection pipe which is a component of the said conventional manufacturing apparatus. It is a principal part expansion vertical front view which shows the pot which is a component of the said conventional manufacturing apparatus. It is a principal part expansion vertical front view which shows the other example of the pot which is a component of the said conventional manufacturing apparatus. It is a principal part expansion vertical front view which shows the bending part of the large diameter pipe which is a component of the said conventional manufacturing apparatus. It is a principal part expansion vertical front view which shows the downstream end part of the large diameter pipe which is a component of the said conventional manufacturing apparatus.

  Embodiments of the present invention will be described below with reference to the accompanying drawings.

First, based on FIG. 1, the schematic structure of the manufacturing apparatus of the plate glass which concerns on 1st Embodiment of this invention is demonstrated. The manufacturing apparatus 1 shown in FIG. 1 differs from the manufacturing apparatus 1 shown in FIG. 7 in that the structure of the connecting pipe 5, the shape of the flow passage area restricting portion 7 of the pot 6, and the large-diameter pipe 10. the shape of the bent portion 9, and Ru shape der of the downstream end portion 11 of the large-diameter pipe 10. Since other configurations are substantially the same, common configuration requirements are denoted by the same reference numerals and description thereof is omitted. Further, the molten glass flowing down the supply flow path of the manufacturing apparatus 1 has a characteristic that the temperature corresponding to the viscosity of 1000 poise is 1350 ° C. or higher, and the sheet glass is formed by the overflow down draw method in the molded body 12. At the same time, the finally obtained plate glass is a glass substrate used for manufacturing a liquid crystal display panel.

  FIG. 2A shows a cross-sectional shape including the flow path center axis of the connection pipe 5 (diameter 230 mm) according to this embodiment, and the connection pipe 5 is completely formed with a conventional circumferential groove. It has not been. Therefore, the stagnation of the molten glass G does not occur in the vicinity of the flow path peripheral surface 5x of the connecting pipe 5, and accordingly, the oxygen concentration in the molten glass G in the vicinity of the flow path peripheral surface 5x reaches a saturated state. As a result, a situation in which bubbles are generated in the molten glass G hardly occurs.

  FIG. 2B shows the same cross-sectional shape of another example of the connecting pipe 5 according to this embodiment. Although the connecting pipe 5 has a circumferential groove (recessed part) 5a, the recessed part is shown in FIG. The depth L1 of 5a is 3 mm or less. Thus, if the depth L1 of the recessed part 5a is as shallow as 3 mm or less, the stagnation of the molten glass G does not occur in the vicinity of the flow path peripheral surface 5x as described above, and the occurrence of problematic bubbles is caused. Is avoided.

  On the other hand, as in the conventional example shown in FIG. 8, when the depth L1 of the recess 5a is about 5 mm and exceeds 3 mm, it is directly on the upstream side of the recess 5a in the vicinity of the flow passage circumferential surface 5x. A stagnation portion Gx of the molten glass G is generated on the downstream side, which causes the generation of unjustified bubbles. However, any of the embodiments shown in FIGS. 2A and 2B according to this embodiment Even the structure is remarkably superior to the conventional example.

  FIG. 3 shows a cross-sectional shape including the channel center axis of the channel area restricting portion 7 formed in the lower part of the pot 6 (maximum diameter 50 mm) according to this embodiment. The aperture angle (inclination angle of the inclined portion 7c with respect to the non-inclined portion 7b) α1 is 30 degrees or less, preferably 20 degrees or less. In such a form, when the molten glass G flows downward, the molten glass G does not stagnate in the vicinity of the flow channel peripheral surface 7x of the flow channel area restricting portion 7, and melted accordingly. It is difficult to cause a situation in which bubbles are generated in the glass G.

  On the other hand, as in the conventional example shown in FIG. 9, when the throttle angle α1 of the flow path area throttle portion 7 is about 35 to 40 degrees and exceeds 30 degrees, the flow path circumference of the throttle portion 7 is increased. A stagnant portion Gx of the molten glass G is generated in the vicinity of the surface 7x, which causes unreasonable bubbles to be generated. However, if the form shown in FIG. In comparison, it is remarkably superior.

  FIG. 4 is the same cross-sectional shape showing another example of the flow path area restricting portion 7 formed in the lower portion of the pot 6 according to this embodiment, and the flow path area restricting portion 7 (its start end) is curved. The curvature radius R1 of the curved portion is 30 mm or more, preferably 50 mm or more. Even in such a configuration, the molten glass G does not stagnate in the vicinity of the flow channel peripheral surface 7x of the flow channel area restricting portion 7, and therefore, a situation in which bubbles are generated in the molten glass G hardly occurs. Become.

  On the other hand, as shown in FIG. 10, if the radius of curvature R1 of the curved portion of the flow path area restricting portion 7 is about 20 mm and less than 30 mm, the vicinity of the flow passage peripheral surface 7x of the restricting portion 7 The stagnation portion Gx of the molten glass G is generated, and this causes the generation of inappropriate bubbles. However, the embodiment shown in FIG. 4 according to this embodiment is remarkably excellent. .

  FIG. 5 shows a cross-sectional shape including the flow path center axis of the bent portion 9 of the large-diameter pipe 10 according to this embodiment, and the bent portion 9 has an outer periphery from the inner peripheral side without having a bent portion. The shape is curved across the side. In such a shape, the stagnation of the molten glass G does not occur in the vicinity of the flow path peripheral surface 9x of the bent portion 9 which is a part that converts the flow direction of the molten glass G from the lower side to the horizontal direction. Accordingly, it is difficult for a situation that bubbles are generated in the molten glass G.

  On the other hand, as in the conventional example shown in FIG. 11, when the bent portion 9 of the large-diameter pipe 10 connects three straight pipes and bends with an inclination angle β of about 45 degrees between them. The stagnant portion Gx of the molten glass G is generated in the vicinity of the flow passage peripheral surface 9x where the bent portion 9 bends, and this causes the generation of inappropriate bubbles. If it is the form shown in FIG. 5, it will become the outstanding thing compared with a prior art example.

  FIG. 6A shows a vertical cross-sectional shape including the flow path center axis of the downstream end portion 11 of the large-diameter pipe 10 according to this embodiment, and the upper surface portion 11a of the flow path at the downstream end portion 11 is shown. The inclination angle α2 is 30 degrees or less, preferably 20 degrees or less. With such a shape, the stagnation of the molten glass G does not occur in the vicinity of the flow passage peripheral surface 11x of the upper surface portion 11a at the downstream end portion 11 of the large-diameter pipe 10, and therefore bubbles are generated in the molten glass G. It becomes difficult to happen.

  FIG. 6B shows the same cross-sectional shape of another example of the downstream end portion 11 of the large-diameter pipe 10 according to this embodiment, and the upper surface portion 11a of the flow path at the downstream end portion 11 has a curvature. The radius R2 is smoothly connected via a curved portion having a radius of 30 mm or more, preferably 50 mm or more. In such a form, the stagnation of the molten glass G does not occur in the vicinity of the flow passage peripheral surface 11x as described above, and it is avoided that the generation of bubbles that pose a problem is caused.

  On the other hand, as in the conventional example shown in FIG. 12, the inclination angle α2 of the upper surface portion 11a at the downstream end portion 11 of the large-diameter pipe 10 is about 45 degrees and is bent without exceeding 30 degrees and without bending. If this is the case, a stagnant portion Gx of the molten glass G is generated in the vicinity of the flow passage peripheral surface 11x of the upper surface portion 11a, thereby causing the generation of inappropriate bubbles. If it is a form shown in FIG. 6, it will become a significantly superior thing compared with a prior art example.

  In the above embodiment, the present invention is applied to the case where the glass sheet is formed by the overflow down draw method. However, the present invention can also be applied to the case where the glass sheet is formed by, for example, the slot down draw method. However, in that case, the improvement of the downstream end portion 11 of the large-diameter pipe 10 as shown in FIGS. 6A and 6B is unnecessary.

DESCRIPTION OF SYMBOLS 1 Sheet glass manufacturing apparatus 2 Melting chamber 4 Stirrer tank 5 Connection pipe 5a Recess 6 Pot 7 Flow path area restricting part 8 Small diameter pipe 9 Large diameter pipe bending part 10 Large diameter pipe 11 Downstream end part 11a of large diameter pipe Large diameter Upper surface portion 12 at downstream end of pipe Molded body G Molten glass

Claims (8)

The molten glass that has flowed out of the melting chamber passes through the clarification chamber and flows down from the agitation tank to the pot through the connecting pipe, and then flows down the flow channel area throttle portion of the pot where the molten glass flow direction is downward. Large diameter pipe having a bent portion that is a portion that passes through the downstream side of the small-diameter pipe connected to the downstream side thereof and converts the molten glass flow direction from the downward direction to the lateral direction. In the manufacturing method of the plate glass in which the molten glass is supplied to the molded body and the molten glass is molded into a plate shape with the molded body.
On the downstream side of the periphery of the clarification chamber, at least the flow path area throttle portion of the pot is bent with a throttle angle of 30 degrees or less or smooth with a radius of curvature of 50 mm or more in a cross section including the flow path center axis. The shape of the glass is curved, the flow of the molten glass is adjusted, and the oxygen concentration in the vicinity of the flow channel peripheral surface of the molten glass flowing down the flow channel area throttle portion of the pot is suppressed from reaching a saturated state. The manufacturing method of plate glass. The plate glass manufacturing method according to claim 1, wherein a flow path peripheral surface of the pot is formed of platinum or a platinum alloy.   3. The method for producing a sheet glass according to claim 1, wherein the sheet glass is formed by an overflow down draw method or a slot down draw method.   When the molten glass flows down, the oxygen concentration in the molten glass in the vicinity of the peripheral surface of the flow channel reaches a saturated state when the molten glass flows down from the downstream end of the large-diameter pipe to the molded body. The method for producing a plate glass according to any one of claims 1 to 3, wherein the flow of the molten glass is adjusted as a flow path shape that suppresses the above.   The upper surface portion of the flow path leading from the downstream end portion of the large-diameter pipe to the molded body is inclined while rising at an angle of 30 degrees or less toward the molded body side in a vertical section including the flow path center axis, or the curvature. The method for producing a plate glass according to claim 4, wherein the glass plate is curved while smoothly rising at a radius of 30 mm or more.   6. The method for producing a plate glass according to claim 4, wherein the plate glass is formed by an overflow down draw method. The supply flow path for supplying the molten glass flowing out from the melting chamber to the molded body through the clarification chamber, the connecting pipe for communicating the stirring tank and the pot on the downstream side thereof, and the molten glass flow direction is the downward direction The pot flow area narrowing part, a small diameter pipe connected to the downstream side thereof, and a curved part that is a part that communicates with the downstream side of the small diameter pipe and changes the molten glass flow direction from the downward direction to the horizontal direction in the middle. In a plate glass manufacturing apparatus configured to form the molten glass supplied through the downstream end of the large diameter pipe into a plate shape with the molded body,
On the downstream side of the periphery of the clarification chamber, at least the flow path area throttle portion of the pot is bent with a throttle angle of 30 degrees or less or smooth with a radius of curvature of 50 mm or more in a cross section including the flow path center axis. The shape of the molten glass is adjusted so that the flow of the molten glass is adjusted , and the flow channel shape of the flow channel area restricting portion of the pot exists in the vicinity of the flow channel peripheral surface when the molten glass flows down. An apparatus for producing plate glass, characterized in that the flow of molten glass is adjusted to have a flow path shape that suppresses the oxygen concentration in the molten glass from reaching a saturated state .   When the molten glass flows down, the oxygen concentration in the molten glass in the vicinity of the peripheral surface of the flow channel reaches a saturated state when the molten glass flows down from the downstream end of the large-diameter pipe to the molded body. The apparatus for producing sheet glass according to claim 7, wherein the flow path shape is such that the flow of molten glass is adjusted.

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