Disclosure of Invention
In order to solve the existing problems, the invention provides a tin bath physical simulation method suitable for float glass; according to the invention, the temperature of each area can be ensured to be accurate by adopting contact type temperature measurement in different areas at the bottom of the tin bath model; the viscosity of the simulation liquid can be adjusted according to different float glass viscosity-temperature characteristics to be simulated, namely the viscosity of the simulation liquid is different due to different glass simulation batch mixture proportions; the effect of the edge finishing and drawing system process parameters on the thickness and width of the glass ribbon was simulated.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
a tin bath physical simulation method suitable for float glass comprises a heating and stirring device (2), a valve (3), a tin bath model (4), an edge roller (7), a drawing system (8) and a heating system (9); the device is characterized in that the following devices are added: temperature sensors (10) are arranged in different areas at the bottom of the tin bath model, and an image acquisition system (11) is arranged above the tin bath model;
the method comprises the following steps:
s1, weighing glass simulation batch according to the float glass viscosity-temperature characteristic curve to be simulated;
s2, putting the weighed glass simulation batch into a heating and stirring device for heating and stirring, and stirring for 120-180 minutes at 90-180 ℃ to fully homogenize the glass simulation batch;
s3, opening a heating system of the tin bath model to heat the polishing solution in four areas in the model, setting the temperature within the range of 40-120 ℃, and feeding back the temperature of the polishing solution by a bottom temperature sensor;
s4, after the four areas of the tin bath model reach the set time and temperature, simultaneously opening an edge roller, a drawing system and an image acquisition system in the tin bath model, and setting parameters of the edge roller and the drawing system;
s5, opening a valve of the heating and stirring device and an image acquisition system, simulating glass liquid to flow into the tin bath model, starting the polishing, flattening, thinning and forming processes, recording the simulation process by the image acquisition system, and leading out the formed glass belt by a drawing system;
and S6, measuring the thickness and the width of the formed glass ribbon, recording process parameters and other experimental data.
Further, the viscosity-temperature characteristic curve of the float glass in the step S1, i.e. the viscosity-temperature curve of the glass, is calculated according to the viscosity-temperature curve of the float glass and a similarity theory, and then the viscosity of the simulation liquid at the corresponding temperature segment is weighed out, and then a certain proportion of glass simulation batch is weighed.
Further, the heating area of the tin bath model in the step S3 is divided into four areas of polishing, flattening, thinning and forming, the temperature sensor is inserted into the polishing solution from the bottom of the model, and when the temperature of the polishing solution reaches a set temperature, the heating system stops heating; when the temperature of the polishing solution is lower than the set temperature, the heating system heats the polishing solution.
Further, the temperature sensor in the tin bath model of the step S3 adopts contact type temperature measurement, the temperature control precision is +/-0.1 ℃, baffles are arranged among different heating areas to realize the temperature gradient of different areas, and the accuracy of the temperature of each heating area is effectively ensured.
Further, the number of pairs of the edge rollers in the step S4 is 3-6, the swing angle of the edge rollers is 0-10 degrees, and the speed of the drawing system is 10-36 m/h.
Further, the step S5 of recording the simulation process by the image acquisition system is to record the polishing, flattening, thinning and forming processes of the simulation liquid in the tin bath model by means of video images, so as to facilitate visual analysis of the influence of the simulation liquid with different process viscosities and process parameters on the forming process of the glass ribbon.
Compared with the prior art, the invention has the following advantages:
1) the temperature sensor in the tin bath model adopts contact temperature measurement, the temperature control precision is +/-0.1 ℃, baffles are arranged among different heating areas to realize the temperature gradient of the different areas, and the accuracy of the temperature of each heating area is effectively ensured;
2) the forming process of the glass tin bath internal floating method with different viscosities can be simulated by adjusting the viscosity of the simulation liquid;
3) an image acquisition system is adopted to record the simulation process, so that the influence of simulation liquid with different process viscosities and process parameters on the forming process of the glass ribbon can be conveniently and visually analyzed;
4) the method can obtain the tin bath process parameters of the glass simulation liquid, and provides corresponding simulation data for the process design of the float glass tin bath and the process technology route optimization of the float glass production line.
Detailed Description
For a further understanding of the invention, the invention is described in detail below with reference to fig. 1, 2, 3 and the specific embodiments, wherein fig. 2 and 3: 1-simulation liquid, 2-heating and stirring device, 3-valve, 4-tin bath model, 5-formed glass belt, 6-polishing liquid, 7-edge roller, 8-drawing system, 9-heating system, 10-temperature sensor and 11-image acquisition system.
Example 1
A tin bath physical simulation method suitable for float glass comprises the following specific implementation steps:
s1, weighing a No. 4 sample simulation batch in the figure 1 according to a certain proportion according to a float glass viscosity-temperature characteristic curve to be simulated;
s2, putting the weighed glass simulation batch into a heating and stirring device 2 for heating and stirring, and stirring for 120 minutes at 150 ℃ to fully homogenize the glass simulation batch;
s3, opening a heating system 9 in the tin bath model 4 to heat the polishing solution 6 in four areas in the model, wherein the temperature setting range is 40-90 ℃, and a bottom temperature sensor 10 feeds back the temperature of the polishing solution 6;
s4, setting parameters of the edge roller 7 and the drawing system 8 after the four areas of the tin bath model reach the set time and temperature, wherein the number of pairs of the edge roller is 3, the angle is 0-10 degrees, and opening the edge roller 7 and the drawing system 8 in the tin bath model;
s5, opening a valve 3 and an image acquisition system 11 on the side surface of the heating and stirring device, simulating that the molten glass 1 flows into the tin bath model 4, starting the polishing, flattening, thinning and forming processes, recording the simulation process by the image acquisition system 11, and leading out the formed glass ribbon 5 through a drawing system 8;
and S6, measuring the thickness and the width of the formed glass ribbon, recording process parameters and other experimental data.
The influence of the process parameters of the edge roller, the drawing system and the like on the thickness and the width of the glass strip can be obtained by combining the experimental data and the process parameters obtained by the physical simulation of the tin bath, and corresponding simulation data is provided for the process design of the float glass tin bath and the process technology route optimization of the float glass production line by comparing the process parameters with the process parameters of the float glass production line.
Example 2
A tin bath physical simulation method suitable for float glass comprises the following specific implementation steps:
s1, weighing a No. 4 sample simulation batch in the figure 1 according to a certain proportion according to a float glass viscosity-temperature characteristic curve to be simulated;
s2, putting the weighed glass simulation batch into a heating and stirring device 2 for heating and stirring, and stirring for 120 minutes at 150 ℃ to fully homogenize the glass simulation batch;
s3, opening a heating system 9 in the tin bath model 4 to heat the polishing solution 6 in four areas in the model, wherein the temperature setting range is 40-90 ℃, and a bottom temperature sensor 10 feeds back the temperature of the polishing solution 6;
s4, setting parameters of the edge roller 7 and the drawing system 8 after the four areas of the tin bath model reach the set time and temperature, wherein the number of pairs of the edge roller is 4, the angle is 0-10 degrees, and opening the edge roller 7 and the drawing system 8 in the tin bath model;
s5, opening a valve 3 and an image acquisition system 11 on the side surface of the heating and stirring device, simulating that the molten glass 1 flows into the tin bath model 4, starting the polishing, flattening, thinning and forming processes, recording the simulation process by the image acquisition system 11, and leading out the formed glass ribbon 5 through a drawing system 8;
and S6, measuring the thickness and the width of the formed glass ribbon, recording process parameters and other experimental data.
The influence of the process parameters of the edge roller, the drawing system and the like on the thickness and the width of the glass strip can be obtained by combining the experimental data and the process parameters obtained by the physical simulation of the tin bath, and corresponding simulation data is provided for the process design of the float glass tin bath and the process technology route optimization of the float glass production line by comparing the process parameters with the process parameters of the float glass production line.
Example 3
A tin bath physical simulation method suitable for float glass comprises the following specific implementation steps:
s1, weighing the 5# sample simulation batch in the figure 1 according to a certain proportion according to a float glass viscosity-temperature characteristic curve to be simulated;
s2, putting the weighed glass simulation batch into a heating and stirring device 2 for heating and stirring, and stirring for 150 minutes at 180 ℃ to fully homogenize the glass simulation batch;
s3, opening a heating system 9 in the tin bath model 4 to heat the polishing solution 6 in four areas in the model, wherein the temperature setting range is 40-110 ℃, and a bottom temperature sensor 10 feeds back the temperature of the polishing solution 6;
s4, setting parameters of the edge roller 7 and the drawing system 8 after the four areas of the tin bath model reach the set time and temperature, wherein the number of pairs of the edge roller is 4, the angle is 0-10 degrees, and opening the edge roller 7 and the drawing system 8 in the tin bath model;
s5, opening a valve 3 and an image acquisition system 11 on the side surface of the heating and stirring device, simulating that the molten glass 1 flows into the tin bath model 4, starting the polishing, flattening, thinning and forming processes, recording the simulation process by the image acquisition system 11, and leading out the formed glass ribbon 5 through a drawing system 8;
and S6, measuring the thickness and the width of the formed glass ribbon, recording process parameters and other experimental data.
The influence of the process parameters of the edge roller, the drawing system and the like on the thickness and the width of the glass strip can be obtained by combining the experimental data and the process parameters obtained by the physical simulation of the tin bath, and corresponding simulation data is provided for the process design of the float glass tin bath and the process technology route optimization of the float glass production line by comparing the process parameters with the process parameters of the float glass production line.
Example 4
A tin bath physical simulation method suitable for float glass comprises the following specific implementation steps:
s1, weighing the sample No. 5 in the figure 1 according to a certain proportion according to a float glass viscosity-temperature characteristic curve to be simulated;
s2, putting the weighed glass simulation batch into a heating and stirring device 2 for heating and stirring, and stirring for 150 minutes at 180 ℃ to fully homogenize the glass simulation batch;
s3, opening a heating system 9 in the tin bath model 4 to heat the polishing solution 6 in four areas in the model, wherein the temperature setting range is 40-110 ℃, and a bottom temperature sensor 10 feeds back the temperature of the polishing solution 6;
s4, setting parameters of the edge roller 7 and the drawing system 8 after the four areas of the tin bath model reach the set time and temperature, wherein the number of pairs of the edge roller is 5, the angle is 0-10 degrees, and opening the edge roller 7 and the drawing system 8 in the tin bath model;
s5, opening a valve 3 and an image acquisition system 11 on the side surface of the heating and stirring device, simulating that the molten glass 1 flows into the tin bath model 4, starting the polishing, flattening, thinning and forming processes, recording the simulation process by the image acquisition system 11, and leading out the formed glass ribbon 5 through a drawing system 8;
and S6, measuring the thickness and the width of the formed glass ribbon, recording process parameters and other experimental data.
The influence of the process parameters such as the edge roller, the drawing system and the like on the thickness and the width of the glass strip can be obtained by combining the experimental data and the process parameters obtained by the physical simulation of the tin bath, and corresponding simulation data is provided for the process design of the float glass tin bath and the process technology route optimization of the float glass production line by comparing the parameters with the parameters of the float glass production line.
Secondly, the specific process parameter settings and simulation data results of each implementation example are shown in table 1.
Table 1 simulation parameter settings and simulation data results for each example
Examples
|
Example one
|
Example two
|
EXAMPLE III
|
Example four
|
Heating and stirring temperature (. degree.C.)
|
150
|
150
|
180
|
180
|
Heating and stirring time (minutes)
|
120
|
120
|
150
|
150
|
Log edge roller (pair)
|
3
|
4
|
4
|
5
|
Swing angle (degree) of edge roller
|
0~10
|
0~10
|
0~10
|
0~10
|
Pulling speed (meter/hour)
|
12
|
15
|
18
|
28
|
Thickness of glass ribbon (mm)
|
2.35
|
1.24
|
0.81
|
0.46
|
Glass width (mm)
|
195
|
208
|
223
|
239 |
The foregoing is merely a preferred embodiment of the invention and is not intended to limit the invention in any manner; those skilled in the art can make numerous possible variations and modifications to the present teachings, or modify equivalent embodiments to equivalent variations, without departing from the scope of the present teachings, using the methods and techniques disclosed above. Therefore, any simple modification, equivalent replacement, equivalence, change and modification of the above embodiments according to the technical essence of the present invention are still within the protection scope of the technical solution of the present invention.