TWI417256B - Manufacture of glass plates - Google Patents

Description

Glass plate manufacturing method

The present invention relates to a method of manufacturing a glass sheet using a down-draw method.

In a glass substrate used for a flat panel display such as a liquid crystal display or a plasma display (hereinafter referred to as "FPD"), a thin glass plate having a thickness of, for example, 0.5 to 0.7 mm is used. The glass substrate for FPD has a size of, for example, 300 × 400 mm in the first generation, but has a size of 2,850 × 3050 mm in the 10th generation.

In order to manufacture such a glass substrate for FPD of a larger size after the eighth generation, an overflow down draw method is most often used. The overflow down-draw method includes a step of forming a sheet glass under the molded body by overflowing the molten glass from the upper portion of the molded body in the forming furnace, and a step of slowly cooling the sheet glass in the quenching furnace. The cold furnace is cooled to a desired thickness by introducing the sheet glass into a pair of rolls, and then slowly cooling the sheet glass by reducing internal strain or heat shrinkage of the sheet glass. Thereafter, the sheet glass is cut into a specific size and stored as a glass plate on another glass plate and stored. Or transport the glass plate to the next step.

A glass plate manufactured by such molding is used as a glass substrate of a liquid crystal display in which a semiconductor element is formed on a glass surface, but in order not to deteriorate the characteristics of the semiconductor element formed on the surface of the glass due to the glass composition of the glass substrate, It is preferred to use a glass plate which does not contain an alkali metal component at all or even contains a small amount.

However, if bubbles are present in the glass plate, the defects are caused. Therefore, the glass plate in which the bubbles are present is not suitable as a glass substrate for a flat panel display. Therefore, it is required that the bubbles do not remain in the glass plate. In particular, in glass substrates for liquid crystal displays or glass substrates for organic EL (Electro Luminescent) displays, the requirements for bubbles are strict.

However, in order to suppress the deterioration of the characteristics of the semiconductor element, the alkali metal component is not contained, or even a glass plate having a small amount thereof has a problem that high temperature viscosity is higher than that of a glass plate containing an alkali metal such as a large amount of soda lime glass. Higher, the bubbles are difficult to detach from the molten glass in the manufacturing.

From the standpoint of reducing environmental load, it is required to limit the use of As ₂ O _{3 which} is previously used with higher toxicity. Therefore, in recent years, in place of As ₂ O ₃ , SnO ₂ or Fe ₂ O _{3 having} a poorer clarification function than As ₂ O ₃ has been used as a clarifying agent. Since SnO ₂ or Fe ₂ O _{3 is} a cause of devitrification or coloration of the glass, it is not possible to add a large amount to the glass in order to secure a clarifying function equivalent to As ₂ O ₃ . Therefore, bubbles become more likely to remain in the glass plate as the final product.

In order to improve the defoaming effect, a technique for producing a glass substrate in which the temperature of the alkali-free glass produced by the vitrification reaction at 1300 to 1500 ° C is raised to, for example, 1650 ° C, is disclosed. The β-OH value of the molten glass is 0.485/mm or more (Patent Document 1).

[Previous Technical Literature] [Patent Literature]

[Patent Document 1] Japanese Patent Laid-Open Publication No. 2005-97090

Here, for example, in the glass composition which does not contain an alkali metal or contains a small amount, the degree of melting of SO ₂ which can be melted in the molten glass is small, and therefore, once the bubble of SO ₂ is generated, it is finally The defects in the glass sheet of the product are easily left as bubbles.

However, in the technique described in Patent Document 1, there is a problem that the generation of SO ₂ bubbles after the clarification step cannot be sufficiently suppressed.

Accordingly, an object of the present invention is to provide a method for producing a glass sheet which can efficiently reduce bubbles remaining in a glass sheet when a glass sheet is produced.

The first aspect of the present invention is a method for producing a glass sheet.

The manufacturing method includes a melting step of melting a glass raw material containing SnO ₂ as a fining agent by at least electric heating to prepare a molten glass, and a clarifying step comprising: a defoaming treatment, after the melting step, a temperature increase rate of 2° C./min or more to raise the temperature of the molten glass to 1630° C. or higher, thereby generating bubbles in the molten glass and performing defoaming; and an absorption treatment, after the defoaming treatment, the molten glass is formed Cooling, thereby absorbing bubbles in the molten glass in the molten glass; and a forming step of forming the molten glass after the clarification step into a sheet glass.

In this case, it is preferred that the SnO ₂ of the glass plate to be produced contains 0.01 to 0.5% by mass. Further, it is preferable that the glass plate to be produced contains SnO ₂ and Fe ₂ O _{3 in combination} , and in this case, it is preferable to contain 0.01 to 0.5% by mass of SnO ₂ and 0.01 to 0.1% by mass of Fe ₂ O _{3 .} .

According to a second aspect of the invention, in the method of producing a glass sheet according to the first aspect of the invention, in the forming step, the sheet glass is formed from the molten glass by an overflow down-draw method.

According to a third aspect of the present invention, in the method for producing a glass sheet according to the first or second aspect of the present invention, in the clarifying step, the temperature of the molten glass is increased by at least a melting tank for performing the melting step and the clarification. The step of clarifying the metal tube between the grooves is performed by controlling the current flowing into the metal tube.

A method of producing a glass sheet according to any one of the first to third aspects of the present invention, wherein the viscosity of the molten glass in the temperature of 1630 ° C is 130 to 350 poise.

A method of producing a glass sheet according to any one of the first to fourth aspects of the present invention, wherein the glass sheet has a R' ₂ O content of 0 to 2.0% by mass (R' ₂ O is the total of the components contained in Li ₂ O, Na ₂ O, and K ₂ O).

A method of producing a glass sheet according to any one of the first to fifth aspects of the present invention, wherein the glass sheet contains: SiO ₂ : 50 to 70% by mass, B ₂ O ₃ : 5 ~18% by mass, Al ₂ O ₃ : 10 to 25% 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, RO: 5 to 20% by mass (wherein R is at least one selected from the group consisting of Mg, Ca, Sr, and Ba, and RO is a total of components contained in MgO, CaO, SrO, and BaO).

A method of producing a glass sheet according to any one of the first to sixth aspects of the present invention, wherein, in the absorbing treatment, the molten glass is in a range of from 1600 ° C to 1500 ° C Cooling at a cooling rate of 2 ° C / min or more.

A method of producing a glass sheet according to any one of the first to seventh aspects of the invention, wherein the clarifying step and the forming step comprise uniformly stirring the components of the molten glass. Stirring step, and In the melting step, the molten glass is supplied to the clarification step at a temperature higher than a temperature at which the melting of the molten glass is started, and In the clarification step, the molten glass is supplied to the stirring step at a temperature lower than the temperature after the absorption treatment. In the above-described forming step, the molten glass is supplied to the molten glass in a viscosity η (poise) of the molten glass to a temperature of log η = 4.3 to 5.7, and is formed into a sheet glass.

The method for producing a glass plate of the above aspect can efficiently reduce bubbles remaining in the glass plate.

Hereinafter, a method of producing the glass sheet of the present embodiment will be described.

(Overall summary of the manufacturing method of glass plate)

Fig. 1 is a view showing the steps of a method for producing a glass sheet of the embodiment.

The manufacturing method of the glass plate mainly includes a melting step (ST1) and a clarification step (ST2), homogenization step (ST3), supply step (ST4), molding step (ST5), slow cooling step (ST6), and cutting step (ST7). In addition to this, a grinding step, a grinding step, a washing step, an inspection step, a packing step, and the like are included, and a plurality of glass sheets stacked in the packing step are transported to the ordering party.

Fig. 2 is a view schematically showing a glass substrate manufacturing apparatus that performs a melting step (ST1) to a cutting step (ST7). As shown in FIG. 2, the apparatus mainly includes a melting device 200, a forming device 300, and a cutting device 400. The melting device 200 mainly includes a melting tank 201, a clarification tank 202, a stirring tank 203, and glass supply pipes 204, 205, and 206. Further, since the glass supply pipes 204 and 205 are metal pipes for flowing the molten glass MG as described below and have a clarifying function, they are also substantially clarification grooves. Hereinafter, the glass supply pipe 204 is referred to as a first clarification tank 204, the clarification tank 202 is referred to as a second clarification tank 202, and the glass supply pipe 205 is referred to as a third clarification tank 205. Further, after the melting tank 201 is connected, the first clarification tank 204, the third clarification tank 205, the glass supply pipe 206, the second clarification tank 202, and the stirring tank 203 between the respective grooves of the molding apparatus 300 include platinum or platinum. Alloy tube. The first clarification tank 204 and the third clarification tank 205 are formed in a cylindrical shape or a groove shape.

In the melting step (ST1), the glass raw material to which the SnO _{2 is} added as a clarifying agent and supplied to the melting tank 201, that is, the glass raw material containing SnO ₂ as a clarifying agent is melted by at least electric heating using an electrode, This obtains molten glass. Further, in addition to the electric heating by the electrodes, the glass frit may be melted by a flame (not shown) to obtain molten glass. In the case of performing the melting of the glass raw material by the electric heating and the flame, specifically, the glass raw material is dispersed and supplied to the liquid surface of the molten glass MG by a raw material input device (not shown). The glass raw material is heated and slowly melted by a gas phase which becomes a high temperature in the flame, and is melted in the molten glass MG. The molten glass MG is heated by electric heating. Further, foaming with oxygen may be performed in the molten glass between the melting step or the melting step and the clarifying step. Further, it is preferred that no foaming is performed at the beginning of the melting step. This is because, in the initial stage of the melting step (for example, the temperature at which the molten glass is less than 1540 ° C), when the molten glass MG is electrically heated in the melting tank 201, the resistance of the member such as the brick constituting the melting tank 201, the resistance of the glass Since it is larger, the electric current easily flows into a member such as a brick, and it is difficult to heat the electric power to the molten glass MG by the electrode.

The clarification step (ST2) is performed at least in the first clarification tank 204, the second clarification tank 202, and the third clarification tank 205. In the clarification step, by heating the molten glass MG in the first clarification tank 204, the bubbles contained in the molten glass MG containing gas components such as O ₂ , CO ₂ or SO ₂ are absorbed by SnO ₂ as a fining agent. The O ₂ produced by the reduction reaction grows and floats up to the liquid surface of the molten glass MG to be released. Further, in the clarification step, the internal pressure of the gas component in the bubble is lowered due to the decrease in the temperature of the molten glass MG, and the SnO obtained by the reduction reaction of SnO ₂ is generated due to the decrease in the temperature of the molten glass MG. By the oxidation reaction, the gas component such as O ₂ remaining in the bubbles in the molten glass MG is reabsorbed into the molten glass MG, and the bubbles disappear. The oxidation reaction and the reduction reaction using the clarifying agent are carried out by adjusting the temperature of the molten glass MG. The temperature adjustment of the molten glass MG is performed by adjusting the temperatures of the first clarification tank 204, the second clarification tank 202, and the third clarification tank 205. The temperature of each of the clarification tanks is adjusted by any one of the following heating and cooling methods, or a combination of the methods: direct electric heating to energize the tube itself, or use in the first clarification tank 204 and the second clarification tank 202. The heaters around the third clarification tank 205 are heated by heating between the respective tanks, and further cooled by air-cooled and water-cooled coolers to the first clarification tank 204, the second clarification tank 202, and the third clarification tank 205. Blowing, or water spray, etc. In addition, in FIG. 2, the tank which clarified is divided into the three parts of the 1st clarification tank 204, the 2nd clarification tank 202, and the 3rd clarification tank 205, and it can carry out further refinement.

In the adjustment of the temperature of the molten glass MG of the present embodiment, direct electric heating as one of the above methods is used. Specifically, the metal flange (not shown) provided in the first clarification tank 204 for supplying the molten glass MG to the second clarification tank 202 is made of metal (not shown) provided in the second clarification tank 202. A current flows between the flanges (arrows in FIG. 3), and a metal flange (not shown) provided in the second clarification tank 202 is provided downstream of the molten glass MG with respect to the metal flange. An electric current (arrow in FIG. 3) flows between metal flanges (not shown) in the second clarification tank 202 on the side, whereby the temperature of the molten glass MG is adjusted. In the present embodiment, the first clarification tank 204 and the second clarification tank 202 are electrically heated by flowing a constant current in the first region between the metal flanges and the second region between the metal flanges. Therefore, the temperature of the molten glass MG is adjusted, but the electric heating is not limited to the temperature adjustment by the electric heating of the two regions, and the electric heating may be performed in one region or the electric heating may be performed in three or more regions. Thereby, the temperature adjustment of the molten glass MG is performed.

In the homogenization step (ST3), the molten glass MG in the stirring tank 203 supplied through the third clarification tank 205 is stirred by the agitator 203a, whereby the glass component is homogenized. Two or more stirring tanks 203 may be provided.

In the supply step (ST4), the molten glass is supplied to the molding apparatus 300 through the glass supply tube 206.

In the molding apparatus 300, a molding step (ST5) and a slow cooling step (ST6) are performed.

In the molding step (ST5), the molten glass is formed into a sheet glass G, and the flow direction of the sheet glass G is produced. In the present embodiment, an overflow down-draw method using the molded body 310 described below is used. In the slow cooling step (ST6), the sheet glass G which has been formed to flow is cooled so as not to generate internal strain.

In the cutting step (ST7), in the cutting device 400, the sheet glass G supplied from the forming device 300 is cut to a specific length, thereby obtaining a glass plate. The cut glass sheet is further cut into a specific size to produce a glass sheet of a target size. Thereafter, the end surface of the glass is ground, polished, and cleaned with a glass plate. Further, after checking for defects such as bubbles or streaks, the glass plate of the inspected product is packaged as a final product.

(clarification step)

Fig. 3 is a view mainly showing the configuration of a device for performing a clarification step. The clarification step includes a defoaming step and an absorbing step. In the defoaming step, the molten glass MG is heated to 1630 ° C or higher, and the SnO ₂ as a clarifying agent releases oxygen, and the oxygen is absorbed into the existing bubble B of the molten glass MG to cause the bubble of the existing bubble B. The diameter is enlarged. In this way, the expansion of the bubble diameter caused by the increase in the internal pressure of the gas component in the bubble B due to the increase in the temperature of the molten glass MG is synergistic with the decrease in the viscosity of the molten glass MG due to the increase in the temperature of the molten glass MG. The effect is that the floating speed of the bubble B is increased to promote defoaming.

In the absorption treatment, by lowering the temperature of the molten glass MG as opposed to the defoaming treatment, the oxygen in the bubble B in the molten glass MG is again absorbed into the molten glass MG, and the temperature by the molten glass MG The synergistic effect of lowering the internal pressure of the gas component in the bubble B is reduced, the bubble diameter is reduced, and the bubble B is eliminated in the molten glass MG.

Further, in the defoaming step, the temperature of the molten glass MG is raised to 1630 ° C or higher at a temperature increase rate of 2 ° C / min or more. The temperature increase rate of 2 ° C / min or more means that the temperature of the molten glass MG reaches the clarification temperature (for example, 1630 to 1700 ° C) from the temperature of the molten glass MG (for example, 1580 ° C and in the range of 1560 to 1620 ° C) after the melting step. The average temperature increase rate of the molten glass MG in the range of 2 ° C / min or more. For example, when the temperature of the molten glass MG is 1630 ° C or higher in the first clarification tank 204, the temperature increase rate is expressed from the outlet of the melting tank 200 to the molten glass MG in the connected first clarification tank 204. The average rate of temperature increase from inflow to outflow.

The first clarification tank 204, the second clarification tank 202, and the third clarification tank 205 are means for performing defoaming of the molten glass MG and absorption of the bubbles B by applying the above-described temperature history to the molten glass MG. Therefore, there is a temperature adjustment function capable of heating or cooling the first clarification tank 204, the second clarification tank 202, and the third clarification tank 205 to a target temperature.

The temperature adjustment of each of the first clarification tank 204, the second clarification tank 202, and the third clarification tank 205 is performed by any one of the following methods or a combination of the methods: Directly energizing and heating the respective clarification tanks themselves, or heating them by clarification tanks of heaters (not shown) disposed around the respective tanks, and further cooling them by air-cooling and water-cooling coolers to each clarification tank Blowing, water spray, etc.

According to Figure 3, the clarification is explained in more detail.

The liquid molten glass MG which is melted in the melting tank 201 and contains a large number of bubbles B formed by the decomposition reaction of the glass raw material is introduced into the first clarification tank 204.

In the first clarification tank 204, the molten glass MG is heated to 1630 ° C or higher by heating of the platinum or platinum alloy tube as the main body of the first clarification tank 204, and a large amount of the clarifying agent is promoted by a reduction reaction. Oxygen is released into the molten glass MG. The bubble B inherent in the molten glass MG is expanded by the bubble diameter of the effect of increasing the pressure of the gas component in the bubble B due to the temperature rise of the molten glass MG, and the oxygen released by the reduction reaction of the clarifying agent The bubble B is diffused and enters the bubble B, and the bubble diameter of the bubble B inherent to the synergistic effect is enlarged. At this time, the molten glass MG is heated to a temperature of 1630 ° C or higher at a temperature increase rate of 2 ° C /min or more. Further, the first clarification tank 204 has a smaller cross section than the second clarification tank 202, and the upper cleavage space does not have a gas phase environment space unlike the second clarification tank 202. Therefore, in other words, the first clarification tank 204 is melted. Since the glass MG is filled and flows through the entire inner cross section of the first clarification tank 204, the temperature of the molten glass MG can be efficiently increased as compared with the second clarification tank 202. In other words, in the first clarification tank 204, the temperature of the molten glass MG is raised to 1630 ° C or higher, and the temperature of the molten glass MG is raised to 1630 ° C or higher in the second clarification tank 202. Since the heating temperature of the cleaning tank 202 is suppressed, it is preferable from the viewpoint of suppressing volatilization or melt loss of the platinum alloy constituting the second clarification tank 202.

Then, the molten glass MG is introduced into the second clarification tank 202.

The second clarification tank 202 is different from the first clarification tank 204 in that the upper open space inside the second clarification tank 202 is an environmental space in the gas phase, and the bubbles B in the molten glass MG can be floated to the liquid surface of the molten glass MG and released. To the outside of the molten glass MG.

In the second clarification tank 202, the molten glass MG is maintained at a high temperature of 1630 ° C or higher by heating of the platinum or platinum alloy tube as the main body of the second clarification tank 202, and the bubble B in the molten glass MG is second. The clarification tank 202 floats upward to break the surface of the molten glass MG, whereby the molten glass MG is defoamed. In particular, when the molten glass MG is heated to 1630 ° C or higher (for example, 1630 to 1700 ° C), the SnO ₂ accelerates the reduction reaction. In this case, for example, in the case of producing a glass plate for a flat panel display such as a liquid crystal display, the viscosity of the glass is changed to a viscosity (200 to 800 poise) suitable for floating and defoaming of the bubble B due to an increase in the temperature of the molten glass MG.

Here, the gas component which is bubbled in the upper portion above the second clarification tank 202 and released is released from the gas discharge port (not shown) to the outside of the second clarification tank 202. In the second clarification tank 202, the molten glass MG in which the bubble B having a large bubble diameter with a high floating speed is removed by the floating and defoaming of the bubble B is introduced into the third clarification tank 205.

In the present embodiment, for example, as shown in FIG. 3, the second clarification tank 202 to the third clarification tank 205 may be controlled by two along the length direction of the platinum or platinum alloy tube constituting the main body. The temperature of the molten glass MG is raised by the current flowing in each of the different regions. By controlling The temperature of the molten glass MG is raised by a current flowing in each of three or more different regions extending in the longitudinal direction of the platinum or platinum alloy tube which is the body of the clarification tank.

As described above, the temperature rise of the molten glass MG is preferably performed by controlling the current flowing in at least two regions different from each other in the clarification tank, and the defoaming treatment is preferably carried out efficiently.

In the third clarification tank 205, the molten glass MG is cooled by cooling the platinum or platinum alloy tube as the main body of the third clarification tank 205 or by suppressing the heating of the third clarification tank 205. Since the temperature of the molten glass MG is lowered by the cooling, the floating and defoaming of the bubbles B are not performed, and the pressure of the gas component in the small remaining bubbles B is lowered, and the bubble diameter is gradually reduced. Further, when the temperature of the molten glass MG is 1600 ° C or lower, one part of SnO obtained by the reduction reaction of SnO ₂ in the defoaming treatment absorbs oxygen, and is restored to SnO ₂ . Therefore, oxygen which is a gas component in the bubble B is reabsorbed into the molten glass MG, and the bubble B becomes smaller and smaller, and is absorbed into the molten glass MG and eventually disappears. At this time, the molten glass MG is cooled at a temperature of 1600 ° C to 1500 ° C at an average temperature of 2 ° C / min or more, more preferably 3 ° C / min or more. Further, since the third clarification tank 205 has a smaller cross section than the second clarification tank 202, the molten glass MG can be cooled more efficiently than the second clarification tank 202. In other words, it is preferable that the temperature of the molten glass MG is cooled in the third clarification tank 205 to accelerate the temperature drop rate as compared with the temperature at which the molten glass MG is cooled in the second clarification tank 202.

In the example shown in FIG. 3, the clarification tank for performing the clarification step is divided into three parts of the first clarification tank 204, the second clarification tank 202, and the third clarification tank 205, of course. The clarification tank can be further refined. The refining and clarifying tank can perform temperature adjustment of the molten glass MG in more detail. In particular, it is advantageous to refine the clarification tank in the case where the type or the amount of melting of the molten glass MG is changed, and it is easier to adjust the temperature.

In the above description, the molten glass MG is heated to 1630 ° C in the first clarification tank 204, and the bubble B of the molten glass MG is floated and defoamed in the second clarification tank 202. In the clarification tank 205, the molten glass MG is described as being divided into the clarification tank so that the function of the bubble B is absorbed by the cooling of the molten glass MG. However, the function may not be completely divided into the clarification tank. The portion to the middle of the longitudinal direction of the second clarification tank 202 may be configured to increase the temperature of the molten glass MG, or may be used to make the molten glass halfway between the longitudinal direction of the second clarification tank 202 and the third clarification tank 205. The MG's cooling begins with a part of the way.

In the present embodiment, the surface temperature of the first clarification tank 204, the second clarification tank 202, and the third clarification tank 205, that is, the surface temperature of the outer side of the clarification tank to which the molten glass MG does not flow is measured, and temperature control is performed. Manage the heating rate and cooling rate of the molten glass MG. The surface temperature of the first clarification tank 204, the second clarification tank 202, and the third clarification tank 205 can be calculated in advance by the computer simulation using the flow rate and temperature conditions of the molten glass MG supplied to the clarification tank. The relationship between the average temperature of the molten glass MG flowing in the groove 204, the second clarification tank 202, and the third clarification tank 205 (the average value of the temperature of the molten glass MG having a temperature distribution in the clarification tank). Therefore, the temperature increase rate and the temperature decrease rate can be calculated from the measured surface temperature on the outer side of the clarification tank, and the temperature increase rate and the temperature decrease rate can be managed. Again, melting The flow rate of the molten glass MG can be calculated from the volume of each device and the amount of molten glass MG per unit time flowing into the forming device 300. Further, the temperature of the molten glass MG can be calculated from the viscosity and thermal conductivity of the glass.

After the defoaming treatment, the temperature of the molten glass MG is lowered in a temperature range of 1600 ° C to 1500 ° C at a temperature decreasing rate of, for example, 2 ° C / min or more, so as to remain in the glass as a final product as described below. The number of bubbles per unit mass in the panel is reduced. The term "bubble" as used herein means a bubble having a volume equal to or larger than the volume of a predetermined bubble, for example, a volume of a bubble having a diameter of 20 μm.

Further, the faster the temperature drop rate is, the lower the number of bubbles remaining in the glass sheet can be reduced, but the reduction effect becomes smaller as the temperature drop rate increases. The above cooling rate is preferably 3 ° C / min or more. Further, the upper limit of the above-described cooling rate is not particularly set. However, in the case of manufacturing a glass plate industrially, the upper limit is 50 ° C / min for the following reasons.

In other words, when the temperature drop rate of the molten glass MG is too fast, the oxygen in the bubble B of the molten glass MG is prevented from being reabsorbed to the molten glass MG, and as a result, the bubble B itself in the molten glass MG may not be reduced. Moreover, the thermal conductivity of the glass is as small as 20 to 50 W/(m.K) even at high temperatures. Therefore, the rapid cooling of the molten glass MG can only be performed from the third place as long as it does not take special measures. When the outer side of the clarification tank 205 is cooled, the molten glass MG near the outer surface of the third clarification tank 205 is cooled, and the molten glass MG at the center of the third clarification tank 205 is maintained at a high temperature. In other words, in the third clarification tank 205, the temperature difference between the outer surface portion and the center portion of the molten glass MG is increased. In this case, production The problem of precipitation of crystals from the molten glass MG of the outer surface portion. In the third clarification tank 205, when the molten glass MG is stirred while the temperature difference between the surface portion and the center portion of the molten glass MG is increased, the glass having a large temperature difference is mixed. In addition to the generation of the bubble B, the composition of the glass tends to hinder the homogeneity. Further, in order to increase the temperature drop rate of the molten glass MG, it is necessary to increase the heat dissipation from the third clarification tank 205. Therefore, it is necessary to make the thickness of the support member such as the support brick supporting the body of the platinum or platinum alloy tube of the third clarification tank 205 thin. . However, only the thickness of the support member is made thin, and the strength of the device is lowered. Therefore, in the case of manufacturing a glass plate industrially, it is not appropriate to accelerate the cooling rate of the molten glass MG only to cause the above problems.

From the above, it is understood that the upper limit of the temperature drop rate of the molten glass MG from 1600 ° C to 1500 ° C is preferably 50 ° C / min, more preferably 35 ° C / min. That is, in the present embodiment, the temperature drop rate is preferably 2 ° C / min to 50 ° C / min, more preferably 2.5 ° C / min to 50 ° C / min, and still more preferably 3 ° C / min ~ 35 ° C / min. .

(forming step)

Fig. 4 is a view mainly showing the configuration of a device for performing a forming step and a cutting step. The forming apparatus 300 includes a forming furnace 340 and a quenching furnace 350.

The forming furnace 340 and the quenching furnace 350 are surrounded by a furnace wall (not shown) including a refractory such as refractory brick. The forming furnace 340 is disposed vertically above the quenching furnace 350. The molded body 310, the environmental spacing member 320, the cooling roller 330, the cooling unit 335, and the conveying rollers 350a to 350d are provided in the furnace internal space surrounded by the furnace walls of the forming furnace 340 and the quenching furnace 350.

In the molded body 310, the molten glass MG that has flowed in from the melting device 200 through the glass supply pipe 206 shown in FIG. 2 is formed into a sheet glass G. The molten glass supplied to the molded body 310 becomes a temperature at which the viscosity η (poise) becomes log η = 4.3 to 5.7. The temperature of the molten glass MG differs depending on the type of glass, and is, for example, 1200 to 1300 ° C in the case of glass for liquid crystal display. Thereby, the flow direction of the plate glass G under the vertical direction is produced in the molding apparatus 300. In the formed body 310, an elongated structure composed of refractory bricks or the like is formed into a wedge shape as shown in FIG. A supply groove 312 as a flow path for guiding the molten glass is provided on the upper portion of the molded body 310. The supply groove 312 is connected to the third clarification tank 205 in the supply port provided in the molding apparatus 300, and the molten glass MG flowing in through the third clarification tank 205 flows along the supply groove 312. The supply groove 312 is configured such that the molten glass MG overflows from the supply groove 312.

The molten glass MG overflowing from the supply groove 312 flows down along the vertical wall surface and the inclined wall surface of the side walls on both sides of the molded body 310. The molten glass flowing through the side walls merges at the lower end portion 313 of the formed body 310 shown in Fig. 4 to form one sheet glass G.

(glass composition)

The glass plate produced by the method for producing a glass plate of the present embodiment is preferably used for a glass substrate for a flat panel display. For example, it has substantially no Li ₂ O, Na ₂ O, and K ₂ O, or contains at least one of Li ₂ O, Na ₂ O, and K ₂ O, Li ₂ O, Na ₂ O. In the case where the total amount of the components contained in the K ₂ O is also 2% by mass or less, the effect of the embodiment can be effectively exhibited. The glass composition is preferably exemplified below.

(a) SiO ₂ : 50 to 70% by mass, (b) B ₂ O ₃ : 5 to 18% by mass, (c) Al ₂ O ₃ : 10 to 25% by mass, (d) MgO: 0 to 10% by mass (e) CaO: 0 to 20% by mass, (f) SrO: 0 to 20% by mass, (g) BaO: 0 to 10% by mass, (h) RO: 5 to 20% by mass (where R is selected from At least one of Mg, Ca, Sr, and Ba, and a total of components contained in the RO-based MgO, CaO, SrO, and BaO, and (i) R' ₂ O: more than 0.1% by mass and not more than 2.0% by mass. (wherein R' is selected from at least one of Li, Na, and K, and R' ₂ O is a total of components contained in Li ₂ O, Na ₂ O, and K ₂ O), and (j) is selected from The total amount of the metal oxides of at least one of SnO ₂ , Fe ₂ O _{3 ,} and cerium oxide is 0.05 to 1.5% by mass.

Further, the compositions of the above (i) and (j) are not essential, but may have the composition of (i) and (j). In the above glass, substantially no As ₂ O ₃ and PbO are contained, and SnO ₂ is contained. Further, from the viewpoint of environmental problems, it is preferred that substantially no Sb ₂ O ₃ is contained.

Further, the content of R' ₂ O of (i) may be 0% by mass.

In addition to the above components, the glass plate of the present embodiment may contain various other oxides in order to adjust various physical properties, melting, clarification, and molding properties of the glass. Examples of such other oxides are not limited to the following, but examples thereof include 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 .

Further, in the present embodiment, SnO ₂ is a component which tends to devitrify the glass. Therefore, in order to improve the clarity and prevent devitrification, the content is preferably 0.01 to 0.5% by mass, more preferably 0.05 to 0.3% by mass. % is further preferably 0.1 to 0.3% by mass.

Fe ₂ O ₃ is a component that enhances infrared absorption of glass, and defoaming is promoted by containing Fe ₂ O ₃ . However, Fe ₂ O ₃ is a component that lowers the transmittance of glass. Therefore, when the content of Fe ₂ O ₃ is too large, it becomes unsuitable for a glass substrate for a display. As seen from the above, the case containing the Fe ₂ O ₃ in the metal oxide on the improvement of clarification and to suppress decrease in transmittance of the glass viewpoint of the Fe ₂ O ₃ content of preferably 0.01 to 0.1 The mass % is more preferably 0.01 to 0.08 mass%. Further, in terms of improving the clarification property and completing the defoaming step in a shorter period of time, and also suppressing the generation of the SO ₂ bubble in the absorption step, it is preferred to combine 0.01 to 0.5% by mass of SnO ₂ and 0.01 to 0.1 mass. % of Fe ₂ O ₃ is used.

Further, the R' ₂ O of the above (i) is characterized in that the characteristics of the TFT (Thin Film Transistor) are deteriorated by elution from the glass, and the thermal expansion coefficient of the glass is increased to break the substrate during the heat treatment. When it is used as a glass substrate for a liquid crystal display or a glass substrate for an organic EL display, it is preferable that it is not substantially contained. However, since the glass contains a certain amount of the above-mentioned components, the thermal expansion of the glass can be suppressed to a certain range without deteriorating the characteristics of the TFT, and the alkalinity of the glass can be increased, and the metal having a valence change can be obtained. The oxidation becomes easy and clarifies. Further, R' ₂ O lowers the specific resistance of the glass and improves the meltability. Therefore, R' ₂ O is preferably 0 to 2.0% by mass, more preferably more than 0.1% by mass and 1.0% by mass or less, and still more preferably 0.2 to 0.5% by mass. Further, preferably not contain Li ₂ O, Na ₂ O, and containing the above components in the most difficult since the dissolution of the glass of the TFT characteristics deterioration arising K ₂ O. The content of K ₂ O is preferably 0 to 2.0% by mass, more preferably 0.1 to 1.0% by mass, still more preferably 0.2 to 0.5% by mass.

In order to obtain characteristics of a glass substrate which is preferably used for a liquid crystal display or an organic EL display, the glass plate of the present embodiment has a higher viscosity in a clarification temperature of the molten glass MG than a glass plate containing a large amount of alkali, and the like. Therefore, the floating speed of the bubbles in the defoaming treatment tends to be slow. In particular, low temperature polycrystalline germanium is formed on the surface of the glass. Since the glass substrate of the TFT requires a high strain point, the high-temperature viscosity is liable to become high, and the viscosity in the clarification temperature of the molten glass MG is further increased. Therefore, for example, in the case of producing a glass having a strain point of 680 ° C or higher, particularly a glass having a strain point of 690 ° C or higher, the floating speed of the bubbles in the defoaming treatment is likely to be further slowed down. In the case where the glass plate of the present embodiment is a glass substrate such as a liquid crystal display or an organic EL display, for example, the viscosity of the molten glass MG at a temperature of 1630 ° C is preferably 130 to 350 poise. Further, in the case where the glass viscosity of the glass constituting the glass substrate is 1550 ° C to 1680 ° C when the glass temperature is log η = 2.5, the present embodiment is preferable, and the effect of the embodiment is in the range of 1570 ° C to 1680 ° C. It becomes remarkable, and the effect of this embodiment becomes more remarkable in the range of 1590 ° C - 1680 °C.

(temperature history of molten glass)

Fig. 5 is a view showing an example of the temperature history of the melting step to the forming step in the embodiment.

In order to obtain a target chemical composition, the glass raw materials used in the production of the glass sheet of the present embodiment are weighed and mixed well to form a glass raw material. At this time, a specific amount of SnO ₂ was added as a clarifying agent to the glass raw material. The glass raw material to which SnO ₂ is added, which has been produced in this manner, is placed in the melting tank 201 and melted by at least electric heating to produce molten glass MG. The glass raw material charged into the melting tank 201 is decomposed when it reaches the decomposition temperature of its components, and becomes molten glass MG by a vitrification reaction. The molten glass MG gradually increases in temperature while flowing through the melting tank 201, and advances toward the first clarification tank 204 (glass supply pipe 204) from the vicinity of the bottom of the melting tank 201.

Therefore, in the melting tank 201, the temperature of the molten glass MG has a temperature history which rises gently from the temperature T1 at the time of input of the glass raw material to the temperature T3 at the time of entering the first clarification tank 204 (glass supply pipe 204). Furthermore, in FIG. 5, T1 < T2 < T3, but it may be T2 = T3 or T2 > T3, and at least T1 < T3.

Platinum or platinum alloy tube of the first clarification tank 204 by a constant current flowing between a metal flange (not shown) of the first clarification tank 204 and a metal flange (not shown) of the second clarification tank 202 The electric heating is performed, and the second clarifying tank is flowed between the metal flange (not shown) of the second clarification tank 202 and the other metal flange of the second clarification tank 202 (not shown). The platinum or platinum alloy of 202 is electrically heated, and the molten glass MG entering the first clarification tank 204 is rapidly released from the temperature T3 to the SnO ₂ by a temperature T4 (for example, 1630 ° C or higher, more preferably 1630 to 1700 ° C). Further, it is preferably 1650 to 1700 ° C) and is heated at a temperature increase rate of 2 ° C /min or more. When the temperature increase rate is 2° C./min or more, as described below, when the temperature increase rate is 2° C./min or more, the amount of O ₂ gas released is rapidly increased. Further, the larger the difference between the temperature T3 and the temperature T4, the larger the amount of O ₂ released by the SnO ₂ in the molten glass MG, and the more the defoaming is promoted. Therefore, it is preferable that the temperature T4 is higher than the temperature T3 by, for example, about 50 °C.

Further, the molten glass MG entering the second clarification tank 202 is maintained at a temperature T4 to a temperature T5 substantially equal to the temperature T4. Further, the temperature adjustment in the temperature T3 to the temperature T5 is a method in which the respective clarification tanks are electrically heated by the present embodiment, but the method is not limited thereto. For example, the temperature adjustment may be performed by heating between heaters (not shown) disposed around the respective clarification tanks.

At this time, the reduction reaction of SnO ₂ as a fining agent is promoted by heating the molten glass MG to 1630 ° C or higher. Thereby, a large amount of oxygen is released into the molten glass MG. The bubble B inherent in the molten glass MG is expanded by the effect of increasing the pressure of the gas component in the bubble B due to the temperature rise of the molten glass MG, and is released by the reduction reaction of the clarifying agent. The oxygen diffuses and enters into the bubble B, and the bubble diameter is enlarged by the synergistic effect.

The bubble B after the bubble diameter is enlarged follows the Stokes law, and the floating speed of the bubble B is increased, thereby promoting the floating and breaking of the bubble B.

In the second clarification tank 202, the molten glass MG is also maintained at a high temperature of 1630 ° C or higher, and therefore, the bubbles B in the molten glass MG float to the molten glass. The surface of the liquid of the glass MG is broken on the surface of the liquid, whereby defoaming of the molten glass MG is performed.

The defoaming treatment is carried out in FIG. 5, and the temperature of the molten glass MG is raised from the temperature T3 to the temperature T4, and then maintained at a temperature T5 substantially the same as the temperature T4. In Fig. 5, T4 and T5 are substantially the same, but may be T4 < T5 or T4 > T5.

Further, although the example in which the temperature of the molten glass MG reaches the temperature T4 in the first clarification tank 204 has been described, the inside of the second clarification tank 202 may be used.

Moreover, it is preferable that the first maximum temperature of the molten glass when the molten glass MG flows through the first clarification tank 204 is equal to or higher than the second highest temperature of the molten glass MG when flowing through the second clarification tank 202. . Therefore, when the molten glass moves from the first clarification tank 204 to the second clarification tank 202, the temperature of the molten glass MG is relatively high and is maintained at a temperature higher than the temperature at which the clarifying agent generates a reduction reaction. Therefore, the second clarification tank 202 does not need to be used. It is used to further heat the molten glass. Therefore, the heating temperature of the second clarification tank 202 can be suppressed lower than before. Therefore, it is possible to suppress the volatilization of platinum from the second clarification tank 202 containing platinum or a platinum alloy, and it is possible to produce impurities such as platinum crystals adhered to the inner wall surface of the second clarification tank 202 due to the volatilization of platinum, which are mixed into the molten glass MG. A defect, that is, a glass plate resulting from less defects of the above impurities. When the molten glass MG flows through the first clarification tank 204, the temperature of the molten glass MG preferably reaches the first maximum temperature. In this case, the heating temperature of the second clarification tank 202 is lower than the case where the molten glass reaches the first highest temperature and the second highest temperature at the connection position between the first clarification tank 204 and the second clarification tank 202. , it is easier to inhibit the platinum from the second clarification tank 202 containing platinum or platinum alloy hair.

Then, since the molten glass MG entering the third clarification tank 205 from the second clarification tank 202 absorbs the remaining bubbles B, it is cooled from the temperature T5 to the temperature T7 via the temperature T6 (for example, 1600 ° C) (the temperature suitable for the stirring step) And depending on the type of glass nitrate and the type of stirring device, for example, 1500 ° C).

When the temperature of the molten glass MG is lowered, the floating and defoaming of the bubbles B are not generated, and the pressure of the gas component remaining in the small bubbles in the molten glass MG is also lowered, and the bubble diameter is gradually reduced. Further, when the temperature of the molten glass MG is 1600 ° C or lower, oxygen is partially absorbed by one of SnO (which is obtained by reduction of SnO ₂ ), and is returned to SnO ₂ . Therefore, the oxygen in the remaining bubbles B in the molten glass MG is reabsorbed into the molten glass MG, and the vesicles are further reduced. The molten glass MG absorbs the vesicles, and the vesicles eventually disappear.

The treatment of absorbing O _{2 as} a gas component in the bubble B by the oxidation reaction of SnO is an absorption treatment, and is performed while the temperature T5 is lowered to a temperature T7 via the temperature T6. In FIG. 5, the temperature drop rate of the temperature T5~T6 is faster than the temperature T6~T7, but the temperature drop rate of the temperature T5~T6 may be slower than the temperature T6~T7, and may be equal. Preferably, at least during the absorption treatment, the temperature of the molten glass MG is lowered in a temperature range of 1600 ° C to 1500 ° C at a temperature drop rate of 2 ° C / min or more. However, the molten glass MG is increased at a higher temperature of the cooling rate during the state, and the following early suppress the diffusion of SO ₂ of the aspect of the terms to be absorbed within the bubble B ₂ SO reduction, the temperature is preferably The cooling rate of T5~T6 is faster than the temperature drop of temperature T6~T7. That is, in the absorption treatment, it is preferred that the molten glass MG is in a temperature range of 1500 ° C or lower (specifically, from 1500 ° C to the range of the molten glass temperature supplied to the forming step, for example, 1500 ° C to 1300 ° C). The cooling rate is slower than the temperature drop in the temperature range of 1600 ° C to 1500 ° C.

Further, by making the temperature drop rate of the temperature T6 to T7 slower than the temperature drop rate of the temperature T5 to T6, the SO ₂ absorbed into the bubble B can be reduced, and the third portion of the molten glass MG flowing into the stirring tank 203 can be reduced. The temperature difference between the outer side surface portion and the center portion in the clarification tank 205 (glass supply tube 205) becomes small.

Further, in terms of improvement in productivity of the glass sheet and reduction in equipment cost, in the absorption treatment, it is preferred that the molten glass MG is 1500 ° C or lower (specifically, from 1500 ° C to supply to the forming step). The temperature range in the range of the molten glass temperature, for example, 1500 ° C to 1300 ° C, is faster than the temperature drop in the temperature range of 1600 ° C to 1500 ° C. Further, in the case of performing temperature control of the molten glass MG, it is preferable to provide a flow rate adjusting device for adjusting the amount of the molten glass MG supplied to the molding step.

Further, the SO ₂ absorbed into the bubble B can be reduced, and the amount of the molten glass MG supplied to the forming step can be adjusted by the temperature management of the molten glass MG in the glass supply pipe 206. Preferably, the temperature drop rate of the molten glass MG in a temperature range of 1500 ° C or lower is slower than the temperature drop rate in a temperature range of 1600 ° C to 1500 ° C. Thereby, it is not necessary to process the glass supply pipe 206 into a special shape, or to provide a flow rate adjustment device other than the glass supply pipe 206, and the amount of the molten glass MG which flows into a shaping|molding process can be adjusted easily. Further, the temperature difference between the outer surface portion and the center portion of the glass supply tube 206 flowing into the molten glass MG of the molding step can be made small.

After the above-described absorption treatment or during the absorption treatment, the molten glass MG enters the stirring tank 203. The agitation vessel 203 reduces the composition unevenness in the molten glass MG to homogenize the molten glass MG. Further, in the stirring tank 203, the above-described absorption treatment may be continued. Thereafter, the molten glass MG is cooled until it becomes a temperature T8 suitable for molding in the forming step, for example, 1200 to 1300 °C.

As described above, a stirring step of uniformly agitating the components of the molten glass MG is included between the clarification step and the forming step. The term between the clarification step and the forming step means that the timing of the start of the stirring step is between the timing at which the clarification step starts and the timing at which the forming step starts. The stirring step of the molten glass MG may be started halfway through the clarification step or after the clarification step. Further, in Fig. 1, the clarification step (ST2) and the homogenization step (ST3) are expressed in the order of the start timing. In the melting step, the molten glass MG is supplied to the clarification step at a temperature T3 higher than the temperature T1 at the start of melting of the molten glass MG. In the clarification step, the molten glass MG is supplied to the stirring step at a temperature lower than the temperature T7. In the stirring step, the molten glass MG is supplied to the forming step at a temperature at which the viscosity η (poise) becomes log η = 4.3 to 5.7. In the molding step, the molten glass MG is formed into a sheet glass in a state where the temperature of the molten glass MG is, for example, 1200 to 1300 °C. Further, the liquid phase viscosity of the glass plate is preferably log η = 4 or more, and the liquidus temperature of the glass plate is preferably 1050 ° C to 1270 ° C. By setting such a liquid phase viscosity and a liquidus temperature, an overflow down-draw method can be applied as a forming method.

Fig. 6 is a graph showing the relationship between the amount of emission of O ₂ contained in the molten glass and the temperature increase rate when the defoaming treatment is performed. The rate of temperature rise is the average speed in the temperature range from 1550 ° C to 1640 ° C. The glass plate used for the measurement has the same glass composition as the glass substrate for liquid crystal display having a small content of alkali metal, and uses SnO ₂ as a clarifying agent. Specifically, the measurement results shown in FIG. 6 were obtained by using a glass substrate for a liquid crystal display having the glass composition shown below.

SiO ₂ : 60% by mass

Al ₂ O ₃ : 19.5% by mass

B ₂ O ₃ : 10% by mass

CaO: 5.3% by mass

SrO: 5 mass%

SnO ₂ : 0.2% by mass

As can be seen from Fig. 6, in order to increase the discharge amount of O ₂ , the temperature increase rate of the molten glass MG can be 2 ° C / min or more. Further, in the measurement result of FIG. 6, the CO ₂ seals the gas (CO ₂ ) in the cavity by laminating another glass substrate on the glass substrate on which the cavity is formed, and heats each of the glass substrates in this state. This is fused, whereby it exists as a bubble in the molten glass MG.

In the present embodiment, there is no substantial upper limit of the temperature increase rate, and for example, it may be 10 ° C / min or less. Since the thermal conductivity of the glass is small, in order to increase the temperature increase rate, it is necessary to increase the heat transfer area. In order to increase the heat transfer area, the inner diameter of the first clarification tank 204 or the second clarification tank 202 as a metal pipe is reduced, and the first clarification tank 204 is formed long in the longitudinal direction. Or the second clarification tank 202 or the like. Moreover, in order to increase the heat transfer area, the temperature of the first clarification tank 204 or the second clarification tank 202 may be raised to a temperature significantly higher than the temperature of the molten glass MG. However, when the inner diameter of the first clarification tank 204 or the second clarification tank 202 is reduced, and the first clarification tank 204 or the second clarification tank 202 is formed in the longitudinal direction, the glass plate manufacturing apparatus is enlarged. Not good. When the temperature of the first clarification tank 204 or the second clarification tank 202 is raised to a temperature which is significantly higher than the temperature of the molten glass MG, the glass sheet manufacturing apparatus is damaged due to high temperature. Therefore, the upper limit of the substantial temperature rise rate is preferably 10 ° C / min or less. From the above, it is understood that the temperature increase rate is preferably from 2 ° C / min to 10 ° C / min, more preferably from 3 ° C / min to 8 ° C / min, and still more preferably from 3 ° C to 6.5 ° C / min. Within this range, the defoaming treatment can be efficiently performed, and the bubbles remaining in the glass plate can be efficiently reduced.

Further, as described above, in the bubble absorption treatment performed after the defoaming treatment, the molten glass MG is cooled at a temperature decreasing rate of 2 ° C / min or more in a temperature range of 1600 ° C to 1500 ° C. This is done for the reasons described below.

When the molten glass MG is heated from the temperature T3 to the temperature T4 and the temperature T5, the SnO ₂ releases oxygen and the molten glass MG is heated to a temperature of 1600 to 1630 ° C or more as the reduction temperature, so that bubbles in the molten glass MG are promoted. other than the release of absorbed oxygen SnO _2, and promote a high temperature becomes dissolved in the molten glass within the O MG _2, CO _2, SO ₂ diffusion of the dissolved O in the molten glass within the MG _2, CO _2, SO ₂ was also The above bubble B is absorbed. Further, the degree of melting of the gas component in the molten glass MG varies depending on the glass component. However, in the case of SO ₂ , the degree of melting in the glass having a large content of the alkali metal is high, but the alkali metal is not contained. Even if it contains a glass plate used for the glass substrate for liquid crystal displays of this embodiment, it is melt|dissolved in the molten glass MG, and the melting degree is low. In the glass plate used for the glass substrate for liquid crystal display, the S (sulfur) component is not artificially added as a glass raw material, but the impurity in the raw material or the combustion gas used in the melting tank 201 (natural gas, In a city gas, a propane gas, or the like, it is contained in a trace amount as an impurity. Therefore, the S component contained as the impurities is oxidized to become SO ₂ and diffused into the bubbles B contained in the molten glass MG. Since SO _{2 is} hard to be reabsorbed, it remains as bubbles B. This phenomenon occurs very significantly compared to the previous use of As ₂ O ₃ as a fining agent.

In the case where SnO _{2 is} used as the glass composition of the clarifying agent, the holding time in the high temperature of the molten glass MG becomes longer, and the SO _{2 is} promoted to diffuse into the bubble B inherent in the molten glass MG. This is considered to be because the diffusion rate in the molten glass MG of SO ₂ is increased at a high temperature, and it is easy to enter the bubble B.

In addition, when the temperature of the molten glass MG is maintained at a high temperature of 1630 ° C or higher for a long period of time, the molten glass MG is excessively reduced, and when the molten glass MG is cooled, the following SO ₂ bubbles are likely to be generated. On the other hand, if the time kept at 1630 ° C or more is too short, defoaming in the defoaming step becomes insufficient. Therefore, the time for maintaining the temperature of the molten glass MG at 1630 ° C or higher is preferably 15 minutes to 90 minutes, more preferably 30 minutes to 60 minutes.

Thereafter, when the temperature T5 to T7 to cool to a temperature of the molten glass MG, SnO ₂ by reduction of SnO is obtained by the oxidation reaction of O ₂ and oxygen absorption. Therefore, O ₂ present in the bubble B remaining in the molten glass MG is absorbed by SnO. However, the diffusion into the inherent bubble B of SO ₂ or CO ₂ in the molten glass MG is maintained. Therefore, the concentration of SO ₂ and CO ₂ in the gas component in the bubble B during the period from the temperature T5 to the temperature T7 is higher than the concentration of the SO ₂ and CO _{2 in} the period from the temperature T3 to the temperature T5. In particular, in the molten glass MG used in the present embodiment, since the composition of the alkali metal is small, the degree of melting in the molten glass MG of SO ₂ is small. Therefore, when SO ₂ is absorbed as a gas by the bubble B, the SO ₂ is hardly absorbed into the molten glass MG in the absorption process.

As described above, during the period from the temperature T5 to the temperature T7, the O _{2 in the} bubble B is absorbed by the SnO by the oxidation reaction of SnO, but the diffusion into the inherent bubble B of SO ₂ and CO ₂ is maintained. When this period is short, the diffusion into the bubble B inherent to the SO ₂ and CO ₂ can be reduced, and the growth of the bubble B can be suppressed. Therefore, during the absorption process from the temperature T5 to the temperature T7, the molten glass MG is cooled at a temperature drop rate of 2 ° C/min or more in a temperature range of 1600 ° C to 1500 ° C, whereby the glass plate can be suppressed as described below. The number of bubbles.

Fig. 7 is a graph showing the measurement results of the content of SO ₂ contained in the pores after the bubble B in the glass is reproduced, and shows the dependence on the content of SO ₂ with respect to the temperature condition of the glass and the temperature maintenance time. The size of the black dot in Fig. 7 indicates the size of the bubble B and indicates the content of SO ₂ .

The glass plate has the same glass composition as the above-described glass substrate for liquid crystal display having a small content of alkali metal, and contains SnO ₂ as a clarifying agent. Specifically, a glass substrate for a liquid crystal display having the same glass composition as that of the glass plate produced when the measurement results of FIG. 6 were obtained was used.

Forming the glass into a plate-shaped glass plate by artificially opening the glass, and clamping the glass plate of the same kind of glass in an oxygen environment on both sides of the glass plate after the opening, thereby filling A hole having O ₂ is reproduced as a bubble. The glass plate having the pores was heat-treated at various temperatures and temperature maintenance times of 1200 ° C or higher, and the content of SO _{2 in} the pores was measured by gas analysis. Since the glass plate is heated to 1200 ° C or higher, the glass plate is in a molten state, and the bubbles B remaining in the molten glass can be reproduced.

According to Fig. 7, it is understood that SO ₂ is contained in the pores filled with O ₂ at a temperature of approximately 1500 ° C or higher. In particular, the higher the temperature, and the longer the temperature maintenance time, the more the content of SO ₂ increases. It means that the diffusion of SO ₂ dissolved in the glass in a molten state is promoted by high temperature and absorbed into the pores.

Therefore, in the absorption treatment of the molten glass MG after the defoaming treatment, it is preferred to rapidly cool down to less than 1500 ° C. In the present embodiment, it is preferred that the molten glass MG is in the temperature range of 1600 ° C to 1500 ° C to 2 Cooling down at a temperature above °C/min.

Fig. 8 is a graph showing the results of measurement of the relationship between the bubble level and the temperature drop rate when the glass plate was produced in the experimental furnace simulating the temperature history of the molten glass MG shown in Fig. 5. The cooling rate is an average speed in a temperature range of 1600 ° C to 1500 ° C. The glass plate produced had the same glass composition as the glass substrate for liquid crystal display having a small content of alkali metal, and SnO _{2 was} used as a clarifying agent. Specifically, a glass substrate for a liquid crystal display having the same glass composition as that of the glass plate produced when the measurement results of FIG. 6 were obtained was used.

It can be seen that if the cooling rate is less than 2 ° C / min, the bubble level rises sharply. In addition, the bubble level means that the number of bubbles per unit glass mass when the temperature drop rate is 10 ° C /min is a standard, and the number of bubbles is deteriorated to what extent. For example, the bubble level 3 indicates the number of bubbles three times the number of bubbles when the temperature drop rate is set to 10 ° C / minute. Therefore, it can be seen that if the temperature drop rate is less than 2 ° C / min, the number of bubbles rises sharply.

According to Fig. 8, in order to reduce the number of bubbles, it is preferable to set the temperature drop rate to 2 ° C / min or more.

(Example 1)

Fig. 9 is a view showing the results of measurement of the relationship between the number of bubbles existing in the glass plate and the temperature drop rate when the glass plate is produced by the apparatus for producing a glass plate shown in Fig. 2 . After the melting step, the clarification step, and the stirring step, the glass plate is produced by an overflow down-draw method. At this time, the temperature history of the molten glass MG adopts the history shown in FIG. 5 in addition to the temperature drop rate. The so-called cooling rate is an average speed in a temperature range of 1600 ° C to 1500 ° C. The glass plate produced had the same glass composition as the glass substrate for liquid crystal display having a small content of alkali metal, and SnO _{2 was} used as a clarifying agent. Specifically, a glass substrate for a liquid crystal display having the same glass composition as that of the glass plate produced when the measurement results of FIG. 6 were obtained was used. The bubble level shown in Fig. 9 indicates how much the number of bubbles is deteriorated by the number of bubbles per unit mass when the temperature drop rate is set to 8.4 ° C / minute. For example, the bubble level 5 indicates the number of bubbles which are five times as large as the number of bubbles when the temperature drop rate is 8.4 ° C /min. The bubble level of the cooling rate of 7.9 ° C / min is 1.1, the bubble level of the cooling rate of 4.9 ° C / min is 1.6, the bubble level of the cooling rate of 4.2 ° C / min is 1.8, and the bubble level of the cooling rate of 3.0 ° C / min is 1.8. On the other hand, the bubble level of the cooling rate of 1.8 ° C / min is 3.0, the bubble level of the cooling rate of 0.5 ° C / min is 83, and the number of bubbles when the cooling rate is set to 8.4 ° C / min is more than 3 times. bubble.

As can be seen from Fig. 9, when the temperature drop rate is less than 2 ° C / min, the bubble level rises sharply, so the number of bubbles rises sharply. Therefore, when the molten glass MG is cooled in a temperature range of 1600 ° C to 1500 ° C at a temperature drop rate of 2 ° C / min or more, more preferably 2.5 ° C / min or more, the number of bubbles is lowered. As can be seen from Fig. 9, for example, it is more effective in reducing the number of bubbles in the cooling rate of 3 ° C / min to 8 ° C / min. Further, it has SiO ₂ : 60% by mass, Al ₂ O ₃ : 19.5% by mass, B ₂ O ₃ : 10% by mass, CaO: 5.3% by mass, SrO: 5% by mass, SnO ₂ : 0.15% by mass, Fe _The number of bubbles in the glass plate of ₂ O ₃ : 0.05% by mass was substantially reduced by a small amount, but substantially the same result was obtained. Further, it has SiO ₂ : 61% by mass, Al ₂ O ₃ : 19.5% by mass, B ₂ O ₃ : 10% by mass, CaO: 9% by mass, SnO ₂ : 0.3% by mass, and R ₂ O (R-based Li, In the production of a 0.2% by mass glass plate (strain point: 700 ° C), the same results as described above were also obtained in the case of the total composition contained in the glass plate among Na and K.

(Example 2)

Fig. 10 is a graph showing the relationship between the number of bubbles existing in the glass plate and the temperature increase rate. The glass plate produced had the same glass composition as the glass substrate for liquid crystal display having a small content of alkali metal, and SnO _{2 was} used as a clarifying agent. Specifically, a glass substrate for a liquid crystal display having the same glass composition as that of the glass plate produced when the measurement results of FIG. 6 were obtained was used. The glass raw material which was blended so as to have the above-described glass composition was melted at 1,580 ° C (= T3), and then heated to 1,640 ° C (= T4). After maintaining at 1640 ° C for a certain period of time, the temperature was lowered to 1600 ° C (= T6) at a rate of 10 ° C / min, and further, the temperature was lowered to 1500 ° C (= T5) at a rate of 5 ° C / min. At this time, the temperature increase rate was changed to 0.5 ° C / min, 1 ° C / min, 1.5 ° C / min, 2 ° C / min, 3 ° C / min, 4 ° C / min, 5 ° C / min, 6 ° C / min, and observed The number of bubbles changes. The bubble level shown in Fig. 10 indicates how much the number of bubbles is deteriorated by the number of bubbles per unit mass at a temperature increase rate of 2 ° C / minute. For example, the bubble level 5 indicates the number of bubbles which are five times the number of bubbles when the temperature increase rate is 2 ° C / minute. The bubble level of the temperature increase rate of 2 ° C / min is 1, the bubble rate of the temperature increase rate of 3 ° C / min is 0.8, the bubble rate of the temperature increase rate of 4 ° C / min is 0.7, and the bubble rate bubble of the temperature increase rate of 5 ° C / min. At 0.7, the bubble level at a rate of 6 ° C/min was 0.6. On the other hand, the bubble level of the temperature increase rate of 0.5 ° C / min was 4.8, the bubble rate of the temperature increase rate of 1 ° C / min was 2.3, the bubble rate of the temperature increase rate of 1.5 ° C / min was 1.6, and the temperature increase rate was 2 The number of bubbles at ° C/min contains 1.5 times or more of bubbles.

As can be seen from Fig. 10, when the temperature increase rate is less than 2 ° C /min, the bubble level rises sharply and the number of bubbles rises sharply. Therefore, after the melting step, when the molten glass MG is heated to 1630 ° C or higher at a temperature increase rate of 2 ° C / min or more, more preferably 2.5 ° C / min or more, the number of bubbles is lowered. Therefore, it is preferably from 2 ° C / min to 10 ° C / min, more preferably from 3 ° C / min to 8 ° C / min, and further preferably from 3 ° C to 6.5 ° C / min. Further, as can be seen from Fig. 10, for example, the temperature increase rate is 3 ° C / min to 8 ° C / min, 3 ° C / min to 6 ° C / min, 4 ° C / min ~ 6 ° C / min or 4 ° C / min ~ 10 ° C / It is more effective in terms of reducing the number of bubbles in minutes. Further, it has SiO ₂ : 60% by mass, Al ₂ O ₃ : 19.5% by mass, B ₂ O ₃ : 10% by mass, CaO: 5.3% by mass, SrO: 5% by mass, SnO ₂ : 0.15% by mass, Fe _The number of bubbles in the glass plate of ₂ O ₃ : 0.05% by mass was substantially reduced by a small amount, but substantially the same result was obtained. Further, it has SiO ₂ : 61% by mass, Al ₂ O ₃ : 19.5% by mass, B ₂ O ₃ : 10% by mass, CaO: 9% by mass, SnO ₂ : 0.3% by mass, and R ₂ O (R-based Li, In the production of a 0.2% by mass glass plate (strain point: 700 ° C), the same results as described above were also obtained in the case of the total composition contained in the glass plate among Na and K.

As described above, according to the present embodiment, the number of bubbles of SO ₂ in the molten glass can be reduced, and therefore, the bubbles which become the core of cavitation due to the rotation of the stirring blade in the stirring step can be reduced, and as a result, the glass plate can be lowered. The number of bubbles. This effect is more remarkable in the method of producing a glass substrate having a small glass composition of BaO or SrO.

More specifically, MgO, CaO, SrO, and BaO contained as a glass composition are often added as a carbonate to a raw material, and MgO is the lowest in the decomposition temperature, and is changed in the order of CaO, SrO, and BaO. high. That is, the higher the decomposition temperature, the higher the temperature at which CO ₂ is released. From the above, it is understood that if the molten glass MG is cooled after the defoaming treatment, the higher the decomposition temperature, the higher the temperature starts to absorb CO ₂ . For example, BaO begins to absorb CO ₂ at around 1300 °C.

However, in the manufacture of a glass sheet having a glass composition which is low in the amount of BaO or SrO which starts to absorb CO ₂ in a relatively high temperature region, the viscosity of the molten glass MG after the temperature of the molten glass MG is lowered by the absorption of the CO ₂ . Start after getting higher. Here, CO ₂ rapidly diffuses into the molten glass MG when the viscosity of the molten glass MG is low. Therefore, in the method for producing a glass sheet in which the absorption of CO ₂ is started after the viscosity of the molten glass MG is increased (after the temperature is lowered), the CO ₂ is likely to remain as bubbles in the molten glass MG.

According to the present embodiment, if the SO ₂ which is present as a gas component of the bubble in the molten glass can be reduced, even if it is a glass plate which is likely to remain CO ₂ as described above, the core which becomes cavitation can be suppressed. The generation of bubbles, as a result, also reduces the number of bubbles in the glass sheet as the final product. From the above, it is understood that the present embodiment is suitable for the production of a glass substrate having a BaO content of 0 to 1.0% by mass, and further suitable for a method for producing a glass substrate substantially free of BaO. Further, this embodiment is suitable for the production of a glass substrate having a content of SrO of 0 to 3.0% by mass, and is further suitable for a method for producing a glass substrate which does not substantially contain SrO.

The method of producing the glass sheet of the present invention has been described in detail above, but 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.

200‧‧‧melting device

201‧‧‧melting tank

202‧‧‧Clarification tank

203‧‧‧Stirring tank

203a‧‧‧Agitator

204, 205, 206‧‧‧ glass supply tube

300‧‧‧Forming device

310‧‧‧Formed body

312‧‧‧ supply trench

313‧‧‧ bottom end

320‧‧‧Environmental spacers

330‧‧‧Cooling roller

335‧‧‧Cooling unit

350a~350d‧‧‧Transport roller

340‧‧‧Forming furnace

350‧‧‧Xu cold furnace

400‧‧‧ cutting device

Fig. 1 is a view showing the steps of a method for producing a glass sheet of the embodiment.

Fig. 2 is a view schematically showing an apparatus for performing a melting step to a cutting step in the method for producing a glass sheet of the embodiment.

Fig. 3 is a view mainly showing the configuration of a device for performing a clarification step in the embodiment.

Fig. 4 is a view mainly showing the configuration of a device for performing a forming step and a cutting step in the embodiment.

Fig. 5 is a view showing an example of a temperature history from the melting step to the forming step in the embodiment.

Fig. 6 is a graph showing the relationship between the discharge amount of O ₂ contained in the molten glass and the temperature increase rate when the defoaming treatment is performed in the present embodiment.

Fig. 7 is a graph showing the measurement results of the content of SO ₂ contained in the pores in the glass after the bubbles remaining in the glass plate are reproduced.

Fig. 8 is a graph showing the relationship between the bubble level and the temperature drop rate when a glass plate is produced in a laboratory furnace simulating the temperature history of the molten glass shown in Fig. 5.

Fig. 9 is a view showing the relationship between the bubble level and the temperature drop rate existing in the glass sheet when the glass sheet is produced by the apparatus for producing a glass sheet shown in Fig. 2;

Fig. 10 is a view showing the relationship between the bubble level and the temperature increase rate which are present in the glass sheet when the glass sheet is produced by the apparatus for producing a glass sheet shown in Fig. 2;

Claims (7)

A method for producing a glass sheet, comprising: a melting step of melting a glass raw material containing SnO ₂ as a fining agent by at least electric heating to form a molten glass; and a clarifying step comprising: a defoaming treatment, wherein After the melting step, the temperature of the molten glass is raised to 1630 ° C or higher at a temperature increase rate of 2 ° C /min or more, whereby bubbles are formed in the molten glass to perform defoaming; and an absorption treatment is performed in the above defoaming treatment. Thereafter, the molten glass is cooled to absorb bubbles in the molten glass into the molten glass, and a forming step of forming the molten glass after the clarification step into a sheet glass; wherein in the absorbing treatment The molten glass is cooled at a temperature drop rate of 2.5 ° C / min or more in the range of 1600 ° C to 1500 ° C. The method for producing a glass sheet according to claim 1, wherein in the forming step, the sheet glass is formed from the molten glass by an overflow down-draw method. The method for producing a glass sheet according to claim 1 or 2, wherein the temperature rise of the molten glass in the clarification step is at least a metal tube between the melting tank for performing the melting step and the clarifying tank for performing the clarification step, and It is carried out by controlling the current flowing into the metal tube. The method for producing a glass sheet according to claim 1 or 2, wherein the viscosity of the molten glass in the temperature of 1630 ° C is 130 to 350 poise. The method for producing a glass plate according to claim 1 or 2, wherein the content of R' ₂ O of the glass plate is 0 to 2.0% by mass (R' ₂ O is among Li ₂ O, Na ₂ O and K ₂ O) The total of the ingredients contained). The method for producing a glass plate according to claim 1 or 2, wherein the glass plate contains: SiO ₂ : 50 to 70% by mass, B ₂ O ₃ : 5 to 18% by mass, and Al ₂ O ₃ : 10 to 25% 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 20% by mass (wherein R is selected from Mg, Ca, Sr) And at least one of Ba, and RO is a total of components contained in MgO, CaO, SrO, and BaO). The method for producing a glass plate according to claim 1 or 2, wherein a stirring step of uniformly stirring the components of the molten glass is included between the clarifying step and the forming step; and melting in the molten glass is performed in the melting step The molten glass is supplied to the clarification step at a temperature higher at the beginning; in the clarification step, the molten glass is supplied to the stirring step at a temperature lower than the temperature after the absorbing treatment; In the above, the molten glass is supplied to the molten glass by the viscosity η (poise) of the molten glass to a temperature of log η = 4.3 to 5.7, and is formed into a sheet glass.