CN201183770Y - A glass melting furnace suitable for vacuum clarification technology - Google Patents
A glass melting furnace suitable for vacuum clarification technology Download PDFInfo
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- CN201183770Y CN201183770Y CNU2008200174268U CN200820017426U CN201183770Y CN 201183770 Y CN201183770 Y CN 201183770Y CN U2008200174268 U CNU2008200174268 U CN U2008200174268U CN 200820017426 U CN200820017426 U CN 200820017426U CN 201183770 Y CN201183770 Y CN 201183770Y
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- decompression
- clarification
- melting furnace
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/225—Refining
- C03B5/2252—Refining under reduced pressure, e.g. with vacuum refiners
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/18—Stirring devices; Homogenisation
- C03B5/183—Stirring devices; Homogenisation using thermal means, e.g. for creating convection currents
- C03B5/185—Electric means
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
本实用新型公开一种适合减压澄清技术的玻璃熔窑,其特征在于:熔化池(A)和冷却池(C)之间设置一个减压澄清装置(D),它由上升管道(D1)、水平的减压澄清区(D2)和下降管道(D3)组成,熔化池(A)通过流液洞(B)与减压澄清装置(D)入口端相连,减压澄清装置(D)出口端与冷却池(C)连通,减压澄清装置(D)的顶部设有一组真空泵接口(1、2、3、4)以及对应连接的真空泵(10)。在减压澄清装置入口端(D1)中设置电加热元件(5、6、7、8),以保持玻璃液的粘度和温度。该新型熔窑的澄清效果好,能够节省玻璃熔化过程中所消耗的大量能源,具有良好的通用性和可操作性。
The utility model discloses a glass melting furnace suitable for decompression and clarification technology. , a horizontal decompression clarification area (D2) and a descending pipe (D3), the melting pool (A) is connected to the inlet of the decompression clarification device (D) through the flow hole (B), and the outlet of the decompression clarification device (D) The end communicates with the cooling pool (C), and the top of the decompression clarification device (D) is provided with a set of vacuum pump ports (1, 2, 3, 4) and correspondingly connected vacuum pumps (10). Electric heating elements (5, 6, 7, 8) are arranged in the inlet port (D1) of the decompression clarification device to maintain the viscosity and temperature of the glass liquid. The new melting furnace has a good clarification effect, can save a large amount of energy consumed in the glass melting process, and has good versatility and operability.
Description
技术领域: Technical field:
本实用新型涉及玻璃制造领域中的玻璃熔窑,特别涉及一种一种适合减压澄清技术的玻璃熔窑。The utility model relates to a glass melting furnace in the field of glass manufacturing, in particular to a glass melting furnace suitable for decompression and clarification technology.
背景技术: Background technique:
在玻璃熔制过程中,配合料的高温分解会产生大量的气体,同时配合料本身也会带入大量的气体,这些气体会引入到熔融的玻璃液中。通常,这些气体将会在玻璃液的澄清过程中被去除。但是,其中小部分仍然会以气泡的形式存在与玻璃液中,如果气泡的含量过多将会直接影响玻璃成品的质量。因此,澄清过程就变的十分重要。During the glass melting process, the pyrolysis of the batch material will generate a large amount of gas, and the batch material itself will also bring a large amount of gas, which will be introduced into the molten glass. Usually, these gases will be removed during the clarification of the molten glass. However, a small part of it will still exist in the glass liquid in the form of bubbles. If the content of bubbles is too much, it will directly affect the quality of the finished glass. Therefore, the clarification process becomes very important.
现有的熔窑结构,主要包括的熔化池、流液洞和冷却池结构,流液洞结构有较好的降温效果,可以有效的减少冷却面积;同时又能很好的挡住浮渣,提高玻璃的熔化率和熔化质量。玻璃的形成温度大概是在1350℃左右,但一般的玻璃熔窑的温度会保持在1500℃到1600℃之间,所高出来的约200℃就是为了使玻璃液能够进行更好的澄清。通过热工计算,我们可以知道,在高温时每继续升高1℃所需的热量将会呈几何倍数增长。例如将熔窑的温度从1599℃升高到1600℃所需热量为680kJ/m2·h,按照500t/d规模的熔窑计算,少升高1℃则可每天可减少使用约0.72吨重油。现今社会中能源问题越来越严重,各行业对节能的要求越来越高,因此采用一种新型的更加节能的澄清装置就变的十分重要。根据物理学定律:当气压降低时,玻璃熔体中气泡的直径将增大。并且随着气压的持续降低,玻璃熔体中的气泡直径会持续增大,真空时效果达到最佳。但如何将上述原理应有到熔窑结构中尚没有理想的技术方案。The existing melting furnace structure mainly includes the structure of the melting pool, the liquid flow hole and the cooling pool. The liquid flow hole structure has a good cooling effect and can effectively reduce the cooling area; at the same time, it can well block the scum and improve Melting rate and melting quality of glass. The forming temperature of glass is about 1350°C, but the temperature of a general glass melting furnace will be kept between 1500°C and 1600°C, and the increase of about 200°C is to make the glass liquid better clarified. Through thermal calculation, we can know that the heat required for every 1°C increase at high temperature will increase geometrically. For example, the heat required to increase the temperature of the furnace from 1599°C to 1600°C is 680kJ/m 2 ·h. Based on the calculation of a 500t/d scale furnace, a 1°C increase can reduce the use of heavy oil by about 0.72 tons per day . In today's society, energy problems are becoming more and more serious, and various industries have higher and higher requirements for energy saving. Therefore, it is very important to adopt a new type of clarification device that is more energy-saving. According to the laws of physics: when the air pressure is reduced, the diameter of the bubbles in the glass melt will increase. And as the air pressure continues to decrease, the diameter of the bubbles in the glass melt will continue to increase, and the effect is best in vacuum. However, there is no ideal technical solution for how to apply the above principles to the furnace structure.
实用新型内容:Utility model content:
本实用新型的目的在于提供一种结构简单、澄清效果良好,节约能源的新型熔窑结构,其能够适合于减压澄清技术共同运用,以促进玻璃液中气体的排出,较少气泡对玻璃液质量产生的影响,提高玻璃的生产质量,The purpose of this utility model is to provide a new melting furnace structure with simple structure, good clarification effect and energy saving, which can be used together with decompression clarification technology to promote the discharge of gas in the glass liquid and reduce the impact of air bubbles on the glass liquid. The impact of quality, improve the quality of glass production,
本实用新型专利采用以下技术方案:The utility model patent adopts the following technical solutions:
一种适合减压澄清技术的玻璃熔窑,它包括熔化池、流液洞和冷却池,其特征在于:熔化池和冷却池之间设置一个减压澄清装置,熔化池通过流液洞与减压澄清装置入口端相连,减压澄清装置出口端与冷却池连通,减压澄清装置的顶部设有一组真空泵接口以及对应连接的真空泵,所述的真空泵接口可以呈对称分布。A glass melting furnace suitable for decompression and clarification technology, which includes a melting pool, a liquid flow hole and a cooling pool. The inlet of the clarification device is connected, the outlet of the decompression clarification device is connected with the cooling pool, and the top of the decompression clarification device is provided with a set of vacuum pump ports and correspondingly connected vacuum pumps, and the vacuum pump ports can be symmetrically distributed.
所述的减压澄清装置由向上的上升管道、水平的减压澄清区和向下的下降管道组成,并且可以使上升管道与减压澄清区以及下降管道与减压澄清区之间均呈弧形连接。还可以在上升管道的内池壁上安装有电加热器。The decompression clarification device is composed of an upward ascending pipeline, a horizontal decompression clarification area and a downward descending pipeline, and can make an arc between the ascending pipeline and the decompression clarification area as well as the descending pipeline and the decompression clarification area. shape connection. An electric heater can also be installed on the inner pool wall of the ascending pipeline.
采用以上的技术方案,本实用新型具有以下优点:Adopt above technical scheme, the utility model has the following advantages:
(1)本实用新型中在上升管道中布置有电加热元件。可以保证在减压澄清过程中,玻璃仍然具有相当的粘度,可以顺利的通过减压澄清区。以耐火材料制备的减压澄清区,可以达到较好的密封性,保证玻璃液在减压环境中进行澄清。(1) In the utility model, an electric heating element is arranged in the ascending pipeline. It can ensure that the glass still has considerable viscosity during the decompression clarification process, and can pass through the decompression clarification zone smoothly. The decompression clarification zone made of refractory materials can achieve better sealing and ensure that the glass liquid is clarified in a decompression environment.
(2)本实用新型中在上升管与减压澄清区以及下降管与减压澄清区之间采用弧形连接,可以减少玻璃液流动时的阻力,同时提高玻璃液的澄清质量。(2) In the utility model, an arc connection is adopted between the ascending pipe and the decompression clarification area as well as between the downcomer and the decompression clarification area, which can reduce the resistance when the glass liquid flows and improve the clarification quality of the glass liquid.
(3)本实用新型中采用对称布置的真空泵接口。可以保证在整个减压澄清区域内的气压基本保持恒定,从而使通过减压澄清区的玻璃液能够达到良好均匀的澄清效果,保证玻璃的质量。(3) In the utility model, symmetrically arranged vacuum pump interfaces are adopted. It can ensure that the air pressure in the entire decompression clarification area is basically kept constant, so that the glass liquid passing through the decompression clarification area can achieve a good and uniform clarification effect and ensure the quality of the glass.
(4)本实用新型中的熔窑采用流液洞结构,可以有效的减少冷却面积,提高玻璃的熔化率和熔化质量,并且有利于保持熔窑的密封性。(4) The melting furnace in the utility model adopts a liquid flow hole structure, which can effectively reduce the cooling area, improve the melting rate and melting quality of the glass, and is conducive to maintaining the sealing of the melting furnace.
附图说明 Description of drawings
图一为本实用新型的主视结构剖面图Fig. 1 is the front view structure sectional view of the utility model
具体实施方式: Detailed ways:
下面结合附图和实例对本实用新型进行进一步说明:Below in conjunction with accompanying drawing and example the utility model is further described:
如图1所示,本实用新型设有熔化池(A)、流液洞(B)、减压澄清装置(D)、冷却池(C)。其中减压澄清装置(D)又包括有上升管道(D1)、水平的减压澄清区(D2)以及下降管道(D3)。流液洞(B)连接减压澄清装置中的上升管(D1)。在上升管(D1)设有电加热器(5、6、7、8)。在减压澄清区的顶部设有真空泵接口(1、2、3、4)以及对应连接的真空泵(10),真空泵接口呈对成分布。减压澄清装置中的下降管(D3)连接到熔窑的冷却池(C)。As shown in Figure 1, the utility model is provided with a melting pool (A), a liquid flow hole (B), a decompression clarification device (D), and a cooling pool (C). The decompression clarification device (D) further includes an ascending pipeline (D1), a horizontal decompression clarification area (D2) and a descending pipeline (D3). The liquid flow hole (B) is connected to the rising pipe (D1) in the decompression clarification device. Electric heaters (5, 6, 7, 8) are provided on the riser pipe (D1). Vacuum pump ports (1, 2, 3, 4) and correspondingly connected vacuum pumps (10) are arranged on the top of the decompression clarification area, and the vacuum pump ports are arranged in pairs. The downcomer (D3) in the vacuum clarification unit is connected to the cooling pool (C) of the furnace.
设置流液洞(B)是为了可以有效的减少冷却面积;同时又能很好的挡住浮渣,提高玻璃的熔化率和熔化质量。将上升管(D1)与减压澄清区(D2)以及下降管(D3)与减压澄清区(D2)的连接处设计为弧形,是为了减少玻璃液流动时的阻力,提高玻璃的澄清质量。利用分布在减压澄清区(D2)顶部的(1、2、3、4)真空泵接口,使用外接的真空泵将减压澄清区的上部空间抽成低于标准大气压的状态,使得玻璃液中的气泡在该空间内能充分的长大,从而从玻璃液中排出,达到澄清的效果。在上升管(D1)中设置的电加热元件是为了保持玻璃液在减压澄清区中的温度。The liquid flow hole (B) is provided to effectively reduce the cooling area; at the same time, it can well block the scum and improve the melting rate and melting quality of the glass. The connection between the riser (D1) and the decompression clarification zone (D2) and the downcomer (D3) and the decompression clarification zone (D2) is designed as an arc, in order to reduce the resistance of the glass liquid flow and improve the clarification of the glass. quality. Utilize the (1, 2, 3, 4) vacuum pump interfaces distributed on the top of the decompression clarification zone (D2), use an external vacuum pump to pump the upper space of the decompression clarification zone into a state lower than the standard atmospheric pressure, so that the glass liquid Bubbles can grow sufficiently in this space to be discharged from the glass liquid to achieve clarification. The electric heating element arranged in the riser (D1) is to keep the temperature of the glass liquid in the decompression clarification zone.
本实用新型的工作原理:Working principle of the utility model:
熔制好的玻璃液(11)从熔化池(A)通过流液洞(B),到达上升管(D1)后,通过虹吸作用被提升到减压澄清区(D2)中,然后在减压澄清区中进行减压澄清。在整个过程中会产生一定的温度降低,通过设置在上升管的电加热元件使玻璃液的温度保持在适合的温度范围。用设置在外面的真空泵使减压澄清区内的气压低于标准大气压,从而使得玻璃液能够得到充分的澄清。经过澄清后的玻璃液通过下降管(D3)进入冷却池均化、冷却。The melted glass (11) passes through the liquid hole (B) from the melting pool (A) to the riser (D1), and is lifted into the decompression clarification area (D2) by siphon action, and then decompressed Clarification under reduced pressure in the clarification zone. During the whole process, there will be a certain temperature drop, and the temperature of the molten glass is kept in a suitable temperature range through the electric heating element arranged in the riser. The air pressure in the decompression clarification area is lower than the standard atmospheric pressure with a vacuum pump arranged outside, so that the glass liquid can be fully clarified. The clarified glass liquid enters the cooling pool through the downcomer (D3) for homogenization and cooling.
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| Application Number | Priority Date | Filing Date | Title |
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| CNU2008200174268U CN201183770Y (en) | 2008-02-01 | 2008-02-01 | A glass melting furnace suitable for vacuum clarification technology |
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| Application Number | Priority Date | Filing Date | Title |
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| CNU2008200174268U CN201183770Y (en) | 2008-02-01 | 2008-02-01 | A glass melting furnace suitable for vacuum clarification technology |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016041353A1 (en) * | 2014-09-16 | 2016-03-24 | 中国建材国际工程集团有限公司 | Large melting furnace suitable for borosilicate glass |
| CN115974366A (en) * | 2022-12-30 | 2023-04-18 | 中国建材国际工程集团有限公司 | A rapid clarification device for molten glass |
| CN116947298A (en) * | 2023-08-18 | 2023-10-27 | 本溪玉晶玻璃有限公司 | Ultra-large tonnage one-kiln two-line glass production line |
-
2008
- 2008-02-01 CN CNU2008200174268U patent/CN201183770Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016041353A1 (en) * | 2014-09-16 | 2016-03-24 | 中国建材国际工程集团有限公司 | Large melting furnace suitable for borosilicate glass |
| CN115974366A (en) * | 2022-12-30 | 2023-04-18 | 中国建材国际工程集团有限公司 | A rapid clarification device for molten glass |
| CN116947298A (en) * | 2023-08-18 | 2023-10-27 | 本溪玉晶玻璃有限公司 | Ultra-large tonnage one-kiln two-line glass production line |
| CN116947298B (en) * | 2023-08-18 | 2024-02-27 | 本溪玉晶玻璃有限公司 | Ultra-large tonnage one-kiln two-line glass production line |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
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| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Bengbu Zhongheng New Materials Scientific and Technological Co., Ltd. Assignor: China Triumph International Engineering Co., Ltd.|Bengbu design Institute of Glass Industry Contract fulfillment period: 2009.3.25 to 2018.3.12 Contract record no.: 2009340000267 Denomination of utility model: Glass melting furnace for pressure reducing clarification technology Granted publication date: 20090121 License type: Exclusive license Record date: 20090904 |
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Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.3.25 TO 2018.3.12; CHANGE OF CONTRACT Name of requester: BENGBU ZHONGHENG NEW-MATERIAL SCIENCE AND TECHNOLO Effective date: 20090904 |
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Owner name: BENGBU ZHONGHENG LIGHT NEW MATERIAL TECHNOLOGY CO. Free format text: FORMER OWNER: CHINA TRIUMPH INTERNATIONAL ENGINEERING CO., LTD. Effective date: 20120428 Free format text: FORMER OWNER: BENGBU GLASS INDUSTRY AND DESIGN INSTITUTE;CHINA TRIUMPH INTERNATIONAL ENGINEERING CO., LTD. Effective date: 20120428 |
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Effective date of registration: 20120428 Address after: 233000 Anhui city of Bengbu Province east of Long Jin Lu (Kai Shengxin materials science and Technology Industrial Park) Patentee after: Bengbu Zhongheng New Materials Scientific and Technological Co., Ltd. Address before: 233010 No. 1032 Tu Shan Road, Anhui, Bengbu Co-patentee before: Bengbu design Institute of Glass Industry Patentee before: China Triumph International Engineering Co., Ltd. |
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