CN220245898U - Substrate glass extraction amount control and glass liquid homogenization feeding device - Google Patents
Substrate glass extraction amount control and glass liquid homogenization feeding device Download PDFInfo
- Publication number
- CN220245898U CN220245898U CN202321570347.0U CN202321570347U CN220245898U CN 220245898 U CN220245898 U CN 220245898U CN 202321570347 U CN202321570347 U CN 202321570347U CN 220245898 U CN220245898 U CN 220245898U
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- feeding
- tube
- heater
- pipe
- glass
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- 239000011521 glass Substances 0.000 title claims abstract description 71
- 239000007788 liquid Substances 0.000 title claims abstract description 38
- 239000000758 substrate Substances 0.000 title claims abstract description 31
- 238000000605 extraction Methods 0.000 title claims abstract description 20
- 238000000265 homogenisation Methods 0.000 title claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 14
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 20
- 229910052697 platinum Inorganic materials 0.000 claims description 10
- 239000012774 insulation material Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 229910000629 Rh alloy Inorganic materials 0.000 claims description 3
- 239000000956 alloy Substances 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 3
- PXXKQOPKNFECSZ-UHFFFAOYSA-N platinum rhodium Chemical compound [Rh].[Pt] PXXKQOPKNFECSZ-UHFFFAOYSA-N 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 10
- 230000001276 controlling effect Effects 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 230000035484 reaction time Effects 0.000 abstract description 3
- 230000001105 regulatory effect Effects 0.000 abstract description 2
- 238000001816 cooling Methods 0.000 abstract 1
- 239000006060 molten glass Substances 0.000 description 4
- 230000007547 defect Effects 0.000 description 2
- 238000003280 down draw process Methods 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
The utility model discloses a substrate glass extraction amount control and glass liquid homogenization feeding device and a method, which belong to the field of substrate glass manufacture, and comprise a feeding device and an auxiliary heating device, wherein the feeding device consists of a feeding inner tube and a feeding outer tube; the auxiliary heating device consists of an inner heater and an outer heater. According to the utility model, the internal and external glass liquid is heated simultaneously by adjusting the differential current of the internal heater and the external heater, so that the temperature of the internal and external glass liquid is raised and lowered simultaneously, the temperature uniformity of the glass liquid after heating or cooling is ensured, the reaction time for regulating and controlling the extraction quantity is shortened, and the accurate control of the extraction quantity is realized.
Description
Technical Field
The utility model belongs to the field of substrate glass manufacturing, and particularly relates to a substrate glass output control and glass liquid homogenization feeding device.
Background
The substrate glass is one of important raw materials for forming the liquid crystal panel, has great influence on the performance of the panel product, and the indexes such as resolution, transmittance, thickness, weight, visual angle and the like of the panel product are closely related to the quality of the adopted substrate glass.
The production process of the substrate glass is to melt the batch materials at high temperature through a tank furnace to form glass liquid, and the temperature of the high-temperature glass liquid can meet the forming feeding conditions through the processes of temperature rising, clarification, temperature lowering, stirring and the like of a platinum channel. The feeding device is one of key equipment in the production and manufacture process of the substrate glass, and has the main function of stably and uniformly feeding glass liquid into the forming process to realize high-quality overflow down-drawing of the forming process.
Based on the fluctuation of the glass liquid feeding temperature and the reason of stable control of the extraction quantity, the feeding device needs to continuously heat the glass liquid to ensure the required feeding temperature and stable extraction quantity, however, the heating of a single-side heater in the current feeding device can cause the non-uniformity of the internal and external temperatures of the fed glass liquid, meanwhile, the reaction time of the glass liquid to the temperature is prolonged, the rapid reaction and the accurate control of the extraction quantity adjustment cannot be realized, the molding overflow down-drawing quality is further influenced, and the defects of non-uniformity of the thickness, stress, and warping of the substrate glass do not meet the requirements and the like are caused.
Disclosure of Invention
The utility model provides a precise control and glass liquid homogenizing and feeding device for substrate glass, which is used for solving the problems that the substrate glass is defective and rapid reaction and precise control of the adjustment of the extraction amount cannot be realized due to the uneven temperature inside and outside the glass liquid to be fed.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
a substrate glass output control and glass liquid homogenization feeding device comprises a feeding device and an auxiliary heating device; the feeding device comprises a feeding inner pipe and a feeding outer pipe, wherein the feeding inner pipe is arranged inside the feeding outer pipe, the feeding outer pipe comprises a feeding upper outer pipe, a feeding middle outer pipe, a feeding lower outer pipe and a reducing circular pipe, the feeding upper outer pipe is arranged at the upper port of the feeding middle outer pipe, the feeding lower outer pipe is arranged at the lower port of the feeding middle outer pipe, and the feeding upper outer pipe, the feeding middle outer pipe and the feeding lower outer pipe are connected through the reducing circular pipe; the auxiliary heating device comprises an inner heater and an outer heater, wherein the inner heater is arranged inside the feeding inner pipe and is matched with the feeding inner pipe, and the outer heater surrounds the feeding outer pipe and is matched with the feeding outer pipe.
Further, the upper feeding outer tube, the middle feeding outer tube and the lower feeding outer tube adopt round straight tubes, the round straight tubes are hollow cylinders, and the diameter-changing round tubes are hollow round tables.
Further, the circular cross-section diameter of the outer tube in the feeding is larger than that of the lower outer tube in the feeding; the length of the outer tube in the feeding is equal to the length of the lower outer tube in the feeding and the length of the upper outer tube in the feeding.
Further, the feeding inner tube adopts a circular straight tube and a conical tube, and the conical tube is arranged at the port of the circular straight tube of the feeding inner tube.
Further, the inner feeding pipe and the outer feeding pipe are made of platinum-rhodium alloy materials, the outer side of the outer heater is wrapped with heat-insulating materials, and the heat-insulating materials, the inner heater and the outer heater are made of aluminum oxide materials.
Further, the inner heater is cylindrical in shape.
Further, an inner filling gap is formed between the inner heater and the feeding inner pipe, an outer filling gap is formed between the outer heater and the feeding outer pipe, and a feeding space is formed between the feeding inner pipe and the feeding outer pipe; the width of the inner filling gap and the outer filling gap is 10-20 mm.
Further, alumina powder is used as the filler for the inner filling gap and the outer filling gap.
Further, the length of the feeding inner pipe is smaller than that of the feeding outer pipe, and glass liquid in the feeding space is guaranteed to be integrated at the outlet of the feeding device.
Further, the inner heater and the outer heater are internally embedded with pure platinum wires, and the diameter of the pure platinum wires is 2.5-3.0 mm.
Compared with the prior art, the utility model has the following beneficial effects:
the utility model provides a substrate glass extraction amount control and glass liquid homogenization feeding device, which is provided with a feeding device and an auxiliary heating device, wherein the feeding device consists of an inner feeding pipe and an outer feeding pipe, and the inner feeding pipe is arranged in the outer feeding pipe; the auxiliary heating device comprises an inner heater and an outer heater, the inner heater is arranged inside the feeding inner pipe, the outer heater is arranged outside the feeding outer pipe, the structure can ensure uniformity of temperature of formed glass liquid, defects of substrate glass caused by non-uniformity of temperature are avoided, and the arrangement of the inner heater and the outer heater can realize rapid reaction and accurate control of lead-out quantity adjustment, so that production efficiency is effectively improved.
Drawings
FIG. 1 is a schematic diagram of a supply device for precisely controlling the amount of glass drawn from a substrate and homogenizing the glass.
FIG. 2 is an axial sectional view of a supply device for precise control of the amount of extraction of glass from a substrate and homogenization of the glass liquid.
FIG. 3 is a longitudinal sectional view of a supply device for precisely controlling the amount of drawn glass from a substrate and homogenizing the glass.
FIG. 4 is an enlarged partial view of a longitudinal section of a supply device for precisely controlling the amount of glass drawn from a substrate.
Wherein, 1, a feeding device; 2. an auxiliary heating device; 3. a feeding inner tube; 4. a feed outer tube; 4-1, feeding an upper outer tube; 4-2, feeding middle and outer tubes; 4-3, feeding the lower outer tube; 5. a feed space; 6. an inner heater; 7. filling a gap; 8. an external heater; 9. filling the gap; 10. a thermal insulation material.
Detailed Description
In order that those skilled in the art may better understand the present utility model, a further detailed description of the technical solution of the present utility model will be given below with reference to the accompanying drawings, which are given by way of illustration and not limitation.
It should be noted that the terms "comprises" and "comprising," and any variations thereof, in the description and claims of the present utility model are intended to cover a non-exclusive inclusion, such that a process, method, system, article, or apparatus that comprises a list of steps or elements is not necessarily limited to those steps or elements that are expressly listed or inherent to such process, method, article, or apparatus.
The device comprises a platinum feeding device 1 and an auxiliary heating device 2, wherein the platinum feeding device 1 comprises a feeding inner tube 3 and a feeding outer tube 4, and a feeding space 5 is formed between the feeding inner tube 3 and the feeding outer tube 4; the auxiliary heating device 2 comprises an inner heater 6 and an outer heater 8, an inner filling gap 7 is formed between the inner heater 6 and the feeding inner wall 3, and an outer filling gap 9 is formed between the outer heater 8 and the feeding outer wall 4; the periphery of the external heater 8 is provided with a heat insulation material 10; the molten glass in the feed space 5 is collected at the outlet of the feed device.
The feeding inner pipe 3 is a circular straight pipe with the diameter of 130-150 mm;
the outer feeding pipe 4 is a circular straight pipe with unequal diameters,
the diameter of the feeding upper outer tube 4-1 is 150-170 mm, and the height is 300-400 mm;
the diameter of the outer tube 4-2 in the feeding is 300-340 mm, and the height is 300-350 mm;
the diameter of the feeding lower outer tube 4-3 is 190-230 mm, and the height is 900-1000 mm;
the upper part 4-1 of the outer feeding pipe and the lower part 4-3 of the outer feeding pipe are connected through a reducing circular pipe;
the wall thickness of the feeding inner pipe 3 and the feeding outer pipe 4 is 0.8 mm-1.2 mm, the materials are platinum-rhodium alloy materials, and the rhodium mass ratio is more than or equal to 5%;
the auxiliary heating device 2 is divided into 5-10 groups from top to bottom, each group comprises an inner heater (6) and an outer heater (8), the outer heater (8) and the feeding outer tube (4) have the same shape and are installed in a matched manner; the inner heater (6) is cylindrical in shape.
The inner heater 6, the outer heater 8 and the heat insulation material 10 are made of aluminum oxide, the heat conductivity coefficient is less than or equal to 3 kcal/(m.h. DEGC), and the thickness of the heat insulation material 10 is 50-150 mm;
pure platinum wires are embedded and wound inside the inner heater 6 and the outer heater 8, and heat is spontaneously generated through the platinum after the power is on, wherein the diameter of the pure platinum wires is 2.5-3.0 mm;
the widths of the inner filling gap 7 and the outer filling gap 9 are 10-20 mm;
the filler in the inner filling gap 7 and the outer filling gap 9 is alumina powder, which is mixed with pure water with the temperature of 60-90 ℃ according to the following proportion (2-5): 1 are prepared into slurry according to the proportion for casting.
A method for precisely controlling the extraction amount of substrate glass and homogenizing and feeding glass liquid comprises the following steps: when the molten glass enters the feeding device from the feeding inlet and the forming sends out a command of reducing or increasing the extraction quantity, the feeding device adjusts the temperature of the molten glass to rise or fall for extraction quantity control, namely, the current of the inner heater 6 and the current of the outer heater 8 are adjusted to realize the same rise and fall of the internal temperature and the external temperature of the molten glass, so that the reaction time for regulating and controlling the extraction quantity is shortened, and the accurate control of the extraction quantity is realized.
Glass liquid enters the feeding device from the feeding inlet, when the temperature of the glass liquid is smaller than or larger than the feeding temperature required by molding, the glass liquid is required to be heated or cooled, namely, the inside and the outside of the glass liquid are heated simultaneously by adjusting the differential current of the inner heater 6 and the outer heater 8, and the temperature uniformity of the glass liquid after the temperature is raised or cooled is ensured.
It will be appreciated by those skilled in the art that the utility model can be practiced in other embodiments that depart from the spirit or essential characteristics thereof. Accordingly, the above disclosed embodiments are illustrative in all respects only and not restrictive, and all changes coming within the meaning and equivalency range of the utility model are intended to be embraced therein.
Claims (10)
1. The substrate glass discharge amount control and glass liquid homogenization feeding device is characterized by comprising a feeding device (1) and an auxiliary heating device (2);
the feeding device (1) comprises an inner feeding pipe (3) and an outer feeding pipe (4), the inner feeding pipe (3) is arranged inside the outer feeding pipe (4), the outer feeding pipe (4) comprises an upper feeding pipe (4-1), an middle feeding pipe (4-2), a lower feeding pipe (4-3) and a reducing circular pipe, the upper port of the middle feeding pipe (4-2) is provided with the upper feeding pipe (4-1), the lower port of the middle feeding pipe (4-2) is provided with the lower feeding pipe (4-3), and the upper feeding pipe (4-1), the middle feeding pipe (4-2) and the lower feeding pipe (4-3) are connected through the reducing circular pipe;
the auxiliary heating device (2) comprises an inner heater (6) and an outer heater (8), wherein the inner heater (6) is arranged inside the feeding inner tube (3) and is matched with the feeding inner tube (3), and the outer heater (8) surrounds the feeding outer tube (4) and is matched with the feeding outer tube (4).
2. The substrate glass extraction amount control and glass liquid homogenization feeding device according to claim 1, wherein the upper feeding outer tube (4-1), the middle feeding outer tube (4-2) and the lower feeding outer tube are round straight tubes, the shape of the round straight tubes is a hollow cylinder, and the shape of the diameter-variable round tubes is a hollow round table.
3. The substrate glass discharge amount control and glass liquid homogenizing and feeding device according to claim 2, wherein the circular cross-sectional diameter of the feeding middle outer tube (4-2) is larger than the circular cross-sectional diameter of the feeding lower outer tube (4-3) by larger than the circular cross-sectional diameter of the feeding upper outer tube (4-1);
the length of the feeding middle outer tube (4-2) is equal to the length of the feeding lower outer tube (4-3) and the length of the feeding upper outer tube (4-1).
4. The substrate glass extraction amount control and glass liquid homogenization feeding device according to claim 1, wherein the feeding inner tube (3) adopts a circular straight tube and a conical tube, and the conical tube is arranged at the port of the circular straight tube of the feeding inner tube (3).
5. The substrate glass extraction amount control and glass liquid homogenization feeding device according to claim 1, wherein the feeding inner tube (3) and the feeding outer tube (4) are made of platinum-rhodium alloy materials, the outer side of the outer heater (8) is wrapped with a heat insulation material (10), and the heat insulation material (10), the inner heater (6) and the outer heater (8) are made of aluminum oxide materials.
6. The substrate glass discharge amount control and glass liquid homogenizing and feeding device according to claim 1, wherein the inner heater (6) has a cylindrical shape.
7. The substrate glass discharge amount control and glass liquid homogenizing and feeding device according to claim 1, wherein an inner filling gap (7) is formed between the inner heater (6) and the feeding inner tube (3), an outer filling gap (9) is formed between the outer heater (8) and the feeding outer tube (4), and a feeding space (5) is formed between the feeding inner tube (3) and the feeding outer tube (4); the width of the inner filling gap (7) and the outer filling gap (9) is 10-20 mm.
8. The substrate glass discharge amount control and glass liquid homogenizing and feeding device according to claim 7, wherein alumina powder is used as the filler for the inner filling gap (7) and the outer filling gap (9).
9. The substrate glass discharge amount control and glass liquid homogenizing and feeding device according to claim 7, wherein the length of the inner feeding tube (3) is smaller than the length of the outer feeding tube (4), and the glass liquid in the feeding space (5) is ensured to be integrated at the outlet of the feeding device.
10. The substrate glass extraction amount control and glass liquid homogenization feeding device according to claim 1, wherein pure platinum wires are embedded and wound inside the inner heater (6) and the outer heater (8), and the diameter of the pure platinum wires is 2.5-3.0 mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321570347.0U CN220245898U (en) | 2023-06-19 | 2023-06-19 | Substrate glass extraction amount control and glass liquid homogenization feeding device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321570347.0U CN220245898U (en) | 2023-06-19 | 2023-06-19 | Substrate glass extraction amount control and glass liquid homogenization feeding device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220245898U true CN220245898U (en) | 2023-12-26 |
Family
ID=89231406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321570347.0U Active CN220245898U (en) | 2023-06-19 | 2023-06-19 | Substrate glass extraction amount control and glass liquid homogenization feeding device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220245898U (en) |
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2023
- 2023-06-19 CN CN202321570347.0U patent/CN220245898U/en active Active
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