Liquid glass flow distribution device for a glass manufacturing system

By introducing an inert gas into the liquid glass flow device of the glass manufacturing system, the problem of platinum volatiles mixing into the liquid glass was solved, thus improving the composition and quality of the glass.

CN116730585BActive Publication Date: 2026-05-26AVANSTRATE TAIWAN INC +1

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Patents(China)
Current Assignee / Owner
AVANSTRATE TAIWAN INC
Filing Date
2023-02-14
Publication Date
2026-05-26

AI Technical Summary

Technical Problem

In traditional glass manufacturing systems, liquid glass flow devices are prone to contamination by platinum volatiles, affecting the glass composition and quality.

Method used

By setting up a gas transmission section in the liquid glass flow device, an inert gas, such as argon, is introduced into the glass flow section to form a gas space to suppress the mixing of platinum volatiles.

Benefits of technology

It effectively inhibits platinum volatiles from entering the liquid glass, improving the glass's composition and quality.

✦ Generated by Eureka AI based on patent content.

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Abstract

This invention discloses a liquid glass flow device for a glass manufacturing system, comprising: a glass flow section having a first end and a second end; a first gas transmission section connected to the glass flow section, the first gas transmission section having a first connecting opening and a first external opening, the first connecting opening communicating with the glass flow section, the first external opening being disposed outside the glass flow section; and a second gas transmission section connected to the glass flow section, the second gas transmission section having a second connecting opening and a second external opening, the second connecting opening communicating with the glass flow section, the second external opening being disposed outside the glass flow section; wherein the first connecting opening is close to the first end, and the second connecting opening is close to the second end. The liquid glass flow device for a glass manufacturing system of this invention can suppress the mixing of platinum volatiles into the liquid glass.
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Description

Technical Field

[0001] This invention relates to the field of glass manufacturing equipment technology, and in particular to a liquid glass flow device for a glass manufacturing system that can suppress the mixing of platinum volatiles into liquid glass. Background Technology

[0002] Traditional glass manufacturing systems often use platinum-based liquid glass flow devices. Therefore, during the glass manufacturing process, platinum volatiles generated at high temperatures in these devices can easily mix into the liquid glass, affecting its composition and quality. In view of this, there is a need for a liquid glass flow device in glass manufacturing systems that can suppress the mixing of platinum volatiles into the liquid glass. Summary of the Invention

[0003] The purpose of this invention is to provide a liquid glass flow device for a glass manufacturing system that can suppress the mixing of platinum volatiles into liquid glass.

[0004] The present invention provides a liquid glass flow device for a glass manufacturing system, comprising: a glass flow section having a first end and a second end; a first gas transmission section connected to the glass flow section, the first gas transmission section having a first connecting opening and a first external opening, the first connecting opening communicating with the glass flow section, the first external opening being disposed outside the glass flow section; and a second gas transmission section connected to the glass flow section, the second gas transmission section having a second connecting opening and a second external opening, the second connecting opening communicating with the glass flow section, the second external opening being disposed outside the glass flow section; wherein the first connecting opening is close to the first end, and the second connecting opening is close to the second end.

[0005] In a preferred embodiment of the present invention, the first gas transmission section has a first turning section extending into the glass flow section, and the first connecting opening is disposed at a first end of the first turning section; wherein the second gas transmission section has a second turning section extending into the glass flow section, and the second connecting opening is disposed at a second end of the second turning section; wherein the first turning section extends toward the first end and the second turning section extends toward the second end.

[0006] In a preferred embodiment of the present invention, the first gas transmission section is an air inlet section, the second gas transmission section is an air outlet section, the glass manufacturing system injects a gas into the glass flow section through the first gas transmission section, and the glass manufacturing system discharges the gas out of the glass flow section through the second gas transmission section.

[0007] In a preferred embodiment of the present invention, the gas is argon.

[0008] In a preferred embodiment of the present invention, the second gas transmission section is an air inlet and the first gas transmission section is an exhaust section. The glass manufacturing system injects a gas into the glass flow section via the second gas transmission section and discharges the gas out of the glass flow section via the first gas transmission section.

[0009] In a preferred embodiment of the present invention, the gas is argon.

[0010] In a preferred embodiment of the present invention, the liquid glass flow device for a glass manufacturing system further includes: a third gas transmission section connected to the glass flow section, the third gas transmission section having a third connecting opening and a third external opening, the third connecting opening communicating with the glass flow section, and the third external opening disposed outside the glass flow section; wherein the third gas transmission section is disposed between the first gas transmission section and the second gas transmission section.

[0011] In a preferred embodiment of the present invention, the first gas transmission section has a first turning section disposed within the glass flow section, and the first connecting opening is disposed at a first end of the first turning section; wherein the second gas transmission section has a second turning section disposed within the glass flow section, and the second connecting opening is disposed at a second end of the second turning section; wherein the first turning section extends toward the first end and the second turning section extends toward the second end.

[0012] In a preferred embodiment of the present invention, the first gas transmission section is a first air inlet, the second gas transmission section is a second air inlet, and the third gas transmission section is an exhaust section. The glass manufacturing system injects a gas into the glass flow section through the first gas transmission section and the second gas transmission section, and the glass manufacturing system discharges the gas to the outside of the glass flow section through the third gas transmission section.

[0013] In a preferred embodiment of the present invention, the gas is argon.

[0014] In a preferred embodiment of the present invention, the liquid glass flow device is a clarification tank.

[0015] In a preferred embodiment of the present invention, the liquid glass flow device is a stirring tank.

[0016] In a preferred embodiment of the present invention, the distance between the first connecting opening and the first end is less than 200 mm, and the distance between the second connecting opening and the second end is less than 200 mm.

[0017] In a preferred embodiment of the present invention, the distance between the first connecting opening and the first end is less than 150 mm, and the distance between the second connecting opening and the second end is less than 150 mm.

[0018] In a preferred embodiment of the present invention, the distance between the first connecting opening and the first end is less than 100 mm, and the distance between the second connecting opening and the second end is less than 100 mm.

[0019] In a preferred embodiment of the present invention, the distance between the first connecting opening and the first end is less than 50 mm, and the distance between the second connecting opening and the second end is less than 50 mm.

[0020] Compared with the prior art, the technical solution of the present invention has the following characteristics and advantages:

[0021] The liquid glass flow device for a glass manufacturing system described in this invention introduces gas into the liquid glass flow device through a gas transmission section, thereby suppressing platinum volatiles from mixing into the liquid glass. Attached Figure Description

[0022] Figure 1 This is a system architecture diagram of the liquid glass flow device for a glass manufacturing system according to the present invention.

[0023] Figure 2 This is a schematic diagram of a specific embodiment of the liquid glass circulation device of the present invention;

[0024] Figure 3 This is a schematic diagram of a specific embodiment of the liquid glass circulation device of the present invention;

[0025] Figure 4 This is a schematic diagram of a specific embodiment of the liquid glass circulation device of the present invention;

[0026] Figure 5 This is a schematic diagram of a specific embodiment of the gas transmission unit.

[0027] Explanation of icon numbers:

[0028] 100. Melting device; 101. Melting tank; 104. Conveying pipe; 120. Refining tank; 105. Conveying pipe; 103. Stirring tank; 106. Conveying pipe; 200. Forming device; 200. Liquid glass circulation device; 210. First gas transmission section; 212. First connecting opening; 214. First external opening; 220. Second gas transmission section; 222. Second connecting opening; 224. Second external opening; 230. Glass circulation section; 232. First end; 234. Second end; 250. Brick-making section; 260. Brick-making section; 272. Blocking section; 274. Blocking section; 276. Blocking section; 280. Gas space; 290. Liquid surface; 300. Liquid glass circulation device; 310. First gas transmission section; 312. First connecting opening; 314. First external opening; 316. First turning section; 3 20. Second gas transmission section; 322. Second connecting opening; 324. Second external opening; 326. Second turning section; 330. Glass flow section; 332. First end; 334. Second end; 400. Liquid glass flow device; 410. First gas transmission section; 412. First connecting opening; 414. First external opening; 416. First turning section; 420. Second gas transmission section; 422. Second connecting opening; 424. Second external opening; 426. Second turning section; 430. Third gas transmission section; 432. Third connecting opening; 434. Third external opening; 440. Glass flow section; 442. First end; 444. Second end; 510. Gas transmission section; 512. Connecting opening; 514. External opening; 516. Turning section; 518. Main body; 530. Glass flow section. Detailed Implementation

[0029] Please see Figure 1 The illustration shows a system architecture diagram of a glass manufacturing system incorporating the liquid glass flow device of the present invention for a glass manufacturing system. For example... Figure 1 In the illustrated embodiment, the glass manufacturing system includes a melting device 100 and a forming device 200. The melting device 100 includes a melting tank 101, a conveying pipe 104, a refining tank 120, a conveying pipe 105, a stirring tank 103, and a conveying pipe 106. The liquid glass flow device is either the refining tank 120 or the stirring tank 103. The conveying pipe 104 is disposed between the melting tank 101 and the refining tank 120, and connects the melting tank 101 and the refining tank 120. The conveying pipe 105 is disposed between the refining tank 120 and the stirring tank 103, and connects the refining tank 120 and the stirring tank 103. The conveying pipe 106 is disposed between the stirring tank 103 and the forming device 200, and connects the stirring tank 103 and the forming device 200.

[0030] exist Figure 1In the illustrated embodiment, the melting tank 101 dissolves the glass raw material within it into liquid glass, which is then conveyed to the refining tank 120 via the conveying pipe 104. The refining tank 120 removes air bubbles from the liquid glass using a refining agent, and the liquid glass is then conveyed to the stirring tank 103 via the conveying pipe 105. The stirring tank 103 uses stirring rods to uniformly agitate the liquid glass, and the liquid glass is then conveyed to the forming apparatus 200 via the conveying pipe 106. All or at least a portion of the refining tank 120 or the stirring tank 103 is made of platinum, or is a mixed metal containing platinum or a platinum plating.

[0031] Please see Figure 2 The illustration depicts a schematic diagram of a specific embodiment of the liquid glass flow device according to the present invention. For example... Figure 2 In the illustrated embodiment, the liquid glass flow device 200 of the glass manufacturing system includes a first gas transmission section 210, a second gas transmission section 220, and a glass flow section 230. Both the first gas transmission section 210 and the second gas transmission section 220 are connected to the glass flow section 230. The glass flow section 230 has a first end portion 232 and a second end portion 234. The first gas transmission section 210 has a first connecting opening 212 and a first external opening 214. The first connecting opening 212 connects to the glass flow section 230, and the first external opening 214 is located outside the glass flow section 230. The second gas transmission section 220 has a second connecting opening 222 and a second external opening 224. The second connecting opening 222 connects to the glass flow section 230, and the second external opening 224 is located outside the glass flow section 230. A brick-forming section 250 and a brick-forming section 260 may be provided on the outer side of the liquid glass flow device 200 to protect the liquid glass flow device 200 or to prevent hot gas from flowing out. In one specific embodiment, the glass flow section 230 is provided with a blocking section 272, a blocking section 274, and a blocking section 276.

[0032] In one specific embodiment, liquid glass (the area below the liquid surface 290 is the molten glass) flows from the first end 232 of the glass flow section 230 to the second end 234 of the glass flow section 230. The first gas transmission section 210 is an inlet, and the second gas transmission section 220 is an outlet. The glass manufacturing system can inject gas into the glass flow section 230 through the first gas transmission section 210, and the glass manufacturing system can discharge gas to the outside of the glass flow section 230 through the second gas transmission section 220 (thereby forming a gas space 280 in the glass flow section 230). The first gas transmission section 210 is located near the first end 232 of the glass flow section 230 (i.e., the first gas transmission section 210 is positioned near the first end 232, or it can be said that the first gas transmission section 210 is actually located at the first end 232), and the second gas transmission section 220 is located near the second end 234 of the glass flow section 230 (i.e., the second gas transmission section 220 is positioned near the second end 234, or it can be said that the second gas transmission section 220 is actually located at the second end 234). This avoids the situation where the liquid glass located at the first end 232 or the second end 234 has difficulty contacting the gas. Preferably, the gas is an inert gas, nitrogen, hydrogen, or a combination thereof. Preferably, the inert gas is argon. It should be understood that the aforementioned “first gas transmission section 210 near the first end 232 of glass flow section 230” also includes an embodiment in which “the first gas transmission section 210 is directly disposed at the first end 232 of glass flow section 230 (that is, the distance between the first gas transmission section 210 and the first end 232 of glass flow section 230 is 0mm)”, and the aforementioned “second gas transmission section 220 near the second end 234 of glass flow section 230” also includes an embodiment in which “the second gas transmission section 220 is directly disposed at the second end 234 of glass flow section 230 (that is, the distance between the second gas transmission section 220 and the second end 234 of glass flow section 230 is 0mm)”.

[0033] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 200 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 200 mm. This achieves a better effect.

[0034] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 200mm and greater than 0mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 200mm and greater than 0mm.

[0035] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 200 mm and greater than 5 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 200 mm and greater than 5 mm.

[0036] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 150 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 150 mm. This achieves a better effect.

[0037] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 150 mm and greater than 0 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 150 mm and greater than 0 mm.

[0038] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 150 mm and greater than 5 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 150 mm and greater than 5 mm.

[0039] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 100 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 100 mm. This achieves a better effect.

[0040] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 100mm and greater than 0mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 100mm and greater than 0mm.

[0041] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 100 mm and greater than 5 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 100 mm and greater than 5 mm.

[0042] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 50 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 50 mm. This achieves optimal results.

[0043] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 50 mm and greater than 0 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 50 mm and greater than 0 mm.

[0044] In one specific embodiment, the distance between the first gas transmission section 210 and the first end 232 of the glass flow section 230 is less than 50 mm and greater than 5 mm, and the distance between the second gas transmission section 220 and the second end 234 of the glass flow section 230 is less than 50 mm and greater than 5 mm.

[0045] In one specific embodiment, liquid glass (the area below the liquid surface 290 is the molten glass) flows from the first end 232 of the glass flow section 230 to the second end 234 of the glass flow section 230. The second gas transmission section 220 is an inlet, and the first gas transmission section 210 is an outlet. The glass manufacturing system can inject inert gas into the glass flow section 230 through the second gas transmission section 220, and the glass manufacturing system can discharge inert gas to the outside of the glass flow section 230 through the first gas transmission section 210 (thereby forming a gas space 280 in the glass flow section 230). The first gas transmission section 210 is located near the first end 232 of the glass flow section 230 (that is, the first gas transmission section 210 is disposed near the first end 232, or it can be said that the first gas transmission section 210 is actually disposed at the first end 232), and the second gas transmission section 220 is located near the second end 234 of the glass flow section 230 (that is, the second gas transmission section 220 is disposed near the second end 234, or it can be said that the second gas transmission section 220 is actually disposed at the second end 234). This avoids the situation where the liquid glass located at the first end 232 or the second end 234 has difficulty contacting the inert gas. Preferably, the inert gas is argon. It should be understood that the aforementioned “first gas transmission section 210 near the first end 232 of the glass flow section 230” also includes the embodiment of “the first gas transmission section 210 being directly disposed at the first end 232 of the glass flow section 230”, and the aforementioned “second gas transmission section 220 near the second end 234 of the glass flow section 230” also includes the embodiment of “the second gas transmission section 220 being directly disposed at the second end 234 of the glass flow section 230”.

[0046] Please see Figure 3 The illustration depicts a schematic diagram of a specific embodiment of the liquid glass flow device according to the present invention. For example... Figure 3In the illustrated embodiment, the liquid glass flow device 300 of the glass manufacturing system includes a first gas transmission section 310, a second gas transmission section 320, and a glass flow section 330. Both the first gas transmission section 310 and the second gas transmission section 320 are connected to the glass flow section 330. The glass flow section 330 has a first end portion 332 and a second end portion 334. The first gas transmission section 310 has a first connecting opening 312, a first external opening 314, and a first turning portion 316. The first turning portion 316 extends into the glass flow section 330, and the first connecting opening 312 is located at the end of the first turning portion 316. The first connecting opening 312 connects to the glass flow section 330, and the first external opening 314 is located outside the glass flow section 330. The second gas transmission section 320 has a second connecting opening 322, a second external opening 324, and a second turning section 326. The second turning section 326 extends into the glass flow section 330, and the second connecting opening 322 is located at the end of the second turning section 326. The second connecting opening 322 connects to the glass flow section 330, and the second external opening 324 is located outside the glass flow section 330. The first turning section 316 extends toward the first end 332, so that the first connecting opening 312 is close to and faces the first end 332. The second turning section 326 extends toward the second end 334, so that the second connecting opening 322 is close to and faces the second end 334. Therefore, when inert gas is injected into the glass flow section 330 from the first connecting opening 312 or the second connecting opening 322, the inert gas can be sprayed along the extending direction of the first turning section 316 or along the extending direction of the second turning section 326 to the first end 332 or the second end 334.

[0047] exist Figure 3In the illustrated embodiment, the first connecting opening 312 of the first gas transmission section 310 is located near the first end 332 of the glass flow section 330 (that is, the first gas transmission section 310 is disposed near the first end 332, or it can be said that the first gas transmission section 310 is actually disposed at the first end 332), while the second connecting opening 322 of the second gas transmission section 320 is located near the second end 334 of the glass flow section 330 (that is, the second gas transmission section 320 is disposed near the second end 334, or it can be said that the second gas transmission section 320 is actually disposed at the second end 334). This avoids the situation where the liquid glass located at the first end 332 or the second end 334 has difficulty contacting the injected gas. The gas is an inert gas, nitrogen, hydrogen, or a combination thereof. Preferably, the inert gas is argon. In one specific embodiment, the first connecting opening 312 of the first gas transmission section 310 is directly disposed at the first end 332 of the glass flow section 330, and the second connecting opening 322 of the second gas transmission section 320 is directly disposed at the second end 334 of the glass flow section 330. It should be understood that the aforementioned "the first connecting opening 312 of the first gas transmission section 310 is close to the first end 332 of the glass flow section 330" also includes the embodiment where "the first connecting opening 312 of the first gas transmission section 310 is directly disposed at the first end 332 of the glass flow section 330," and the aforementioned "the second connecting opening 322 of the second gas transmission section 320 is close to the second end 334 of the glass flow section 330" also includes the embodiment where "the second connecting opening 322 of the second gas transmission section 320 is directly disposed at the second end 334 of the glass flow section 330."

[0048] In one specific embodiment, liquid glass flows from the first end 332 of the glass flow section 330 to the second end 334 of the glass flow section 330. The first gas transmission section 310 is an inlet, and the second gas transmission section 320 is an outlet. The glass manufacturing system can inject gas into the glass flow section 330 via the first gas transmission section 310, and the glass manufacturing system can discharge gas to the outside of the glass flow section 330 via the second gas transmission section 320.

[0049] Please see Figure 4 The illustration depicts a schematic diagram of a specific embodiment of the liquid glass flow device according to the present invention. For example... Figure 4The illustrated embodiment shows a liquid glass flow device 400 in a glass manufacturing system, comprising a first gas transmission section 410, a second gas transmission section 420, a third gas transmission section 430, and a glass flow section 440. The first gas transmission section 410 and the second gas transmission section 420 are both connected to the glass flow section 440, and the third gas transmission section 430 is also connected to the glass flow section 440. The glass flow section 440 has a first end 442 and a second end 444. The first gas transmission section 410 has a first connecting opening 412, a first external opening 414, and a first turning section 416. The first turning section 416 extends into the glass flow section 440, and the first connecting opening 412 is located at the end of the first turning section 416. The first connecting opening 412 connects to the glass flow section 440, and the first external opening 414 extends outside the glass flow section 440. The second gas transmission section 420 has a second connecting opening 422, a second outer opening 424, and a second turning section 426. The second turning section 426 extends into the glass flow section 440, and the second connecting opening 422 is located at the end of the second turning section 426. The second connecting opening 422 connects to the glass flow section 440, and the second outer opening 424 is located outside the glass flow section 440. The third gas transmission section 430 is located between the first gas transmission section 410 and the second gas transmission section 420. The third gas transmission section 430 has a third connecting opening 432 and a third outer opening 434. The third connecting opening 432 connects to the glass flow section 440, and the third outer opening 434 is located outside the glass flow section 440. The first turning section 416 extends toward the first end portion 442, so that the first connecting opening 412 is close to and faces the first end portion 442. The second steering portion 426 extends toward the second end portion 444, so that the second connecting opening 422 is close to and faces the second end portion 444. This allows gas to be sprayed onto the first end portion 442 along the extending direction of the first steering portion 416 when gas is injected into the glass flow portion 440 from the first connecting opening 412. Furthermore, when gas is injected into the glass flow portion 440 from the second connecting opening 422, gas can be sprayed onto the second end portion 444 along the extending direction of the second steering portion 426.

[0050] exist Figure 4In the illustrated embodiment, the first gas transmission section 410 is an air inlet (which can be considered as the first air inlet), the second gas transmission section 420 is an air inlet (which can be considered as the second air inlet), and the third gas transmission section 430 is an exhaust section. The glass manufacturing system can inject inert gas into the glass flow section 440 through the first gas transmission section 410 and the second gas transmission section 420, and the glass manufacturing system can exhaust the gas to the outside of the glass flow section 440 through the third gas transmission section 430. The first connecting opening 412 of the first gas transmission section 410 is located near the first end 442 of the glass flow section 440 (that is, the first gas transmission section 410 is located near the first end 442, or it can be said that the first gas transmission section 410 is actually located at the first end 442), and the second connecting opening 422 of the second gas transmission section 420 is located near the second end 444 of the glass flow section 440 (that is, the second gas transmission section 420 is located near the second end 444, or it can be said that the second gas transmission section 420 is actually located at the second end 444). This avoids the situation where the liquid glass located at the first end 442 or the second end 444 cannot come into contact with the injected gas. The gas is an inert gas, nitrogen, hydrogen, or a combination thereof. Preferably, the inert gas is argon. It should be understood that the aforementioned “the first communication opening 412 of the first gas transmission section 410 is close to the first end 442 of the glass flow section 440” also includes the embodiment where “the first communication opening 412 of the first gas transmission section 410 is directly disposed at the first end 442 of the glass flow section 440”, and the aforementioned “the second communication opening 422 of the second gas transmission section 420 is close to the second end 444 of the glass flow section 440” also includes the embodiment where “the second communication opening 422 of the second gas transmission section 420 is directly disposed at the second end 444 of the glass flow section 440”.

[0051] Please see Figure 5 The illustration shows a schematic diagram according to a specific embodiment of the gas transmission unit. For example... Figure 5 In the illustrated embodiment, the gas transmission section 500 has a communicating opening 512, an external opening 514, a turning section 516, and a main body 518. The turning section 516 is connected to the main body 518, the communicating opening 512 is located at the end of the turning section 516, and the external opening 514 is located at the end of the main body 518. Preferably, the main body 518 is connected to the glass flow section 530 of the liquid glass flow device, and the turning section 516 extends into the glass flow section 530. The main body 518 may be perpendicular or substantially perpendicular to the glass flow section 530 as needed, and the turning section 516 may be parallel or substantially parallel to the glass flow section 530 as needed. It should be understood that both the first gas transmission section and the second gas transmission section of the liquid glass flow device 400 of the present invention can be adopted. Figure 5 The embodiment of the gas transmission unit 500 shown.

[0052] Thus, the liquid glass flow device for a glass manufacturing system of the present invention has been described above with reference to the accompanying drawings. However, it should be understood that the various specific embodiments of the present invention are merely illustrative, and various modifications can be made without departing from the scope of protection of the claims of the present invention, and all such modifications should be included within the scope of protection of the claims of the present invention. Therefore, the specific embodiments described in this specification are not intended to limit the present invention, and the actual scope of protection of the present invention should be determined by the contents of the claims.

Claims

1. A liquid glass flow device for a glass manufacturing system, characterized in that, include: A glass flow section having a first end and a second end; A first gas transmission section is connected to the glass flow section. The first gas transmission section has a first connecting opening and a first external opening. The first connecting opening is connected to the glass flow section, and the first external opening is located outside the glass flow section. as well as A second gas transmission section is connected to the glass flow section. The second gas transmission section has a second communication opening and a second external opening. The second communication opening is connected to the glass flow section, and the second external opening is located outside the glass flow section. The first connecting opening is close to and faces the first end, and the second connecting opening is close to and faces the second end; the first gas transmission section has a first deflecting section extending into the glass flow section, and the first connecting opening is located at a first end of the first deflecting section; the second gas transmission section has a second deflecting section extending into the glass flow section, and the second connecting opening is located at a second end of the second deflecting section; the first deflecting section extends toward the first end, and the second deflecting section extends toward the second end; when inert gas is injected into the glass flow section from the first connecting opening or the second connecting opening, the inert gas can be sprayed to the first end or the second end along the extending direction of the first deflecting section or along the extending direction of the second deflecting section.

2. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The first gas transmission section is an inlet section, and the second gas transmission section is an outlet section. The glass manufacturing system injects a gas into the glass flow section through the first gas transmission section, and the glass manufacturing system discharges the gas out of the glass flow section through the second gas transmission section.

3. The liquid glass flow device for a glass manufacturing system according to claim 2, characterized in that, The gas is argon.

4. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The second gas transmission section is an inlet section, and the first gas transmission section is an outlet section. The glass manufacturing system injects a gas into the glass flow section through the second gas transmission section, and the glass manufacturing system discharges the gas out of the glass flow section through the first gas transmission section.

5. The liquid glass flow device for a glass manufacturing system according to claim 4, characterized in that, The gas is argon.

6. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The liquid glass flow device for the glass manufacturing system further includes: A third gas transmission section is connected to the glass flow section. The third gas transmission section has a third connecting opening and a third external opening. The third connecting opening is connected to the glass flow section, and the third external opening is located outside the glass flow section. The third gas transmission unit is disposed between the first gas transmission unit and the second gas transmission unit.

7. The liquid glass flow device for a glass manufacturing system according to claim 6, characterized in that, The first gas transmission section is a first air inlet, the second gas transmission section is a second air inlet, and the third gas transmission section is an exhaust section. The glass manufacturing system injects a gas into the glass flow section through the first gas transmission section and the second gas transmission section, and the glass manufacturing system exhausts the gas to the outside of the glass flow section through the third gas transmission section.

8. The liquid glass flow device for a glass manufacturing system according to claim 7, characterized in that, The gas is argon.

9. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The liquid glass flow device is a clarification tank.

10. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The liquid glass circulation device is a stirring tank.

11. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The distance between the first connecting opening and the first end is less than 200mm, and the distance between the second connecting opening and the second end is less than 200mm.

12. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The distance between the first connecting opening and the first end is less than 150mm, and the distance between the second connecting opening and the second end is less than 150mm.

13. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The distance between the first connecting opening and the first end is less than 100mm, and the distance between the second connecting opening and the second end is less than 100mm.

14. The liquid glass flow device for a glass manufacturing system according to claim 1, characterized in that, The distance between the first connecting opening and the first end is less than 50 mm, and the distance between the second connecting opening and the second end is less than 50 mm.