CN203922969U - A kind of glass-melting furnace - Google Patents
A kind of glass-melting furnace Download PDFInfo
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- CN203922969U CN203922969U CN201420344527.1U CN201420344527U CN203922969U CN 203922969 U CN203922969 U CN 203922969U CN 201420344527 U CN201420344527 U CN 201420344527U CN 203922969 U CN203922969 U CN 203922969U
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- 238000002844 melting Methods 0.000 title claims abstract description 58
- 230000008018 melting Effects 0.000 claims abstract description 47
- 238000005352 clarification Methods 0.000 claims abstract description 33
- 238000000265 homogenisation Methods 0.000 claims abstract description 33
- 238000001816 cooling Methods 0.000 claims abstract description 28
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 238000009413 insulation Methods 0.000 claims abstract description 3
- 239000012530 fluid Substances 0.000 claims abstract 7
- 238000003723 Smelting Methods 0.000 claims abstract 4
- 229910001120 nichrome Inorganic materials 0.000 claims abstract 2
- 230000021715 photosynthesis, light harvesting Effects 0.000 abstract 1
- 239000011521 glass Substances 0.000 description 24
- 239000006060 molten glass Substances 0.000 description 17
- 239000007788 liquid Substances 0.000 description 15
- 239000000155 melt Substances 0.000 description 10
- 239000000156 glass melt Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000010309 melting process Methods 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 238000005485 electric heating Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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Abstract
Description
技术领域technical field
本实用新型涉及一种熔炉,具体地说是涉及一种玻璃熔炉。The utility model relates to a melting furnace, in particular to a glass melting furnace.
背景技术Background technique
玻璃熔制是指将合格的配合料经过高温加热熔融,形成透明、纯净、均匀并适合于成型玻璃液的过程。玻璃的熔制包括一系列物理化学的现象和反应;这些现象和反应的结果,使各种配合料变成了复杂的熔融物即玻璃液。玻璃的熔制过程大致可分为五个阶段:硅酸盐的形成→玻璃液的形成→玻璃液的澄清→玻璃液的均化→玻璃液的冷却。玻璃液形成阶段结束后,整个熔融体包含有许多气泡(其中直径小于0.3毫米的叫小气泡),继续加温,降低粘度,从玻璃液中除去可见的气体夹杂物的过程,称为玻璃液的澄清,它是玻璃熔制过程中的重要阶段。实际生产中要设法提高澄清温度,以降低玻璃液粘度,促使气泡快速排除。玻璃液的冷却是熔制过程的最后阶段,其目的是为了将玻璃液的粘度提高到成型所需的范围。玻璃液的冷却必须均匀,不能破坏均化的成果。一般采取自然冷却,主要依靠玻璃液面以及池壁池底向外均匀的热辐射来进行冷却。Glass melting refers to the process of heating and melting qualified batch materials at high temperature to form transparent, pure, uniform and suitable for forming glass liquid. The melting of glass includes a series of physical and chemical phenomena and reactions; as a result of these phenomena and reactions, various batch materials become complex melts, namely molten glass. The glass melting process can be roughly divided into five stages: the formation of silicate → the formation of molten glass → the clarification of molten glass → the homogenization of molten glass → the cooling of molten glass. After the glass melt formation stage is over, the whole melt contains many bubbles (among which the diameter is less than 0.3 mm called small bubbles), continue to heat, reduce the viscosity, and remove visible gas inclusions from the glass melt, called glass melt The clarification of glass is an important stage in the glass melting process. In actual production, it is necessary to try to increase the clarification temperature to reduce the viscosity of the glass liquid and promote the rapid removal of air bubbles. The cooling of the molten glass is the final stage of the melting process, and its purpose is to increase the viscosity of the molten glass to the range required for molding. The cooling of the molten glass must be uniform, and the result of homogenization must not be damaged. Generally, natural cooling is adopted, mainly relying on the uniform heat radiation from the glass liquid surface and the pool wall and bottom to the outside for cooling.
现在使用的玻璃粉熔化窑炉大部分是采用煤或煤气灯为燃料进行加热,能量浪费严重而且存在污染的问题。玻璃粉熔化窑炉的设置基本上采用在窑炉底部开始熔体口引流的方式,熔融体和需要熔化的原料混杂一体,造成玻璃制品质量不高;或者是整体融化后进入冷却后进行产品作业,造成作业流程时间延长。Most of the glass powder melting furnaces currently in use use coal or gas lamps as fuel for heating, which leads to serious energy waste and pollution problems. The setting of the glass powder melting furnace basically adopts the method of starting the melt port drainage at the bottom of the furnace. The molten body and the raw materials to be melted are mixed together, resulting in low quality glass products; , resulting in an extended operating process time.
发明内容Contents of the invention
本实用新型的目的是提供一种采用电能熔融,熔体均一性佳、可连续化生产的玻璃熔炉。The purpose of the utility model is to provide a glass melting furnace which adopts electric energy melting, has good melt uniformity and can be produced continuously.
本实用新型解决的是现有的玻璃熔化窑炉存在的能源浪费大、连续生产性差、玻璃熔体均一度差、玻璃制品质量不高等缺陷。The utility model solves the defects of the existing glass melting furnaces such as large energy waste, poor continuous productivity, poor uniformity of glass melt, and low quality of glass products.
本实用新型解决技术问题所采用的技术方案是:一种玻璃熔炉,包括包围整个熔炉的保温层,所述熔炉包括熔化区、澄清均化区和冷却区;所述熔化区和澄清均化区的炉壁上设有加热层;所述加热层内布满电热丝;所述的熔化区与进料口相连;所述的冷却区与出料口相连;所述熔化区与澄清均化区之间设有第一隔离墙;所述的第一隔离墙上均匀开设有若干个第一流液孔;所述澄清均化区和冷却区之间设有第二隔离墙;所述的第二隔离墙底部设有第二流液孔;所述澄清均化区的顶部设有出气口;所述冷却区内纵向设有若干挡板。The technical solution adopted by the utility model to solve the technical problem is: a glass melting furnace, including an insulating layer surrounding the entire melting furnace, the melting furnace includes a melting zone, a clarification homogenization zone and a cooling zone; the melting zone and the clarification homogenization zone A heating layer is provided on the furnace wall; the heating layer is covered with electric heating wires; the melting zone is connected to the feed port; the cooling zone is connected to the discharge port; the melting zone is connected to the clarification and homogenization zone A first partition wall is provided between them; several first flow holes are evenly opened on the first partition wall; a second partition wall is provided between the clarification and homogenization zone and the cooling zone; A second flow hole is provided at the bottom of the partition wall; an air outlet is provided at the top of the clarification and homogenization zone; several baffles are longitudinally provided in the cooling zone.
所述冷却区内的挡板数为三个,依次为第一挡板、第二挡板和第三挡板;所述第一挡板的底部与炉体相连,顶部为熔体流道;所述第二挡板的顶部与炉体相连,底部为熔体流道;所述第三挡板的底部与炉体相连,顶部为熔体流道。使玻璃液沿着挡板曲线流动,流动过程中玻璃液通过与挡板之间的热交换实现降温;可以根据出料时玻璃液温度的需要,调整挡板的个数和高度。The number of baffles in the cooling zone is three, which are the first baffle, the second baffle and the third baffle in turn; the bottom of the first baffle is connected to the furnace body, and the top is a melt flow channel; The top of the second baffle is connected to the furnace body, and the bottom is a melt flow channel; the bottom of the third baffle is connected to the furnace body, and the top is a melt flow channel. The molten glass flows along the curve of the baffle, and the temperature of the molten glass is reduced through heat exchange with the baffle during the flow process; the number and height of the baffles can be adjusted according to the temperature of the molten glass during discharge.
所述的第一流液孔有三个;所述第一流液孔的高度为15~20cm。第一流液孔的设计,可以使玻璃液流经时产生一定的湍流,有助于气泡逸出和均化。There are three first liquid flow holes; the height of the first liquid flow holes is 15-20 cm. The design of the first flow hole can generate a certain turbulent flow when the molten glass flows through, which is helpful for the escape and homogenization of bubbles.
所述的第二流液孔的高度为20~25cm。The height of the second liquid flow hole is 20-25 cm.
所述熔化区的侧壁和底部设有测温热电偶。Temperature measuring thermocouples are installed on the side wall and bottom of the melting zone.
所述澄清均化区的侧壁和底部设有测温热电偶。The side wall and bottom of the clarification and homogenization zone are provided with temperature measuring thermocouples.
所述出料口两侧设有测温热电偶。Temperature-measuring thermocouples are arranged on both sides of the discharge port.
所述澄清均化区中加热层的温度高于所述熔化区中加热层的温度。The temperature of the heating layer in the clarification and homogenization zone is higher than the temperature of the heating layer in the melting zone.
本实用新型的有益效果是:与现有技术相比,本实用新型提供的玻璃熔炉,炉体内分隔成熔化区、澄清均化区和冷却区,熔化区和澄清均化区采用不同的加热温度以及第一流液孔的设计,使玻璃熔体充分澄清均化;冷却区中采用挡板使熔体曲线流动,使冷却均匀、稳定,最终得到高品质的玻璃熔体。此外,本实用新型提供的玻璃熔炉采用电能加热,减少了能源浪费;整个玻璃的熔化过程可以持续进行,利于连续化生产。The beneficial effects of the utility model are: compared with the prior art, in the glass melting furnace provided by the utility model, the furnace body is divided into a melting zone, a clarification and homogenization zone and a cooling zone, and the melting zone and the clarification and homogenization zone adopt different heating temperatures And the design of the first flow hole makes the glass melt fully clarified and homogenized; the baffle plate is used in the cooling zone to make the melt curve flow, so that the cooling is uniform and stable, and finally a high-quality glass melt is obtained. In addition, the glass melting furnace provided by the utility model is heated by electric energy, which reduces energy waste; the entire glass melting process can be continuously carried out, which is beneficial to continuous production.
附图说明Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
具体实施方式Detailed ways
下面结合附图和实施例对本实用新型作进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is further described.
如图1所示,一种玻璃熔炉,包括包围整个熔炉的保温层1,所述熔炉包括熔化区15、澄清均化区12和冷却区9;所述熔化区15和澄清均化区12的炉壁上设有加热层2;所述加热层2内布满电热丝3;所述的熔化区15与进料口17相连;所述的冷却区9与出料口8相连;所述熔化区15与澄清均化区12之间设有第一隔离墙13;所述的第一隔离墙13上均匀开设有三个第一流液孔14;所述第一流液孔14的高度为15~20cm,本实施例中优选的高度为18cm。所述澄清均化区12和冷却区9之间设有第二隔离墙10;所述的第二隔离墙10底部设有第二流液孔11;所述的第二流液孔11的高度为20~25cm,本实施例中优选的高度为22cm。所述澄清均化区12的顶部设有出气口4。所述冷却区9内纵向设有三块挡板,依次为第一挡板5、第二挡板6和第三挡板7;所述第一挡板的底部与炉体相连,顶部为熔体流道;所述第二挡板的顶部与炉体相连,底部为熔体流道;所述第三挡板的底部与炉体相连,顶部为熔体流道。所述熔化区15、澄清均化区12的侧壁和底部均设有测温热电偶16,所述出料口8两侧也设有测温热电偶。所述澄清均化区12中加热层的温度高于所述熔化区15中加热层的温度。As shown in Figure 1, a kind of glass melting furnace comprises the insulation layer 1 that surrounds the whole melting furnace, and the melting furnace includes a melting zone 15, a clarification and homogenization zone 12 and a cooling zone 9; The furnace wall is provided with a heating layer 2; the heating layer 2 is covered with electric heating wires 3; the melting zone 15 is connected to the feed port 17; the cooling zone 9 is connected to the discharge port 8; the melting A first separation wall 13 is provided between the zone 15 and the clarification and homogenization zone 12; three first liquid flow holes 14 are evenly opened on the first separation wall 13; the height of the first liquid flow holes 14 is 15 to 20 cm , the preferred height in the present embodiment is 18cm. A second separation wall 10 is provided between the clarification homogenization zone 12 and the cooling zone 9; a second liquid flow hole 11 is provided at the bottom of the second separation wall 10; the height of the second liquid flow hole 11 is It is 20~25cm, and the preferred height in the present embodiment is 22cm. The top of the clarification and homogenization zone 12 is provided with an air outlet 4 . Three baffles are longitudinally arranged in the cooling zone 9, which are the first baffle 5, the second baffle 6 and the third baffle 7 in sequence; the bottom of the first baffle is connected to the furnace body, and the top is the melt Flow channel; the top of the second baffle is connected with the furnace body, and the bottom is a melt flow channel; the bottom of the third baffle is connected with the furnace body, and the top is a melt flow channel. Temperature-measuring thermocouples 16 are installed on the side walls and bottom of the melting zone 15 and clarification and homogenization zone 12, and temperature-measuring thermocouples are also installed on both sides of the discharge port 8. The temperature of the heating layer in the clarification and homogenization zone 12 is higher than the temperature of the heating layer in the melting zone 15 .
工作时,将待熔化的玻璃原料从进料口17加入熔炉,玻璃原料在熔化区15中受热熔化后,形成半透明状的玻璃液;玻璃液经第一流液孔14流入到澄清均化区12,所述澄清均化区12内的温度高于熔化区15,利于玻璃液内的气泡逸出,也有利于玻璃液各成份更加均匀、一致,顶部的出气口4利于排出气泡和挥发性物质;第一流液孔14的设计,可以使玻璃液流经时产生一定的湍流,有助于气泡逸出和均化;澄清均化后的玻璃液基本上呈透明状,经第二流液孔11流入到冷却区9内,冷却区9内设置挡板,使玻璃液沿着挡板曲线流动,流动过程中玻璃液通过与挡板之间的热交换实现降温;可以根据出料时玻璃液温度的需要,调整挡板的个数和高度。熔化区15和澄清均化区12内均设有热电偶16检测各区域内的温度。出料口8也设置有热电偶,用于检测出料温度。When working, the glass raw material to be melted is put into the melting furnace from the feed port 17, and the glass raw material is heated and melted in the melting zone 15 to form a translucent molten glass; the molten glass flows into the clarification and homogenization zone through the first flow hole 14 12. The temperature in the clarification and homogenization zone 12 is higher than that in the melting zone 15, which is conducive to the escape of bubbles in the molten glass, and is also conducive to more uniform and consistent components of the molten glass. The air outlet 4 on the top is conducive to the discharge of bubbles and volatile Material; the design of the first liquid flow hole 14 can make the glass liquid flow through to produce a certain turbulent flow, which helps the bubbles to escape and homogenize; the glass liquid after clarification and homogenization is basically transparent, and passes through the second flow liquid The hole 11 flows into the cooling zone 9, and a baffle is set in the cooling zone 9, so that the molten glass flows along the curve of the baffle. According to the liquid temperature, adjust the number and height of the baffles. Both the melting zone 15 and the clarifying and homogenizing zone 12 are provided with thermocouples 16 to detect the temperature in each zone. The discharge port 8 is also provided with a thermocouple for detecting the discharge temperature.
且在生产过程中,当熔体由熔化区向后方流动时,可以继续进料,实现连续化生产。And in the production process, when the melt flows from the melting zone to the rear, it can continue to feed and realize continuous production.
Claims (8)
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106517736A (en) * | 2015-09-15 | 2017-03-22 | 上海耀皮玻璃集团股份有限公司 | Melting furnace for founding high-volatility-component glass |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106517736A (en) * | 2015-09-15 | 2017-03-22 | 上海耀皮玻璃集团股份有限公司 | Melting furnace for founding high-volatility-component glass |
CN106517736B (en) * | 2015-09-15 | 2020-01-17 | 江苏华东耀皮玻璃有限公司 | Melting furnace for melting glass with high volatile components |
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