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WO2020008782A1 - Glass article manufacturing method and manufacturing apparatus - Google Patents

Glass article manufacturing method and manufacturing apparatus Download PDF

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Publication number
WO2020008782A1
WO2020008782A1 PCT/JP2019/022208 JP2019022208W WO2020008782A1 WO 2020008782 A1 WO2020008782 A1 WO 2020008782A1 JP 2019022208 W JP2019022208 W JP 2019022208W WO 2020008782 A1 WO2020008782 A1 WO 2020008782A1
Authority
WO
WIPO (PCT)
Prior art keywords
molten glass
flow direction
glass
inflow
tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2019/022208
Other languages
French (fr)
Japanese (ja)
Inventor
周作 玉村
西村 康宏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Electric Glass Co Ltd
Original Assignee
Nippon Electric Glass Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Electric Glass Co Ltd filed Critical Nippon Electric Glass Co Ltd
Priority to CN201980042092.0A priority Critical patent/CN112368244B/en
Priority to KR1020217003192A priority patent/KR102699833B1/en
Publication of WO2020008782A1 publication Critical patent/WO2020008782A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B17/00Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
    • C03B17/06Forming glass sheets
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/26Outlets, e.g. drains, siphons; Overflows, e.g. for supplying the float tank, tweels

Definitions

  • the present invention relates to a method and an apparatus for manufacturing a glass article, and more particularly to a technique for improving a layout of a manufacturing line by improving a conveying route of a molten glass to a molded article.
  • a production line for a glass roll or a flat glass includes a melting line in which molten glass flows and a processing line in which a glass ribbon flows.
  • the melting line includes, in order from the upstream side, a dissolving tank, a refining tank, a homogenizing tank such as a stirring tank, a condition adjusting tank, and a molded body.
  • a supply pipe of molten glass for example, see Patent Document 1.
  • the transport direction of a glass ribbon is changed from a vertical direction to a horizontal direction (for example, see Patent Document 2).
  • the processing line extends in a direction perpendicular to the melting line from the end (molded body) of the melting line in a state where the production line is viewed in plan.
  • the melting line and the processing line are arranged in a direction orthogonal to each other.
  • the distance between the melting lines must be increased by the amount corresponding to the processing lines, which wastes installation space.
  • the layout of the manufacturing line is limited, and it is difficult to flexibly change the layout.
  • FIGS. 9 and 10 a layout shown in FIGS. 9 and 10 can be considered.
  • the condition adjusting tank 101 is located downstream of a not-shown homogenizing tank, and the molded body 102 is located downstream of the condition adjusting tank 101 (see FIG. 9).
  • the homogenizing tank and the condition adjusting tank 101 are connected by a connection pipe 103 having a predetermined shape (see FIG. 10), and the condition adjusting tank 101 and the molded body 102 have a shape bent in a predetermined direction. They are connected by a connection pipe 104 (see FIG. 9).
  • the outlet 101a of the condition adjusting tank 101 faces downward (see FIG.
  • the connecting pipe 104 connected to the outlet 101a adjusts the state of the connecting pipe 104 in a plan view. It is bent in a direction orthogonal to the inflow direction d0 of the molten glass Gm into the tank 101 (see FIG. 10). In this manner, by bending the connection pipe 104, the feeding direction D0 of the glass ribbon Gr and the flow direction of the molten glass Gm (inflow direction d0 of the molten glass Gm into the inside of the condition adjusting tank 101) are parallel. Therefore, the melting line and the processing line can be arranged in parallel.
  • reference numeral 101b indicates an inlet of the condition adjusting tank 101
  • reference numeral 102a indicates an inlet of the molded body 102
  • reference numerals Gr1 and Gr2 indicate both ends in the width direction of the glass ribbon Gr to be formed.
  • the stagnation region R1 of the molten glass Gm is placed in each of the tanks (for example, the homogenizing tank 105 and the condition adjusting tank 101 shown in FIG. 11) up to the compact 102. , R2 may occur.
  • the molten glass Gm1 'and Gm2' in the stagnation regions R1 and R2 are likely to be different from the molten glass Gm that has reached the molded body 102 without passing through the stagnation regions R1 and R2 because they have different temperature histories.
  • a conventional melting line as shown in FIG.
  • the molten glass Gm1 ′ and Gm2 ′ in the stagnation regions R1 and R2 flow through the connecting pipe 106 from below the condition adjusting tank 101, and
  • the glass ribbon Gr passes through the upper or lower part of the inflow port 102a and becomes both ends Gr1 and Gr2 in the width direction of the glass ribbon Gr as a molded product. Since both ends Gr1 and Gr2 in the width direction of the glass ribbon Gr are usually removed by cutting or the like in a subsequent processing line, there is no particular problem without the foreign molten glass Gm1 ′ and Gm2 ′ remaining in the final product. .
  • the melting line proposed above see FIGS.
  • the connecting pipe 104 is moved from below in a direction orthogonal to the flowing direction d0 of the molten glass Gm into the conditioning tank 101.
  • the molten glass Gm1 ′, Gm2 ′ in the stagnation regions R1, R2 is different from the portion (FIG. 12) of the connecting pipe 104 flowing in the conventional melting line. It flows through a different portion, passes through an intermediate portion in the vertical direction of the inlet 102 a of the molded body 102, and flows into the molded body 8. Therefore, as shown in FIG.
  • the molten glass Gm1 ′ and Gm2 ′ of the stagnation regions R1 and R2 are mixed into the product portion located between both ends Gr1 and Gr2 in the width direction of the glass ribbon Gr and processed.
  • Foreign glass melts Gm1 'and Gm2' remain on the glass ribbon Gr (that is, a glass roll or a glass plate as a product), causing a product defect.
  • the present specification solves the problem of increasing the degree of freedom regarding the layout of a manufacturing line of glass articles while preventing a situation in which a foreign molten glass that may be generated in a melting line remains in a product portion of a glass ribbon. It is a technical task to be done
  • this manufacturing method includes forming a molten glass in a molten glass generating apparatus, forming a molten glass in a state adjusting tank, and adjusting a state of the generated molten glass in a state adjusting tank. And a forming step of forming a glass ribbon by supplying the molten glass to the body, in the method of manufacturing a glass article, the molten glass inflow port provided in the conditioning tank, from the side of the molten glass generating device into the conditioning tank.
  • An inflow pipe for inflow of the molten glass is connected, and the flow direction of the molten glass when passing through one end of the inflow pipe on the upstream side in the flow direction of the molten glass is set as a reference flow direction, and the state is adjusted from the other end of the inflow pipe.
  • the flow direction of the molten glass when flowing into the inside of the tank is the flow direction at the time of inflow
  • the flow direction at the time of inflow is either one of the left and right sides with respect to the reference flow direction in a state where the inflow pipe is viewed in plan.
  • the inflow pipe is characterized with a point where the inlet tube is bent.
  • the shape of the inflow pipe connected to the inflow port of the conditioning tank attention is paid to the shape of the inflow pipe connected to the inflow port of the conditioning tank.
  • the inflow so that the flow direction of the molten glass when flowing into the inside of the tank is directed to one of the left and right sides with respect to the reference flow direction (the flow direction of the molten glass when passing through one end of the inflow pipe).
  • the tube was bent.
  • a stagnation region of the molten glass is generated in a layer (such as a homogenization tank) upstream of the condition adjusting tank by bending the inflow pipe which has been conventionally formed in a straight line, the stagnation area of the stagnation region is not changed.
  • the molten glass reaches the other end of the inflow pipe, that is, the inflow port of the conditioning tank, while maintaining as much as possible the position (for example, the lower part of the inflow pipe) at the time of flowing into one end of the inflow pipe. Therefore, the molten glass passes through the upper or lower part of the inflow port of the molded body without changing the relative position of the molten glass in the connection pipe by connecting the condition adjusting tank and the molded body in a conventional manner. Will be. Thereby, even if the molten glass in the stagnant area flows in, the molten glass can be flowed into the regions at both ends in the width direction of the glass ribbon formed by the molded body.
  • the direction of the inflow port of the conditioning tank connected to the downstream end of the inflow pipe is such that molten glass is generated by the molten glass generation device. Later, the flow direction is different from the flow direction leading to the conditioning tank. Therefore, by adjusting the flow direction (flow direction at the time of inflow) when flowing into the inside of the condition adjusting tank, the direction of the inflow port of the molded body can be appropriately set.
  • the outlet of the condition adjusting tank and the inlet of the molded body are connected by a connecting pipe, and the connecting pipe is formed by flattening the connecting pipe from the same direction as the outlet of the condition adjusting tank. It may be bent in the same direction as the flow direction at the time of inflow when viewed.
  • the inflow pipe extends straight from the one end side of the inflow pipe to the other right and left sides with respect to the reference flow direction in a state where the inflow pipe is viewed in plan. And a bent portion bent from the downstream end of the straight portion in the flow direction at the time of inflow and connected to the inflow port of the conditioning tank.
  • the inflow pipe is provided with a straight portion that extends linearly from one end of the inflow pipe to the other side on the left and right sides with respect to the reference flow direction, and from the downstream end of the straight section to the flow direction during inflow.
  • the straight portion is inclined in the right and left opposite directions to the bending direction (one of the left and right sides) of the bent portion with respect to the reference flow direction (described later). 3 etc.). Therefore, the length of the pipe from one end of the inflow pipe to the upstream end of the bent portion can be reduced.
  • the molded article is a method of molding a glass ribbon by causing molten glass overflowing from the overflow groove to flow down along both sides, and the inlet of the molded article is formed on both sides.
  • the angle between the reference flow direction and the inflow flow direction may be set to 90 °.
  • the glass article may be a glass roll formed by winding a glass ribbon into a roll.
  • the inflow pipe or bent portion
  • the reference flow direction and the orientation of the main surface of the glass ribbon molded by the molded body are connected.
  • the formed glass ribbon is drawn downward, and then turned and transported in the horizontal direction via the catenary.
  • the melting line, the processing line, Can be arranged in parallel.
  • the production line of the glass roll is narrowed in the width direction (the same direction as the short direction in the melting line, and the width direction of the glass ribbon in the processing line; hereinafter the same in the present specification). This is suitable when a plurality of glass roll production lines are arranged in parallel.
  • this manufacturing apparatus includes a molten glass generating apparatus that generates molten glass, a state adjusting tank that adjusts the state of the generated molten glass, and a molded body that forms the molten glass whose state has been adjusted into a glass ribbon.
  • a glass article manufacturing apparatus comprising: an inflow pipe for flowing molten glass from the side of the molten glass producing device into the inside of the conditioning glass, to an inlet of the molten glass provided in the conditioning glass,
  • the flow direction of the molten glass when passing through one end of the inflow pipe on the upstream side in the flow direction of the glass is defined as the reference flow direction
  • the flow direction of the molten glass when flowing into the inside of the condition adjusting tank from the other end of the inflow pipe is defined as the flow direction.
  • the point at which the flow direction of the inflow pipe is bent is such that the flow direction at the time of inflow is directed to one of the left and right sides with respect to the reference flow direction in a state where the inflow pipe is viewed in plan. Attached butterflies.
  • the molten glass in the stagnant region reaches the inlet of the condition adjusting tank while maintaining as much as possible the position of the molten glass at one end of the inflow pipe. Therefore, by connecting the condition adjusting tank and the compact in a conventional manner, the molten glass can be supplied to the compact without changing the relative position of the molten glass in the connection pipe.
  • the direction of the inflow port of the conditioning tank connected to the downstream end of the inflow pipe is such that molten glass is generated by the molten glass generation device. Later, the flow direction is different from the flow direction leading to the conditioning tank. Therefore, by adjusting the flow direction when flowing into the inside of the condition adjusting tank, the direction of the inlet of the molded body can be appropriately set.
  • FIG. 2 is a plan view of a main part of the manufacturing apparatus shown in FIG. 1. It is the figure which looked at the 3rd connection pipe shown in FIG. 1, and its peripheral part from top view. It is the side view which looked at the 3rd connection pipe shown in FIG. 1, and its peripheral part from the Y direction. It is the figure which looked at the 3rd connection pipe shown in FIG. 3, and its peripheral part from the front.
  • FIG. 2 is a front view schematically illustrating a flow of molten glass in a stagnant region to the inside of a molded body in the manufacturing apparatus illustrated in FIG. 1.
  • FIG. 6 It is the side view which looked at the flow of the molten glass around the 3rd connection pipe shown in FIG. 6 from the Y direction. It is the figure which looked at the principal part of the manufacturing device of the glass article concerning other embodiments of the present invention from the front. It is the figure which looked at the principal part of the manufacturing apparatus of the glass article used for comparison with this invention from the side, and was the side view which looked at the connection pipe which connects a condition adjustment tank and a molded object from the Y direction. It is the figure which looked at the connecting pipe shown in FIG. 9 and its periphery from top.
  • FIG. 9 It is the side view which looked at the flow of the molten glass around the 3rd connection pipe shown in FIG. 6 from the Y direction. It is the figure which looked at the principal part of the manufacturing device of the glass article concerning other embodiments of the present invention from the front. It is the figure which looked at the principal part of the manufacturing apparatus of the glass article used for comparison with this invention from the side, and was the side view which looked
  • FIG. 11 is a front view schematically illustrating a flow of molten glass in a stagnant region to the inside of a molded product in the apparatus for manufacturing a glass article provided with the connection pipe illustrated in FIG. 10. It is the front view which drawn typically the flow until the molten glass of the stagnation area reaches the inside of a molded object in the manufacturing device of the glass article concerning the conventional composition. It is the side view which looked at the flow of the molten glass of the stagnation area shown in Drawing 11 from the Y direction.
  • FIG. 1 is a front view of a glass article manufacturing apparatus 1 according to the present embodiment
  • FIG. 2 is a plan view of the same glass article manufacturing apparatus 1.
  • the manufacturing apparatus 1 includes a melting line 2 through which a molten glass Gm flows, and a processing line 3 for a glass ribbon Gr formed by the melting line 2.
  • the melting line 2 is a melting tank 4 serving as a molten glass generating device arranged in the uppermost stream area, a refining tank 5 disposed downstream of the melting tank 4, and disposed downstream of the refining tank 5.
  • a homogenizing tank 6, a conditioning tank 7 disposed downstream of the homogenizing tank 6, a molded body 8 disposed downstream of the conditioning tank 7, and respective tanks 4 to 7, and Connection pipes 9 to 12 for connecting between the molded bodies 8 are provided.
  • the processing line 3 for the glass ribbon Gr is located below the molded body 8, and is provided with a slow cooling processing unit that performs a slow cooling process on the glass ribbon Gr formed by the molded body 8.
  • the first cutting portion for separating both ends (also called ears) in the width direction of the glass ribbon Gr conveyed in the lateral direction from the glass ribbon Gr main body, and the glass ribbon Gr with both ends in the width direction removed along the width direction.
  • a second cutting unit for cutting and a winding unit for winding the glass ribbon Gr that has passed through the second cutting unit into a roll shape are provided.
  • the above-described configuration is merely an example, and some of the above-described components may be changed or omitted, or components other than the above may be added as necessary.
  • the melting line 2 will be described focusing on the connection between the homogenizing tank 6 and the condition adjusting tank 7.
  • the melting tank 4 is a container for performing a generation process of melting the charged glass raw material to generate the molten glass Gm.
  • the dissolution tank 4 is connected to the fining tank 5 by a first connection pipe 9.
  • the refining tank 5 is a container for performing a refining step of refining the molten glass Gm supplied from the melting tank 4 through the first connection pipe 9 by the action of a refining agent or the like.
  • the fining tank 5 is connected to the homogenizing tank 6 by a second connection pipe 10.
  • the homogenizing tank 6 is a container for performing a homogenizing step of stirring and homogenizing the clarified molten glass Gm.
  • the homogenizing tank 6 is connected to the condition adjusting tank 7 by a third connection pipe 11.
  • the number of the homogenizing tanks 6 may be one as shown in the figure, or two or more may be arranged side by side.
  • the condition adjusting tank 7 is a container for performing a state adjusting step of adjusting the molten glass Gm to a state suitable for molding, and adjusts, for example, a flow rate of the molten glass Gm supplied to the molded body 8.
  • the state adjusting tank 7 is connected to the third connection pipe 11, and the upper part 7 a into which the molten glass Gm flows from the third connection pipe 11, and the molten glass Gm whose state has been adjusted flows out. And an intermediate portion 7c connecting the upper portion 7a and the lower portion 7b.
  • An inflow port 7d through which the molten glass Gm flows is provided on a side surface of the upper portion 7a.
  • An outlet 7e for molten glass Gm is provided at the lower end of the lower portion 7b.
  • the condition adjusting tank 7 having the above configuration is connected to the molded body 8 by the fourth connection pipe 12.
  • the molded body 8 is for molding the molten glass Gm into a desired shape.
  • the molded body 8 is formed by molding the molten glass Gm into a belt shape by an overflow down draw method.
  • the molded body 8 has a substantially wedge-shaped cross section, has an overflow groove 8a at an upper portion thereof, and has both side surfaces 8b, 8b through which the molten glass Gm overflowing from the overflow groove 8a flows.
  • the molten glass Gm that has flowed down along the side surfaces 8b, 8b is fused at the lower apexes of the side surfaces 8b, 8b, and can be formed into a belt-shaped glass ribbon Gr.
  • the formed glass ribbon Gr has a thickness of, for example, 0.01 to 2 mm (preferably 0.3 mm or less), and is a substrate for a flat panel display such as a liquid crystal display or an organic EL display, an organic EL lighting, a solar cell, or the like. And used for protective covers.
  • the molded body 8 may execute another downdraw method such as a slot downdraw method.
  • the first connection pipe 9 to the fourth connection pipe 12 are each formed of a cylindrical pipe made of, for example, platinum or a platinum alloy, and are connected to the tanks 5 to 7 adjacent to the downstream side from the melting tank 4 and the molded body 8.
  • the molten glass Gm is sequentially conveyed.
  • FIG. 3 is a plan view of the third connection pipe 11 that connects the homogenization tank 6 and the condition adjustment tank 7 and a peripheral portion thereof.
  • the third connection pipe 11 has a shape bent in a predetermined direction.
  • This third connection pipe 11 corresponds to the inflow pipe according to the present invention.
  • the third connecting pipe 11 bends in a predetermined direction from the downstream end of the straight section 13 and the straight section 13 extending linearly in a state where the third connecting pipe 11 is viewed in plan, It has a first bent portion 14 connected to the inlet 7 a of the condition adjusting tank 7 and a second bent portion 15 connecting the outlet 6 a of the homogenizing tank 6 and the upstream end of the straight portion 13.
  • the flow direction of the molten glass Gm passing through the upstream end 11a of the third connection pipe 11 (reference flow direction d0) and the flow direction of the molten glass Gm passing through the downstream end 11b (flow direction d1 during inflow).
  • the third connection pipe 11 is configured such that the flow direction d1 at the time of inflow with respect to the reference flow direction d0 is either left or right in a state where the third connection pipe 11 is viewed in plan as shown in FIG.
  • the third connecting pipe 11 is bent so as to face the side.
  • the X direction and the Y direction are horizontal directions
  • the Z direction is a vertical direction. As shown in FIG.
  • the reference flow direction d0 is in the Y direction when viewed from above vertically.
  • the inflow flow direction d1 is in the X direction when viewed from vertically above.
  • the reference flow direction d0 and the inflow flow direction d1 are orthogonal to each other on the XY plane that is the horizontal plane.
  • the straight portion 13 extends linearly from the upstream end 11a of the third connection pipe 11 in a state of being inclined to the other right and left sides with respect to the reference flow direction d0.
  • the first bent portion 14 connected to the downstream end of the straight portion 13 is bent such that the inflow flow direction d1 faces one of the left and right sides with respect to the reference flow direction d0.
  • the straight portion 13 while the straight portion 13 extends linearly while being inclined rightward (downward in FIG. 3) with respect to the reference flow direction d0, the first bent portion 14 , From the extending direction of the straight portion 13 to the right (downward in FIG. 3) with respect to the reference flow direction d0.
  • FIG. 3 shows a result, as shown in FIG.
  • the condition adjusting tank 7 is at a position shifted from the outlet 6a of the homogenizing tank 6 in the ⁇ X direction (to the left in FIG. 4).
  • the straight portion 13 is inclined upward at a predetermined angle with respect to the horizontal direction so as to move in the + Z direction from the upstream end side (left side) to the downstream end side (right side). are doing. Therefore, the first bent portion 14 is at a position higher than the second bent portion 15.
  • the fourth connection pipe 12 connects the condition adjusting tank 7 and the molded body 8 so that the molten glass Gm flowing out of the condition adjusting tank 7 can be supplied to the molded body 8, and as shown in FIG. , From the same direction as the outflow port 7e of the condition adjusting tank 7 to the same direction as the inflow flow direction d1.
  • the fourth connection pipe 12 is moved from the Z direction (vertical direction) as shown in FIG. It is bent 90 ° in the X direction (horizontal direction).
  • the inflow direction d2 of the molten glass Gm into the molded body 8 and the inflow direction (inflow flow direction d1) into the condition adjusting tank 7 are parallel to each other.
  • a glass raw material is charged into a melting tank 4 located at the uppermost stream area of a melting line 2, By melting the raw materials, molten glass Gm is generated.
  • the molten glass Gm is supplied to the fining tank 5 via the first connection pipe 9, and the molten glass Gm clarified in the fining tank 5 is supplied to the homogenization tank 6 via the second connection pipe 10.
  • the molten glass Gm supplied to the homogenizing tank 6 is homogenized by stirring or the like, and then supplied to the condition adjusting tank 7 through the third connection pipe 11.
  • the molten glass Gm whose flow rate has been adjusted, for example, in the condition adjusting tank 7 is supplied to the molded body 8 through the fourth connection pipe 12.
  • the molten glass Gm is formed into a strip-shaped glass ribbon Gr by, for example, an overflow down draw method.
  • the formed glass ribbon Gr is conveyed on a processing line 3 extending in parallel with the melting line 2 and subjected to the above-described appropriate processing or processing such as cutting, thereby obtaining, for example, a glass roll. In this way, the production of glass articles is performed continuously.
  • a stagnation region R1 of the molten glass Gm may be generated at the bottom of the homogenization tank 6, as shown in FIG. 6, for example.
  • the molten glass Gm ⁇ b> 1 ′ in the stagnation region R ⁇ b> 1 flows from the outlet 6 a of the homogenization tank 6 to a lower portion of the upstream end 11 a of the third connection pipe 11.
  • a stagnant region R2 of the molten glass Gm may be formed at the top of the condition adjusting tank 7 (region of the upper part 7a above the inlet 7d).
  • the molten glass Gm2 'in the stagnation region R2 flows into the upstream end of the fourth connection pipe 12 through the side of the outlet 7e close to the formed body 8 (the side in the + X direction in the XYZ coordinate system).
  • the flow direction d1 at the time of inflow of the molten glass Gm faces either the left or right with respect to the reference flow direction d0 in a state where the third connection pipe 11 is viewed in a plan view.
  • the third connection pipe 11 as the inflow pipe was bent (see FIG. 3). Even if the stagnation region R1 of the molten glass Gm is generated in the homogenization tank 6 as shown in FIG.
  • the molten glass Gm1 ′ of the stagnation region R1 becomes The position at the time of flowing into the upstream end 11a of the three connection pipes 11 is maintained as much as possible (here, the lower part of the upstream end 11a, the lower part 15a of the second bent part 15, the lower part 13a of the straight part 13, the first part 13a, (Through the lower portion 14a of the bent portion 14 and the lower portion of the downstream end 11b) to reach the inlet 7d of the conditioning tank 7. Further, by connecting the condition adjusting tank 7 and the molded body 8 with the fourth connection pipe 12 having a bent form as shown in FIG. 4, the molten glass Gm1 ′ in the stagnation region R1 becomes as shown in FIG.
  • the outer side 12a of the bent portion of the fourth connecting pipe 12 passes through the outer side 12a of the formed body 8 It passes below the inflow port 8c.
  • the molten glass Gm2 'of the stagnant region R2 is closer to the molded body 8 in the outlet 7e of the condition adjusting tank 7.
  • the position of the molten glass Gm1 ′ in the stagnant region R1 when flowing into the third connection pipe 11 is set to the lower part of the third connection pipe 11 and the position of the fourth connection pipe 12 It is possible to pass through the lower part of the inlet 8c of the molded body 8 while maintaining as much as possible on the outside 12a of the bent portion. Further, the position of the molten glass Gm2 ′ in the stagnation region R2 when flowing into the fourth connection pipe 12 is maintained as much as possible inside the bent portion 12b of the fourth connection pipe 12, and It can pass through the upper part of the inflow port 8c.
  • the bending direction of the third connection pipe 11 may be any one of the left and right directions with respect to the reference flow direction d0 in a state where the third connection pipe 11 is viewed in a plan view.
  • the inlet 8c of the molded body 8 is provided in a direction perpendicular to both side surfaces 8b, 8b through which the molten glass Gm overflowing from the upper overflow groove 8a flows down, and the reference flow direction d0.
  • the flow direction d1 at the time of inflow are set to 90 °, and the bending direction of the fourth connecting pipe 12 (the inflow direction d2 into the molded body 8) is the same as the outlet 7e of the condition adjusting tank 7. From the direction, the fourth connection pipe 12 is bent in the same direction as the inflow flow direction d1 in a state where the fourth connection pipe 12 is viewed in a plan view (see FIGS. 3 and 4).
  • the bending direction of the third connection pipe 11 and the bending direction of the fourth connection pipe 12 are determined based on the relationship between the inlet 8c of the molded body 8 and the reference flow direction d0 and the molding by the molded body 8.
  • the direction of the main surface of the glass ribbon Gr to be performed (that is, the feeding direction D0 of the glass ribbon Gr) can be matched. After the formed glass ribbon Gr is drawn downward, it is conveyed while turning in the horizontal direction via the catenary, so that according to the above configuration, the melting line 2 and the processing line 3 are arranged in parallel. can do.
  • the reference flow direction d0 which is the reference when defining the bending direction of the third connection pipe 11 (the direction of the downstream end 11b, which is the direction after bending), is set as the horizontal direction.
  • the reference flow direction d0 is not limited to the horizontal direction (see FIG. 5).
  • the flow direction d1 at the time of inflow is not limited to the horizontal direction.
  • the flow direction d1 faces one of the left and right sides with respect to the reference flow direction d0 when viewed from above vertically (in a plan view). As long as it is possible, the flow direction d1 at the time of inflow can be set to an arbitrary direction.
  • the flow direction d2 of the molten glass Gm into the molded body 8 is not limited to the illustrated direction (+ X direction).
  • the inflow direction d2 can be set to a direction other than the + X direction.
  • the bending angle (the angle between the reference flow direction d0 and the inflow flow direction d1 when the third connection pipe 11 is viewed in a plan view) in the third connection pipe 11 is limited to 90 °. Absent.
  • the bending angle of the fourth connection pipe 12 (the angle between the direction of the outflow port 7e of the condition adjusting tank 7 and the inflow direction d2) is not limited to 90 °, but may be any angle within a range satisfying the above-described conditions. Can be adopted.
  • the third connecting pipe 11 is formed by connecting the straight portion 13 extending linearly, the first bent portion 14 connecting the straight portion 13 and the condition adjusting tank 7, and the homogenizing tank 6 to the straight portion.
  • the third connection pipe 11 can of course adopt a configuration other than the above.
  • a first straight portion extending in the ⁇ X direction is connected to the downstream end of the second bent portion 15 in a plan view, and a third bent portion is connected to the downstream end of the first straight portion.
  • the second straight portion extending in the + Y direction is connected to the downstream end of the third bent portion, the first bent portion 14 is connected to the downstream end of the second straight portion, and the downstream end of the first bent portion 14 is connected to the conditioning tank. It is also possible to take a form connected to the inflow port 7d of 7.
  • FIG. 8 is a view of a connection portion between the third connection pipe 11 and the condition adjusting tank 7 according to one example (another embodiment of the present invention) viewed from the Y direction. As shown in FIG. 8, the third connecting pipe 11 is located on the downstream side of the first bent portion 14, and is located between the first bent portion 14 and the condition adjusting tank 7.
  • a cross-sectional area changing portion 16 whose cross-sectional area (area in a cross section perpendicular to the longitudinal direction, hereinafter, also simply referred to as “cross-sectional area”) gradually changes from the side toward the condition adjusting tank 7 side.
  • cross-sectional area areas in a cross section perpendicular to the longitudinal direction
  • the sectional area S1 of the first bent portion 14 is the upper portion 7a. More specifically, the cross-sectional area S1 of the first bent portion 14 is smaller than the cross-sectional area S2 of the upper portion 7a.
  • the shape of the inner surface 16a of the cross-sectional area changing portion 16 is set such that the cross-sectional area of the cross-sectional area changing portion 16 gradually increases from the first bending portion 14 side toward the condition adjusting tank 7 side.
  • the vertical cross section (cross section along the longitudinal direction) of the inner surface 16a of the cross-sectional area changing portion 16 is arc-shaped.
  • the inner surface 16a of the cross-sectional area changing portion 16 is cylindrical, and the diameter is increased from the first bending portion 14 side toward the condition adjusting tank 7 side.
  • the cross-sectional area S1 of the first bent portion 14 is preferably set to be 0.75 times or more and 1.25 times or less the cross-sectional area S2 of the upper portion 7a.
  • the cross-sectional area S1 of the first bent portion 14 is set to 0. It is preferable to set it to 75 times or more and 0.96 times or less.
  • the inner diameter of the first bent portion 14 can be set to 150 mm or more and 300 mm or less, and the radius of curvature of the inner surface 16a of the cross-sectional area change portion 16 can be set to 10 mm or more and 50 mm or less, and is preferable. Is preferably set to 20 mm or more and 40 mm or less.
  • the lower part 7b of the condition adjusting tank 7 and the upstream end 12c of the fourth connecting pipe 12 are cut off (a state in which the lower part 7b of the condition adjusting tank 7 does not contact the upstream end 12c of the fourth connecting pipe 12). ),
  • the molten glass Gm can be supplied from the condition adjusting tank 7 to the fourth connection pipe 12. Specifically, as shown in FIG. 8, in a state where the lower portion 7b is inserted into the inner periphery of the upstream end 12c of the fourth connection pipe 12, the molten glass Gm whose state has been adjusted in the state adjustment tank 7 is The molded product 8 can be supplied through the fourth connection pipe 12.
  • the sectional area S3 of the lower part 7b of the condition adjusting tank 7 is S3 and the sectional area of the upstream end 12c of the fourth connection pipe 12 is S4, the sectional area S3 of the lower part 7b is changed to the sectional area S4 of the upstream end 12c. It is preferable to set it to 0.75 times or more and 0.96 times or less.
  • the viscosity of the molten glass Gm passing through the cross-sectional area changing portion 16 between the first bending portion 14 and the condition adjusting tank 7 is preferably 800 Pa ⁇ s or more. , More preferably 1000 Pa ⁇ s or more.
  • the viscosity of the molten glass Gm passing through the cross-sectional area changing portion 16 be set to 50,000 Pa ⁇ s or less.
  • the third connecting pipe 11 has a sectional area between the first bent portion 14 and the condition adjusting tank 7 that gradually increases in cross section from the first bent portion 14 side toward the condition adjusting tank 7 side. It has a cross-sectional area changing portion 16 that changes.
  • a situation in which a separation flow is generated in the molten glass Gm flowing into the inside of the condition adjusting tank 7 from the third connection pipe 11 is prevented as much as possible, and the molten glass stagnating at the bottom of the homogenizing tank 6 is prevented.
  • the glass Gm1 ′ passes through the outer side 12a of the fourth connection pipe 12, and is surely formed in the region of the molded body 8 that becomes one end portion Gr2 (see FIG.
  • the molten glass Gm2 ′ stagnating in the upper portion 7a of the condition adjusting tank 7 passes through the inner side 12b of the fourth connection pipe 12, and the other end Gr1 in the width direction of the glass ribbon Gr of the molded body 8 (see FIG. (See Reference)).
  • the foreign molten glass Gm1 ′ (Gm2 ′) that causes a molding defect remains on the processed glass ribbon Gr and serves as a product. It is possible to prevent a situation in which the quality of the glass article is deteriorated as much as possible.

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  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
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  • Glass Melting And Manufacturing (AREA)
  • Glass Compositions (AREA)

Abstract

Where molten glass Gm having a state adjusted in a state adjustment tank 7 is supplied to a molding body 8 to mold a glass ribbon Gr, an inflow pipe 11 is connected to an inflow port 7a of the state adjustment tank 7, and the inflow pipe 11 is bent so that a flow direction d1 at the time of inflow faces the left or right side with respect to a reference flow direction d0 in a plan view of the inflow pipe 11, where the reference flow direction d0 is the flow direction of the molten glass Gm passing through one end 11a of the inflow pipe 11 that is the upstream end in the flow direction of the molten glass Gm, and the flow direction d1 at the time of inflow is the flow direction of the molten glass Gm flowing into the state adjustment tank 7 from the other end 11b of the inflow pipe 11.

Description

ガラス物品の製造方法及び製造装置Method and apparatus for manufacturing glass articles

 本発明は、ガラス物品の製造方法及び製造装置に関し、特に成形体に至る溶融ガラスの搬送経路を改良することで、製造ラインのレイアウトの自由度を高めるための技術に関する。 The present invention relates to a method and an apparatus for manufacturing a glass article, and more particularly to a technique for improving a layout of a manufacturing line by improving a conveying route of a molten glass to a molded article.

 周知のように、ガラスロールや板ガラスの製造ラインは、溶融ガラスが流れる溶融ラインと、ガラスリボンが流れる加工ラインとからなる。この場合、溶融ラインは、例えば、上流側から順に、溶解槽と、清澄槽と、撹拌槽などの均質化槽と、状態調整槽と、成形体とを備えると共に、これら各槽と成形体とが溶融ガラスの供給管で接続された構成をなす(例えば特許文献1を参照)。また、ガラスロールの製造ラインにおいて、ガラスリボンの搬送方向は縦方向から横方向に転換される(例えば特許文献2を参照)。このため、加工ラインは、製造ラインを平面視した状態で、溶融ラインの終端(成形体)から溶融ラインに直交する向きに延伸している。 As is well known, a production line for a glass roll or a flat glass includes a melting line in which molten glass flows and a processing line in which a glass ribbon flows. In this case, for example, the melting line includes, in order from the upstream side, a dissolving tank, a refining tank, a homogenizing tank such as a stirring tank, a condition adjusting tank, and a molded body. Are connected by a supply pipe of molten glass (for example, see Patent Document 1). In a glass roll manufacturing line, the transport direction of a glass ribbon is changed from a vertical direction to a horizontal direction (for example, see Patent Document 2). For this reason, the processing line extends in a direction perpendicular to the melting line from the end (molded body) of the melting line in a state where the production line is viewed in plan.

特開2016-88754号公報JP 2016-88754 A 特開2011-16705号公報JP 2011-16705 A

 このように、ガラスロールの製造ラインにおいては、溶融ラインと加工ラインとが直交する向きに配置される。この場合、ガラスロールの製造ラインを並列に配置すると、加工ラインの分だけ溶融ライン間の距離を開けなくてはならず、設置スペース上の無駄が生じる。また、溶融ラインと加工ラインとが直交する位置関係しか採れないようだと、製造ラインのレイアウトが制限され、レイアウトを柔軟に変更することも難しい。 Thus, in the glass roll production line, the melting line and the processing line are arranged in a direction orthogonal to each other. In this case, if the production lines for the glass rolls are arranged in parallel, the distance between the melting lines must be increased by the amount corresponding to the processing lines, which wastes installation space. Further, if the melting line and the processing line seem to have only a perpendicular positional relationship, the layout of the manufacturing line is limited, and it is difficult to flexibly change the layout.

 上記問題を解決するための対策として、例えば図9及び図10に示すレイアウトが考えられる。このレイアウトにおいては、状態調整槽101は、図示しない均質化槽の下流側に位置し、成形体102は、状態調整槽101の下流側に位置している(図9を参照)。そして、均質化槽と状態調整槽101とが所定形状の接続管103(図10を参照)で接続されると共に、状態調整槽101と成形体102とが、所定の向きに曲がった形状をなす接続管104(図9を参照)で接続されている。この場合、状態調整槽101の流出口101aは下方を向いており(図9を参照)、この流出口101aに接続される接続管104が、この接続管104を平面視した状態で、状態調整槽101内への溶融ガラスGmの流入方向d0に対して直交する向きへと曲げられている(図10を参照)。このように、接続管104を曲げた構成とすることで、ガラスリボンGrの送り方向D0と、溶融ガラスGmの流れ方向(状態調整槽101内部への溶融ガラスGmの流入方向d0)とが平行になるので、溶融ラインと加工ラインとを平行に配置することが可能となる。なお、図9及び図10中、符号101bは状態調整槽101の流入口、符号102aは成形体102の流入口、符号Gr1,Gr2は成形されるガラスリボンGrの幅方向両端部を示している。 レ イ ア ウ ト As a measure for solving the above problem, for example, a layout shown in FIGS. 9 and 10 can be considered. In this layout, the condition adjusting tank 101 is located downstream of a not-shown homogenizing tank, and the molded body 102 is located downstream of the condition adjusting tank 101 (see FIG. 9). Then, the homogenizing tank and the condition adjusting tank 101 are connected by a connection pipe 103 having a predetermined shape (see FIG. 10), and the condition adjusting tank 101 and the molded body 102 have a shape bent in a predetermined direction. They are connected by a connection pipe 104 (see FIG. 9). In this case, the outlet 101a of the condition adjusting tank 101 faces downward (see FIG. 9), and the connecting pipe 104 connected to the outlet 101a adjusts the state of the connecting pipe 104 in a plan view. It is bent in a direction orthogonal to the inflow direction d0 of the molten glass Gm into the tank 101 (see FIG. 10). In this manner, by bending the connection pipe 104, the feeding direction D0 of the glass ribbon Gr and the flow direction of the molten glass Gm (inflow direction d0 of the molten glass Gm into the inside of the condition adjusting tank 101) are parallel. Therefore, the melting line and the processing line can be arranged in parallel. 9 and 10, reference numeral 101b indicates an inlet of the condition adjusting tank 101, reference numeral 102a indicates an inlet of the molded body 102, and reference numerals Gr1 and Gr2 indicate both ends in the width direction of the glass ribbon Gr to be formed. .

 ところで、上述した溶融ラインを備えた製造ラインを稼働した場合、成形体102に至るまでの各槽(例えば図11に示す均質化槽105や状態調整槽101)内に溶融ガラスGmの停滞領域R1,R2が生じることがある。これら停滞領域R1,R2内の溶融ガラスGm1’,Gm2’は、停滞領域R1,R2を通過することなく成形体102に至った溶融ガラスGmと、異なる温度履歴を経ているため、異質となり易い。従来構成の溶融ラインであれば、図12に示すように、停滞領域R1,R2内の溶融ガラスGm1’,Gm2’は、状態調整槽101の下方から接続管106を流れて、成形体102の流入口102aの上部又は下部を通過し、成形品であるガラスリボンGrの幅方向両端部Gr1,Gr2となる。ガラスリボンGrの幅方向両端部Gr1,Gr2は、通常、その後の加工ラインにおいて切断等により除去されるため、異質な溶融ガラスGm1’,Gm2’が最終製品内に残ることもなく特に問題はない。これに対して、上記提案の溶融ライン(図9及び図10を参照)の場合、接続管104を、下方から、状態調整槽101への溶融ガラスGmの流入方向d0に対して直交する向きへと曲げているため、図11及び図13に示すように、停滞領域R1,R2の溶融ガラスGm1’,Gm2’は、接続管104のうち従来構成の溶融ラインにおいて流れる部分(図12)とは異なる部分を流れ、成形体102の流入口102aのうち上下方向の中間部を通過し、成形体8内に流入する。そのため、これら停滞領域R1,R2の溶融ガラスGm1’,Gm2’は、図13に示すように、ガラスリボンGrの幅方向両端部Gr1,Gr2の間に位置する製品部分に混入し、加工後のガラスリボンGr(すなわち、製品としてのガラスロールやガラス板)に異質な溶融ガラスGm1’,Gm2’が残り、製品不良を発生させる。 By the way, when the production line provided with the above-mentioned melting line is operated, the stagnation region R1 of the molten glass Gm is placed in each of the tanks (for example, the homogenizing tank 105 and the condition adjusting tank 101 shown in FIG. 11) up to the compact 102. , R2 may occur. The molten glass Gm1 'and Gm2' in the stagnation regions R1 and R2 are likely to be different from the molten glass Gm that has reached the molded body 102 without passing through the stagnation regions R1 and R2 because they have different temperature histories. In the case of a conventional melting line, as shown in FIG. 12, the molten glass Gm1 ′ and Gm2 ′ in the stagnation regions R1 and R2 flow through the connecting pipe 106 from below the condition adjusting tank 101, and The glass ribbon Gr passes through the upper or lower part of the inflow port 102a and becomes both ends Gr1 and Gr2 in the width direction of the glass ribbon Gr as a molded product. Since both ends Gr1 and Gr2 in the width direction of the glass ribbon Gr are usually removed by cutting or the like in a subsequent processing line, there is no particular problem without the foreign molten glass Gm1 ′ and Gm2 ′ remaining in the final product. . On the other hand, in the case of the melting line proposed above (see FIGS. 9 and 10), the connecting pipe 104 is moved from below in a direction orthogonal to the flowing direction d0 of the molten glass Gm into the conditioning tank 101. As shown in FIGS. 11 and 13, the molten glass Gm1 ′, Gm2 ′ in the stagnation regions R1, R2 is different from the portion (FIG. 12) of the connecting pipe 104 flowing in the conventional melting line. It flows through a different portion, passes through an intermediate portion in the vertical direction of the inlet 102 a of the molded body 102, and flows into the molded body 8. Therefore, as shown in FIG. 13, the molten glass Gm1 ′ and Gm2 ′ of the stagnation regions R1 and R2 are mixed into the product portion located between both ends Gr1 and Gr2 in the width direction of the glass ribbon Gr and processed. Foreign glass melts Gm1 'and Gm2' remain on the glass ribbon Gr (that is, a glass roll or a glass plate as a product), causing a product defect.

 以上の事情に鑑み、本明細書では、溶融ラインで生じ得る異質な溶融ガラスがガラスリボンの製品部分に残る事態を防止しつつ、ガラス物品の製造ラインのレイアウトに関する自由度を高めることを、解決すべき技術課題とする。 In view of the above circumstances, the present specification solves the problem of increasing the degree of freedom regarding the layout of a manufacturing line of glass articles while preventing a situation in which a foreign molten glass that may be generated in a melting line remains in a product portion of a glass ribbon. It is a technical task to be done

 前記課題の解決は、本発明に係るガラス物品の製造方法により達成される。すなわち、この製造方法は、溶融ガラス生成装置で溶融ガラスを生成する生成工程と、生成した溶融ガラスの状態を状態調整槽で調整する状態調整工程と、状態の調整が成された溶融ガラスを成形体に供給してガラスリボンを成形する成形工程とを備える、ガラス物品の製造方法において、状態調整槽に設けられた溶融ガラスの流入口に、溶融ガラス生成装置の側から状態調整槽の内部に溶融ガラスを流入させるための流入管が接続され、溶融ガラスの流れ方向上流側となる流入管の一端を通過する際の溶融ガラスの流れ方向を基準流れ方向とし、流入管の他端から状態調整槽の内部に流入する際の溶融ガラスの流れ方向を流入時流れ方向としたとき、流入管を平面視した状態で、流入時流れ方向が基準流れ方向に対して左右何れか一方の側を向くように、流入管が曲がっている点をもって特徴付けられる。 の The solution to the above-mentioned problem is achieved by the method for manufacturing a glass article according to the present invention. In other words, this manufacturing method includes forming a molten glass in a molten glass generating apparatus, forming a molten glass in a state adjusting tank, and adjusting a state of the generated molten glass in a state adjusting tank. And a forming step of forming a glass ribbon by supplying the molten glass to the body, in the method of manufacturing a glass article, the molten glass inflow port provided in the conditioning tank, from the side of the molten glass generating device into the conditioning tank. An inflow pipe for inflow of the molten glass is connected, and the flow direction of the molten glass when passing through one end of the inflow pipe on the upstream side in the flow direction of the molten glass is set as a reference flow direction, and the state is adjusted from the other end of the inflow pipe. When the flow direction of the molten glass when flowing into the inside of the tank is the flow direction at the time of inflow, the flow direction at the time of inflow is either one of the left and right sides with respect to the reference flow direction in a state where the inflow pipe is viewed in plan. As directed, characterized with a point where the inlet tube is bent.

 このように、本発明に係る製造方法では、状態調整槽の流入口に接続される流入管の形状に着目し、この流入管を平面視した状態で、溶融ガラスの流入時流れ方向(状態調整槽の内部に流入する際の溶融ガラスの流れ方向)が基準流れ方向(流入管の一端を通過する際の溶融ガラスの流れ方向)に対して左右何れか一方の側を向くように、当該流入管を曲げるようにした。このように、従来直線状をなしていた流入管を曲げることにより、仮に状態調整槽よりも上流側の層(均質化槽など)で溶融ガラスの停滞領域が生じたとしても、この停滞領域の溶融ガラスは、流入管の一端に流入した際の位置(例えば流入管の下部)を可及的に維持して、流入管の他端、すなわち状態調整槽の流入口に至る。従って、状態調整槽と成形体とを従来の態様で接続することにより、接続管内での溶融ガラスの相対位置を変化させることなく当該溶融ガラスは、成形体の流入口の上部又は下部を通過することになる。これにより、停滞領域の溶融ガラスが流れ込んできたとしても、当該溶融ガラスを、成形体により成形されるガラスリボンの幅方向両端部となる領域に流れ込ませることが可能となる。また、従来直線状をなしていた流入管を上述のように曲げることにより、流入管の下流端と接続される状態調整槽の流入口の向きは、溶融ガラスが溶融ガラス生成装置で生成された後、状態調整槽に至る間の流れ方向とは異なる向きとなる。よって、この状態調整槽内部に流入する際の流れ方向(流入時流れ方向)を調整することにより、成形体の流入口の向きを適宜設定することができる。以上より、本発明によれば、異質な溶融ガラスが加工後のガラスリボンに残って、製品の品質低下を招く事態を可及的に防止しつつ、製造ラインのレイアウトの自由度を高めることが可能となる。 As described above, in the manufacturing method according to the present invention, attention is paid to the shape of the inflow pipe connected to the inflow port of the conditioning tank. The inflow so that the flow direction of the molten glass when flowing into the inside of the tank is directed to one of the left and right sides with respect to the reference flow direction (the flow direction of the molten glass when passing through one end of the inflow pipe). The tube was bent. As described above, even if a stagnation region of the molten glass is generated in a layer (such as a homogenization tank) upstream of the condition adjusting tank by bending the inflow pipe which has been conventionally formed in a straight line, the stagnation area of the stagnation region is not changed. The molten glass reaches the other end of the inflow pipe, that is, the inflow port of the conditioning tank, while maintaining as much as possible the position (for example, the lower part of the inflow pipe) at the time of flowing into one end of the inflow pipe. Therefore, the molten glass passes through the upper or lower part of the inflow port of the molded body without changing the relative position of the molten glass in the connection pipe by connecting the condition adjusting tank and the molded body in a conventional manner. Will be. Thereby, even if the molten glass in the stagnant area flows in, the molten glass can be flowed into the regions at both ends in the width direction of the glass ribbon formed by the molded body. In addition, by bending the conventional inflow pipe that has been formed in a straight line as described above, the direction of the inflow port of the conditioning tank connected to the downstream end of the inflow pipe is such that molten glass is generated by the molten glass generation device. Later, the flow direction is different from the flow direction leading to the conditioning tank. Therefore, by adjusting the flow direction (flow direction at the time of inflow) when flowing into the inside of the condition adjusting tank, the direction of the inflow port of the molded body can be appropriately set. As described above, according to the present invention, it is possible to increase the degree of freedom in the layout of a production line while preventing as much as possible a situation in which a foreign molten glass remains on a glass ribbon after processing and causes a deterioration in product quality. It becomes possible.

 また、本発明に係る製造方法においては、状態調整槽の流出口と成形体の流入口とが接続管で接続され、接続管は、状態調整槽の流出口と同じ向きから、接続管を平面視した状態で流入時流れ方向と同じ向きに曲がっていてもよい。 Further, in the manufacturing method according to the present invention, the outlet of the condition adjusting tank and the inlet of the molded body are connected by a connecting pipe, and the connecting pipe is formed by flattening the connecting pipe from the same direction as the outlet of the condition adjusting tank. It may be bent in the same direction as the flow direction at the time of inflow when viewed.

 このように流入時流れ方向と同じ向きに曲がった接続管で、状態調整槽の流出口と成形体の流入口とを接続することによって、接続管内での溶融ガラスの相対位置を維持して、成形体の流入口の上部又は下部に溶融ガラスを供給することができる。よって、仮に停滞領域の溶融ガラスが流入管を通じて状態調整槽に流れ込んできたとしても、当該停滞領域の溶融ガラスは、流入管の一端に流入した際の位置(例えば流入管内部空間の下部)を維持して状態調整槽の流入口に至り、かつ接続管内でもその相対位置を維持したまま成形体の流入口(この場合、流入口の下部)に至る。これにより、停滞領域の溶融ガラスが流れ込んできたとしても、この好ましくない溶融ガラスがガラスリボンの製品部分に混入する事態を確実に防止することが可能となる。 By connecting the outlet of the conditioning tank and the inlet of the molded body with the connecting pipe bent in the same direction as the flow direction at the time of inflow, the relative position of the molten glass in the connecting pipe is maintained, Molten glass can be supplied to the upper or lower part of the inlet of the molded body. Therefore, even if the molten glass in the stagnation area flows into the condition adjusting tank through the inflow pipe, the molten glass in the stagnation area is located at the position (for example, the lower part of the inflow pipe internal space) when it flows into one end of the inflow pipe. It is maintained to reach the inlet of the conditioning tank, and also to the inlet of the molded body (in this case, the lower part of the inlet) while maintaining its relative position in the connection pipe. Thus, even if the molten glass in the stagnant area flows in, it is possible to reliably prevent the undesirable molten glass from being mixed into the product part of the glass ribbon.

 また、本発明に係る製造方法においては、流入管は、流入管を平面視した状態で、流入管の一端側から基準流れ方向に対して左右他方の側に傾斜した状態で直線状に伸びるストレート部と、ストレート部の下流端から流入時流れ方向へと曲がって、状態調整槽の流入口に接続される曲げ部とを有するものであってもよい。 Further, in the manufacturing method according to the present invention, the inflow pipe extends straight from the one end side of the inflow pipe to the other right and left sides with respect to the reference flow direction in a state where the inflow pipe is viewed in plan. And a bent portion bent from the downstream end of the straight portion in the flow direction at the time of inflow and connected to the inflow port of the conditioning tank.

 上述のように、流入管にその一端側から基準流れ方向に対して左右他方の側に傾斜した状態で直線状に伸びるストレート部を設けると共に、このストレート部の下流端から流入時流れ方向へと曲がって成形体の流入口に接続される曲げ部とを設けることで、基準流れ方向に対する曲げ部の曲げ方向(左右一方の側)とは左右逆向きにストレート部が傾斜した状態となる(後述する図3等を参照)。よって、流入管の一端側から曲げ部の上流端までの管長さを短くすることができる。 As described above, the inflow pipe is provided with a straight portion that extends linearly from one end of the inflow pipe to the other side on the left and right sides with respect to the reference flow direction, and from the downstream end of the straight section to the flow direction during inflow. By providing a bent portion that is bent and connected to the inlet of the molded body, the straight portion is inclined in the right and left opposite directions to the bending direction (one of the left and right sides) of the bent portion with respect to the reference flow direction (described later). 3 etc.). Therefore, the length of the pipe from one end of the inflow pipe to the upstream end of the bent portion can be reduced.

 また、本発明に係る製造方法においては、成形体は、オーバーフロー溝から溢れ出た溶融ガラスを両側面に沿って流下させることでガラスリボンを成形するもので、成形体の流入口は、両側面の向きに対して直交する向きに設けられ、かつ基準流れ方向と流入時流れ方向とがなす角度が90°に設定されてもよい。また、本発明に係る製造方法においては、ガラス物品は、ガラスリボンをロール状に巻き取ってなるガラスロールであってもよい。 Further, in the production method according to the present invention, the molded article is a method of molding a glass ribbon by causing molten glass overflowing from the overflow groove to flow down along both sides, and the inlet of the molded article is formed on both sides. And the angle between the reference flow direction and the inflow flow direction may be set to 90 °. In the manufacturing method according to the present invention, the glass article may be a glass roll formed by winding a glass ribbon into a roll.

 上述のように構成した成形体に、上述のように曲げた形態をなす流入管(あるいは曲げ部)を接続することによって、基準流れ方向と、成形体により成形されるガラスリボンの主表面の向き(法線方向)とを一致させることができる。ガラスロールの製造工程では、成形されたガラスリボンは、下方に引き出された後、カテナリを介して水平方向に方向転換して搬送されるので、上記構成によれば、溶融ラインと、加工ラインとを平行に配置することができる。これにより、ガラスロールの製造ラインをその幅方向(溶融ラインにおいてはその短手方向と同じ向きをいい、加工ラインにおいてはガラスリボンの幅方向をいう。以下、本明細書において同じ。)に狭めることができるので、ガラスロールの製造ラインを並列に複数配置する場合に好適である。 By connecting the inflow pipe (or bent portion) having the bent shape as described above to the molded body configured as described above, the reference flow direction and the orientation of the main surface of the glass ribbon molded by the molded body are connected. (In the normal direction). In the manufacturing process of the glass roll, the formed glass ribbon is drawn downward, and then turned and transported in the horizontal direction via the catenary.According to the above configuration, the melting line, the processing line, Can be arranged in parallel. As a result, the production line of the glass roll is narrowed in the width direction (the same direction as the short direction in the melting line, and the width direction of the glass ribbon in the processing line; hereinafter the same in the present specification). This is suitable when a plurality of glass roll production lines are arranged in parallel.

 また、前記課題の解決は、本発明に係るガラス物品の製造装置によっても達成される。すなわち、この製造装置は、溶融ガラスを生成する溶融ガラス生成装置と、生成した溶融ガラスの状態を調整する状態調整槽と、状態の調整が成された溶融ガラスをガラスリボンに成形する成形体とを備えるガラス物品の製造装置において、状態調整槽に設けられた溶融ガラスの流入口に、溶融ガラス生成装置の側から状態調整槽の内部に溶融ガラスを流入させるための流入管が接続され、溶融ガラスの流れ方向上流側となる流入管の一端を通過する際の溶融ガラスの流れ方向を基準流れ方向とし、流入管の他端から状態調整槽の内部に流入する際の溶融ガラスの流れ方向を流入時流れ方向としたとき、流入管を平面視した状態で、流入時流れ方向が基準流れ方向に対して左右何れか一方の側を向くように、流入管が曲がっている点をもって特徴付けられる。 解決 In addition, the solution of the above-mentioned problems is also achieved by the apparatus for manufacturing a glass article according to the present invention. That is, this manufacturing apparatus includes a molten glass generating apparatus that generates molten glass, a state adjusting tank that adjusts the state of the generated molten glass, and a molded body that forms the molten glass whose state has been adjusted into a glass ribbon. In a glass article manufacturing apparatus comprising: an inflow pipe for flowing molten glass from the side of the molten glass producing device into the inside of the conditioning glass, to an inlet of the molten glass provided in the conditioning glass, The flow direction of the molten glass when passing through one end of the inflow pipe on the upstream side in the flow direction of the glass is defined as the reference flow direction, and the flow direction of the molten glass when flowing into the inside of the condition adjusting tank from the other end of the inflow pipe is defined as the flow direction. When the flow direction at the time of inflow is set, the point at which the flow direction of the inflow pipe is bent is such that the flow direction at the time of inflow is directed to one of the left and right sides with respect to the reference flow direction in a state where the inflow pipe is viewed in plan. Attached butterflies.

 このように、本発明に係る製造装置においても、従来直線状をなしていた流入管を曲げることにより、仮に状態調整槽よりも上流側の層で溶融ガラスの停滞領域が生じたとしても、この停滞領域の溶融ガラスは、流入管の一端に流入した際の位置を可及的に維持して、状態調整槽の流入口に至る。従って、状態調整槽と成形体とを従来の態様で接続することにより、接続管内での溶融ガラスの相対位置を変化させることなく成形体に供給することができる。これにより、停滞領域の溶融ガラスが流れ込んできたとしても、成形体の流入口の下部又は上部を通過して、当該溶融ガラスをガラスリボンの幅方向両端部となる領域に流れ込ませることが可能となる。また、従来直線状をなしていた流入管を上述のように曲げることにより、流入管の下流端と接続される状態調整槽の流入口の向きは、溶融ガラスが溶融ガラス生成装置で生成された後、状態調整槽に至る間の流れ方向とは異なる向きとなる。よって、この状態調整槽内部に流入する際の流れ方向を調整することにより、成形体の流入口の向きを適宜設定することができる。以上より、本発明によれば、異質な溶融ガラスが製品に残って、製品の品質低下を招く事態を可及的に防止しつつ、製造ラインのレイアウトの自由度を高めることが可能となる。 As described above, even in the manufacturing apparatus according to the present invention, even if a stagnation region of the molten glass is generated in the layer on the upstream side of the conditioning tank by bending the inflow pipe that has been conventionally formed linearly, The molten glass in the stagnant region reaches the inlet of the condition adjusting tank while maintaining as much as possible the position of the molten glass at one end of the inflow pipe. Therefore, by connecting the condition adjusting tank and the compact in a conventional manner, the molten glass can be supplied to the compact without changing the relative position of the molten glass in the connection pipe. Thereby, even if the molten glass in the stagnation region flows in, it is possible to pass the lower or upper portion of the inflow port of the molded body, and to flow the molten glass into regions that are both ends in the width direction of the glass ribbon. Become. In addition, by bending the conventional inflow pipe that has been formed in a straight line as described above, the direction of the inflow port of the conditioning tank connected to the downstream end of the inflow pipe is such that molten glass is generated by the molten glass generation device. Later, the flow direction is different from the flow direction leading to the conditioning tank. Therefore, by adjusting the flow direction when flowing into the inside of the condition adjusting tank, the direction of the inlet of the molded body can be appropriately set. As described above, according to the present invention, it is possible to increase the degree of freedom in the layout of a production line while preventing a situation in which a foreign molten glass remains in a product and causes deterioration in product quality as much as possible.

 以上に述べたように、本発明によれば、溶融ラインで生じ得る異質な溶融ガラスがガラスリボンの製品部分に残る事態を防止しつつ、ガラス物品の製造ラインのレイアウトに関する自由度を高めることが可能となる。 As described above, according to the present invention, it is possible to increase the degree of freedom regarding the layout of a glass article manufacturing line while preventing a situation in which a foreign molten glass that may be generated in a melting line remains in a product portion of a glass ribbon. It becomes possible.

本発明の一実施形態に係るガラス物品の製造装置の要部を正面から見た図である。It is the figure which looked at the principal part of the manufacturing device of the glass article concerning one embodiment of the present invention from the front. 図1に示す製造装置の要部を平面視した図である。FIG. 2 is a plan view of a main part of the manufacturing apparatus shown in FIG. 1. 図1に示す第三の接続管及びその周辺部を平面視した図である。It is the figure which looked at the 3rd connection pipe shown in FIG. 1, and its peripheral part from top view. 図1に示す第三の接続管及びその周辺部をY方向から見た側面図である。It is the side view which looked at the 3rd connection pipe shown in FIG. 1, and its peripheral part from the Y direction. 図3に示す第三の接続管及びその周辺部を正面から見た図である。It is the figure which looked at the 3rd connection pipe shown in FIG. 3, and its peripheral part from the front. 図1に示す製造装置において、停滞領域の溶融ガラスが成形体内部に至るまでの流れを模式的に描いた正面図である。FIG. 2 is a front view schematically illustrating a flow of molten glass in a stagnant region to the inside of a molded body in the manufacturing apparatus illustrated in FIG. 1. 図6に示す第三の接続管まわりの溶融ガラスの流れをY方向から見た側面図である。It is the side view which looked at the flow of the molten glass around the 3rd connection pipe shown in FIG. 6 from the Y direction. 本発明の他の実施形態に係るガラス物品の製造装置の要部を正面から見た図である。It is the figure which looked at the principal part of the manufacturing device of the glass article concerning other embodiments of the present invention from the front. 本発明との比較に用いるガラス物品の製造装置の要部を側面視した図であって、状態調整槽と成形体とを接続する接続管をY方向から見た側面図である。It is the figure which looked at the principal part of the manufacturing apparatus of the glass article used for comparison with this invention from the side, and was the side view which looked at the connection pipe which connects a condition adjustment tank and a molded object from the Y direction. 図9に示す接続管及びその周辺部を平面視した図である。It is the figure which looked at the connecting pipe shown in FIG. 9 and its periphery from top. 図10に示す接続管を備えたガラス物品の製造装置において、停滞領域の溶融ガラスが成形体内部に至るまでの流れを模式的に描いた正面図である。FIG. 11 is a front view schematically illustrating a flow of molten glass in a stagnant region to the inside of a molded product in the apparatus for manufacturing a glass article provided with the connection pipe illustrated in FIG. 10. 従来構成に係るガラス物品の製造装置において、停滞領域の溶融ガラスが成形体内部に至るまでの流れを模式的に描いた正面図である。It is the front view which drawn typically the flow until the molten glass of the stagnation area reaches the inside of a molded object in the manufacturing device of the glass article concerning the conventional composition. 図11に示す停滞領域の溶融ガラスの流れをY方向から見た側面図である。It is the side view which looked at the flow of the molten glass of the stagnation area shown in Drawing 11 from the Y direction.

 以下、本発明の一実施形態を図1~図7に基づいて説明する。 Hereinafter, an embodiment of the present invention will be described with reference to FIGS.

 図1は、本実施形態に係るガラス物品の製造装置1を正面から見た図、図2は、同じガラス物品の製造装置1を平面視した図である。これらの図に示すように、この製造装置1は、大別して溶融ガラスGmが流れる溶融ライン2と、溶融ライン2で成形されたガラスリボンGrの加工ライン3とを備える。このうち、溶融ライン2は、最上流域に配置された溶融ガラス生成装置としての溶解槽4と、溶解槽4の下流側に配設される清澄槽5と、清澄槽5の下流側に配設される均質化槽6と、均質化槽6の下流側に配設される状態調整槽7と、状態調整槽7の下流側に配設される成形体8と、各槽4~7、及び成形体8の間を接続する接続管9~12とを備える。 FIG. 1 is a front view of a glass article manufacturing apparatus 1 according to the present embodiment, and FIG. 2 is a plan view of the same glass article manufacturing apparatus 1. As shown in these drawings, the manufacturing apparatus 1 includes a melting line 2 through which a molten glass Gm flows, and a processing line 3 for a glass ribbon Gr formed by the melting line 2. Among these, the melting line 2 is a melting tank 4 serving as a molten glass generating device arranged in the uppermost stream area, a refining tank 5 disposed downstream of the melting tank 4, and disposed downstream of the refining tank 5. A homogenizing tank 6, a conditioning tank 7 disposed downstream of the homogenizing tank 6, a molded body 8 disposed downstream of the conditioning tank 7, and respective tanks 4 to 7, and Connection pipes 9 to 12 for connecting between the molded bodies 8 are provided.

 また、ガラスリボンGrの加工ライン3は、例えば、何れも図示は省略するが、成形体8の下方に位置し、成形体8で成形したガラスリボンGrに徐冷処理を施す徐冷処理部と、徐冷処理が施されたガラスリボンGrを所定の温度、例えば室温付近にまで冷却する冷却部と、冷却後のガラスリボンGrの送り方向を縦方向から横方向に転換する方向転換部と、横方向に搬送されるガラスリボンGrの幅方向両端部(耳部ともいう)をガラスリボンGr本体から切り離す第一切断部と、幅方向両端部が除去されたガラスリボンGrを幅方向に沿って切断する第二切断部と、第二切断部を通過したガラスリボンGrをロール状に巻取る巻取り部とを備える。もちろん、上述の構成は一例にすぎず、上述した構成要素の一部を変更、省略してもよく、あるいは上記以外の構成要素を必要に応じて追加してもよい。以下、溶融ライン2について、均質化槽6と状態調整槽7との接続態様を中心に説明する。 Further, the processing line 3 for the glass ribbon Gr, for example, although not shown, is located below the molded body 8, and is provided with a slow cooling processing unit that performs a slow cooling process on the glass ribbon Gr formed by the molded body 8. A cooling unit that cools the glass ribbon Gr that has been subjected to the slow cooling process to a predetermined temperature, for example, around room temperature, and a direction change unit that changes the feeding direction of the cooled glass ribbon Gr from the vertical direction to the horizontal direction, The first cutting portion for separating both ends (also called ears) in the width direction of the glass ribbon Gr conveyed in the lateral direction from the glass ribbon Gr main body, and the glass ribbon Gr with both ends in the width direction removed along the width direction. A second cutting unit for cutting and a winding unit for winding the glass ribbon Gr that has passed through the second cutting unit into a roll shape are provided. Of course, the above-described configuration is merely an example, and some of the above-described components may be changed or omitted, or components other than the above may be added as necessary. Hereinafter, the melting line 2 will be described focusing on the connection between the homogenizing tank 6 and the condition adjusting tank 7.

 溶解槽4は、投入されたガラス原料を溶解して、溶融ガラスGmを生成する生成工程を行うための容器である。溶解槽4は、第一の接続管9によって清澄槽5に接続されている。 (4) The melting tank 4 is a container for performing a generation process of melting the charged glass raw material to generate the molten glass Gm. The dissolution tank 4 is connected to the fining tank 5 by a first connection pipe 9.

 清澄槽5は、第一の接続管9を介して溶解槽4から供給された溶融ガラスGmを清澄剤等の働きにより清澄する清澄工程を行うための容器である。清澄槽5は、第二の接続管10によって均質化槽6に接続されている。 The refining tank 5 is a container for performing a refining step of refining the molten glass Gm supplied from the melting tank 4 through the first connection pipe 9 by the action of a refining agent or the like. The fining tank 5 is connected to the homogenizing tank 6 by a second connection pipe 10.

 均質化槽6は、清澄された溶融ガラスGmを撹拌し、均一化する均質化工程を行うための容器である。均質化槽6は、第三の接続管11によって状態調整槽7に接続されている。なお、均質化槽6は、図示のように一つであってもよいし、二つ以上並べて配設してもよい。 (4) The homogenizing tank 6 is a container for performing a homogenizing step of stirring and homogenizing the clarified molten glass Gm. The homogenizing tank 6 is connected to the condition adjusting tank 7 by a third connection pipe 11. The number of the homogenizing tanks 6 may be one as shown in the figure, or two or more may be arranged side by side.

 状態調整槽7は、溶融ガラスGmを成形に適した状態に調整する状態調整工程を行うための容器であり、例えば成形体8に供給する溶融ガラスGmの流量を調整する。状態調整槽7は、本実施形態では、第三の接続管11が接続され、第三の接続管11から溶融ガラスGmが流入する上部7aと、状態の調整が成された溶融ガラスGmが流出する下部7bと、上部7aと下部7bとを繋ぐ中間部7cとを備える。上部7aの側面には、溶融ガラスGmを流入させるための流入口7dが設けられる。また、下部7bの下端には、溶融ガラスGmの流出口7eが設けられている。上記構成の状態調整槽7は、第四の接続管12によって成形体8に接続されている。 The condition adjusting tank 7 is a container for performing a state adjusting step of adjusting the molten glass Gm to a state suitable for molding, and adjusts, for example, a flow rate of the molten glass Gm supplied to the molded body 8. In this embodiment, the state adjusting tank 7 is connected to the third connection pipe 11, and the upper part 7 a into which the molten glass Gm flows from the third connection pipe 11, and the molten glass Gm whose state has been adjusted flows out. And an intermediate portion 7c connecting the upper portion 7a and the lower portion 7b. An inflow port 7d through which the molten glass Gm flows is provided on a side surface of the upper portion 7a. An outlet 7e for molten glass Gm is provided at the lower end of the lower portion 7b. The condition adjusting tank 7 having the above configuration is connected to the molded body 8 by the fourth connection pipe 12.

 成形体8は、溶融ガラスGmを所望の形状に成形する。本実施形態では、成形体8は、オーバーフローダウンドロー法によって溶融ガラスGmを帯状に成形する。詳細には、成形体8は、断面形状が略楔形状をなし、その上部にオーバーフロー溝8aを有すると共に、オーバーフロー溝8aから溢れ出た溶融ガラスGmを流下させる両側面8b,8bとを有する。上記構成に係る成形体8は、両側面8b,8bに沿って流下させた溶融ガラスGmを両側面8b,8bの下頂部で融合させ、帯状のガラスリボンGrに成形可能としている。成形されたガラスリボンGrは、例えば、厚みが0.01~2mm(好ましくは0.3mm以下)であって、液晶ディスプレイや有機ELディスプレイなどのフラットパネルディスプレイ、有機EL照明、太陽電池などの基板や保護カバーに利用される。なお、成形体8は、スロットダウンドロー法などの他のダウンドロー法を実行するものであってもよい。 The molded body 8 is for molding the molten glass Gm into a desired shape. In the present embodiment, the molded body 8 is formed by molding the molten glass Gm into a belt shape by an overflow down draw method. Specifically, the molded body 8 has a substantially wedge-shaped cross section, has an overflow groove 8a at an upper portion thereof, and has both side surfaces 8b, 8b through which the molten glass Gm overflowing from the overflow groove 8a flows. In the molded body 8 according to the above configuration, the molten glass Gm that has flowed down along the side surfaces 8b, 8b is fused at the lower apexes of the side surfaces 8b, 8b, and can be formed into a belt-shaped glass ribbon Gr. The formed glass ribbon Gr has a thickness of, for example, 0.01 to 2 mm (preferably 0.3 mm or less), and is a substrate for a flat panel display such as a liquid crystal display or an organic EL display, an organic EL lighting, a solar cell, or the like. And used for protective covers. The molded body 8 may execute another downdraw method such as a slot downdraw method.

 第一の接続管9~第四の接続管12は、例えば白金又は白金合金からなる円筒管で構成されており、溶解槽4から下流側に隣接する各槽5~7、並びに成形体8に溶融ガラスGmを順次搬送する。 The first connection pipe 9 to the fourth connection pipe 12 are each formed of a cylindrical pipe made of, for example, platinum or a platinum alloy, and are connected to the tanks 5 to 7 adjacent to the downstream side from the melting tank 4 and the molded body 8. The molten glass Gm is sequentially conveyed.

 図3は、均質化槽6と状態調整槽7とを接続する第三の接続管11及びその周辺部を平面視した図である。図3に示すように、第三の接続管11は、所定の向きに曲がった形状をなしている。この第三の接続管11が、本発明に係る流入管に相当する。本実施形態では、第三の接続管11は、第三の接続管11を平面視した状態で、直線状に伸びるストレート部13と、ストレート部13の下流端から所定の向きへと曲がって、状態調整槽7の流入口7aに接続される第一曲げ部14と、均質化槽6の流出口6aとストレート部13の上流端とを接続する第二曲げ部15とを有する。 FIG. 3 is a plan view of the third connection pipe 11 that connects the homogenization tank 6 and the condition adjustment tank 7 and a peripheral portion thereof. As shown in FIG. 3, the third connection pipe 11 has a shape bent in a predetermined direction. This third connection pipe 11 corresponds to the inflow pipe according to the present invention. In the present embodiment, the third connecting pipe 11 bends in a predetermined direction from the downstream end of the straight section 13 and the straight section 13 extending linearly in a state where the third connecting pipe 11 is viewed in plan, It has a first bent portion 14 connected to the inlet 7 a of the condition adjusting tank 7 and a second bent portion 15 connecting the outlet 6 a of the homogenizing tank 6 and the upstream end of the straight portion 13.

 また、第三の接続管11の上流端11aを通過する溶融ガラスGmの流れ方向(基準流れ方向d0)と、下流端11bを通過する溶融ガラスGmの流れ方向(流入時流れ方向d1)との関係でいえば、第三の接続管11は、図3に示すように第三の接続管11を平面視した状態で、基準流れ方向d0に対して流入時流れ方向d1が左右何れか一方の側を向くように、第三の接続管11が曲がっている。本実施形態では、X方向及びY方向は水平方向、Z方向は鉛直方向であり、基準流れ方向d0は、図3に示すように、鉛直上方から見た場合にはY方向を向いている。また、流入時流れ方向d1は、鉛直上方から見た場合にはX方向を向いている。以上より、基準流れ方向d0と流入時流れ方向d1とは、水平面となるXY平面上で互いに直交している。 The flow direction of the molten glass Gm passing through the upstream end 11a of the third connection pipe 11 (reference flow direction d0) and the flow direction of the molten glass Gm passing through the downstream end 11b (flow direction d1 during inflow). Speaking of the relationship, the third connection pipe 11 is configured such that the flow direction d1 at the time of inflow with respect to the reference flow direction d0 is either left or right in a state where the third connection pipe 11 is viewed in plan as shown in FIG. The third connecting pipe 11 is bent so as to face the side. In the present embodiment, the X direction and the Y direction are horizontal directions, and the Z direction is a vertical direction. As shown in FIG. 3, the reference flow direction d0 is in the Y direction when viewed from above vertically. The inflow flow direction d1 is in the X direction when viewed from vertically above. As described above, the reference flow direction d0 and the inflow flow direction d1 are orthogonal to each other on the XY plane that is the horizontal plane.

 また、本実施形態では、ストレート部13は、第三の接続管11の上流端11a側から基準流れ方向d0に対して左右他方の側に傾斜した状態で直線状に伸びている。これに対して、ストレート部13の下流端と接続される第一曲げ部14は、流入時流れ方向d1が基準流れ方向d0に対して左右一方の側を向くように曲がっている。本実施形態でいえば、ストレート部13が基準流れ方向d0に対して右方向(図3でいえば下方向)に傾斜した状態で直線状に伸びているのに対し、第一曲げ部14は、ストレート部13の延伸方向から、基準流れ方向d0に対して右方向(図3でいえば下方向)へと曲がっている。これにより、状態調整槽7は、図4に示すように、均質化槽6の流出口6aよりも-X方向の側(図4でいえば左側)にずれた位置にある。なお、ストレート部13は、図5に示すように、上流端側(左側)から下流端側(右側)に向かうにつれて+Z方向に移行するように、水平方向に対して所定の角度で上向きに傾斜している。よって、第一曲げ部14は第二曲げ部15よりも高い位置にある。 In the present embodiment, the straight portion 13 extends linearly from the upstream end 11a of the third connection pipe 11 in a state of being inclined to the other right and left sides with respect to the reference flow direction d0. On the other hand, the first bent portion 14 connected to the downstream end of the straight portion 13 is bent such that the inflow flow direction d1 faces one of the left and right sides with respect to the reference flow direction d0. In the present embodiment, while the straight portion 13 extends linearly while being inclined rightward (downward in FIG. 3) with respect to the reference flow direction d0, the first bent portion 14 , From the extending direction of the straight portion 13 to the right (downward in FIG. 3) with respect to the reference flow direction d0. As a result, as shown in FIG. 4, the condition adjusting tank 7 is at a position shifted from the outlet 6a of the homogenizing tank 6 in the −X direction (to the left in FIG. 4). As shown in FIG. 5, the straight portion 13 is inclined upward at a predetermined angle with respect to the horizontal direction so as to move in the + Z direction from the upstream end side (left side) to the downstream end side (right side). are doing. Therefore, the first bent portion 14 is at a position higher than the second bent portion 15.

 第四の接続管12は、状態調整槽7から流出した溶融ガラスGmを成形体8に供給可能なように、状態調整槽7と成形体8とを接続するもので、図3に示すように、状態調整槽7の流出口7eと同じ向きから流入時流れ方向d1と同じ向きへと曲がっている。本実施形態のように、状態調整槽7の下部7b(流出口7e)が鉛直下方を向いている場合、第四の接続管12は、図4に示すように、Z方向(鉛直方向)からX方向(水平方向)へと90°曲がっている。この場合、成形体8内部への溶融ガラスGmの流入方向d2と状態調整槽7内部への流入方向(流入時流れ方向d1)とは、互いに平行な関係にある。 The fourth connection pipe 12 connects the condition adjusting tank 7 and the molded body 8 so that the molten glass Gm flowing out of the condition adjusting tank 7 can be supplied to the molded body 8, and as shown in FIG. , From the same direction as the outflow port 7e of the condition adjusting tank 7 to the same direction as the inflow flow direction d1. When the lower portion 7b (outflow port 7e) of the condition adjusting tank 7 faces vertically downward as in this embodiment, the fourth connection pipe 12 is moved from the Z direction (vertical direction) as shown in FIG. It is bent 90 ° in the X direction (horizontal direction). In this case, the inflow direction d2 of the molten glass Gm into the molded body 8 and the inflow direction (inflow flow direction d1) into the condition adjusting tank 7 are parallel to each other.

 次に、上記構成の製造装置1を用いたガラス物品の製造方法の一例を、特に均質化槽6から成形体8に至る溶融ガラスGmの流れ態様を中心に説明する。 Next, an example of a method for manufacturing a glass article using the manufacturing apparatus 1 having the above-described configuration will be described, particularly focusing on the flow mode of the molten glass Gm from the homogenization tank 6 to the molded body 8.

 上記構成をなす製造装置1を用いてガラス物品を製造するに際しては、図1及び図2に示すように、まずガラス原料を溶融ライン2の最上流域に位置する溶解槽4に投入して、ガラス原料を溶解することで、溶融ガラスGmを生成する。次いで溶融ガラスGmを第一の接続管9を介して清澄槽5に供給し、清澄槽5で清澄した溶融ガラスGmを第二の接続管10を介して均質化槽6に供給する。均質化槽6に供給された溶融ガラスGmは撹拌等により均質化された後、第三の接続管11を通って状態調整槽7に供給される。状態調整槽7内で例えば流量を調整した溶融ガラスGmが第四の接続管12を通って成形体8に供給される。成形体8では、例えばオーバーフローダウンドロー法によって溶融ガラスGmを帯状のガラスリボンGrに成形する。成形されたガラスリボンGrは、溶融ライン2と平行に延在する加工ライン3上を搬送され、切断など上述した適宜の加工ないし処理を施すことにより、例えばガラスロールが得られる。このようにして、ガラス物品の製造が連続的に実施される。 When manufacturing a glass article using the manufacturing apparatus 1 having the above configuration, first, as shown in FIGS. 1 and 2, a glass raw material is charged into a melting tank 4 located at the uppermost stream area of a melting line 2, By melting the raw materials, molten glass Gm is generated. Next, the molten glass Gm is supplied to the fining tank 5 via the first connection pipe 9, and the molten glass Gm clarified in the fining tank 5 is supplied to the homogenization tank 6 via the second connection pipe 10. The molten glass Gm supplied to the homogenizing tank 6 is homogenized by stirring or the like, and then supplied to the condition adjusting tank 7 through the third connection pipe 11. The molten glass Gm whose flow rate has been adjusted, for example, in the condition adjusting tank 7 is supplied to the molded body 8 through the fourth connection pipe 12. In the molded body 8, the molten glass Gm is formed into a strip-shaped glass ribbon Gr by, for example, an overflow down draw method. The formed glass ribbon Gr is conveyed on a processing line 3 extending in parallel with the melting line 2 and subjected to the above-described appropriate processing or processing such as cutting, thereby obtaining, for example, a glass roll. In this way, the production of glass articles is performed continuously.

 ところで、上記構成の製造装置1でガラス物品を連続的に製造する場合、例えば図6に示すように、均質化槽6の底部に溶融ガラスGmの停滞領域R1が生じることがある。この場合、停滞領域R1の溶融ガラスGm1’は均質化槽6の流出口6aから第三の接続管11の上流端11aの下部に流入する。あるいは、同じく図6に示すように、状態調整槽7の頂部(上部7aのうち流入口7dよりも上方の領域)に溶融ガラスGmの停滞領域R2が生じることがある。この場合、停滞領域R2の溶融ガラスGm2’は流出口7eの成形体8に近い側(XYZ座標系でいえば+X方向の側)を通って第四の接続管12の上流端に流入する。 In the meantime, when glass articles are continuously manufactured by the manufacturing apparatus 1 having the above-described configuration, a stagnation region R1 of the molten glass Gm may be generated at the bottom of the homogenization tank 6, as shown in FIG. 6, for example. In this case, the molten glass Gm <b> 1 ′ in the stagnation region R <b> 1 flows from the outlet 6 a of the homogenization tank 6 to a lower portion of the upstream end 11 a of the third connection pipe 11. Alternatively, as shown in FIG. 6, a stagnant region R2 of the molten glass Gm may be formed at the top of the condition adjusting tank 7 (region of the upper part 7a above the inlet 7d). In this case, the molten glass Gm2 'in the stagnation region R2 flows into the upstream end of the fourth connection pipe 12 through the side of the outlet 7e close to the formed body 8 (the side in the + X direction in the XYZ coordinate system).

 ここで、本発明に係る製造装置1では、第三の接続管11を平面視した状態で、溶融ガラスGmの流入時流れ方向d1が基準流れ方向d0に対して左右何れか一方の側を向くように、流入管としての第三の接続管11を曲げるようにした(図3を参照)。このように第三の接続管11を曲げることにより、図6に示すように均質化槽6で溶融ガラスGmの停滞領域R1が生じたとしても、この停滞領域R1の溶融ガラスGm1’は、第三の接続管11の上流端11aに流入した際の位置を可及的に維持して(ここでは上流端11aの下部、第二曲げ部15の下部15a、ストレート部13の下部13a、第一曲げ部14の下部14a、そして下流端11bの下部を通って)、状態調整槽7の流入口7dに至る。また、状態調整槽7と成形体8とを図4に示すように曲がった形態の第四の接続管12で接続することにより、停滞領域R1の溶融ガラスGm1’は、図7に示すように状態調整槽7の流出口7eのうちで成形体8から遠い側(XYZ座標系でいえば-X方向の側)から第四の接続管12の曲げ部の外側12aを通って成形体8の流入口8cの下部を通過する。あるいは、状態調整槽7の頂部に溶融ガラスGmの停滞領域R2が生じたとしても、この停滞領域R2の溶融ガラスGm2’は、状態調整槽7の流出口7eのうちで成形体8に近い側(XYZ座標系でいえば+X方向の側)から第四の接続管12の曲げ部の内側12bを通って成形体8の流入口8cの上部を通過する。上述のようにして成形体8の流入口8cを通過した各停滞領域R1,R2の溶融ガラスGm1’,Gm2’は、ガラスリボンGrの幅方向両端部Gr1,Gr2となる領域に流れ込む(図7を参照)。 Here, in the manufacturing apparatus 1 according to the present invention, the flow direction d1 at the time of inflow of the molten glass Gm faces either the left or right with respect to the reference flow direction d0 in a state where the third connection pipe 11 is viewed in a plan view. Thus, the third connection pipe 11 as the inflow pipe was bent (see FIG. 3). Even if the stagnation region R1 of the molten glass Gm is generated in the homogenization tank 6 as shown in FIG. 6 by bending the third connection pipe 11, the molten glass Gm1 ′ of the stagnation region R1 becomes The position at the time of flowing into the upstream end 11a of the three connection pipes 11 is maintained as much as possible (here, the lower part of the upstream end 11a, the lower part 15a of the second bent part 15, the lower part 13a of the straight part 13, the first part 13a, (Through the lower portion 14a of the bent portion 14 and the lower portion of the downstream end 11b) to reach the inlet 7d of the conditioning tank 7. Further, by connecting the condition adjusting tank 7 and the molded body 8 with the fourth connection pipe 12 having a bent form as shown in FIG. 4, the molten glass Gm1 ′ in the stagnation region R1 becomes as shown in FIG. Out of the outlet 7e of the condition adjusting tank 7, from the side farther from the formed body 8 (the −X direction side in the XYZ coordinate system), the outer side 12a of the bent portion of the fourth connecting pipe 12 passes through the outer side 12a of the formed body 8 It passes below the inflow port 8c. Alternatively, even if a stagnant region R2 of the molten glass Gm occurs at the top of the condition adjusting tank 7, the molten glass Gm2 'of the stagnant region R2 is closer to the molded body 8 in the outlet 7e of the condition adjusting tank 7. From the (in the XYZ coordinate system, the side in the + X direction) passes through the inside 12b of the bent portion of the fourth connection pipe 12, and passes above the inlet 8c of the molded body 8. The molten glass Gm1 ′, Gm2 ′ in each of the stagnant regions R1, R2 that has passed through the inlet 8c of the molded body 8 as described above flows into the regions that will be both ends Gr1, Gr2 in the width direction of the glass ribbon Gr (FIG. 7). See).

 このように、本発明によれば、第三の接続管11内に流入した際の停滞領域R1の溶融ガラスGm1’の位置を第三の接続管11の下部、並びに第四の接続管12の曲げ部の外側12aで可及的に維持して、成形体8の流入口8cの下部を通過させることができる。また、第四の接続管12内に流入した際の停滞領域R2の溶融ガラスGm2’の位置を第四の接続管12の曲げ部の内側12bで可及的に維持して、成形体8の流入口8cの上部を通過させることができる。従って、これら異質な溶融ガラスGm1’,Gm2’が加工後のガラスリボンGrに残って、製品(加工後のガラスリボンGr)の品質が低下する事態を可及的に防止することが可能となる。また、第三の接続管11の曲げ方向については、第三の接続管11を平面視した状態で基準流れ方向d0に対して左右何れかの向きであればよいため、曲げ後の方向、すなわち、状態調整槽7の流入口7dの向き(流入時流れ方向d1)を適宜設定することにより、成形体8の流入口8cの向き、ひいては成形体8で成形されるガラスリボンGrの送り方向D0(すなわち加工ライン3の向き)を比較的自由に設定することが可能となる。 As described above, according to the present invention, the position of the molten glass Gm1 ′ in the stagnant region R1 when flowing into the third connection pipe 11 is set to the lower part of the third connection pipe 11 and the position of the fourth connection pipe 12 It is possible to pass through the lower part of the inlet 8c of the molded body 8 while maintaining as much as possible on the outside 12a of the bent portion. Further, the position of the molten glass Gm2 ′ in the stagnation region R2 when flowing into the fourth connection pipe 12 is maintained as much as possible inside the bent portion 12b of the fourth connection pipe 12, and It can pass through the upper part of the inflow port 8c. Therefore, it is possible to prevent as much as possible such a situation that these different molten glasses Gm1 ′ and Gm2 ′ remain on the processed glass ribbon Gr and the quality of the product (the processed glass ribbon Gr) is reduced. . Further, the bending direction of the third connection pipe 11 may be any one of the left and right directions with respect to the reference flow direction d0 in a state where the third connection pipe 11 is viewed in a plan view. By appropriately setting the direction of the inflow port 7d (flow direction d1 during inflow) of the condition adjusting tank 7, the direction of the inflow port 8c of the molded body 8, and thus the feeding direction D0 of the glass ribbon Gr formed by the molded body 8 are set. (That is, the direction of the processing line 3) can be set relatively freely.

 また、本実施形態では、成形体8の流入口8cを、上部のオーバーフロー溝8aから溢れ出た溶融ガラスGmを流下させる両側面8b,8bに対して直交する向きに設けると共に、基準流れ方向d0と流入時流れ方向d1とがなす角度を90°に設定し、かつ第四の接続管12の曲げ方向(成形体8内部への流入方向d2)を、状態調整槽7の流出口7eと同じ向きから、第四の接続管12を平面視した状態で流入時流れ方向d1と同じ向きに曲げるようにした(図3及び図4を参照)。このように第三の接続管11の曲げ方向と第四の接続管12の曲げ方向とを成形体8の流入口8cとの関係で定めることによって、基準流れ方向d0と、成形体8により成形されるガラスリボンGrの主表面の向き(すなわちガラスリボンGrの送り方向D0)とを一致させることができる。成形されたガラスリボンGrは、下方に引き出された後、カテナリを介して水平方向に方向転換して搬送されるので、上記構成によれば、溶融ライン2と、加工ライン3とを平行に配置することができる。 Further, in the present embodiment, the inlet 8c of the molded body 8 is provided in a direction perpendicular to both side surfaces 8b, 8b through which the molten glass Gm overflowing from the upper overflow groove 8a flows down, and the reference flow direction d0. And the flow direction d1 at the time of inflow are set to 90 °, and the bending direction of the fourth connecting pipe 12 (the inflow direction d2 into the molded body 8) is the same as the outlet 7e of the condition adjusting tank 7. From the direction, the fourth connection pipe 12 is bent in the same direction as the inflow flow direction d1 in a state where the fourth connection pipe 12 is viewed in a plan view (see FIGS. 3 and 4). In this manner, the bending direction of the third connection pipe 11 and the bending direction of the fourth connection pipe 12 are determined based on the relationship between the inlet 8c of the molded body 8 and the reference flow direction d0 and the molding by the molded body 8. The direction of the main surface of the glass ribbon Gr to be performed (that is, the feeding direction D0 of the glass ribbon Gr) can be matched. After the formed glass ribbon Gr is drawn downward, it is conveyed while turning in the horizontal direction via the catenary, so that according to the above configuration, the melting line 2 and the processing line 3 are arranged in parallel. can do.

 以上、本発明の一実施形態を説明したが、本発明に係るガラス物品の製造方法及び製造装置は、上記実施形態には限定されることなく、本発明の範囲内で種々の形態を採ることが可能である。 As mentioned above, although one Embodiment of this invention was described, the manufacturing method and manufacturing apparatus of the glass article which concern on this invention take various forms within the scope of this invention, without being limited to the said embodiment. Is possible.

 例えば、上記実施形態では、第三の接続管11の曲げ方向(曲げた後の方向となる下流端11bの方向)を規定する際の基準となる基準流れ方向d0を水平方向とした場合を例示(図5を参照)したが、基準流れ方向d0は水平方向には限らない。流入時流れ方向d1についても水平方向には限られることはなく、上述の通り、鉛直上方から見た状態(平面視した状態)で、基準流れ方向d0に対して左右何れか一方の側を向く限りにおいて、流入時流れ方向d1を任意の向きに設定することが可能である。また、成形体8内部への溶融ガラスGmの流入方向d2についても、図示の向き(+X方向)には限定されない。例えば、流入方向d2を+X方向以外の向きに設定することも可能である。また、以上のことから、第三の接続管11における曲げ角度(第三の接続管11を平面視した状態で基準流れ方向d0と流入時流れ方向d1とがなす角度)は90°に限られない。同様に、第四の接続管12における曲げ角度(状態調整槽7の流出口7eの向きと流入方向d2とがなす角度)も90°に限らず、上述した条件を満たす範囲内において任意の角度を採り得る。 For example, in the above embodiment, the case where the reference flow direction d0, which is the reference when defining the bending direction of the third connection pipe 11 (the direction of the downstream end 11b, which is the direction after bending), is set as the horizontal direction. However, the reference flow direction d0 is not limited to the horizontal direction (see FIG. 5). The flow direction d1 at the time of inflow is not limited to the horizontal direction. As described above, the flow direction d1 faces one of the left and right sides with respect to the reference flow direction d0 when viewed from above vertically (in a plan view). As long as it is possible, the flow direction d1 at the time of inflow can be set to an arbitrary direction. Further, the flow direction d2 of the molten glass Gm into the molded body 8 is not limited to the illustrated direction (+ X direction). For example, the inflow direction d2 can be set to a direction other than the + X direction. From the above, the bending angle (the angle between the reference flow direction d0 and the inflow flow direction d1 when the third connection pipe 11 is viewed in a plan view) in the third connection pipe 11 is limited to 90 °. Absent. Similarly, the bending angle of the fourth connection pipe 12 (the angle between the direction of the outflow port 7e of the condition adjusting tank 7 and the inflow direction d2) is not limited to 90 °, but may be any angle within a range satisfying the above-described conditions. Can be adopted.

 また、上記実施形態では、第三の接続管11を、直線状に伸びるストレート部13と、ストレート部13と状態調整槽7とを接続する第一曲げ部14、及び均質化槽6とストレート部13とを接続する第二曲げ部15とで構成した場合を例示したが、もちろん第三の接続管11は上記以外の構成を採ることも可能である。例えば図示は省略するが、平面視した状態で、第二曲げ部15の下流端に-X方向に伸びる第一ストレート部を接続し、第一ストレート部の下流端に第三曲げ部を接続し、第三曲げ部の下流端に+Y方向に伸びる第二ストレート部を接続し、第二ストレート部の下流端に第一曲げ部14を接続し、第一曲げ部14の下流端を状態調整槽7の流入口7dに接続した形態をとることも可能である。 Further, in the above embodiment, the third connecting pipe 11 is formed by connecting the straight portion 13 extending linearly, the first bent portion 14 connecting the straight portion 13 and the condition adjusting tank 7, and the homogenizing tank 6 to the straight portion. Although the case where the third connection pipe 11 is constituted by the second bent portion 15 connecting the first connection pipe 13 and the second connection pipe 13 is exemplified, the third connection pipe 11 can of course adopt a configuration other than the above. For example, although not shown, a first straight portion extending in the −X direction is connected to the downstream end of the second bent portion 15 in a plan view, and a third bent portion is connected to the downstream end of the first straight portion. The second straight portion extending in the + Y direction is connected to the downstream end of the third bent portion, the first bent portion 14 is connected to the downstream end of the second straight portion, and the downstream end of the first bent portion 14 is connected to the conditioning tank. It is also possible to take a form connected to the inflow port 7d of 7.

 また、上記実施形態では、外径寸法が一定の第三の接続管11を状態調整槽7に直接接続した場合を例示したが(図3及び図4を参照)、もちろんこれ以外の接続形態をとることも可能である。図8は、その一例(本発明の他の実施形態)に係る第三の接続管11と状態調整槽7との接続部分をY方向から見た図である。図8に示すように、第三の接続管11は、その下流側に位置する第一曲げ部14と、第一曲げ部14と状態調整槽7側の間に位置し、第一曲げ部14側から状態調整槽7側に向けて横断面積(長手方向と垂直な断面における面積、以下、単に「断面積」ともいう)が漸次変化する断面積変化部16とを有する。これにより、第三の接続管11の第一曲げ部14と状態調整槽7とが、断面積変化部16を介して接続される。この場合、断面積変化部16が、第三の接続管11の下流端11bとなる。 Further, in the above embodiment, the case where the third connection pipe 11 having a constant outer diameter is directly connected to the condition adjusting tank 7 is exemplified (see FIGS. 3 and 4). Of course, other connection forms are used. It is also possible to take. FIG. 8 is a view of a connection portion between the third connection pipe 11 and the condition adjusting tank 7 according to one example (another embodiment of the present invention) viewed from the Y direction. As shown in FIG. 8, the third connecting pipe 11 is located on the downstream side of the first bent portion 14, and is located between the first bent portion 14 and the condition adjusting tank 7. A cross-sectional area changing portion 16 whose cross-sectional area (area in a cross section perpendicular to the longitudinal direction, hereinafter, also simply referred to as “cross-sectional area”) gradually changes from the side toward the condition adjusting tank 7 side. Thereby, the first bent portion 14 of the third connection pipe 11 and the condition adjusting tank 7 are connected via the cross-sectional area changing portion 16. In this case, the cross-sectional area change portion 16 becomes the downstream end 11b of the third connection pipe 11.

 本実施形態では、第三の接続管11の第一曲げ部14の断面積をS1、状態調整槽7の上部7aの断面積をS2とすると、第一曲げ部14の断面積S1は上部7aの断面積S2と異なり、より具体的には、第一曲げ部14の断面積S1は上部7aの断面積S2より小さい。この場合、断面積変化部16の断面積が、第一曲げ部14側から状態調整槽7側に向けて漸次増大するよう、断面積変化部16の内面16aの形状が設定されている。具体的には、断面積変化部16の内面16aの、縦断面(長手方向に沿う断面)の形状が円弧状である。このため、断面積変化部16の内面16aは、筒状であり、第一曲げ部14側から状態調整槽7側に向けて拡径している。 In this embodiment, assuming that the sectional area of the first bent portion 14 of the third connection pipe 11 is S1 and the sectional area of the upper portion 7a of the condition adjusting tank 7 is S2, the sectional area S1 of the first bent portion 14 is the upper portion 7a. More specifically, the cross-sectional area S1 of the first bent portion 14 is smaller than the cross-sectional area S2 of the upper portion 7a. In this case, the shape of the inner surface 16a of the cross-sectional area changing portion 16 is set such that the cross-sectional area of the cross-sectional area changing portion 16 gradually increases from the first bending portion 14 side toward the condition adjusting tank 7 side. Specifically, the vertical cross section (cross section along the longitudinal direction) of the inner surface 16a of the cross-sectional area changing portion 16 is arc-shaped. For this reason, the inner surface 16a of the cross-sectional area changing portion 16 is cylindrical, and the diameter is increased from the first bending portion 14 side toward the condition adjusting tank 7 side.

 第一曲げ部14の断面積S1は、上部7aの断面積S2の0.75倍以上でかつ1.25倍以下に設定するのがよい。本実施形態のように、第一曲げ部14の断面積S1を上部7aの断面積S2より小さくする場合には、第一曲げ部14の断面積S1を、上部7aの断面積S2の0.75倍以上でかつ0.96倍以下に設定するのがよい。例えば、第一曲げ部14の内径は150mm以上でかつ300mm以下に設定することができ、断面積変化部16の内面16aの曲率半径は、10mm以上でかつ50mm以下に設定することができ、好ましくは20mm以上でかつ40mm以下に設定することが好ましい。 断面 The cross-sectional area S1 of the first bent portion 14 is preferably set to be 0.75 times or more and 1.25 times or less the cross-sectional area S2 of the upper portion 7a. When the cross-sectional area S1 of the first bent portion 14 is smaller than the cross-sectional area S2 of the upper portion 7a as in the present embodiment, the cross-sectional area S1 of the first bent portion 14 is set to 0. It is preferable to set it to 75 times or more and 0.96 times or less. For example, the inner diameter of the first bent portion 14 can be set to 150 mm or more and 300 mm or less, and the radius of curvature of the inner surface 16a of the cross-sectional area change portion 16 can be set to 10 mm or more and 50 mm or less, and is preferable. Is preferably set to 20 mm or more and 40 mm or less.

 状態調整槽7の下部7bと、第四の接続管12の上流端12cとは、縁切りされた状態で(状態調整槽7の下部7bと第四の接続管12の上流端12cが接触しない状態で)、溶融ガラスGmを状態調整槽7側から第四の接続管12側へ供給可能としている。具体的には、図8に示すように、下部7bを第四の接続管12の上流端12c内周に挿入した状態で、状態調整槽7で状態の調整が成された溶融ガラスGmを、第四の接続管12を通じて成形体8に供給可能としている。 The lower part 7b of the condition adjusting tank 7 and the upstream end 12c of the fourth connecting pipe 12 are cut off (a state in which the lower part 7b of the condition adjusting tank 7 does not contact the upstream end 12c of the fourth connecting pipe 12). ), The molten glass Gm can be supplied from the condition adjusting tank 7 to the fourth connection pipe 12. Specifically, as shown in FIG. 8, in a state where the lower portion 7b is inserted into the inner periphery of the upstream end 12c of the fourth connection pipe 12, the molten glass Gm whose state has been adjusted in the state adjustment tank 7 is The molded product 8 can be supplied through the fourth connection pipe 12.

 ここで、状態調整槽7の下部7bの断面積をS3、第四の接続管12の上流端12cの断面積をS4とした場合、下部7bの断面積S3を、上流端12cの断面積S4の0.75倍以上でかつ0.96倍以下に設定するのがよい。 Here, when the sectional area of the lower part 7b of the condition adjusting tank 7 is S3 and the sectional area of the upstream end 12c of the fourth connection pipe 12 is S4, the sectional area S3 of the lower part 7b is changed to the sectional area S4 of the upstream end 12c. It is preferable to set it to 0.75 times or more and 0.96 times or less.

 また、第三の接続管11が上記構成をなす場合、第一曲げ部14と状態調整槽7との間の断面積変化部16を通過する溶融ガラスGmの粘度は、好ましくは800Pa・s以上に設定され、より好ましくは1000Pa・s以上に設定される。一方、失透を抑制する観点から、断面積変化部16を通過する溶融ガラスGmの粘度は、50000Pa・s以下に設定されることが好ましい。 When the third connection pipe 11 has the above-described configuration, the viscosity of the molten glass Gm passing through the cross-sectional area changing portion 16 between the first bending portion 14 and the condition adjusting tank 7 is preferably 800 Pa · s or more. , More preferably 1000 Pa · s or more. On the other hand, from the viewpoint of suppressing devitrification, it is preferable that the viscosity of the molten glass Gm passing through the cross-sectional area changing portion 16 be set to 50,000 Pa · s or less.

 このように、本実施形態では、第三の接続管11が、第一曲げ部14と状態調整槽7の間に、第一曲げ部14側から状態調整槽7側に向けて断面積が漸次変化する断面積変化部16を有するようにした。この構成によれば、第三の接続管11から状態調整槽7内部に流入した溶融ガラスGmに剥離流が発生する事態を可及的に防止して、均質化槽6の底部に停滞する溶融ガラスGm1’(図6を参照)を、第四の接続管12の外側12aを通って、成形体8のうちガラスリボンGrの幅方向一端部Gr2(図7を参照)となる領域に確実に流れ込ませることができる。また、状態調整槽7の上部7aに停滞する溶融ガラスGm2’を、第四の接続管12の内側12bを通って、成形体8のうちガラスリボンGrの幅方向他端部Gr1(図7を参照)となる領域により確実に流れ込ませることができる。以上より、本実施形態に係るガラス物品の製造方法及び製造装置によれば、成形不良の原因となる異質な溶融ガラスGm1’(Gm2’)が加工後のガラスリボンGrに残って、製品としてのガラス物品の品質低下を招く事態を可及的に防止することが可能となる。 As described above, in the present embodiment, the third connecting pipe 11 has a sectional area between the first bent portion 14 and the condition adjusting tank 7 that gradually increases in cross section from the first bent portion 14 side toward the condition adjusting tank 7 side. It has a cross-sectional area changing portion 16 that changes. According to this configuration, a situation in which a separation flow is generated in the molten glass Gm flowing into the inside of the condition adjusting tank 7 from the third connection pipe 11 is prevented as much as possible, and the molten glass stagnating at the bottom of the homogenizing tank 6 is prevented. The glass Gm1 ′ (see FIG. 6) passes through the outer side 12a of the fourth connection pipe 12, and is surely formed in the region of the molded body 8 that becomes one end portion Gr2 (see FIG. 7) of the glass ribbon Gr in the width direction. Can be poured. Further, the molten glass Gm2 ′ stagnating in the upper portion 7a of the condition adjusting tank 7 passes through the inner side 12b of the fourth connection pipe 12, and the other end Gr1 in the width direction of the glass ribbon Gr of the molded body 8 (see FIG. (See Reference)). As described above, according to the method and the apparatus for manufacturing a glass article according to the present embodiment, the foreign molten glass Gm1 ′ (Gm2 ′) that causes a molding defect remains on the processed glass ribbon Gr and serves as a product. It is possible to prevent a situation in which the quality of the glass article is deteriorated as much as possible.

Claims (6)

 溶融ガラス生成装置で溶融ガラスを生成する生成工程と、生成した前記溶融ガラスの状態を状態調整槽で調整する状態調整工程と、状態の調整が成された前記溶融ガラスを成形体に供給してガラスリボンを成形する成形工程とを備える、ガラス物品の製造方法において、
 前記状態調整槽に設けられた前記溶融ガラスの流入口に、前記溶融ガラス生成装置の側から前記状態調整槽の内部に前記溶融ガラスを流入させるための流入管が接続され、
 前記溶融ガラスの流れ方向上流側となる前記流入管の一端を通過する際の前記溶融ガラスの流れ方向を基準流れ方向とし、前記流入管の他端から前記状態調整槽の内部に流入する際の前記溶融ガラスの流れ方向を流入時流れ方向としたとき、
 前記流入管を平面視した状態で、前記流入時流れ方向が前記基準流れ方向に対して左右何れか一方の側を向くように、前記流入管が曲がっていることを特徴とするガラス物品の製造方法。
A generating step of generating molten glass in a molten glass generating apparatus, a state adjusting step of adjusting the state of the generated molten glass in a state adjustment tank, and supplying the molten glass whose state has been adjusted to a molded body. Comprising a forming step of forming a glass ribbon, a method of manufacturing a glass article,
An inflow pipe for allowing the molten glass to flow into the inside of the condition adjusting tank from the side of the molten glass generating device is connected to an inlet of the molten glass provided in the condition adjusting tank,
The flow direction of the molten glass when passing through one end of the inflow pipe on the upstream side in the flow direction of the molten glass is defined as a reference flow direction, and when flowing into the inside of the condition adjusting tank from the other end of the inflow pipe. When the flow direction of the molten glass is the flow direction at the time of inflow,
The method of manufacturing a glass article, wherein the inflow pipe is bent such that the flow direction at the time of inflow is directed to one of left and right sides with respect to the reference flow direction in a state where the inflow pipe is viewed in a plan view. Method.
 前記状態調整槽の流出口と前記成形体の流入口とが接続管で接続され、
 前記接続管は、前記状態調整槽の流出口と同じ向きから、前記接続管を平面視した状態で前記流入時流れ方向と同じ向きに曲がっている請求項1に記載のガラス物品の製造方法。
An outlet of the condition adjusting tank and an inlet of the molded body are connected by a connection pipe,
The method for manufacturing a glass article according to claim 1, wherein the connection pipe is bent in the same direction as the flow direction at the time of inflow in a state where the connection pipe is viewed in a plan view from the same direction as the outlet of the condition adjusting tank.
 前記流入管は、前記流入管を平面視した状態で、前記流入管の一端側から前記基準流れ方向に対して左右他方の側に傾斜した状態で直線状に伸びるストレート部と、前記ストレート部の下流端から前記流入時流れ方向へと曲がって、前記状態調整槽の流入口に接続される曲げ部とを有する請求項1又は2に記載のガラス物品の製造方法。 A straight portion extending straight from one end of the inflow pipe to one of the right and left sides with respect to the reference flow direction in a state where the inflow pipe is viewed in a plan view; The method for producing a glass article according to claim 1, further comprising a bent portion that bends from the downstream end in the flow direction at the time of the inflow and that is connected to an inflow port of the conditioning tank.  前記成形体は、オーバーフロー溝から溢れ出た前記溶融ガラスを両側面に沿って流下させることで前記ガラスリボンを成形するもので、
 前記成形体の流入口は、前記両側面の向きに対して直交する向きに設けられ、かつ前記基準流れ方向と前記流入時流れ方向とがなす角度が90°に設定される請求項1~3の何れか一項に記載のガラス物品の製造方法。
The molded body is for molding the glass ribbon by flowing down the molten glass overflowing from the overflow groove along both side surfaces,
The inflow port of the molded body is provided in a direction orthogonal to the directions of the both side surfaces, and an angle formed by the reference flow direction and the inflow flow direction is set to 90 °. The method for producing a glass article according to any one of the above.
 前記ガラス物品は、前記ガラスリボンをロール状に巻き取ってなるガラスロールである請求項1~4の何れか一項に記載のガラス物品の製造方法。 The method for producing a glass article according to any one of claims 1 to 4, wherein the glass article is a glass roll formed by winding the glass ribbon into a roll.  溶融ガラスを生成する溶融ガラス生成装置と、生成した前記溶融ガラスの状態を調整する状態調整槽と、状態の調整が成された前記溶融ガラスを流下させて前記ガラスリボンを成形する成形体とを備えるガラス物品の製造装置において、
 前記状態調整槽に設けられた前記溶融ガラスの流入口に、前記溶融ガラス生成装置の側から前記状態調整槽の内部に前記溶融ガラスを流入させるための流入管が接続され、
 前記溶融ガラスの流れ方向上流側となる前記流入管の一端を通過する際の前記溶融ガラスの流れ方向を基準流れ方向とし、前記流入管の他端から前記状態調整槽の内部に流入する際の前記溶融ガラスの流れ方向を流入時流れ方向としたとき、
 前記流入管を平面視した状態で、前記流入時流れ方向が前記基準流れ方向に対して左右何れか一方の側を向くように、前記流入管が曲がっていることを特徴とするガラス物品の製造装置。
A molten glass generating apparatus that generates molten glass, a condition adjusting tank that adjusts the state of the generated molten glass, and a formed body that flows down the molten glass whose state has been adjusted to form the glass ribbon. In a manufacturing apparatus of a glass article provided,
An inflow pipe for allowing the molten glass to flow into the inside of the condition adjusting tank from the side of the molten glass generating device is connected to an inlet of the molten glass provided in the condition adjusting tank,
The flow direction of the molten glass when passing through one end of the inflow pipe on the upstream side in the flow direction of the molten glass is defined as a reference flow direction, and when flowing into the inside of the condition adjusting tank from the other end of the inflow pipe. When the flow direction of the molten glass is the flow direction at the time of inflow,
The method of manufacturing a glass article, wherein the inflow pipe is bent such that the flow direction at the time of inflow is directed to one of left and right sides with respect to the reference flow direction in a state where the inflow pipe is viewed in a plan view. apparatus.
PCT/JP2019/022208 2018-07-03 2019-06-04 Glass article manufacturing method and manufacturing apparatus Ceased WO2020008782A1 (en)

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