Molten glass stirring device and molten glass quality improvement method
阅读说明:本技术 玻璃液搅拌装置及玻璃液质量改进方法 (Molten glass stirring device and molten glass quality improvement method ) 是由 陈筱丽 郭富强 周思宇 易平 刘小宁 于 2019-12-18 设计创作,主要内容包括:本发明提供一种可以在1550℃以上长期稳定运行的搅拌装置,并解决玻璃液均化问题。玻璃液搅拌装置,包括搅拌器和搅拌室,搅拌室是由侧壁、底壁和顶壁构成的空心体结构,在搅拌室上设置有顶孔、玻璃液出口和玻璃液入口,搅拌器包括中心轴、左横杆、右横杆、左竖杆和右竖杆,中心轴分别与左横杆和右横杆连接,左横杆与左竖杆连接,右横杆与右竖杆连接。本发明通过搅拌器左横杆、右横杆、左竖杆、右竖杆以及底横杆的作用,玻璃液内部分子扩散、溶解及搅拌器混合效果得到显著改善,玻璃液的均匀性得到提升;搅拌器内层冷却系统使搅拌器整体温度得到控制,降低了搅拌器材料在高温下失效的风险,对保持搅拌器形状,延长搅拌器使用寿命具有显著改进。(The invention provides a stirring device which can stably operate for a long time at the temperature of more than 1550 ℃, and solves the problem of homogenization of molten glass. Glass liquid agitating unit, including agitator and teeter chamber, the teeter chamber is the hollow body structure that comprises lateral wall, diapire and roof, is provided with apical pore, glass liquid export and glass liquid entry on the teeter chamber, and the agitator includes center pin, left horizontal pole, right horizontal pole, left montant and right montant, and the center pin is connected with left horizontal pole and right horizontal pole respectively, and left horizontal pole is connected with left montant, and right horizontal pole is connected with right montant. According to the invention, through the action of the left cross rod, the right cross rod, the left vertical rod, the right vertical rod and the bottom cross rod of the stirrer, the diffusion and dissolution effects of the molecules in the glass liquid and the mixing effect of the stirrer are obviously improved, and the uniformity of the glass liquid is improved; the stirrer inner layer cooling system controls the whole temperature of the stirrer, reduces the failure risk of stirrer materials at high temperature, and has obvious improvement on the shape maintenance and the service life extension of the stirrer.)
1. Glass liquid agitating unit, including agitator (1) and teeter chamber (2), its characterized in that, teeter chamber (2) are the hollow body structure that comprises lateral wall (21), diapire (22) and roof (23) be provided with apical pore (24), glass liquid export (25) and glass liquid entry (27) on teeter chamber (2), agitator (1) is including center pin (11), left horizontal pole (12), right horizontal pole (13), left montant (14) and right montant (15), center pin (11) are connected with left horizontal pole (12) and right horizontal pole (13) respectively, left horizontal pole (12) are connected with left montant (14), right horizontal pole (13) are connected with right montant (15).
2. The molten glass stirring device according to claim 1, wherein the stirrer (1) is further provided with a bottom cross bar (16), and the right vertical bar (15) and the left vertical bar (15) are respectively connected with the bottom cross bar (16).
3. The molten glass stirring device according to claim 1 or 2, wherein the central shaft (11), the left cross bar (12), the right cross bar (13), the left vertical bar (14), the right vertical bar (15) and the bottom cross bar (16) are all composed of an outer layer (17), an intermediate layer (18) and an inner layer (19), and the inner layers (19) on the central shaft (11), the left cross bar (12), the right cross bar (13), the left vertical bar (14), the right vertical bar (15) and the bottom cross bar (16) are communicated.
4. The molten glass stirring device according to claim 3, wherein the outer layer (17) is made of a noble metal material, and the thickness of the outer layer (17) is 0.5mm to 1.8mm, and preferably 0.8mm to 1.0 mm.
5. A molten glass stirring apparatus according to claim 3, wherein the outer layer (17) is made of platinum metal; or is made of platinum-rhodium alloy or platinum-rhodium dispersion material, wherein the weight percentage content of rhodium is 5% -15%, and the optimal content is 8% -12%; or a platinum gold alloy, wherein the weight percentage content of the gold is 2-12%, and the optimal content is 5-8%.
6. A molten glass stirring apparatus according to claim 3, wherein the intermediate layer (18) is made of a refractory material, preferably a refractory material having an upper temperature limit of more than 1600 ℃ and a density of less than 2000kg/m at ambient temperature3。
7. A molten glass stirring apparatus according to claim 3, wherein the inner layer (19) is composed of a cooling pipe and a cooling medium.
8. The molten glass stirring device according to claim 3, wherein the inner layer (19) is a sleeve structure of a large sleeve and a small sleeve which are concentric or eccentric round pipes; or a separate multiple tube structure.
9. A molten glass stirring apparatus according to claim 3, wherein a fulcrum (20) is provided at regular intervals outside the inner layer (19).
10. The molten glass stirring device according to claim 1 or 2, wherein the outer surfaces of the left cross bar (12), the right cross bar (13), the left vertical bar (14), the right vertical bar (15) and the bottom cross bar (16) are uniformly provided with a plurality of small prisms, cylinders or cones.
11. Glass stirring device according to claim 1 or 2, wherein the maximum length L of the left vertical bar (14) and the right vertical bar (15) is 0.3-0.8, preferably 0.4-0.7 of the height of the glass-liquid line (3) in the stirring chamber (2).
12. A molten glass stirring apparatus according to claim 1 or 2, wherein the left cross bar (12) and the right cross bar (13) are connected to the left vertical bar (14) and the right vertical bar (15), respectively, at their highest points; or the left cross bar (12) and the right cross bar (13) are respectively connected with the left vertical bar (14) and the right vertical bar (15) at the lowest points; or the left cross bar (12) and the right cross bar (13) are respectively connected with the middle points of the left vertical bar (14) and the right vertical bar (15) in the length direction.
13. The molten glass stirring device according to claim 1 or 2, wherein the minimum distance w between the outer surfaces of the left and right vertical rods (14, 15) and the side wall (21) of the stirring chamber (2) is 0.11 to 0.25 of the diameter of the inscribed circle formed by the side wall (21) of the stirring chamber (2).
14. A molten glass stirring device according to claim 1 or 2, wherein the minimum distance m between the bottom surface of the left vertical rod (14) and the bottom surface of the right vertical rod (15) and the bottom wall (22) of the stirring chamber (2) is within 100 mm; or the minimum distance between the outer layer surface of the bottom cross bar (16) and the bottom wall (22) of the stirring chamber (2) is within 100 mm.
15. The glass-stirring device as claimed in claim 1 or 2, characterized in that the outer layer (17) of the left cross bar (12), the right cross bar (13) and the bottom cross bar (16) of the stirrer (1) is provided with an expansion zone consisting of a plurality of expansion rings, the maximum distance between the wave crest and the wave trough of which does not exceed 12mm, preferably 5-10 mm.
16. A method for modifying the quality of molten glass, the method comprising the steps of:
1) the inner layer (19) of the stirrer (1) is filled with a cooling medium, and the temperature difference between the inlet and the outlet of the cooling medium is controlled to meet the requirement;
2) when the continuous melting is adopted to produce the ultra-high temperature glass, the glass liquid is input into the stirring chamber (2) through the glass liquid inlet (27) and reaches the stable liquid level line of the process design; when the discontinuous melting production is adopted, powder of glass components, a mixture of the powder and glass slag or glass liquid is input into the stirring chamber (2) through a glass liquid inlet (27), when the glass liquid in the stirring chamber (2) has stirring conditions, the stirrer (1) is placed into the glass liquid, and at the moment, the glass liquid level reaches a stable liquid level line of process design; controlling the temperature of the glass liquid in the stirring and homogenizing process to enable the glass liquid to be in a viscosity range capable of homogenizing and eliminating stripes;
3) the stirrer (1) rotates clockwise or anticlockwise at a constant speed according to design requirements, and by means of speed difference between the stirrer (1) and the glass liquid, the glass liquid in the stirring chamber (2) is forced to generate horizontal rotation motion and vertical convection in a local vertical direction, so that inhomogeneity in the glass liquid is elongated, thinned and cut, the contact area of homogeneous and heterogeneous glass liquid in the glass liquid is increased, and the homogeneous main body glass liquid and the heterogeneous glass liquid are mutually dissolved, diffused and mixed;
4) the glass liquid is influenced by stirring circulation in the stirring chamber (2), the retention time is greatly increased, so that the influence of heterogeneous glass liquid is gradually reduced, when the uniformity of the glass liquid meets the technical requirement of a product, the glass liquid is homogenized in the stirring chamber (2), and the glass liquid is discharged from a glass liquid outlet (25) to enter the next production procedure.
17. The method for improving the quality of molten glass according to claim 16, wherein the step 3) is: the stirrer (1) rotates clockwise or anticlockwise at a constant speed according to design requirements, so that the glass metal in the stirring chamber (2) generates forced convection, the glass metal in the stirring chamber (2) moves along with the stirrer (1) and is divided into three conditions, the first condition is that the glass metal near the outer layer surface of the stirrer generates rotary motion, and the region with the maximum speed generates a glass metal adhesive layer on the outer layer surface of the stirrer; the second is that the glass liquid in the area covered by the left cross bar (12), the right cross bar (13) and the bottom cross bar (16) partially presents the movement of up-down convection near the central line; the third is that the glass liquid outside the coverage area of the left vertical rod (14) and the right vertical rod (15) generates fluid section change when moving relative to the side wall of the stirring chamber through the left vertical rod (14) and the right vertical rod (15) to form the effect of extruding fluid, so that the glass liquid is in regular up-and-down convection motion; through the three movement modes, the internal mixing and diffusion effects of the molten glass in the stirring chamber (2) are obviously improved.
18. The method of claim 16, wherein the rotational speed in step 3) is between 0.5 and 30 revolutions per minute, preferably between 0.5 and 15 revolutions per minute.
19. The molten glass quality improvement method according to claim 16, characterized in that when the left cross bar (12) and the right cross bar (13) are respectively connected with the left vertical bar (14) and the right vertical bar (15) at the highest points, the distance d from the outer layer surfaces of the left cross bar (12) and the right cross bar (13) to the glass liquid surface is 0.1-0.6L, preferably 0.3-0.6L; when the left cross bar (12) and the right cross bar (13) are respectively connected with the left vertical bar (14) and the right vertical bar (15) at the lowest points; or when the left cross bar (12) and the right cross bar (13) are respectively connected with the midpoint positions of the left vertical bar (14) and the right vertical bar (15) in the length direction, the distance d from the highest point of the left vertical bar (14) and the right vertical bar (15) to the glass liquid level is 0.1-0.8L, and the optimal distance d is 0.3-0.6L.
Technical Field
The invention relates to a stirring device for homogenizing molten glass in an ultrahigh-temperature glass production process, and a method for homogenizing non-uniform components in the molten glass by using the stirring device so as to improve the quality of the molten glass.
Background
The ultra-high temperature glass production generally means that the highest temperature of one or more of three processes of melting, clarifying and homogenizing of molten glass reaches or exceeds 1550 ℃ in the production process due to special composition. In the production of the ultra-high temperature glass, the process temperature reaches more than 1550 ℃, so that the ultra-high temperature glass has high requirements on the temperature resistance of production equipment, and meanwhile, the ultra-high temperature glass is usually applied to special industries, such as aerospace, weaponry, high-precision equipment and the like, so that the ultra-high temperature glass has strict requirements on the product quality.
The production process of the ultra-high temperature glass is similar to the production process flow of the common glass, and generally comprises the processes of melting, clarifying, homogenizing, forming, annealing, packaging and the like of molten glass in a melting furnace. The homogenization process in the process mainly eliminates the non-uniform components in the glass liquid, improves the optical performance of the glass product and plays an extremely important role in production.
In a general glass production process, the homogenization process usually adopts stirrers with different shapes to increase the homogeneity of the molten glass in a mechanical stirring manner. For the glass liquid with the viscosity changing along with the temperature, the non-uniform parts in the glass melt are stretched into thin stripes by mechanical stirring, the stretched stripes are cut into a plurality of short segments by a stirrer blade perpendicular to the main flow direction, the short stripe segments are dispersed in the glass liquid main body by the action of a stirring rotating area, and the contact surface between the homogeneous glass liquid and the non-homogeneous glass liquid in the glass liquid is greatly increased by the action, so that the mutual dissolution, diffusion and mixing of the components between the homogeneous glass liquid and the non-homogeneous glass liquid are facilitated, and the required uniformity index requirement is met when the glass liquid is formed into a glass product after the homogenization process. The influence factors of the homogenization effect of the molten glass are mainly determined by the homogenization efficiency of the stirrer and the stirring chamber, the difference between the quality of the molten glass and the quality of the heterogeneous molten glass, and the like. The improvement of the homogenizing efficiency of the stirrer and the stirring chamber is generally realized by designing the stirrer into a paddle type, a frame type, a disc type and the like and a distance between the stirrer and the wall surface of the stirring chamber. The difference in properties between homogeneous and heterogeneous glass melts mainly arises from differences in glass melt composition caused by previous processes, the influence of temperature gradients caused by flow, and the like.
In the homogenization process of the ultra-high temperature glass, the size of a stirring chamber is usually larger than that of common optical glass, display plate glass and the like, and the operation temperature is also higher, so that the mechanical strength of the stirrer adopting common structural design and materials is sharply reduced due to high-temperature creep of the materials, and the service life of the stirrer is also greatly reduced; meanwhile, the mechanical strength is reduced, the original design shape is difficult to maintain, and the stirring efficiency is greatly reduced. On the other hand, the use temperature of the stirrer is greatly increased in the homogenization process, and the control of impurity defects in the mechanical stirring process is also required to be noticed, so that the secondary pollution to the molten glass is prevented, and the product quality is prevented from being influenced.
Disclosure of Invention
The invention aims to provide a stirring device which can stably operate for a long time at the temperature of more than 1550 ℃, solve the problem of homogenization of molten glass in the production process of ultra-high temperature glass and improve the quality of the molten glass.
The invention also provides a quality improvement method of the molten glass.
The technical scheme adopted by the invention for solving the technical problem is as follows: glass liquid agitating unit, including agitator and teeter chamber, the teeter chamber is the hollow body structure that comprises lateral wall, diapire and roof be provided with apical pore, glass liquid export and glass liquid entry on the teeter chamber, the agitator includes center pin, left horizontal pole, right horizontal pole, left montant and right montant, the center pin is connected with left horizontal pole and right horizontal pole respectively, left horizontal pole is connected with left montant, right horizontal pole is connected with right montant.
Further, the stirrer is further provided with a bottom cross rod, and the right vertical rod and the left vertical rod are respectively connected with the bottom cross rod.
Further, center pin, left horizontal pole, right horizontal pole, left montant, right montant and end horizontal pole constitute by skin, intermediate level and inlayer, just the inlayer on center pin, left horizontal pole, right horizontal pole, left montant, right montant and the end horizontal pole is the intercommunication.
Further, the outer layer is made of a noble metal material, the thickness of the outer layer is 0.5mm-1.8mm, and the optimal thickness is 0.8mm-1.0 mm.
Further, the outer layer is made of platinum metal; or is made of platinum-rhodium alloy or platinum-rhodium dispersion material, wherein the weight percentage content of rhodium is 5% -15%, and the optimal content is 8% -12%; or a platinum gold alloy, wherein the weight percentage content of the gold is 2-12%, and the optimal content is 5-8%.
Furthermore, the intermediate layer is made of refractory materials, preferably refractory materials with the upper temperature limit higher than 1600 ℃ can be used, and the density of the refractory materials at normal temperature is less than 2000kg/m3。
Further, the inner layer is composed of a cooling pipe and a cooling medium.
Furthermore, the inner layer adopts a sleeve structure designed by a large sleeve and a small concentric or eccentric circular pipe; or a separate multiple tube structure.
Furthermore, a pivot is arranged outside the inner layer at intervals.
Furthermore, a plurality of small prisms, cylinders or cones are uniformly arranged on the outer layer surfaces of the left cross bar, the right cross bar, the left vertical bar, the right vertical bar and the bottom cross bar.
Further, the maximum length L of the left vertical rod and the right vertical rod is 0.3-0.8, preferably 0.4-0.7 of the height of the liquid level line of the glass liquid in the stirring chamber.
Further, the left cross rod and the right cross rod are respectively connected with the left vertical rod and the right vertical rod at the highest points; or the left cross bar and the right cross bar are respectively connected with the left vertical bar and the right vertical bar at the lowest points; or the left cross rod and the right cross rod are respectively connected with the middle points of the left vertical rod and the right vertical rod in the length direction.
Furthermore, the minimum distance w between the outer layer surfaces of the left vertical rod and the right vertical rod and the side wall of the stirring chamber is 0.11-0.25 of the diameter of an inscribed circle formed by the side wall of the stirring chamber.
Further, the minimum distance m between the bottom surfaces of the left vertical rod and the right vertical rod and the
Furthermore, expansion areas consisting of a plurality of expansion rings are arranged on the outer layers of the left cross bar, the right cross bar and the bottom cross bar of the stirrer, and the maximum distance between the wave crest and the wave trough of each expansion ring is not more than 12mm, preferably 5-10 mm.
A method for modifying the quality of a molten glass, the method comprising the steps of:
1) cooling medium is introduced into the inner layer of the stirrer, and the temperature difference between the inlet and the outlet of the cooling medium is controlled to meet the requirement;
2) when the continuous melting is adopted to produce the ultra-high temperature glass, the glass liquid is input into the stirring chamber from the glass liquid inlet and reaches the stable liquid level line of the process design; when the discontinuous melting production is adopted, powder of glass components, a mixture of the powder and glass slag or glass liquid is input into a stirring chamber through a glass liquid inlet, when the glass liquid in the stirring chamber has stirring conditions, a stirrer is placed into the glass liquid, and the glass liquid level reaches a stable liquid level line of process design; controlling the temperature of the glass liquid in the stirring and homogenizing process to enable the glass liquid to be in a viscosity range capable of homogenizing and eliminating stripes;
3) the stirrer rotates clockwise or anticlockwise at a constant speed according to design requirements, and by means of speed difference between the stirrer and the glass liquid, the glass liquid in the stirring chamber is forced to generate horizontal rotation motion and vertical convection in a local vertical direction, so that inhomogeneity in the glass liquid is elongated, thinned and cut, the contact area between homogeneous glass liquid and heterogeneous glass liquid in the glass liquid is increased, and the homogeneous main body glass liquid and the heterogeneous glass liquid are mutually dissolved, diffused and mixed;
4) the glass liquid is influenced by stirring circulation in the stirring chamber, the retention time is greatly increased, so that the influence of heterogeneous glass liquid is gradually reduced, when the uniformity of the glass liquid reaches the technical requirement of a product, the glass liquid is homogenized in the stirring chamber and discharged from a glass liquid outlet to enter the next production procedure.
Further, the step 3) is as follows: the stirrer rotates clockwise or anticlockwise at a constant speed according to design requirements, so that the glass metal in the stirring chamber generates forced convection, the glass metal in the stirring chamber moves along with the stirrer and is divided into three conditions, the first condition is that the glass metal near the outer layer surface of the stirrer generates rotary motion, and the region with the maximum speed generates a glass metal adhesive layer on the outer layer surface of the stirrer; the second is that the partial glass liquid in the covered area of the left cross bar, the right cross bar and the bottom cross bar shows the movement of up-down convection; the third is that the glass liquid outside the coverage area of the left vertical rod and the right vertical rod generates fluid section change when the left vertical rod and the right vertical rod move relative to the side wall of the stirring chamber, so as to form an effect of extruding fluid and enable the glass liquid to present regular up-and-down convection motion; through the three movement modes, the internal mixing and diffusion effects of the molten glass in the stirring chamber are obviously improved;
further, the rotation speed in step 3) is between 0.5 and 30 revolutions per minute, preferably between 0.5 and 15 revolutions per minute.
Further, when the left cross bar and the right cross bar are respectively connected with the left vertical bar and the right vertical bar at the highest points, the distance d between the outer layer surfaces of the left cross bar and the right cross bar and the liquid level of the glass is 0.1-0.6L, and the preferable distance d is 0.3-0.6L; when the left cross rod and the right cross rod are respectively connected with the left vertical rod and the right vertical rod at the lowest points; or when the left cross bar and the right cross bar are respectively connected with the middle points of the left vertical bar and the right vertical bar in the length direction, the distance d from the highest point of the left vertical bar and the right vertical bar to the glass liquid level is 0.1-0.8L, and the preferable distance d is 0.3-0.6L.
The invention has the beneficial effects that: the convection efficiency of the glass liquid in the stirring chamber is effectively improved in a mechanical stirring mode; through the action of the left cross rod, the right cross rod, the left vertical rod, the right vertical rod and the bottom cross rod of the stirrer, the diffusion and dissolution effects of molecules in the glass liquid and the mixing effect of the stirrer are obviously improved, and the uniformity of the glass liquid is improved; the inner cooling system of the stirrer controls the whole temperature of the stirrer, reduces the failure risk of stirrer materials at high temperature, and further has obvious improvement on the shape maintenance and the service life prolonging of the stirrer; the surface temperature of the stirrer is controlled, and the quantity of noble metal particles falling off from the surface of the stirrer and entering the molten glass can also be reduced; the optimized design of the cover plate of the stirrer further reduces the possibility that volatile matters at the top of the stirring chamber are condensed and fall into the molten glass to form defects, so that the problem of impurity defects caused by the stirring process is favorably reduced.
Drawings
FIG. 1 is a schematic view of the structure of a stirring apparatus of the present invention.
FIG. 2 is a schematic view of the construction of a blender with a bottom rail for the blending apparatus of the present invention.
FIG. 3 is a partial cross-sectional view of the inner layer of the agitator of the mixing apparatus of the present invention.
FIG. 4 is a partial cross-sectional view of an alternative construction of the inner layer of the agitator of the mixing apparatus of the present invention.
Detailed Description
In the process of the ultrahigh-temperature glass homogenizing process, the problem of nonuniformity caused by factors such as the internal composition and the temperature of molten glass can be mechanically stirred by the stirring device provided by the invention, and finally, the purpose of eliminating nonuniformity in the glass is achieved. As shown in fig. 1, the stirring apparatus of the present invention comprises a stirrer 1 and a
After the glass liquid reaches a certain liquid level height in the
The
The mixer 1 comprises a
In the working process of the stirrer 1, the
The outer layer 17 of the stirrer 1 is made of a noble metal material which can be used for resisting the erosion of the molten glass to the stirrer 1, meanwhile, the overall shape of the stirrer 1 is kept, the pollution of a stirrer material to the molten glass is reduced, and the service life of the stirrer 1 is prolonged. The thickness of the outer layer 17 is 0.5mm to 1.8mm, and the optimum thickness is 0.8mm to 1.0 mm. The outer layer 17 can be made of platinum metal with stable high-temperature performance, or can be made of platinum-rhodium alloy or platinum-rhodium dispersion material with more excellent strength and stable high-temperature performance, wherein the content of rhodium is 5-15% (weight percentage content, the same below), and the optimal content is 8-12%. The outer layer 17 can also be made of platinum alloy which has excellent strength and stable high-temperature performance and can improve the wetting angle of the glass liquid to the outer layer 17, wherein the content of gold is 2-12%, the optimal content is 5-8%, and the improvement of the wetting angle is beneficial to reducing the adhesion amount of the glass liquid on the outer layer 17 and preventing crystallization.
The intermediate layer 18 of the stirrer 1 is made of a refractory material, and in order to prevent the refractory material from losing its effect, the intermediate layer 18 is preferably made of a refractory material having an upper temperature limit of more than 1600 ℃ and a density of less than 2000kg/m at normal temperature, taking into account that the temperature of the molten glass of the stirrer 1 is not lower than 1550 ℃ when the stirrer 1 is operated in the
The inner layer 19 of the stirrer 1 is a cooling zone, consisting of cooling tubes and a cooling medium. The cooling medium is filled in the cooling pipe to provide a cooling source for the stirrer 1, so that the integral temperature of the stirrer 1 is controllable, and the structural strength is controllable. On the other hand, the inner layer 19 provides structural stress support for the whole stirrer 1, and a
The outer shapes of the
The left
The maximum length L of the left
The
The minimum distance w between the outer layer surfaces of the left
The minimum distance m between the bottom surfaces of the left
Expansion areas are arranged on the outer layers 17 of the
A
The present invention can provide the following method for improving the quality of molten glass by using the stirring apparatus having the above structure.
A method for modifying the quality of a molten glass, the method comprising the steps of:
1) before the stirring device works and in the whole stirring process, the flow of the cooling medium in and out of the inner layer 19 of the stirrer 1 is always kept stable, and the temperature difference between the cooling medium in and out is controlled to meet the requirement;
2) when the continuous melting is adopted to produce the ultra-high temperature glass, the glass liquid is input into the stirring
3) the stirrer 1 rotates clockwise or anticlockwise at a constant speed according to design requirements, so that the glass metal in the stirring
4) the glass liquid is influenced by the stirring circulation in the stirring
By adopting the quality improvement method of the glass metal, the convection efficiency of the glass metal in the stirring chamber can be effectively improved in a mechanical stirring mode; simultaneously through the effect of left
In the method for improving the quality of the molten glass, the rotating speed of the stirrer directly influences the convection efficiency of the molten glass in the area, and meanwhile, too high stirring speed can also cause the amount of the noble metal particles on the outer layer of the stirrer entering the molten glass to be increased, so that the stirring speed needs to be reasonably controlled between 0.5 rpm and 30 rpm, and preferably between 0.5 rpm and 15 rpm. In the stirring process, the rotation speed of the stirrer should be kept rotating at a constant speed, and the sudden change of the speed easily causes local fatigue and structural deformation of the stirrer, so that the service life of the stirrer is influenced.
In the method for improving the quality of the molten glass, in order to keep the molten glass in the coverage areas of the
In the method for improving the quality of the molten glass, the stable cooling medium in the inner layer of the stirrer controls the overall temperature of the stirrer, reduces the quantity of noble metal particles falling off from the surface of the stirrer and entering the molten glass, and is beneficial to reducing the problem of impurity defects caused by a stirring process; meanwhile, the viscosity of the glass liquid near the stirrer is slightly increased compared with other areas due to the cooling effect of the cooling medium, so that the speed transmission of the glass liquid close to the surface of the stirrer during the rotation of the stirrer is facilitated, the influence range of the stirring area is indirectly increased, and the homogenization effect of the stirrer on the glass liquid is facilitated to be improved.
The method is particularly suitable for the production operation of the ultra-high temperature glass with the inscribed circle diameter of more than 600mm in the stirring chamber, and is particularly suitable for the internal uniformity quality improvement of the ultra-high temperature glass with the homogenization temperature of more than 1550 ℃ such as borosilicate glass, aluminosilicate glass, special color glass and the like.
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