Control method, device and equipment for improving melting rate of kiln and storage medium

Abstract

The invention relates to the technical field of the glass manufacturing industry, in particular to a control method and device for increasing the melting rate of a kiln, equipment and a storage medium. Heating element identifiers and element output power corresponding to each heating element identifier are obtained according to the kiln heating temperature; the real-time kiln heating temperature is compared with a preset temperature curve, the output power of each element is adjusted according to the comparison result, and a kiln temperature control result is obtained; the current in-furnace pressure is obtained, calculation is conducted according to the current in-furnace pressure, and an in-furnace air pressure adjusting instruction is obtained; and when the in-furnace air pressure adjusting instruction and the in-furnace air pressure adjusting result are obtained, generating an in-furnace gas dynamic switching instruction according to the in-furnace air pressure adjusting result so as to respond to a glass preparation instruction. The method has the effect of solving the problem that the melting rate of a current kiln is low.

Description

Technical Field

[0001] The present application relates to the technical field of glass manufacturing industry, and in particular to a control method, device, equipment and storage medium for improving the melting rate of a kiln. Background Art

[0002] At present, the development of the glass manufacturing industry is inseparable from the efficient kiln melting process. The melting rate directly affects the competitiveness and market position of the enterprise. In recent years, with the advancement of automation technology, more and more glass manufacturers have begun to explore automated control methods in order to break the limitations of traditional manual control and further tap the production potential of kilns.

[0003] The production capacity of glass product manufacturers is determined by the size of the kiln area. When the area of ​​the kiln is certain, if you want to increase the production capacity, you can only do so by increasing the melting rate. The melting rate refers to the amount of qualified glass liquid melted per square meter of the kiln every 24 hours, and the unit is (tons / day. square meter). All glass factories will increase the kiln melting rate as a goal to improve production efficiency and increase economic benefits. Therefore, there is still room for improvement. Summary of the invention

[0004] In order to solve the problem of low melting rate of current kilns, the present application provides a control method, device, equipment and storage medium for improving the melting rate of kilns.

[0005] The above-mentioned invention objective of the present application is achieved through the following technical solutions: A control method for improving the melting rate of a kiln, the control method for improving the melting rate of a kiln comprising: Acquire the kiln heating temperature in real time, and acquire the heating element identification and the element output power corresponding to each heating element identification according to the kiln heating temperature; Compare the real-time heating temperature of the kiln with the preset temperature curve, adjust the output power of each element according to the comparison result, and obtain the kiln temperature control result; Obtaining the current pressure in the furnace, and performing calculations based on the current pressure in the furnace to obtain a furnace pressure adjustment instruction; After obtaining the furnace pressure regulation result of the furnace pressure regulation instruction, a furnace gas dynamic switching instruction is generated according to the furnace pressure regulation result to respond to the glass preparation instruction.

[0006] By adopting the above technical solution, the melting rate of the kiln can be significantly improved, and production efficiency and economic benefits can be improved. Specifically: by pre-installing multiple high-precision temperature sensors, the heating temperature in the kiln is monitored in real time, which not only ensures the accuracy of the temperature data, but also provides reliable data support for subsequent temperature control adjustments. By obtaining the kiln heating temperature in real time, the system can timely capture the changing trend of the kiln temperature and provide an accurate reference for subsequent temperature control; by analyzing the real-time kiln heating temperature data, the identification of each heating element is automatically identified, and the output power corresponding to each heating element is obtained, and fine control can be performed on different heating areas to ensure uniform temperature distribution of the entire kiln, thereby improving the melting effect; by presetting an idealized temperature curve, the real-time kiln heating temperature can be compared with the preset temperature curve to quickly identify the The deviation between the actual temperature and the ideal temperature is detected, and the output power of each heating element is adjusted accordingly, so that the furnace temperature is always in the optimal melting range, thereby effectively improving the melting rate; by pre-installing a pressure sensor, the pressure change inside the furnace is monitored in real time. According to the current pressure in the furnace, the appropriate air pressure adjustment instruction can be calculated to maintain the stability of the pressure inside the furnace, which not only avoids the uneven melting caused by pressure fluctuations, but also improves the operation stability of the furnace and extends the service life of the equipment; after completing the air pressure adjustment, the corresponding gas dynamic switching instruction will be generated to meet various needs in the glass preparation process. For example, during the reversing process, the system will adjust the natural gas, secondary air and kiln pressure in advance to ensure a smooth transition of various parameters and avoid interruptions in the melting process. This dynamic switching mechanism not only improves production efficiency, but also ensures the consistency of product quality. In summary, by adopting the above technical solution, it is possible to achieve all-round intelligent control of furnace temperature, air pressure and gas flow, significantly improve the melting rate of the furnace, optimize production efficiency, reduce energy consumption, and improve economic benefits.

[0007] In a preferred example, the present application can be further configured as follows: comparing the real-time heating temperature of the kiln with a preset temperature curve, adjusting the output power of each element according to the comparison result, and obtaining the kiln temperature control result, specifically including: Obtaining a furnace heating interval from the temperature curve, and obtaining a temperature median from the furnace heating interval; The median temperature and the kiln heating temperature are input into the following formula to obtain the kiln temperature control result: Among them, P(t) is the temperature control result of the kiln, K p , K i and K d are the corresponding proportional coefficient, integral coefficient and differential coefficient respectively, and the T set is the median temperature, and T(t) is the heating temperature of the kiln.

[0008] By adopting the above technical solution, the real-time kiln heating temperature is compared with the preset temperature curve, and the output power of each heating element is adjusted according to the comparison result, so that more precise and accurate temperature control can be achieved; first, the furnace heating range is extracted from the preset temperature curve, and the median temperature is obtained from it. This median temperature is used as a reference point for comparison with the real-time measured kiln heating temperature to evaluate whether the current kiln temperature state meets expectations. Next, the median temperature and the kiln heating temperature are input into a specific control algorithm formula. Through this formula, the output power of each heating element can be dynamically adjusted so that the kiln temperature can quickly and accurately return to the preset temperature curve, which not only improves the accuracy of temperature control, but also greatly reduces the energy waste caused by temperature fluctuations. Through automated temperature control strategies, the kiln temperature can be kept stable under various working conditions, thereby significantly improving the melting rate of the kiln. In addition, this technical solution can effectively extend the service life of the kiln. Frequent temperature fluctuations will accelerate the aging and damage of kiln materials, and through refined temperature control, this negative impact can be minimized. A stable temperature environment also helps to improve product quality, reduce the defective rate, and thus improve overall production efficiency and economic benefits.

[0009] In a preferred example, the present application can be further configured as follows: the current pressure in the furnace is obtained, and calculation is performed according to the current pressure in the furnace to obtain the furnace pressure adjustment instruction, specifically including: Obtain the preset furnace constant pressure data, input the current furnace pressure into the following formula to obtain the exhaust port opening adjustment target value: O(t)=H·(Y set -Y(t)), where (O(t) is the exhaust port opening adjustment target value, H is the preset gain coefficient, and Y set is the constant pressure data in the furnace, and Y(t) is the current pressure in the furnace; The current exhaust port opening data is obtained, and the furnace pressure adjustment instruction is calculated according to the current exhaust port opening data and the exhaust port opening adjustment target value.

[0010] By adopting the above technical solution, the melting rate of the kiln can be effectively improved and the stability of the internal pressure of the kiln can be maintained. Specifically: by obtaining the current pressure in the furnace and comparing it with the preset constant pressure data, the required exhaust port opening adjustment target value can be accurately calculated through the formula, and the change of the pressure in the furnace can be quickly responded to and the exhaust port opening can be adjusted in time to ensure that the internal pressure of the kiln is always maintained within the ideal range. This not only helps to maintain the stable operation of the kiln, but also effectively avoids melting interruptions caused by pressure fluctuations, further improving production continuity and product quality.

[0011] In a preferred example, the present application can be further configured as follows: after obtaining the furnace pressure adjustment result of the furnace pressure adjustment instruction, generating a furnace gas dynamic switching instruction according to the furnace pressure adjustment result to respond to the glass preparation instruction, specifically including: Acquire kiln fuel data, and calculate a preset nonlinear function according to the kiln fuel data, wherein the nonlinear function includes a natural gas consumption function and a secondary air content function; The current natural gas consumption and secondary air content are obtained, and the current natural gas consumption, the secondary air content and the nonlinear function are input into the following formula to obtain the target value of natural gas consumption and the target value of secondary air content: Q gas (t)=f(T(t),Y(t)),R air (t) = g(Q gas (t),T(t),Y(t)), where Q gas is the target value of natural gas consumption, R air is the secondary air content target value, f() is the natural gas consumption function, and g() is the secondary air content function; according to the difference between the natural gas consumption target value and the current natural gas consumption, and the difference between the secondary air content target value and the secondary air content, the dynamic switching instruction of the furnace gas is generated.

[0012] By adopting the above technical solution, the furnace heating temperature is obtained in real time and the output power of each heating element is adjusted according to the preset temperature curve, which can effectively maintain the furnace temperature within the ideal range, thereby improving the melting rate; at the same time, by obtaining the current furnace pressure in real time and calculating the furnace pressure adjustment instruction, and then adjusting the exhaust port opening, the internal pressure of the furnace can be maintained stable to avoid the melting process being affected by pressure fluctuations; on this basis, the furnace fuel data is further obtained, and the preset nonlinear function is calculated based on the furnace fuel data, and then the current natural gas consumption and secondary air content are obtained, and the current natural gas consumption, secondary air content and nonlinear function are input into the corresponding formula to calculate the natural gas consumption target value and secondary air content target value. This process makes full use of the current furnace pressure obtained when adjusting the exhaust port opening, and dynamically adjusts the natural gas consumption and secondary air content in combination with the actual situation of the kiln to ensure full combustion of the fuel, reduce heat energy waste, and further improve melting efficiency; finally, based on the difference between the natural gas consumption target value and the current natural gas consumption, as well as the difference between the secondary air content target value and the current secondary air content, a dynamic switching instruction for the gas in the furnace is generated to ensure a smooth transition of various parameters during the switching process, avoid interruptions in the melting process, and ensure continuous and efficient production. The above technical solution can not only achieve precise control of the kiln temperature, pressure and gas flow, but also can be flexibly adjusted under different working conditions, significantly improving the melting rate of the kiln, and improving production efficiency and economic benefits.

[0013] In a preferred example, the present application can be further configured as follows: the obtaining of the current natural gas consumption and secondary air content specifically includes: Acquire external humidity data, and compare the external humidity data with a preset humidity reference value to obtain humidity change conditions; When the humidity change exceeds a preset value, a ventilation adjustment instruction is triggered to obtain the current natural gas consumption and the secondary air content.

[0014] By adopting the above technical solution, in the specific steps of obtaining the current natural gas consumption and secondary air content, the monitoring and comparison of external humidity data are introduced, which can more accurately reflect the impact of actual environmental changes on the melting process of the kiln; through the integrated meteorological station or humidity sensor, the humidity data of the external environment is monitored in real time, which not only takes into account the temperature and pressure inside the kiln, but also extends to external environmental factors, making the entire control system more comprehensive and intelligent; by real-time monitoring of the external humidity, the possible impact of environmental changes on the melting process of the kiln can be discovered in time, so that measures can be taken in advance to make adjustments; after obtaining the external humidity data, it is compared with the preset humidity reference value to obtain the humidity change. When the humidity change exceeds the preset value, the ventilation adjustment instruction will be automatically triggered, and the current natural gas consumption and secondary air content will be recalculated to ensure that the two can still achieve the optimal combustion effect under the new humidity conditions, thereby ensuring the efficient operation of the kiln: after recalculating the target values ​​of natural gas consumption and secondary air content, the system will generate a dynamic switching instruction for the gas in the furnace according to the difference between these target values ​​and the current actual values. This instruction will guide the various components of the kiln (such as solenoid valves, fans, etc.) to make corresponding adjustments to ensure that the flow of natural gas and secondary air can quickly reach the new target value. Through this dynamic adjustment, the system can ensure that the kiln is always in the optimal combustion state under different humidity conditions, thereby ensuring the stability and improvement of the melting rate. In summary, by introducing the monitoring and comparison of external humidity data, the system can more accurately reflect the impact of external environmental changes on the melting process of the kiln, and by triggering ventilation adjustment instructions and recalculating natural gas consumption and secondary air content, ensure that the kiln can maintain an efficient operating state under various humidity conditions, significantly improving the melting rate and production efficiency of the kiln.

[0015] The second object of the invention is achieved by the following technical solutions: A control device for improving the melting rate of a kiln, the control device for improving the melting rate of a kiln comprising: The element power acquisition module is used to acquire the kiln heating temperature in real time, and acquire the heating element identification and the element output power corresponding to each heating element identification according to the kiln heating temperature; A temperature control and adjustment module is used to compare the real-time heating temperature of the kiln with a preset temperature curve, and adjust the output power of each element according to the comparison result to obtain the kiln temperature control result; A gas pressure regulating module, used to obtain the current pressure in the furnace, and to calculate according to the current pressure in the furnace to obtain a gas pressure regulating instruction in the furnace; The ventilation adjustment module is used to obtain the furnace pressure adjustment result of the furnace pressure adjustment instruction, and generate a furnace gas dynamic switching instruction according to the furnace pressure adjustment result to respond to the glass preparation instruction.

[0016] By adopting the above technical solution, the melting rate of the kiln can be significantly improved, and production efficiency and economic benefits can be improved. Specifically: by pre-installing multiple high-precision temperature sensors, the heating temperature in the kiln is monitored in real time, which not only ensures the accuracy of the temperature data, but also provides reliable data support for subsequent temperature control adjustments. By obtaining the kiln heating temperature in real time, the system can timely capture the changing trend of the kiln temperature and provide an accurate reference for subsequent temperature control; by analyzing the real-time kiln heating temperature data, the identification of each heating element is automatically identified, and the output power corresponding to each heating element is obtained, and fine control can be performed on different heating areas to ensure uniform temperature distribution of the entire kiln, thereby improving the melting effect; by presetting an idealized temperature curve, the real-time kiln heating temperature can be compared with the preset temperature curve to quickly identify the The deviation between the actual temperature and the ideal temperature is detected, and the output power of each heating element is adjusted accordingly, so that the furnace temperature is always in the optimal melting range, thereby effectively improving the melting rate; by pre-installing a pressure sensor, the pressure change inside the furnace is monitored in real time. According to the current pressure in the furnace, the appropriate air pressure adjustment instruction can be calculated to maintain the stability of the pressure inside the furnace, which not only avoids the uneven melting caused by pressure fluctuations, but also improves the operation stability of the furnace and extends the service life of the equipment; after completing the air pressure adjustment, the corresponding gas dynamic switching instruction will be generated to meet various needs in the glass preparation process. For example, during the reversing process, the system will adjust the natural gas, secondary air and kiln pressure in advance to ensure a smooth transition of various parameters and avoid interruptions in the melting process. This dynamic switching mechanism not only improves production efficiency, but also ensures the consistency of product quality. In summary, by adopting the above technical solution, it is possible to achieve all-round intelligent control of furnace temperature, air pressure and gas flow, significantly improve the melting rate of the furnace, optimize production efficiency, reduce energy consumption, and improve economic benefits.

[0017] The third objective of the present application is achieved through the following technical solutions: A computer device comprises a memory, a processor and a computer program stored in the memory and executable on the processor. When the processor executes the computer program, the steps of the control method for improving the melting rate of a kiln are implemented.

[0018] The fourth objective of the present application is achieved through the following technical solutions: A computer-readable storage medium stores a computer program, and when the computer program is executed by a processor, the steps of the control method for improving the melting rate of a kiln are implemented.

[0019] In summary, the present application includes at least one of the following beneficial technical effects: 1. By real-time monitoring of the kiln heating temperature and comparing it with the preset temperature curve, the output power of the heating element is automatically adjusted to keep the kiln temperature in the ideal range, effectively improving the melting rate, production efficiency and economic benefits.

[0020] 2. By real-time monitoring of the internal pressure of the kiln and automatically adjusting the opening of the exhaust port, the internal pressure of the kiln is maintained stable, avoiding uneven melting due to pressure fluctuations, and further improving melting efficiency and production stability.

[0021] 3. By automatically calculating and adjusting the natural gas consumption and secondary air ratio, it ensures a smooth transition of various parameters during the reversing process, avoids melting interruptions, and ensures a continuous and efficient production process. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] Figure 1 is a flow chart of a control method for improving the melting rate of a kiln in one embodiment of the present application; Figure 2 This is a flowchart of the implementation of step S20 of the control method for improving the melting rate of the kiln in one embodiment of the present application; Figure 3 This is a flowchart of the implementation of step S30 of the control method for improving the melting rate of the kiln in one embodiment of the present application; Figure 4 This is a flowchart of the implementation of step S40 of the control method for improving the melting rate of the kiln in one embodiment of the present application; Figure 5 This is a flowchart of the implementation of step S42 of the control method for improving the melting rate of the kiln in one embodiment of the present application; Figure 6 It is a principle block diagram of a control system for improving the melting rate of a kiln in one embodiment of the present application; Figure 7 It is a schematic diagram of a device in an embodiment of the present application. DETAILED DESCRIPTION

[0023] The present application is further described in detail below in conjunction with the accompanying drawings.

[0024] In one embodiment, if Figure 1 As shown, the present application discloses a control method for improving the melting rate of a kiln, which specifically includes the following steps: S10: Acquire the furnace heating temperature in real time, and acquire the heating element identification and the element output power corresponding to each heating element identification according to the furnace heating temperature.

[0025] In this embodiment, the kiln heating temperature refers to the current temperature inside the kiln when the kiln is in working state.

[0026] Specifically, by pre-installing a temperature sensor in the kiln, when the kiln is working, the temperature in the kiln is obtained in real time through the temperature sensor to obtain the heating temperature of the kiln. Furthermore, by pre-setting the working start-up sequence of the heating elements in the kiln, the corresponding number of heating elements are started in sequence according to the specific temperature required for heating. Therefore, after obtaining the real-time kiln heating temperature, the number of elements currently in operation is determined according to the temperature, and according to the start-up sequence of the heating elements, the heating element identification for that element and the output power corresponding to each heating software identification are obtained as the output power of the element.

[0027] S20: Compare the real-time kiln heating temperature with the preset temperature curve, adjust the output power of each component according to the comparison result, and obtain the kiln temperature control result.

[0028] Specifically, the temperature curve is set in advance based on the correlation between the yield rate of historically fired glass and the heating temperature, and is used as a benchmark for temperature control when the glass is subsequently fired in the kiln. Further, the real-time kiln heating temperature is compared with the temperature curve, and the output power adjustment amount of each element is calculated based on the comparison result, including the output power of the activated heating element, and the triggering of the start instruction to the unactivated heating element, so as to obtain the corresponding kiln temperature control result.

[0029] S30: Obtain the current pressure in the furnace, perform calculations based on the current pressure in the furnace, and obtain a furnace pressure adjustment instruction.

[0030] Specifically, after dynamically controlling and adjusting the temperature in the kiln, the air pressure sensor is used to obtain the air pressure data in the kiln through the pre-installed pressure sensor, which is used as the current pressure in the kiln. Based on the current pressure in the kiln, a preset formula is used to calculate the instructions for adjusting the current air pressure in the kiln, thereby controlling the air pressure conditions in the kiln for heating.

[0031] S40: after obtaining the furnace pressure regulation instruction and the furnace pressure regulation result, generate the furnace gas dynamic switching instruction according to the furnace pressure regulation result to respond to the glass preparation instruction.

[0032] Specifically, after calculating and adjusting the gas pressure in the furnace, the switching instructions for natural gas and secondary air are generated according to the current external heating environment, that is, the dynamic switching instructions for the gas in the furnace, so as to correspond to the glass preparation instructions, so that when the kiln is preparing glass, it can control the gas content to maximize combustion, save energy, and reduce the adverse effects of the external environment on combustion during ventilation.

[0033] In this embodiment, the melting rate of the kiln can be significantly improved, and production efficiency and economic benefits can be improved. Specifically: by pre-installing multiple high-precision temperature sensors, the heating temperature in the kiln is monitored in real time, which not only ensures the accuracy of the temperature data, but also provides reliable data support for subsequent temperature control adjustments. By obtaining the kiln heating temperature in real time, the system can timely capture the changing trend of the kiln temperature and provide an accurate reference for subsequent temperature control; by analyzing the real-time kiln heating temperature data, the identification of each heating element is automatically identified, and the output power corresponding to each heating element is obtained, and fine control can be performed for different heating areas to ensure that the temperature distribution of the entire kiln is uniform, thereby improving the melting effect; by presetting an idealized temperature curve, the comparison of the real-time kiln heating temperature with the preset temperature curve can quickly identify The deviation between the actual temperature and the ideal temperature is detected, and the output power of each heating element is adjusted accordingly, so that the kiln temperature is always in the optimal melting range, thereby effectively improving the melting rate; by pre-installing a pressure sensor, the pressure change inside the kiln is monitored in real time. According to the current pressure in the furnace, the appropriate air pressure adjustment instruction can be calculated to maintain the stability of the pressure inside the kiln, which not only avoids the uneven melting caused by pressure fluctuations, but also improves the operation stability of the kiln and extends the service life of the equipment; after completing the air pressure adjustment, the corresponding gas dynamic switching instruction will be generated to meet various needs in the glass preparation process. For example, during the switching process, the system will adjust the natural gas, secondary air and kiln pressure in advance to ensure a smooth transition of various parameters and avoid interruptions in the melting process. This dynamic switching mechanism not only improves production efficiency, but also ensures the consistency of product quality. In summary, by adopting the above technical solution, it is possible to achieve all-round intelligent control of kiln temperature, air pressure and gas flow, significantly improve the melting rate of the kiln, optimize production efficiency, reduce energy consumption, and improve economic benefits.

[0034] In one embodiment, if Figure 2 As shown, in step S20, the real-time kiln heating temperature is compared with the preset temperature curve, and the output power of each component is adjusted according to the comparison result to obtain the kiln temperature control result, which specifically includes: S21: Obtain the furnace heating interval from the temperature curve, and obtain the temperature median from the furnace heating interval.

[0035] Specifically, the maximum and minimum values ​​of the temperature are obtained from the temperature curve to form the furnace heating interval, and each point value in the temperature curve in the furnace heating interval is further obtained within the set of furnace heating intervals as the temperature median.

[0036] S22: Input the median temperature and the kiln heating temperature into the following formula to obtain the kiln temperature control result: Among them, P(t) is the kiln temperature control result, K p , K i and K d are the corresponding proportional coefficient, integral coefficient and differential coefficient respectively, T set is the median temperature, and T(t) is the kiln heating temperature.

[0037] Specifically, the median temperature and the current kiln heating temperature are input into the above formula for calculation, so that according to the temperature curve and the current kiln heating temperature, the output power of the heating element in order to maintain the temperature in the kiln within the furnace heating range is calculated as the kiln temperature control result.

[0038] In one embodiment, if Figure 3 As shown, in step S30, the current pressure in the furnace is obtained, and a calculation is performed according to the current pressure in the furnace to obtain a furnace pressure adjustment instruction, which specifically includes: S31: Obtain the preset furnace constant pressure data, input the current furnace pressure into the following formula, and obtain the exhaust port opening adjustment target value: O(t)=H·(Y set -Y(t)), where O(t) is the target value for adjusting the exhaust port opening, H is the preset gain coefficient, and Y set is the constant pressure data in the furnace, and Y(t) is the current pressure in the furnace.

[0039] In this embodiment, the exhaust port opening adjustment target value refers to an instruction for controlling the opening and closing degree of the kiln exhaust port.

[0040] Specifically, according to the actual situation of the kiln and the historical firing records, the constant pressure data in the kiln is preset. Further, in order to calculate the content of the gas in the kiln that needs to be adjusted, the degree to which the exhaust port needs to be opened and closed is calculated according to the displacement of the kiln exhaust port, that is, the exhaust port opening adjustment target value.

[0041] S32: Obtain current exhaust port opening data, and calculate the furnace pressure adjustment instruction based on the current exhaust port opening data and the exhaust port opening adjustment target value.

[0042] Specifically, the current opening and closing degree of the exhaust port, that is, the exhaust port opening data, is obtained, and based on the difference between the calculated exhaust port adjustment target values, the adjustment amount of the exhaust port opening is generated as the furnace gas pressure adjustment instruction.

[0043] In one embodiment, if Figure 4 As shown, in step S40, after obtaining the furnace pressure adjustment command and the furnace pressure adjustment result, a furnace gas dynamic switching command is generated according to the furnace pressure adjustment result to respond to the glass preparation command, specifically including: S41: Obtain kiln fuel data, and calculate a preset nonlinear function based on the kiln fuel data, wherein the nonlinear function includes a natural gas consumption function and a secondary air content function.

[0044] Specifically, the fuel currently used by the kiln is obtained from the relevant file data as the kiln fuel data. Furthermore, by analyzing the historical firing records in advance, the kiln fuel and the nonlinear function used to calculate the ratio between natural gas and secondary air, that is, the corresponding natural gas consumption function and secondary air content function, are obtained.

[0045] S42: Obtain the current natural gas consumption and secondary air content, input the current natural gas consumption, secondary air content and nonlinear function into the following formula to obtain the natural gas consumption target value and the secondary air content target value: Q gas (t)=f(T(t),Y(t)),R air (t) = g(Q gas (t),T(t),Y(t)), where Q gas is the target value of natural gas consumption, R air is the secondary air content target value, f() is the natural gas consumption function, and g() is the secondary air content function.

[0046] Specifically, after obtaining the natural gas consumption function and the secondary air content function, the amount of natural gas used per unit time and the secondary air content are obtained through corresponding sensors as the current natural gas consumption and secondary air content, and the current natural gas consumption, secondary air content and nonlinear function are input into the above formula, and the natural gas consumption target value and the secondary air content target value are calculated through the natural gas consumption function and the secondary air content function, respectively.

[0047] S43: Generate a dynamic switching instruction for the gas in the furnace according to the difference between the target value of natural gas consumption and the current natural gas consumption, and the difference between the target value of secondary air content and the secondary air content.

[0048] Specifically, the difference between the natural gas consumption and the current natural gas consumption, as well as the difference between the secondary air content target value and the secondary air content are calculated respectively, and then the dynamic switching instruction of the furnace gas is generated according to the difference to adjust the ratio between natural gas and secondary air during kiln combustion.

[0049] In one embodiment, if Figure 5 As shown, in step S42, the current natural gas consumption and secondary air content are obtained, which specifically includes: S421: Acquire external humidity data, and compare the external humidity data with a preset humidity reference value to obtain humidity change conditions.

[0050] Specifically, the maximum humidity that needs to be controlled during firing is obtained in advance according to the actual needs of the glass products to be fired, as the humidity reference value, and the external humidity data is obtained through the humidity sensor during the kiln firing process. The external humidity data is compared with the humidity reference value to compare the humidity changes.

[0051] S422: When the humidity change exceeds the preset value, the ventilation adjustment instruction is triggered to obtain the current natural gas consumption and secondary air content.

[0052] Specifically, when the humidity change exceeds the preset value, it means that the external humidity is too high. Therefore, in order to adjust the humidity in the kiln, the ventilation adjustment instruction is triggered, and the current natural gas consumption and secondary air content are obtained.

[0053] It should be understood that the size of the serial numbers of the steps in the above embodiments does not mean the order of execution. The execution order of each process should be determined by its function and internal logic, and should not constitute any limitation on the implementation process of the embodiments of the present application.

[0054] In one embodiment, a control device for improving the melting rate of a kiln is provided, and the control device for improving the melting rate of a kiln corresponds to the control method for improving the melting rate of a kiln in the above embodiment. Figure 6 As shown, the control device for improving the melting rate of the kiln includes a component power acquisition module, a temperature control module, a gas pressure control module and a ventilation control module. The detailed description of each functional module is as follows: The component power acquisition module is used to obtain the kiln heating temperature in real time, and obtain the heating element identification and the component output power corresponding to each heating element identification according to the kiln heating temperature; The temperature control and adjustment module is used to compare the real-time kiln heating temperature with the preset temperature curve, and adjust the output power of each component according to the comparison result to obtain the kiln temperature control result; The gas pressure regulating module is used to obtain the current pressure in the furnace, calculate according to the current pressure in the furnace, and obtain the gas pressure regulating instruction in the furnace; The ventilation adjustment module is used to obtain the furnace pressure adjustment instruction and the furnace pressure adjustment result, and generate the furnace gas dynamic switching instruction according to the furnace pressure adjustment result to respond to the glass preparation instruction.

[0055] Optionally, the temperature control module includes: The median acquisition submodule is used to obtain the furnace heating interval from the temperature curve and obtain the temperature median from the furnace heating interval; The temperature control calculation submodule is used to input the median temperature and the kiln heating temperature into the following formula to obtain the kiln temperature control result: Among them, P(t) is the kiln temperature control result, K p, K i and K d are the corresponding proportional coefficient, integral coefficient and differential coefficient respectively, T set is the median temperature, and T(t) is the kiln heating temperature.

[0056] Optional, gas pressure regulating module includes: The exhaust port control submodule is used to obtain the preset furnace constant pressure data, input the current furnace pressure into the following formula, and obtain the exhaust port opening adjustment target value: O(t)=H·(Y set -Y(t)), where (O(t) is the target value for adjusting the exhaust port opening, H is the preset gain coefficient, and Y set is the constant pressure data in the furnace, and Y(t) is the current pressure in the furnace; The gas pressure regulating submodule is used to obtain the current exhaust port opening data, and calculate the furnace gas pressure regulating instruction according to the current exhaust port opening data and the exhaust port opening regulating target value.

[0057] Optionally, the ventilation regulation module includes: The function acquisition submodule is used to acquire kiln fuel data and calculate a preset nonlinear function based on the kiln fuel data, wherein the nonlinear function includes a natural gas consumption function and a secondary air content function; The air volume calculation submodule is used to obtain the current natural gas consumption and secondary air content. The current natural gas consumption, secondary air content and nonlinear function are input into the following formula to obtain the target value of natural gas consumption and secondary air content: Q gas (t)=f(T(t),Y(t)),R air (t) = g(Q gas (t),T(t),Y(t)), where Q gas is the target value of natural gas consumption, R air is the secondary air content target value, f() is the natural gas consumption function, and g() is the secondary air content function; The ventilation regulation submodule is used to generate a dynamic switching instruction for the gas in the furnace according to the difference between the target value of natural gas consumption and the current natural gas consumption, and the difference between the target value of secondary air content and the secondary air content.

[0058] Optionally, the air volume calculation submodule includes: The humidity judgment unit is used to obtain external humidity data, and compare the external humidity data with a preset humidity reference value to obtain humidity change conditions; The gas acquisition unit is used to trigger the ventilation adjustment instruction when the humidity change exceeds the preset value to obtain the current natural gas consumption and secondary air content.

[0059] The specific definition of the control device for improving the melting rate of the kiln can refer to the definition of the control method for improving the melting rate of the kiln above, which will not be repeated here. Each module in the above-mentioned control device for improving the melting rate of the kiln can be implemented in whole or in part by software, hardware and a combination thereof. The above-mentioned modules can be embedded in or independent of the processor in the computer device in the form of hardware, or can be stored in the memory of the computer device in the form of software, so that the processor can call and execute the operations corresponding to the above modules.

[0060] In one embodiment, a computer device is provided. The computer device may be a server, and its internal structure diagram may be as follows: Figure 7 As shown. The computer device includes a processor, a memory, a network interface and a database connected through a system bus. Among them, the processor of the computer device is used to provide computing and control capabilities. The memory of the computer device includes a non-volatile storage medium and an internal memory. The non-volatile storage medium stores an operating system, a computer program and a database. The internal memory provides an environment for the operation of the operating system and the computer program in the non-volatile storage medium. The network interface of the computer device is used to communicate with an external terminal through a network connection. When the computer program is executed by the processor, a control method for improving the melting rate of a kiln is implemented.

[0061] In one embodiment, a computer device is provided, including a memory, a processor, and a computer program stored in the memory and executable on the processor, wherein the processor implements the following steps when executing the computer program: Obtain the furnace heating temperature in real time, and obtain the heating element identification and the element output power corresponding to each heating element identification according to the furnace heating temperature; Compare the real-time kiln heating temperature with the preset temperature curve, adjust the output power of each component according to the comparison result, and obtain the kiln temperature control result; Obtain the current pressure in the furnace, perform calculations based on the current pressure in the furnace, and obtain the furnace pressure adjustment instruction; After obtaining the furnace pressure regulation result, a furnace gas dynamic switching instruction is generated according to the furnace pressure regulation result to respond to the glass preparation instruction.

[0062] In one embodiment, a computer readable storage medium is provided, on which a computer program is stored, and when the computer program is executed by a processor, the following steps are implemented: Obtain the furnace heating temperature in real time, and obtain the heating element identification and the element output power corresponding to each heating element identification according to the furnace heating temperature; Compare the real-time kiln heating temperature with the preset temperature curve, adjust the output power of each component according to the comparison result, and obtain the kiln temperature control result; Obtain the current pressure in the furnace, perform calculations based on the current pressure in the furnace, and obtain the furnace pressure adjustment instruction; After obtaining the furnace pressure regulation result, a furnace gas dynamic switching instruction is generated according to the furnace pressure regulation result to respond to the glass preparation instruction.

[0063] Those skilled in the art can understand that all or part of the processes in the above-mentioned embodiment methods can be completed by instructing the relevant hardware through a computer program, and the computer program can be stored in a non-volatile computer-readable storage medium. When the computer program is executed, it can include the processes of the embodiments of the above-mentioned methods. Among them, any reference to memory, storage, database or other media used in the embodiments provided in this application can include non-volatile and / or volatile memory. Non-volatile memory can include read-only memory (ROM), programmable ROM (PROM), electrically programmable ROM (EPROM), electrically erasable programmable ROM (EEPROM) or flash memory. Volatile memory can include random access memory (RAM) or external cache memory. As an illustration and not limitation, RAM is available in many forms, such as static RAM (SRAM), dynamic RAM (DRAM), synchronous DRAM (SDRAM), double data rate SDRAM (DDRSDRAM), enhanced SDRAM (ESDRAM), synchronous link (Synchlink) DRAM (SLDRAM), memory bus (Rambus) direct RAM (RDRAM), direct memory bus dynamic RAM (DRDRAM), and memory bus dynamic RAM (RDRAM).

[0064] Those skilled in the art can clearly understand that for the convenience and simplicity of description, only the division of the above-mentioned functional units and modules is used as an example. In actual applications, the above-mentioned functions can be distributed and completed by different functional units and modules as needed, that is, the internal structure of the device can be divided into different functional units or modules to complete all or part of the functions described above.

[0065] The embodiments described above are only used to illustrate the technical solutions of the present application, rather than to limit them. Although the present application has been described in detail with reference to the aforementioned embodiments, a person skilled in the art should understand that the technical solutions described in the aforementioned embodiments may still be modified, or some of the technical features may be replaced by equivalents. Such modifications or replacements do not deviate the essence of the corresponding technical solutions from the spirit and scope of the technical solutions of the embodiments of the present application, and should all be included in the protection scope of the present application.

Claims

1. A control method for improving the melting rate of a kiln, characterized in that: The control method for improving the melting rate of the kiln includes: obtaining the heating temperature of the kiln in real time, and obtaining the heating element identification and the element output power corresponding to each heating element identification according to the heating temperature of the kiln; Compare the real-time heating temperature of the kiln with the preset temperature curve, and adjust the output power of each element according to the comparison result to obtain the kiln temperature control result; Obtaining the current pressure in the furnace, and performing calculations based on the current pressure in the furnace to obtain a furnace pressure adjustment instruction; After obtaining the furnace pressure regulation result of the furnace pressure regulation instruction, a furnace gas dynamic switching instruction is generated according to the furnace pressure regulation result to respond to the glass preparation instruction.

2. The control method for improving the melting rate of a kiln according to claim 1, characterized in that: The real-time kiln heating temperature is compared with a preset temperature curve, and the output power of each element is adjusted according to the comparison result to obtain the kiln temperature control result, which specifically includes: Obtaining a furnace heating interval from the temperature curve, and obtaining a temperature median from the furnace heating interval; The median temperature and the kiln heating temperature are input into the following formula to obtain the kiln temperature control result: Among them, P(t) is the temperature control result of the kiln, K p , K i and K d are the corresponding proportional coefficient, integral coefficient and differential coefficient respectively, and the T set is the median temperature, and T(t) is the heating temperature of the kiln.

3. The control method for improving the melting rate of a kiln according to claim 1, characterized in that: The obtaining of the current pressure in the furnace and the calculation based on the current pressure in the furnace to obtain the furnace pressure adjustment instruction specifically include: Obtain the preset furnace constant pressure data, input the current furnace pressure into the following formula to obtain the exhaust port opening adjustment target value: O(t)=H·(Y set -Y(t)), where (O(t) is the exhaust port opening adjustment target value, H is the preset gain coefficient, and Y set is the constant pressure data in the furnace, and Y(t) is the current pressure in the furnace; The current exhaust port opening data is obtained, and the furnace pressure adjustment instruction is calculated according to the current exhaust port opening data and the exhaust port opening adjustment target value.

4. The control method for improving the melting rate of a kiln according to claim 3, characterized in that: The step of obtaining the furnace pressure adjustment result of the furnace pressure adjustment instruction and generating a furnace gas dynamic switching instruction according to the furnace pressure adjustment result to respond to the glass preparation instruction specifically includes: Acquire kiln fuel data, and calculate a preset nonlinear function according to the kiln fuel data, wherein the nonlinear function includes a natural gas consumption function and a secondary air content function; The current natural gas consumption and secondary air content are obtained, and the current natural gas consumption, the secondary air content and the nonlinear function are input into the following formula to obtain the target value of natural gas consumption and the target value of secondary air content: Q gas (t)=f(T(t),Y(t)),R air (t) = g(Q gas (t),T(t),Y(t)), where Q gas is the target value of natural gas consumption, R air is the secondary air content target value, f() is the natural gas consumption function, and g() is the secondary air content function; The furnace gas dynamic switching instruction is generated according to the difference between the natural gas consumption target value and the current natural gas consumption, and the difference between the secondary air content target value and the secondary air content.

5. The control method for improving the melting rate of a kiln according to claim 4, characterized in that: The obtaining of the current natural gas consumption and secondary air content specifically includes: Acquire external humidity data, and compare the external humidity data with a preset humidity reference value to obtain humidity change conditions; When the humidity change exceeds a preset value, a ventilation adjustment instruction is triggered to obtain the current natural gas consumption and the secondary air content.

6. A control device for improving the melting rate of a kiln, characterized in that: The control device for improving the melting rate of the kiln includes: an element power acquisition module, which is used to acquire the heating temperature of the kiln in real time, and acquire the heating element identification and the element output power corresponding to each heating element identification according to the heating temperature of the kiln; A temperature control and adjustment module is used to compare the real-time heating temperature of the kiln with a preset temperature curve, and adjust the output power of each element according to the comparison result to obtain the kiln temperature control result; A gas pressure regulating module, used to obtain the current pressure in the furnace, and to calculate according to the current pressure in the furnace to obtain a gas pressure regulating instruction in the furnace; The ventilation adjustment module is used to obtain the furnace pressure adjustment result of the furnace pressure adjustment instruction, and generate a furnace gas dynamic switching instruction according to the furnace pressure adjustment result to respond to the glass preparation instruction.

7. The control device for improving the melting rate of a kiln according to claim 6, characterized in that: The temperature control and regulation module comprises: A median acquisition submodule, used to acquire a furnace heating interval from the temperature curve, and acquire a temperature median from the furnace heating interval; The temperature control calculation submodule is used to input the median temperature and the kiln heating temperature into the following formula to obtain the kiln temperature control result: Among them, P(t) is the temperature control result of the kiln, K p , K i and K d are the corresponding proportional coefficient, integral coefficient and differential coefficient respectively, and the T set is the median temperature, and T(t) is the heating temperature of the kiln.

8. The control device for improving the melting rate of a kiln according to claim 6, characterized in that: The air pressure regulating module comprises: The exhaust port control submodule is used to obtain the preset furnace constant pressure data, input the current furnace pressure into the following formula, and obtain the exhaust port opening adjustment target value: O(t)=H·(Y set -Y(t)), where (O(t) is the exhaust port opening adjustment target value, H is the preset gain coefficient, and Y set is the constant pressure data in the furnace, and Y(t) is the current pressure in the furnace; The gas pressure regulating submodule is used to obtain the current exhaust port opening data, and calculate the furnace gas pressure regulating instruction according to the current exhaust port opening data and the exhaust port opening regulating target value.

9. A computer device comprising a memory, a processor, and a computer program stored in the memory and executable on the processor, characterized in that: When the processor executes the computer program, the steps of the control method for improving the melting rate of the kiln as claimed in any one of claims 1 to 5 are implemented.

10. A computer-readable storage medium storing a computer program, characterized in that: When the computer program is executed by a processor, the steps of the control method for improving the melting rate of a kiln are implemented as claimed in any one of claims 1 to 5.

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