Flow channel structure having one furnace and multiple lines

Abstract

A flow channel structure having one furnace and multiple lines, applied to a float glass production line. An inlet of the flow channel structure is communicated with a cooling part (1) of a glass melting furnace, and an outlet of the flow channel structure is communicated with a main line tin bath (2) and a branch line tin bath (2' / 2"). The flow channel structure comprises a main line flow channel and a branch line flow channel, wherein the main line flow channel comprises a main line inlet section (3), a main line adjustment section (4), a main line control section (5), and a main line outlet section (6). Molten glass passes from the cooling part (1) of the glass melting furnace into the main line tin bath (2) by means of the main line inlet section (3), the main line adjustment section (4), the main line control section (5), and the main line outlet section (6) in sequence. The branch line flow channel comprises a branch line transverse section (16), a branch line control section (5' / 5''), and a branch line outlet section (6' / 6''), wherein the branch line transverse section (16) is communicated with an outlet end of the main line adjustment section (4). The molten glass in the branch line and the molten glass in the main line both flow from the cooling part (1) of the same glass melting furnace, and the quality of glass produced in the main line has no difference from the quality of glass produced in the branch line.

Description

A liquid flow channel structure with multiple lines in one kiln Technical Field

[0001] The present invention relates to the technical field of float glass production equipment, in particular to a one-kiln multi-line liquid flow channel structure. Background Art

[0002] Currently, most flat glass float production lines, both domestically and internationally, are based on a "one kiln, one line" model, with one kiln connected to a single float tin bath via a single flow channel. Daily production capacity has increased from 150 to 1,200 tons per day. Glass produced ranges in thickness from 1.1 to 22 mm. While daily melting tonnage has increased in glass production, energy consumption per unit of flat glass production has decreased. To reduce energy consumption, many domestic glass manufacturers are opting for large-capacity float glass production lines. However, with this "one kiln, one line" model, thin glass, typically 1.1 to 3 mm, becomes difficult to produce as daily production increases.

[0003] To address this challenge, the "one kiln, two lines" high-tonnage float glass production line was born. The current "one kiln, two lines" float glass production line solution builds on the "one kiln, one line" approach by adding a bypass branch to one side of the kiln's cooling section, extending through this bypass branch to a second parallel cooling section. The two cooling sections are connected to their respective flow channels and their corresponding float tin baths to form a single production line. Typically, the production line directly opposite the center of the kiln is called the "main line," while the line parallel to the kiln's centerline is called the "branch line." In the "one kiln, two lines" float glass production line, the main line has a relatively small tonnage and produces thinner glass. The branch line is often larger in tonnage and produces thicker plate glass.

[0004] This "one kiln, two lines" float glass production line also has major disadvantages:

[0005] 1. Glass quality difference. Due to the limitations of the kiln structure, the glass quality of the main line and branch line is quite different. Generally speaking, the main line glass quality is better than the branch line glass quality.

[0006] 2. High energy consumption. The conventional "one kiln, two lines" has two cooling sections, which consumes more energy than the "one kiln, one line" of the same tonnage.

[0007] 3. Increased use of refractory materials. Compared with the "one kiln, one line" of the same tonnage, the "one kiln, two lines" kiln has two cooling sections, and the investment is about 1.5 times that of the "one kiln, one line" of the same tonnage.

[0008] 4. Cold-rolling renovations are difficult. When converting a "one kiln, one line" system to a "one kiln, two lines" system, the original kiln structure cannot be reused, and additional cross passages and cooling units are added. The existing plant structure is difficult to reuse, requiring expansion.

[0009] 5. There must be a certain difference in tonnage between the main line and the branch line. Generally, the main line's tonnage is much lower than that of the branch line, which is 1.5 to 2 times the main line's tonnage. Flexible tonnage adjustment between the two lines is impossible, and the glass specifications produced are also incompatible.

[0010] Summary of the Invention

[0011] In view of the above-mentioned shortcomings of the prior art, an object of the present invention is to provide a multi-line liquid flow channel structure in one kiln to solve the problems existing in the prior art.

[0012] To achieve the above-mentioned purpose and other related purposes, the present invention provides a one-kiln multi-line liquid flow channel structure, which is applied to a float glass production line; the inlet of the liquid flow channel structure is connected to the cooling part of the glass melting furnace, and the outlet of the liquid flow channel structure is connected to the main line tin bath and the branch line tin bath; the liquid flow channel structure includes a main line liquid flow channel and a branch line liquid flow channel, the main line liquid flow channel includes a main line inlet section, a main line quantity adjustment section, a main line quantity control section, and a main line outlet section, and the glass melt enters the main line tin bath from the cooling part of the glass melting furnace through the main line inlet section, the main line quantity adjustment section, the main line quantity control section, and the main line outlet section in sequence; the branch line liquid flow channel includes a branch line cross-through section, a branch line quantity control section, and a branch line outlet section, the branch line cross-through section is connected to the outlet end of the main line quantity adjustment section, and the glass melt enters the branch line tin bath from the main line quantity adjustment section through the branch line cross-through section, the branch line quantity control section, and the branch line outlet section in sequence.

[0013] Preferably, each section in the fluid channel structure is composed of bottom bricks, pool wall bricks, breast wall bricks, and cover plates, the pool wall bricks are arranged on the bottom bricks, the breast wall bricks are arranged on the pool wall bricks, and the cover plates are covered on the breast wall bricks.

[0014] Preferably, the main line inlet section is provided with a main line thermocouple, an inlet section operation hole is opened on the breast wall brick at the main line inlet section, a water bag is passed through the inlet section operation hole, and an inlet section heating electrode is provided on the pool wall brick at the main line inlet section; the water bag in the inlet section operation hole cooperates with the inlet section heating electrode to adjust the glass melt temperature at the main line inlet section.

[0015] Preferably, the main line regulating section is provided with a rotating gate, a main line regulating section heating hole is opened on the pool wall brick at the main line regulating section, and a main line regulating section unloading hole is opened on the bottom brick at the main line regulating section; a natural gas spray gun or a space silicon carbon rod is provided in the main line regulating section heating hole, which is used to adjust the temperature of the glass melt at the main line regulating section.

[0016] Preferably, it further comprises a driving source, which is in transmission connection with the rotating gate, and the rotation direction and rotation speed of the rotating gate are adjustable.

[0017] Preferably, the main line control section is provided with a main line control section gate plate that can be raised and lowered, a main line control section operation hole is opened on the breast wall brick at the main line control section, a water bag is passed through the main line control section operation hole, and a main line control section heating electrode is provided on the pool wall brick at the main line control section; the water bag in the main line control section operation hole cooperates with the main line control section heating electrode to adjust the glass melt temperature at the main line control section.

[0018] Preferably, a main line gas sealing hole is provided at the main line outlet section, and protective gas is introduced into the main line gas sealing hole.

[0019] Preferably, a branch line thermocouple is provided on the top cover of the branch line transverse section, a branch line transverse section unloading hole is provided on the bottom brick at the branch line transverse section, a branch line transverse section heating hole is provided on the breast wall brick at the branch line transverse section, and a branch line transverse section heating electrode is provided in the branch line transverse section heating hole for adjusting the temperature of the molten glass at the branch line transverse section.

[0020] Preferably, the branch line control section is provided with a liftable branch line control section gate plate, a branch line control section operation hole is opened on the breast wall brick at the branch line control section, a water bag is passed through the branch line control section operation hole, and a branch line control section heating electrode is provided on the pool wall brick at the branch line control section; the water bag in the branch line control section operation hole cooperates with the branch line control section heating electrode to adjust the glass melt temperature at the branch line control section.

[0021] Preferably, a branch line gas sealing hole is provided at the branch line outlet section, and protective gas is introduced into the branch line gas sealing hole.

[0022] As described above, the one-kiln-multiple-line liquid channel structure of the present invention has the following beneficial effects:

[0023] 1. The present invention relates to a liquid flow channel structure with multiple lines in one kiln. The quality of glass produced by one main line and multiple branch lines is the same. The glass liquid of the main line and the branch lines all flows out from the cooling part and has the same quality.

[0024] 2. The present invention relates to a liquid flow channel structure with multiple lines in one furnace, which reduces the energy consumption of the glass melting furnace. The glass melting furnace only needs one cooling section, which is less than the multiple cooling sections of one furnace with two lines or one furnace with three lines in the prior art, and the amount of glass liquid cooled and refluxed is reduced.

[0025] 3. The present invention relates to a liquid flow channel structure with multiple lines in one kiln, which reduces the use of refractory materials and the cross-sectional area of ​​the liquid flow channel is much smaller than the cooling part. Therefore, it saves more refractory materials than the one kiln two lines or one kiln three lines in the prior art.

[0026] 4. The present invention relates to a multi-line liquid channel structure for one furnace, which can fully utilize the existing glass melting furnace structure and factory building.

[0027] 5. The present invention relates to a liquid flow channel structure with multiple lines in one kiln. The tonnage of the main line and the branch line can be flexibly changed, and the tonnage and product specifications of each line can be adjusted at any time according to actual production requirements. BRIEF DESCRIPTION OF THE DRAWINGS

[0028] FIG1 is a schematic diagram of a one-kiln-two-line structure of a liquid flow channel structure with multiple lines in one kiln according to the present invention;

[0029] FIG2 is a schematic diagram of a kiln with three lines in a liquid flow channel structure with multiple lines in one kiln according to the present invention;

[0030] FIG3 is a longitudinal cross-sectional view of the main line of a multi-line flow channel structure of a kiln according to the present invention;

[0031] FIG4 is a transverse cross-sectional view of a kiln with two lines in a liquid flow channel structure with multiple lines in one kiln according to the present invention.

[0032] Description of reference numerals:

[0033] 1. Cooling section; 2. Main line tin bath; 3. Main line inlet section; 4. Main line metering section; 5. Main line metering section; 6. Main line outlet section; 7. Main line metering section discharge port; 8. Main line thermocouple; 9. Rotating gate; 10. Main line metering section gate; 11. Cover plate; 12. Main line metering section operating port; 13. Main line metering section heating port; 14. Main line gas seal port; 15. Inlet section heating electrode; 16. Branch line cross-section; 17. Water drum; 18. Natural gas spray gun; 19. Space silicon carbon rod;

[0034] 2' / 2", branch line tin bath; 5' / 5", branch line quantity control section; 6' / 6", branch line outlet section; 7', branch line cross-section discharge hole; 8', branch line thermocouple; 10' / 10", branch line quantity control section gate; 13', branch line cross-section heating hole. DETAILED DESCRIPTION

[0035] The following describes the implementation of the present invention through specific embodiments. People skilled in the art can easily understand other advantages and effects of the present invention from the contents disclosed in this specification.

[0036] It should be noted that the structures, proportions, sizes, etc. illustrated in the drawings of this specification are only used to match the contents disclosed in the specification for people familiar with this technology to understand and read, and are not used to limit the limiting conditions for the implementation of the present invention. Therefore, they have no substantial technical significance. Any modification of the structure, change in the proportional relationship or adjustment of the size should still fall within the scope of the technical content disclosed by the present invention without affecting the efficacy and purpose that can be achieved by the present invention. At the same time, the terms such as "upper", "lower", "left", "right", "middle" and "one" quoted in this specification are only for the convenience of description and are not used to limit the scope of the implementation of the present invention. Changes or adjustments in their relative relationships should also be regarded as the scope of the implementation of the present invention without substantially changing the technical content.

[0037] As shown in Figures 1 to 4, the present invention provides a multi-line flow channel structure for a single furnace, which is applied to a float glass production line. The inlet of the flow channel structure is connected to the cooling section 1 of the glass melting furnace, and the outlet of the flow channel structure is connected to the main line tin bath 2 and the branch line tin bath 2' / 2". The flow channel structure includes a main line flow channel and a branch line flow channel. The main line flow channel includes a main line inlet section 3, a main line flow adjustment section 4, a main line flow control section 5, and a main line outlet section 6. The molten glass flows from the cooling section 1 of the glass melting furnace according to the flow channel structure. The glass melt passes through the main line entrance section 3, the main line quantity adjustment section 4, the main line quantity control section 5, and the main line outlet section 6 to enter the main line tin bath 2; the branch line liquid flow channel includes the branch line cross-through section 16, the branch line quantity control section 5' / 5", and the branch line outlet section 6' / 6", and the branch cross-through section 16 is connected with the outlet end of the main line quantity adjustment section 4. The glass melt enters the branch line tin bath 2' / 2" from the main line quantity adjustment section 4 through the branch line cross-through section 16, the branch line quantity control section 5' / 5", and the branch line outlet section 6' / 6".

[0038] The present invention relates to a multi-line flow channel structure for a single furnace. The main line flow channel section 4 allows for flexible tonnage changes between the main and branch lines. The tonnage and product specifications of each line can be adjusted at any time according to actual production requirements, resulting in high adaptability. The molten glass from both the branch and main lines flows out of the cooling section 1 of the same glass melting furnace, and the quality of the glass produced by the branch and main lines is the same.

[0039] Preferably, as shown in Figures 1 to 4, each section in the flow channel structure is composed of bottom bricks, pool wall bricks, breast wall bricks, and a cover plate 11. The pool wall bricks are arranged on the bottom bricks, the breast wall bricks are arranged on the pool wall bricks, and the cover plate 11 covers the breast wall bricks.

[0040] Preferably, as shown in Figure 3 , a mainline thermocouple 8 is installed on the cover plate 11 of the mainline inlet section 3. An inlet section operation hole is provided on the breast wall bricks at the mainline inlet section 3 (the inlet section operation hole is the hole that intersects the downward extension of the mainline thermocouple 8 in Figure 3 , not labeled). A water bag 17 is inserted into the inlet section operation hole. An inlet section heating electrode 15 is installed on the pool wall bricks at the mainline inlet section 3. The water bag 17 in the inlet section operation hole cooperates with the inlet section heating electrode 15 to regulate the temperature of the molten glass at the mainline inlet section 3. Furthermore, in this embodiment, the width of the mainline inlet section 3 ranges from 4 to 7 meters, and the depth of the mainline inlet section 3 ranges from 0.3 to 0.6 meters. The mainline thermocouple 8 is used to measure the temperature of the molten glass at the mainline inlet section 3. The water bag 17 is used to reduce the temperature of the molten glass at the mainline inlet section 3. The heating end of the inlet section heating electrode 15 is located in the molten glass, thereby heating the molten glass at the mainline inlet section 3. In this way, the glass melt is adjusted to a suitable temperature through the main line thermocouple 8, the water bag 17, and the inlet section heating electrode 15 and enters the main line regulating section 4.

[0041] Preferably, as shown in Figures 1 to 4, the main line regulating section 4 is provided with a plurality of rotating gate plates 9, a main line regulating section heating hole 13 is opened on the pool wall bricks at the main line regulating section 4, and a main line regulating section unloading hole 7 is opened on the bottom bricks at the main line regulating section 4; a natural gas spray gun 18 or a spatial silicon carbon rod 19 is provided in the main line regulating section heating hole 13, which is used to adjust the temperature of the glass melt at the main line regulating section 4 and change the viscosity of the glass melt at the main line regulating section 4. At the same time, under the action of the rotating gate plate 9, the glass melt at the main line regulating section 4 is homogenized to improve the quality of the glass melt.

[0042] Furthermore, a main line regulating section discharge hole 7 is provided, which can periodically discharge the glass melt with poor quality at the bottom of the glass melt.

[0043] Furthermore, in this embodiment, a driving source is provided, which is in transmission connection with the rotating gate plate 9 , and the rotation direction and rotation speed of the rotating gate plate 9 can be adjusted.

[0044] Furthermore, the one kiln multiple lines of the present application has two cases: one branch line and two branch lines, which are as follows:

[0045] 1. An embodiment with one branch line (one kiln and two lines); in this embodiment, the main line flow regulating section 4 has three rotary gates 9, as shown in FIG1 , namely rotary gates a, b, and c. When it is necessary to increase the main line flow and reduce the branch line flow, the a rotary gate 9 rotates clockwise and increases the speed; the b rotary gate 9 rotates counterclockwise, and the speed is the same as the speed of the a rotary gate 9; the c rotary gate 9 rotates clockwise, and the speed is lower than the speed of the a rotary gate 9. When it is necessary to reduce the main line flow and increase the branch line flow, the c rotary gate 9 rotates counterclockwise and increases the speed; the b rotary gate 9 rotates clockwise, and the speed is the same as the speed of the c rotary gate 9; the a rotary gate 9 rotates clockwise, and the speed is lower than the speed of the c rotary gate 9.

[0046] 2. An embodiment with two branches (one kiln and three lines), the branches are 1# branch line and 2# branch line (the parts marked with ' in the embodiment are parts of 1# branch line, and the parts marked with " are parts of 2# branch line); the main line flow regulating section 4 in this embodiment has four rotating gates 9, as shown in Figure 2, namely rotating gates a, b, c, and d. When it is necessary to increase the flow of the main line and reduce the flow of the 1# branch line and the 2# branch line, the rotating gate 9 a rotates clockwise and increases the speed; the rotating gate 9 b rotates clockwise and the speed is the same as the main line flow. The speed of rotating gate plate a is the same; rotating gate plate 9 d rotates counterclockwise and increases; rotating gate plate c rotates counterclockwise at the same speed as rotating gate plate 9 d. When it is necessary to reduce the flow of the main line and increase the flow of branch lines 1# and 2#, rotating gate plate a rotates clockwise and increases the speed; rotating gate plate b rotates counterclockwise at the same speed as rotating gate plate a; rotating gate plate 9 d rotates counterclockwise and increases the speed; rotating gate plate c rotates clockwise at the same speed as rotating gate plate 9 d.

[0047] Preferably, as shown in Figures 1 to 3, the main line control section 5 is provided with a main line control section gate 10 that can be raised and lowered. A main line control section operation hole 12 is opened on the breast wall brick at the main line control section 5. A water bag 17 is inserted into the main line control section operation hole 12. A main line control section heating electrode is provided on the pool wall brick at the main line control section 5 (the main line control section heating electrode is the same as the inlet section heating electrode 15, not marked in Figure 3); the water bag 17 in the main line control section operation hole 12 cooperates with the main line control section heating electrode to adjust the temperature of the molten glass at the main line control section 5. In this embodiment, by controlling the height of the main line control section gate 10, the amount of molten glass at the main line outlet section 6 can be finely controlled. By adjusting the depth of the water bag 17 and cooperating with the main line control section heating electrode, the temperature of the molten glass at the main line control section 5 can be controlled.

[0048] Preferably, as shown in FIG3 , a mainline gas seal hole 14 is provided at the mainline outlet section 6 , through which a protective gas is introduced. In this embodiment, the protective gas is used to isolate the atmosphere from the flow channel entering the mainline tin bath 2 , thereby reducing the volatilization and condensation of the molten glass and minimizing the impact of the external atmosphere on the mainline tin bath 2 .

[0049] Preferably, as shown in Figure 4, the branch line cross-section 16 is provided with a branch line thermocouple 8', a branch line cross-section unloading hole 7' is opened on the bottom brick at the branch line cross-section 16, a branch line cross-section heating hole 13' is opened on the breast wall brick at the branch line cross-section 16, and a branch line cross-section heating electrode is provided in the branch line cross-section heating hole 13' (the branch line cross-section heating electrode is the same as the main line control section heating electrode, not marked in the drawing), which is used to adjust the temperature of the molten glass at the branch line cross-section 16.

[0050] Furthermore, in this embodiment, the temperature of the molten glass is adjusted by the branch line thermocouple 8' and the branch line cross-section heating electrode so that the viscosity and temperature of the molten glass meet the requirements for entering the branch line control section 5' / 5". Adjusting to an appropriate temperature can enable the spacing between the main line and the branch line to reach a range of 15-50 meters, which is far greater than the spacing range of the "one kiln two lines" in the prior art. In addition, the cross-sectional area of ​​the branch line cross-section 16 is much smaller than the cross-sectional area of ​​the cooling section 1 of the glass melting furnace. Therefore, it will also save more refractory materials than the "one kiln two lines" in the prior art. The spacing between the main line and the branch line can be customized according to the specific cold repair line.

[0051] In this embodiment, the branch line cross-section discharge hole 7' is provided to periodically discharge the glass melt of poor quality at the bottom. The branch line thermocouple 8' is used to measure the temperature of the glass melt entering the branch line control section 5' / 5" of the branch line cross-section 16.

[0052] Preferably, as shown in FIG2 , the branch line control section 5' / 5" is provided with a liftable branch line control section gate plate 10' / 10", a branch line control section operation hole is opened on the breast wall brick at the branch line control section 5' / 5", a water bag 17 is passed through the branch line control section operation hole, and a branch line control section heating electrode is provided on the pool wall brick at the branch line control section 5' / 5"; the water bag 17 in the branch line control section operation hole cooperates with the branch line control section heating electrode to adjust the glass melt temperature at the branch line control section 5' / 5". The branch line control section gate plate 10' / 10" finely controls the amount of glass melt entering the branch line outlet section 6' / 6" through the lifting action; the water bag 17 in the branch line control section operation hole is adjustable in depth, and cooperates with the branch line control section heating electrode to adjust the temperature of the glass melt at the branch line control section 5' / 5".

[0053] Preferably, as shown in FIG2 , a branch line air sealing hole is provided at the branch line outlet section 6' / 6" (the branch line air sealing hole is not shown), and a protective gas is introduced into the branch line air sealing hole. In this embodiment, the protective gas is used to isolate the atmosphere from the flow channel entering the branch line tin bath 2' / 2", reduce the volatile condensation of the glass melt, reduce the influence of the external atmosphere on the branch line tin bath 2' / 2", and reduce the influence of the external atmosphere on the branch line tin bath 2' / 2".

[0054] The present invention relates to a one-kiln multi-line liquid flow channel structure, the inlet of which is connected to the cooling part 1 of the glass melting furnace, and is provided with a main line quantity regulating section 4, which can realize the regulation of the amount of molten glass in the main line and the branch line, and the tonnage between the main line and the branch line can be flexibly adjusted. A main line quantity control section gate plate 10 and a branch line quantity control section gate plate 10' / 10" are provided, which can finely control the amount of molten glass entering the main line outlet section 6 and the branch line outlet section 6' / 6". A main line air sealing hole 14 is provided on the main line outlet section 6, and a branch line air sealing hole is provided on the branch line outlet section 6' / 6". Both the main line air sealing hole 14 and the branch line air sealing hole can isolate the liquid flow channel from entering the atmosphere in the main line tin bath 2 and the branch line tin bath 2' / 2", thereby reducing the volatile condensation of the glass melt.

[0055] The present invention relates to a multi-line flow channel structure for a single kiln. The glass quality of a single kiln with two lines is the same as that of a single kiln with three lines. The molten glass of both the main line and the branch lines flows out of the cooling section 1, resulting in consistent glass quality. Furthermore, the cooling section 1 is smaller than the two cooling sections 1 used in the prior art for a single kiln with two lines, resulting in a smaller amount of molten glass being cooled and refluxed. The multi-line flow channel structure of the present invention is easy to retrofit and reconstruct, making full use of the existing glass melting furnace structure and plant. The tonnage of the main line and multiple branch lines can be flexibly adjusted, allowing the tonnage and product specifications of each line to be adjusted at any time according to actual production requirements.

[0056] Therefore, the present invention effectively overcomes various shortcomings of the prior art and has high industrial utilization value.

[0057] The above embodiments are merely illustrative of the principles and effects of the present invention and are not intended to limit the present invention. Anyone skilled in the art may modify or alter the above embodiments without departing from the spirit and scope of the present invention. Therefore, all equivalent modifications or alterations made by one of ordinary skill in the art without departing from the spirit and technical principles disclosed herein are intended to be covered by the claims of the present invention.

Claims

1. A liquid channel structure for multiple lines in one furnace, applied to a float glass production line; the inlet of the liquid channel structure is connected to a cooling part (1) of a glass melting furnace, and the outlet of the liquid channel structure is connected to a main line tin bath (2) and a branch line tin bath (2' / 2"); characterized in that: The liquid flow channel structure comprises a main line liquid flow channel and a branch line liquid flow channel. The main line liquid flow channel comprises a main line inlet section (3), a main line flow regulating section (4), a main line flow control section (5), and a main line outlet section (6). The molten glass enters the main line tin bath (2) from the cooling section (1) of the glass melting furnace through the main line inlet section (3), the main line flow regulating section (4), the main line flow control section (5), and the main line outlet section (6); the branch line liquid flow channel comprises a branch line cross-through section (16), a branch line flow control section (5' / 5"), and a branch line outlet section (6' / 6"), the branch line cross-through section (16) is connected to the outlet end of the main line flow regulating section (4), and the molten glass enters the branch line tin bath (2' / 2") from the main line flow regulating section (4) through the branch line cross-through section (16), the branch line flow control section (5' / 5"), and the branch line outlet section (6' / 6") 2. The one-kiln-multiple-line liquid channel structure according to claim 1, characterized in that: Each section in the fluid channel structure is composed of bottom bricks, pool wall bricks, breast wall bricks, and a cover plate (11). The pool wall bricks are arranged on the bottom bricks, the breast wall bricks are arranged on the pool wall bricks, and the cover plate (11) covers the breast wall bricks.

3. The one-kiln-multiple-line liquid channel structure according to claim 2, characterized in that: The main line inlet section (3) is provided with a main line thermocouple (8); an inlet section operation hole is opened on the breast wall brick at the main line inlet section (3); a water bag (17) is passed through the inlet section operation hole; an inlet section heating electrode (15) is provided on the pool wall brick at the main line inlet section (3); the water bag (17) in the inlet section operation hole cooperates with the inlet section heating electrode (15) to adjust the temperature of the molten glass at the main line inlet section (3).

4. The one-kiln-multiple-line liquid channel structure according to claim 1, characterized in that: The main line regulating section (4) is provided with a rotating gate plate (9), a main line regulating section heating hole (13) is provided on the pool wall brick at the main line regulating section (4), and a main line regulating section discharge hole (7) is provided on the bottom brick at the main line regulating section (4); a natural gas spray gun (18) or a space silicon carbon rod (19) is provided in the main line regulating section heating hole (13) for regulating the temperature of the molten glass at the main line regulating section (4).

5. The one-kiln-multiple-line liquid channel structure according to claim 4, characterized in that: It also comprises a driving source, which is in driving connection with the rotating gate plate (9), and the rotating direction and rotating speed of the rotating gate plate (9) are adjustable.

6. The one-kiln-multiple-line liquid channel structure according to claim 1, characterized in that: The main line control section (5) is provided with a main line control section gate plate (10) that can be raised and lowered; a main line control section operation hole (12) is provided on the breast wall brick at the main line control section (5); a water bag (17) is inserted through the main line control section operation hole (12); a main line control section heating electrode is provided on the pool wall brick at the main line control section (5); the water bag (17) in the main line control section operation hole (12) cooperates with the main line control section heating electrode to adjust the temperature of the molten glass at the main line control section (5).

7. The one-kiln-multiple-line liquid flow channel structure according to claim 1, characterized in that: A main line gas sealing hole (14) is provided at the main line outlet section (6), and protective gas is introduced into the main line gas sealing hole (14).

8. The one-kiln-multiple-line liquid channel structure according to claim 1, characterized in that: The branch line transverse section (16) is provided with a branch line thermocouple (8'), a branch line transverse section discharge hole (7') is provided on the bottom brick at the branch line transverse section (16), a branch line transverse section heating hole (13') is provided on the breast wall brick at the branch line transverse section (16), and a branch line transverse section heating electrode is provided in the branch line transverse section heating hole (13') for adjusting the temperature of the molten glass at the branch line transverse section (16).

9. The one-kiln-multiple-line liquid channel structure according to claim 1, characterized in that: The branch line control section (5' / 5") is provided with a liftable branch line control section gate (10' / 10"), a branch line control section operation hole is opened on the breast wall brick at the branch line control section (5' / 5"), a water bag (17) is passed through the branch line control section operation hole, and a branch line control section heating electrode is provided on the pool wall brick at the branch line control section (5' / 5"); the water bag (17) in the branch line control section operation hole cooperates with the branch line control section heating electrode to adjust the glass melt temperature at the branch line control section (5' / 5").

10. The one-kiln-multiple-line liquid channel structure according to claim 1, characterized in that: A branch line gas sealing hole is provided at the branch line outlet section (6' / 6"), and protective gas is introduced into the branch line gas sealing hole.

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