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CN118637812A - A glass-ceramic dispensing and forming device - Google Patents

A glass-ceramic dispensing and forming device Download PDF

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Publication number
CN118637812A
CN118637812A CN202411095034.3A CN202411095034A CN118637812A CN 118637812 A CN118637812 A CN 118637812A CN 202411095034 A CN202411095034 A CN 202411095034A CN 118637812 A CN118637812 A CN 118637812A
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Prior art keywords
distribution
glass
forming
furnace
forming furnace
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CN202411095034.3A
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CN118637812B (en
Inventor
陆晨
彭寿
张冲
刘尧龙
储静远
张军
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Sichuan Global Microcrystalline Glass Technology Co ltd
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China Building Materials Glass New Materials Research Institute Group Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B17/00Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
    • C03B17/06Forming glass sheets
    • C03B17/067Forming glass sheets combined with thermal conditioning of the sheets
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B23/00Re-forming shaped glass
    • C03B23/02Re-forming glass sheets
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B25/00Annealing glass products
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B32/00Thermal after-treatment of glass products not provided for in groups C03B19/00, C03B25/00 - C03B31/00 or C03B37/00, e.g. crystallisation, eliminating gas inclusions or other impurities; Hot-pressing vitrified, non-porous, shaped glass products
    • C03B32/02Thermal crystallisation, e.g. for crystallising glass bodies into glass-ceramic articles
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/50Glass production, e.g. reusing waste heat during processing or shaping
    • Y02P40/57Improving the yield, e-g- reduction of reject rates

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Ceramic Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Re-Forming, After-Treatment, Cutting And Transporting Of Glass Products (AREA)

Abstract

The invention discloses a microcrystalline glass distribution and forming device, which comprises a distribution forming furnace, wherein refractory materials are filled in the distribution forming furnace, a flow passage for glass flow forming is formed between the refractory materials and the distribution forming furnace, a glass liquid feeding device is arranged at the top of the flow passage, a distribution lip brick is arranged in the flow passage and positioned at the corner of the refractory materials, a high-pressure burner is arranged between the inner walls of the distribution forming furnace and positioned in the flow passage, and the high-pressure burner comprises a main burner and an auxiliary burner. According to the microcrystalline glass distribution and forming device, through the arrangement of the distribution lip bricks, the microcrystalline glass forming temperature interval and the glass liquid residence time are shortened, the problem of glass body crystallization in advance caused by temperature and residence time fluctuation is effectively avoided, and accordingly the forming efficiency and the finished product quality of microcrystalline glass are improved.

Description

一种微晶玻璃分配及成形装置A glass-ceramic dispensing and forming device

技术领域Technical Field

本发明涉及玻璃制造技术领域,具体为一种微晶玻璃分配及成形装置。The present invention relates to the technical field of glass manufacturing, and in particular to a microcrystalline glass distributing and forming device.

背景技术Background Art

微晶玻璃是一种新型玻璃材料,具有优异的性能和广泛的应用。微晶玻璃生产的技术难点在于熔制和成形过程中的技术控制。Glass-ceramics is a new type of glass material with excellent performance and wide application. The technical difficulty of glass-ceramics production lies in the technical control during the melting and forming process.

目前微晶玻璃主要采用的方式有烧结法、压延法和浮法,有些产品都要进行二次加工才能使用。在微晶玻璃成形过程中,特别强调粘度和温度的变化情况,如果成形温度接近析晶温度范围,随着温度和停留时间的波动,玻璃体极易提前析晶,无法完成微晶玻璃的成形过程。经过不断的探索,技术人员不断优化工艺和控制手段,仍然无法完全克服微晶玻璃成形过程析晶的困扰,对此我们提出了一种微晶玻璃分配及成形装置来解决上述问题。At present, the main methods used for microcrystalline glass are sintering, calendering and float processes. Some products need to undergo secondary processing before they can be used. In the process of forming microcrystalline glass, special emphasis is placed on the changes in viscosity and temperature. If the forming temperature is close to the crystallization temperature range, the glass body is very likely to crystallize prematurely with the fluctuation of temperature and residence time, and the forming process of microcrystalline glass cannot be completed. After continuous exploration, technicians have continuously optimized the process and control methods, but still cannot completely overcome the problem of crystallization in the forming process of microcrystalline glass. In this regard, we have proposed a microcrystalline glass distribution and forming device to solve the above problem.

发明内容Summary of the invention

针对现有技术的不足,本发明提供了一种微晶玻璃分配及成形装置,解决了背景技术中提出的问题。In view of the deficiencies in the prior art, the present invention provides a glass-ceramic distribution and forming device, which solves the problems raised in the background technology.

为实现以上目的,本发明通过以下技术方案予以实现:一种微晶玻璃分配及成形装置,包括分配成形炉,所述分配成形炉的内部填充有耐火材料,所述耐火材料与分配成形炉之间形成有用于玻璃流动成型的流道,所述流道的顶部设置有玻璃液给料装置,所述流道中且位于耐火材料的拐角处安装有分配唇砖,所述分配成形炉的内壁之间且位于流道内设置有高压燃烧器,所述高压燃烧器包括主燃烧器和辅燃烧器,所述高压燃烧器对分配唇砖上摊开的玻璃液进行吹薄,所述分配成形炉内壁的一侧设置有高压气体喷射装置,所述高压气体喷射装置喷出高压气体对分配唇砖水平段残留的玻璃液进行吹扫,所述分配唇砖与分配成形炉之间还设置有控制玻璃液形成玻璃带宽度的宽度调节控制组件。To achieve the above objectives, the present invention is implemented through the following technical solutions: a microcrystalline glass distribution and forming device, including a distribution and forming furnace, the interior of the distribution and forming furnace is filled with refractory materials, a flow channel for glass flow forming is formed between the refractory materials and the distribution and forming furnace, a glass liquid feeding device is arranged on the top of the flow channel, a distribution lip brick is installed in the flow channel and at the corner of the refractory material, a high-pressure burner is arranged between the inner walls of the distribution and forming furnace and located in the flow channel, the high-pressure burner includes a main burner and an auxiliary burner, the high-pressure burner blows thin the glass liquid spread on the distribution lip brick, a high-pressure gas injection device is arranged on one side of the inner wall of the distribution and forming furnace, the high-pressure gas injection device sprays high-pressure gas to purge the glass liquid remaining in the horizontal section of the distribution lip brick, and a width adjustment control component for controlling the width of the glass band formed by the glass liquid is also arranged between the distribution lip brick and the distribution and forming furnace.

优选的,所述宽度调节控制组件包括滑动连接在分配唇砖斜段上的两个限位板,所述分配成形炉的内壁之间转动连接有双向丝杆。Preferably, the width adjustment control assembly comprises two limit plates slidably connected to the inclined section of the distribution lip brick, and a bidirectional screw rod is rotatably connected between the inner walls of the distribution forming furnace.

优选的,所述双向丝杆的一端贯穿两个限位板并延伸至限位板的外部,两个所述限位板的内表面均与双向丝杆的外表面螺纹连接。Preferably, one end of the bidirectional screw rod passes through the two limiting plates and extends to the outside of the limiting plates, and the inner surfaces of the two limiting plates are threadedly connected to the outer surface of the bidirectional screw rod.

优选的,所述分配成形炉的一侧固定有电机,所述电机带动双向丝杆转动。Preferably, a motor is fixed on one side of the distribution and forming furnace, and the motor drives the bidirectional screw to rotate.

优选的,所述流道内还设有加热装置,所述加热装置横向分为若干个区,对玻璃带进行加热并调节横向温差。Preferably, a heating device is further provided in the flow channel, and the heating device is divided into a plurality of zones in the transverse direction to heat the glass ribbon and adjust the transverse temperature difference.

优选的,所述流道的底部安装有密封盖板,所述密封盖板由两块耐火材料叠加而成,且两块耐火材料中间夹有电阻丝。Preferably, a sealing cover plate is installed at the bottom of the flow channel, and the sealing cover plate is formed by stacking two pieces of refractory materials, and a resistance wire is sandwiched between the two pieces of refractory materials.

优选的,所述密封盖板中央处贯穿开设有通孔,且玻璃液加热后形成的玻璃带从通孔中穿出。Preferably, a through hole is formed through the center of the sealing cover plate, and a glass ribbon formed after the glass liquid is heated passes through the through hole.

优选的,所述分配成形炉内设置有排气管,所述排气管的顶端贯穿耐火材料和分配成形炉并延伸至分配成形炉的外部,所述排气管的底端延伸至流道的内部,所述排气管上安装有自动调压阀。Preferably, an exhaust pipe is provided in the distribution and forming furnace, the top end of the exhaust pipe penetrates the refractory material and the distribution and forming furnace and extends to the outside of the distribution and forming furnace, the bottom end of the exhaust pipe extends to the inside of the flow channel, and an automatic pressure regulating valve is installed on the exhaust pipe.

本发明提供了一种微晶玻璃分配及成形装置。与现有技术相比具备以下有益效果:The present invention provides a glass-ceramic distribution and forming device. Compared with the prior art, it has the following beneficial effects:

(1)通过分配唇砖的设置,缩短了微晶玻璃成形温度区间和玻璃液停留时间,有效避免了因温度和停留时间波动导致的玻璃体提前析晶问题,从而提高了微晶玻璃的成形效率和成品质量。(1) By setting up the lip bricks, the forming temperature range of the glass-ceramics and the residence time of the glass liquid are shortened, effectively avoiding the problem of premature crystallization of the glass body caused by temperature and residence time fluctuations, thereby improving the forming efficiency of the glass-ceramics and the quality of the finished product.

(2)利用高压燃烧器在玻璃液流动过程中施加高速气流,结合成形装置内的温度和玻璃液流量的协同调整,实现了对玻璃带厚度的精确控制,生产出符合要求的微晶玻璃厚度。(2) By using a high-pressure burner to apply high-speed airflow during the flow of molten glass, combined with the coordinated adjustment of the temperature and molten glass flow rate in the forming device, the thickness of the glass ribbon can be precisely controlled, and the microcrystalline glass thickness that meets the requirements can be produced.

(3)通过加热装置,并设置加热元件分区控制,实现了对玻璃带横向温差的精确调节,提高了能源利用效率,同时,配备排气管和自动调压阀,有效处理燃烧废气,维持成形装置内压力恒定,减少了环境污染。(3) Through the heating device and the setting of heating element zone control, the lateral temperature difference of the glass ribbon can be accurately adjusted, which improves the energy utilization efficiency. At the same time, the exhaust pipe and automatic pressure regulating valve are equipped to effectively treat the combustion exhaust gas, maintain the constant pressure in the forming device, and reduce environmental pollution.

(4)通过宽度调节控制组件的设置,可控制两个限位板在分配唇砖上的距离,进而调节控制了玻璃液平摊在分配唇砖上的宽度,实现了不同宽度玻璃带的成型。(4) By setting the width adjustment control component, the distance between the two limit plates on the distribution lip brick can be controlled, thereby adjusting and controlling the width of the glass liquid spread on the distribution lip brick, thereby realizing the forming of glass strips of different widths.

(5)通过高压气体喷射装置的设置,实现了对分配唇砖水平段上残留玻璃液的吹扫清理,将残留玻璃液清理干净不仅避免了玻璃液的浪费,同时也能使分配唇砖水平段上保持平整,不影响玻璃液的平摊效果。(5) By setting up a high-pressure gas jet device, the residual glass liquid on the horizontal section of the distribution lip brick can be purged and cleaned. Cleaning the residual glass liquid not only avoids the waste of glass liquid, but also keeps the horizontal section of the distribution lip brick flat, without affecting the spreading effect of the glass liquid.

附图说明BRIEF DESCRIPTION OF THE DRAWINGS

图1为本发明的内部结构主视图;Fig. 1 is a front view of the internal structure of the present invention;

图2为本发明的内部结构侧视图;FIG2 is a side view of the internal structure of the present invention;

图3为本发明的局部结构俯视图;FIG3 is a top view of a local structure of the present invention;

图4为本发明的主燃烧器主视图;FIG4 is a front view of the main burner of the present invention;

图5为本发明的主燃烧器侧视图。FIG. 5 is a side view of the main burner of the present invention.

图中:1、分配成形炉;2、耐火材料;3、流道;4、玻璃液给料装置;5、分配唇砖;6、高压燃烧器;61、主燃烧器;62、辅燃烧器;7、高压气体喷射装置;81、限位板;82、双向丝杆;83、电机;9、加热装置;10、密封盖板;11、通孔;12、排气管;13、调压阀。In the figure: 1. distribution forming furnace; 2. refractory material; 3. flow channel; 4. glass liquid feeding device; 5. distribution lip brick; 6. high-pressure burner; 61. main burner; 62. auxiliary burner; 7. high-pressure gas injection device; 81. limit plate; 82. bidirectional screw rod; 83. motor; 9. heating device; 10. sealing cover plate; 11. through hole; 12. exhaust pipe; 13. pressure regulating valve.

具体实施方式DETAILED DESCRIPTION

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

本发明实施例提供三种技术方案,具体包括以下实施例:The present invention provides three technical solutions, including the following embodiments:

实施例1Example 1

请参阅图1、图2、图4、图5,一种微晶玻璃分配及成形装置,包括分配成形炉1,分配成形炉1外部是支撑的钢壳,炉体上部有玻璃液流入口,和烟气排出口,底部有玻璃带出口,侧面有高压燃烧器6插孔和加热元件安装孔,分配成形炉1的内部填充有耐火材料2,耐火材料2起保温隔热作用,耐火材料2与分配成形炉1之间形成有用于玻璃流动成型的流道3,流道3的顶部设置有玻璃液给料装置4,流道3中且位于耐火材料2的拐角处安装有分配唇砖5,分配唇砖5采用耐火材料制得,优选41#AZS,优选高锆砖,优选耐火材料外侧包覆铂金,落料点处设置一水平段,水平段远离玻璃流向有一侧壁,侧壁呈圆弧形,与水平段连接的是斜段,斜面与水平面夹角0°-90°,与斜段相连的是圆弧段,圆弧端点与圆弧垂直切线的距离为0-50mm,圆弧端点低于分配唇砖底面0-50mm,分配唇砖固定在分配及成形装置炉体上,分配成形炉1的内壁之间且位于流道3内设置有高压燃烧器6,高压燃烧器6包括主燃烧器61和辅燃烧器62,高压燃烧器6外侧为套管,一般为刚玉套管,套管中部有一开槽,开槽沿着套管中心线方向,开槽长度根据玻璃带宽度确定,一般为50-1000mm,开槽宽度为1-20mm,槽口有喇叭形导流片,高压燃烧器槽口距玻璃带5-100mm,高压燃烧器6角度可以调整,内侧为高压喷枪,端头有两个接头,分别为天然气和氧气接口,通入的天然气和氧气在腔体内混合后,从喷嘴出喷射进外侧套管燃烧,高压喷枪进入外侧套管的长度可以调节,高压燃烧器6对分配唇砖5上摊开的玻璃液进行吹薄,分配成形炉1内壁的一侧设置有高压气体喷射装置7,高压气体喷射装置7喷出高压气体对分配唇砖5水平段残留的玻璃液进行吹扫,通过高压气体喷射装置7的设置,实现了对分配唇砖5水平段上残留玻璃液的吹扫清理,将残留玻璃液清理干净不仅避免了玻璃液的浪费,同时也能使分配唇砖水平段上保持平整,不影响玻璃液的平摊效果,分配唇砖5与分配成形炉1之间还设置有控制玻璃液形成玻璃带宽度的宽度调节控制组件。Please refer to Figures 1, 2, 4 and 5, a microcrystalline glass distribution and forming device includes a distribution and forming furnace 1, the distribution and forming furnace 1 is supported by a steel shell, the upper part of the furnace body is provided with a glass liquid inlet and a smoke exhaust outlet, the bottom is provided with a glass belt outlet, the side is provided with a high-pressure burner 6 jack and a heating element installation hole, the interior of the distribution and forming furnace 1 is filled with a refractory material 2, the refractory material 2 plays a role in heat preservation and heat insulation, a flow channel 3 for glass flow forming is formed between the refractory material 2 and the distribution and forming furnace 1, a glass liquid feeding device 4 is provided on the top of the flow channel 3, and a distribution lip brick 5 is installed in the flow channel 3 and at the corner of the refractory material 2, and the distribution lip brick 5 is made of refractory material, preferably 41#AZS, preferably high zirconium brick, preferably platinum is coated on the outside of the refractory material, a horizontal section is set at the drop point, the horizontal section has a side wall away from the glass flow direction, the side wall is arc-shaped, connected to the horizontal section is an inclined section, the angle between the inclined surface and the horizontal plane is 0°-90°, connected to the inclined section is an arc section, the distance between the end point of the arc and the vertical tangent of the arc is 0-50mm, the end point of the arc is 0-50mm lower than the bottom surface of the distribution lip brick, the distribution lip brick is fixed on the furnace body of the distribution and forming device, a high-pressure burner 6 is set between the inner walls of the distribution and forming furnace 1 and located in the flow channel 3, and the high-pressure burner 6 includes a main burner 61 and an auxiliary burner 62. Burner 62, the outer side of the high-pressure burner 6 is a sleeve, generally a corundum sleeve, with a slot in the middle of the sleeve, the slot is along the center line of the sleeve, the slot length is determined according to the width of the glass ribbon, generally 50-1000mm, the slot width is 1-20mm, the slot has a trumpet-shaped guide plate, the high-pressure burner slot is 5-100mm away from the glass ribbon, the high-pressure burner 6 can be adjusted in angle, the inner side is a high-pressure spray gun, the end has two joints, respectively, natural gas and oxygen interfaces, the natural gas and oxygen introduced are mixed in the cavity, and then sprayed from the nozzle into the outer sleeve for combustion, the length of the high-pressure spray gun entering the outer sleeve can be adjusted, and the high-pressure burner The device 6 blows thin the glass liquid spread on the distribution lip brick 5, and a high-pressure gas injection device 7 is arranged on one side of the inner wall of the distribution forming furnace 1. The high-pressure gas injection device 7 sprays high-pressure gas to purge the glass liquid remaining in the horizontal section of the distribution lip brick 5. Through the setting of the high-pressure gas injection device 7, the purging and cleaning of the residual glass liquid on the horizontal section of the distribution lip brick 5 is realized. Cleaning the residual glass liquid not only avoids the waste of glass liquid, but also keeps the horizontal section of the distribution lip brick flat without affecting the spreading effect of the glass liquid. A width adjustment control component for controlling the width of the glass belt formed by the glass liquid is also arranged between the distribution lip brick 5 and the distribution forming furnace 1.

成形装置下方可以连接压延机,将微晶玻璃带进一步压薄。A calender can be connected below the forming device to further thin the glass-ceramic ribbon.

成形装置下方可以连接退火炉,对微晶玻璃带进行退火。An annealing furnace can be connected below the forming device to anneal the microcrystalline glass ribbon.

成形装置下方可以连接晶化炉,对微晶玻璃带进行晶化。A crystallization furnace can be connected below the forming device to crystallize the microcrystalline glass ribbon.

实施例2Example 2

在实施例1的基础上,参见图1和图3所示,宽度调节控制组件包括滑动连接在分配唇砖5斜段上的两个限位板81,分配成形炉1的内壁之间转动连接有双向丝杆82。On the basis of Example 1, referring to FIG. 1 and FIG. 3 , the width adjustment control assembly includes two limit plates 81 slidably connected to the inclined section of the distribution lip brick 5 , and a bidirectional screw rod 82 is rotatably connected between the inner walls of the distribution forming furnace 1 .

双向丝杆82的一端贯穿两个限位板81并延伸至限位板81的外部,两个限位板81的内表面均与双向丝杆82的外表面螺纹连接。One end of the bidirectional screw rod 82 passes through the two limiting plates 81 and extends to the outside of the limiting plates 81 . The inner surfaces of the two limiting plates 81 are both threadedly connected to the outer surface of the bidirectional screw rod 82 .

分配成形炉1的一侧固定有电机83,电机83带动双向丝杆82转动。A motor 83 is fixed to one side of the distribution forming furnace 1, and the motor 83 drives the bidirectional screw rod 82 to rotate.

通过宽度调节控制组件的设置,可控制两个限位板81在分配唇砖5上的距离,进而调节控制了玻璃液平摊在分配唇砖5上的宽度,实现了不同宽度玻璃带的成型。By setting the width adjustment control component, the distance between the two limit plates 81 on the distribution lip brick 5 can be controlled, thereby adjusting and controlling the width of the glass liquid spread on the distribution lip brick 5, thereby realizing the forming of glass ribbons of different widths.

实施例3Example 3

在实施例2的基础上,参见图1所示,流道3内还设有加热装置9,玻璃带经过高压燃烧器6成形后,垂直向下流动,在玻璃带的上下表面,设置加热装置9,由若干加热元件水平方向和垂直方向分为若干个区,对玻璃带进行加热并调节横向温差。On the basis of Example 2, as shown in FIG1 , a heating device 9 is further provided in the flow channel 3. After the glass ribbon is formed by the high-pressure burner 6, it flows vertically downward. The upper and lower surfaces of the glass ribbon are provided with a heating device 9, which is divided into a plurality of zones in the horizontal and vertical directions by a plurality of heating elements to heat the glass ribbon and adjust the lateral temperature difference.

流道3的底部安装有密封盖板10,密封盖板10用于炉体开口、开孔的密封,密封盖板10由两块耐火材料2叠加而成,且两块耐火材料2中间夹有电阻丝。A sealing cover plate 10 is installed at the bottom of the flow channel 3. The sealing cover plate 10 is used to seal the furnace opening and the opening. The sealing cover plate 10 is formed by stacking two refractory materials 2, and a resistance wire is sandwiched between the two refractory materials 2.

密封盖板10中央处贯穿开设有通孔11,且玻璃液加热后形成的玻璃带从通孔11中穿出。A through hole 11 is formed through the center of the sealing cover plate 10 , and a glass ribbon formed after the glass liquid is heated passes through the through hole 11 .

分配成形炉1内设置有排气管12,排气管12的顶端贯穿耐火材料2和分配成形炉1并延伸至分配成形炉1的外部,排气管12的底端延伸至流道3的内部,排气管12上安装有自动调压阀13。An exhaust pipe 12 is arranged in the distribution and forming furnace 1. The top end of the exhaust pipe 12 passes through the refractory material 2 and the distribution and forming furnace 1 and extends to the outside of the distribution and forming furnace 1. The bottom end of the exhaust pipe 12 extends to the inside of the flow channel 3. An automatic pressure regulating valve 13 is installed on the exhaust pipe 12.

同时本说明书中未作详细描述的内容均属于本领域技术人员公知的现有技术。Meanwhile, the contents not described in detail in this specification belong to the prior art known to those skilled in the art.

工作时,合格的微晶玻璃液从玻璃液给料装置4向下流出,进入成形装置,玻璃液首先流到分配唇砖5的水平段并摊开,摊开的玻璃液进入分配唇砖5的斜段,玻璃液在重力和分配唇砖5的摩擦阻力作用下进一步摊开并斜向下流动,流至分配唇砖5的圆弧拐点时,玻璃液与分配唇砖5分离并垂直向下离开成形装置,在此过程中通过启动电机83,使电机83带动双向丝杆82转动,进一步双向丝杆82带动两个限位板81对向移动,进而限制了玻璃液摊开的宽度,高压燃烧器6布置在成形装置两侧,分为主燃烧器61和辅燃烧器62从一端分别通入天然气和氧气,燃烧产生的高压气体从燃烧器喷出,当微晶玻璃液流到分配唇砖5斜段时,燃烧器高速喷出的高压气体作用在玻璃带上,主燃烧器61在玻璃带横向作用,辅燃烧器62可以横向调整位置,作用于特定的位置,通过调节天然气和氧气流量、高压燃烧6的数量和位置,调节燃烧器喷出气流的压力和作用区域,将玻璃带吹薄,结合成形装置内的温度和玻璃液流量的协同调整,得到合格厚度的微晶玻璃,启动高压气体喷射装置7对分配唇砖5水平段上残留的玻璃液进行吹扫清理。During operation, qualified microcrystalline glass liquid flows downward from the glass liquid feeding device 4 and enters the forming device. The glass liquid first flows to the horizontal section of the distribution lip brick 5 and spreads out. The spread glass liquid enters the inclined section of the distribution lip brick 5. The glass liquid is further spread out and flows obliquely downward under the action of gravity and the friction resistance of the distribution lip brick 5. When it flows to the arc inflection point of the distribution lip brick 5, the glass liquid separates from the distribution lip brick 5 and leaves the forming device vertically downward. In this process, the motor 83 is started to drive the bidirectional screw 82 to rotate, and the bidirectional screw 82 further drives the two limit plates 81 to move in opposite directions, thereby limiting the width of the glass liquid spreading. The high-pressure burners 6 are arranged on both sides of the forming device, which are divided into a main burner 61 Natural gas and oxygen are introduced into the auxiliary burner 62 from one end respectively, and the high-pressure gas generated by the combustion is ejected from the burner. When the microcrystalline glass liquid flows to the inclined section of the distribution lip brick 5, the high-pressure gas ejected from the burner at high speed acts on the glass ribbon. The main burner 61 acts laterally on the glass ribbon, and the auxiliary burner 62 can adjust its position laterally to act on a specific position. By adjusting the flow rate of natural gas and oxygen, the number and position of high-pressure burners 6, the pressure and action area of the airflow ejected by the burner are adjusted to blow the glass ribbon thin. Combined with the coordinated adjustment of the temperature in the forming device and the glass liquid flow rate, microcrystalline glass of qualified thickness is obtained, and the high-pressure gas injection device 7 is started to blow and clean the residual glass liquid on the horizontal section of the distribution lip brick 5.

以上对发明的实施例进行了详细说明,但所述内容仅为本发明的较佳实施例,不能被认为用于限定本发明的实施范围。凡依本发明申请范围所作的均等变化与改进等,均应仍归属于本发明的专利涵盖范围之内。The embodiments of the invention are described in detail above, but the contents are only preferred embodiments of the invention and cannot be considered to limit the scope of the invention. All equivalent changes and improvements made according to the scope of the invention should still fall within the scope of the invention.

Claims (8)

1.一种微晶玻璃分配及成形装置,包括分配成形炉(1),其特征在于:所述分配成形炉(1)的内部填充有耐火材料(2),所述耐火材料(2)与分配成形炉(1)之间形成有用于玻璃流动成型的流道(3),所述流道(3)的顶部设置有玻璃液给料装置(4),所述流道(3)中且位于耐火材料(2)的拐角处安装有分配唇砖(5),所述分配成形炉(1)的内壁之间且位于流道(3)内设置有高压燃烧器(6),所述高压燃烧器(6)包括主燃烧器(61)和辅燃烧器(62),所述高压燃烧器(6)对分配唇砖(5)上摊开的玻璃液进行吹薄,所述分配成形炉(1)内壁的一侧设置有高压气体喷射装置(7),所述高压气体喷射装置(7)喷出高压气体对分配唇砖(5)水平段残留的玻璃液进行吹扫,所述分配唇砖(5)与分配成形炉(1)之间还设置有控制玻璃液形成玻璃带宽度的宽度调节控制组件。1. A microcrystalline glass distribution and forming device, comprising a distribution forming furnace (1), characterized in that: the interior of the distribution forming furnace (1) is filled with a refractory material (2), a flow channel (3) for glass flow forming is formed between the refractory material (2) and the distribution forming furnace (1), a glass liquid feeding device (4) is arranged on the top of the flow channel (3), a distribution lip brick (5) is installed in the flow channel (3) and at the corner of the refractory material (2), and a high-pressure fuel is arranged between the inner walls of the distribution forming furnace (1) and in the flow channel (3). A burner (6) is provided, wherein the high-pressure burner (6) comprises a main burner (61) and an auxiliary burner (62), wherein the high-pressure burner (6) is used to thin the glass liquid spread on the distribution lip brick (5), and a high-pressure gas injection device (7) is provided on one side of the inner wall of the distribution forming furnace (1), wherein the high-pressure gas injection device (7) sprays high-pressure gas to purge the glass liquid remaining in the horizontal section of the distribution lip brick (5), and a width adjustment control component is also provided between the distribution lip brick (5) and the distribution forming furnace (1) to control the width of the glass ribbon formed by the glass liquid. 2.根据权利要求1所述的一种微晶玻璃分配及成形装置,其特征在于:所述宽度调节控制组件包括滑动连接在分配唇砖(5)斜段上的两个限位板(81),所述分配成形炉(1)的内壁之间转动连接有双向丝杆(82)。2. A glass-ceramic distribution and forming device according to claim 1, characterized in that: the width adjustment control assembly comprises two limit plates (81) slidably connected to the inclined section of the distribution lip brick (5), and a bidirectional screw rod (82) is rotatably connected between the inner walls of the distribution and forming furnace (1). 3.根据权利要求2所述的一种微晶玻璃分配及成形装置,其特征在于:所述双向丝杆(82)的一端贯穿两个限位板(81)并延伸至限位板(81)的外部,两个所述限位板(81)的内表面均与双向丝杆(82)的外表面螺纹连接。3. A glass-ceramic distribution and forming device according to claim 2, characterized in that one end of the bidirectional screw (82) passes through the two limit plates (81) and extends to the outside of the limit plates (81), and the inner surfaces of the two limit plates (81) are threadedly connected to the outer surface of the bidirectional screw (82). 4.根据权利要求2所述的一种微晶玻璃分配及成形装置,其特征在于:所述分配成形炉(1)的一侧固定有电机(83),所述电机(83)带动双向丝杆(82)转动。4. A glass-ceramic distribution and forming device according to claim 2, characterized in that a motor (83) is fixed on one side of the distribution and forming furnace (1), and the motor (83) drives the bidirectional screw rod (82) to rotate. 5.根据权利要求1所述的一种微晶玻璃分配及成形装置,其特征在于:所述流道(3)内还设有加热装置(9),所述加热装置(9)横向分为若干个区,对玻璃带进行加热并调节横向温差。5. A glass-ceramic distribution and forming device according to claim 1, characterized in that: a heating device (9) is also provided in the flow channel (3), and the heating device (9) is divided into a plurality of zones horizontally to heat the glass ribbon and adjust the horizontal temperature difference. 6.根据权利要求1所述的一种微晶玻璃分配及成形装置,其特征在于:所述流道(3)的底部安装有密封盖板(10),所述密封盖板(10)由两块耐火材料(2)叠加而成,且两块耐火材料(2)中间夹有电阻丝。6. A glass-ceramic distribution and forming device according to claim 1, characterized in that: a sealing cover plate (10) is installed at the bottom of the flow channel (3), and the sealing cover plate (10) is formed by stacking two pieces of refractory materials (2), and a resistance wire is sandwiched between the two pieces of refractory materials (2). 7.根据权利要求6所述的一种微晶玻璃分配及成形装置,其特征在于:所述密封盖板(10)中央处贯穿开设有通孔(11),且玻璃液加热后形成的玻璃带从通孔(11)中穿出。7. A glass-ceramic distribution and forming device according to claim 6, characterized in that: a through hole (11) is provided through the center of the sealing cover plate (10), and a glass ribbon formed after the glass liquid is heated passes through the through hole (11). 8.根据权利要求1所述的一种微晶玻璃分配及成形装置,其特征在于:所述分配成形炉(1)内设置有排气管(12),所述排气管(12)的顶端贯穿耐火材料(2)和分配成形炉(1)并延伸至分配成形炉(1)的外部,所述排气管(12)的底端延伸至流道(3)的内部,所述排气管(12)上安装有自动调压阀(13)。8. A microcrystalline glass distribution and forming device according to claim 1, characterized in that: an exhaust pipe (12) is provided in the distribution and forming furnace (1), the top end of the exhaust pipe (12) penetrates the refractory material (2) and the distribution and forming furnace (1) and extends to the outside of the distribution and forming furnace (1), the bottom end of the exhaust pipe (12) extends to the inside of the flow channel (3), and an automatic pressure regulating valve (13) is installed on the exhaust pipe (12).
CN202411095034.3A 2024-08-12 2024-08-12 Microcrystalline glass distributing and forming device Active CN118637812B (en)

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Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB111521A (en) * 1916-11-29 1917-11-29 Libbey Glass Co Apparatus for Forming Molten Glass or like Material in Cylindrical Form.
FR840113A (en) * 1938-06-30 1939-04-19 Hartford Empire Co Method and apparatus for dispensing molten glass
DE4446576C1 (en) * 1994-12-25 1996-04-25 Sorg Gmbh & Co Kg Trough melting kiln
US20030029199A1 (en) * 2001-08-08 2003-02-13 Pitbladdo Richard B. Sheet glass forming apparatus
CN1513781A (en) * 2003-07-25 2004-07-21 ������ҵ�ɷ����޹�˾ Continuous forming equipment for microcrystallized glass
CN104185613A (en) * 2012-04-05 2014-12-03 赫罗伊斯石英玻璃股份有限两合公司 Method for production of mold body from electrically melted synthetic quartz glass
US20180334405A1 (en) * 2017-05-22 2018-11-22 Schott Ag Method and apparatus for thickness control of a material ribbon
CN116438144A (en) * 2020-12-16 2023-07-14 日本电气硝子株式会社 Glass forming device

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB111521A (en) * 1916-11-29 1917-11-29 Libbey Glass Co Apparatus for Forming Molten Glass or like Material in Cylindrical Form.
FR840113A (en) * 1938-06-30 1939-04-19 Hartford Empire Co Method and apparatus for dispensing molten glass
DE4446576C1 (en) * 1994-12-25 1996-04-25 Sorg Gmbh & Co Kg Trough melting kiln
US20030029199A1 (en) * 2001-08-08 2003-02-13 Pitbladdo Richard B. Sheet glass forming apparatus
CN1513781A (en) * 2003-07-25 2004-07-21 ������ҵ�ɷ����޹�˾ Continuous forming equipment for microcrystallized glass
CN104185613A (en) * 2012-04-05 2014-12-03 赫罗伊斯石英玻璃股份有限两合公司 Method for production of mold body from electrically melted synthetic quartz glass
US20180334405A1 (en) * 2017-05-22 2018-11-22 Schott Ag Method and apparatus for thickness control of a material ribbon
CN116438144A (en) * 2020-12-16 2023-07-14 日本电气硝子株式会社 Glass forming device

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