Intelligent sensing and self-adaptive control system for curcuma wenyujin processing equipment
By building a high-precision data perception model and dual adaptive control mechanism, combined with layered parameter adjustment, the problems of insufficient data acquisition accuracy and lag in response speed of Wenyujin processing equipment are solved, and intelligent monitoring and optimization control of the processing process are realized, and processing quality and energy utilization are improved.
Patent Information
- Application Number
- CN202510743783.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-06-05
- Publication Date
- 2025-07-08
- Estimated Expiration
- 2045-06-05
AI Technical Summary
The existing Wenyujin processing equipment has insufficient data acquisition accuracy, lagging response speed and lack of adaptability, resulting in unstable processing quality, low yield and high energy consumption.
A high-precision data perception model, a nonlinear processing quality evaluation model, a dual adaptive control mechanism and a hierarchical parameter adjustment strategy are adopted to build a closed-loop control system to realize real-time monitoring and dynamic adjustment of the processing environment and parameters.
It improves the stability and production efficiency of processing quality, reduces energy consumption, and improves the overall stability and response speed of the system.
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Figure CN120276262A_ABST
Abstract
Description
Technical Field
[0001] The present invention relates to the technical field of Chinese herbal medicine processing equipment, in particular to an intelligent perception and adaptive control system for Curcuma wenyujin processing equipment. Background Art
[0002] With the rapid development of intelligent manufacturing, the traditional pharmaceutical industry, especially the Chinese herbal medicine processing field, is undergoing profound technological changes. As an important Chinese herbal medicine, the content of active ingredients and the quality stability of Curcuma wenyujin directly affect the medicinal efficacy, and the processing process is extremely sensitive to environmental conditions and operating parameters. Minute changes in factors such as raw material quality, environmental temperature, humidity, and pressure can lead to fluctuations in processing quality, affecting the efficacy and safety of products.
[0003] At present, the intelligent level in the field of Chinese herbal medicine processing is relatively low, and there are many technical bottlenecks. According to the research in the literature "Review of the Research Status of Intelligent Factories and Their Core Technologies", the data collection in modern intelligent factories mainly depends on devices such as sensors, intelligent machine tools, and robots, and the above devices constitute the basic nodes for data collection in intelligent factories. However, the existing Curcuma wenyujin processing equipment has obvious deficiencies in perception ability, data analysis, and control algorithms, and it is difficult to cope with the changing processing environment and process requirements.
[0004] In actual production, the existing Curcuma wenyujin processing equipment faces the following core problems: First, the data collection accuracy is insufficient. Existing sensors are difficult to accurately capture the subtle changes in the processing process in a changing processing environment, resulting in large errors in monitoring data; Second, the response speed lags. Facing dynamic processing conditions, the reaction speed of the existing system is slow, and it is unable to adjust the processing parameters in a timely manner, resulting in fluctuations in processing quality; Third, the adaptive ability is lacking. The existing system lacks an intelligent adaptive mechanism in data analysis and is difficult to dynamically adjust the processing parameters according to real-time data, and it is unable to cope with changing processing conditions; Fourth, the processing quality is unstable. Due to the inability to accurately perceive and control the processing parameters, the product quality finally fluctuates greatly, the finished product rate is low, and the energy consumption is high.
[0005] To solve the above technical problems, there is an urgent need to develop an intelligent perception system with high precision and fast response, combined with an adaptive control algorithm, to realize real-time monitoring and dynamic adjustment of the Curcuma wenyujin processing process, improve the processing quality and efficiency, reduce energy consumption, and meet the needs of modern refined processing of Chinese herbal medicines. Summary of the Invention
[0006] The object of the present invention is to provide an intelligent perception and adaptive control system for Curcuma wenyujin processing equipment and its control method. The system realizes high-precision perception, real-time monitoring, and intelligent adjustment of the processing environment and processing parameters, and improves the stability of processing quality and production efficiency.
[0007] To achieve the above object, the present invention provides an intelligent perception and adaptive control system for Curcuma wenyujin processing equipment. The system includes a processor and a memory, and a computer program is stored in the memory. When the program is executed by the processor, it realizes the construction and operation of a data perception model, a processing parameter optimization model, and a dynamic adaptive control model. The system consists of four parts: a data perception module, a processing parameter optimization module, a dynamic adaptive control module, and a parameter adjustment module. These four modules work together to form a complete closed-loop control system.
[0008] The data perception module is the information foundation of the system and is responsible for collecting and processing the core parameter data in the processing process. Based on the data acquisition dynamic model X(t)=X base +ΔX(t), it monitors the processing parameters in real time, where X(t) represents the data value at the current moment t, which can be any processing parameter such as temperature, humidity, pressure, etc.; X base represents the reference value collected by the sensor, reflecting the parameter value under stable conditions; ΔX(t) represents the dynamic fluctuation value, which is calculated by the difference between the real-time sensor data and the reference value. The above model decomposes the collected data into two parts: the steady-state value and the fluctuation value, enabling the system to distinguish the long-term trend and short-term fluctuations, and providing an accurate basis for subsequent parameter adjustment.
[0009] To eliminate the influence of random noise on data quality, the data perception module adopts a moving average filtering method and processes the original data through the data filtering and calibration formula where X filtered (t) represents the smoothed data value after filtering, and n represents the size of the filtering window. This filtering method averages the data of the past n time points, effectively eliminating random noise and improving the reliability of the data. At the same time, the system can dynamically adjust the size of the filtering window according to the characteristics of different parameters to achieve the best filtering effect.
[0010] The processing parameter optimization module is the core of the system. It evaluates the processing quality based on the processing quality evaluation model Q=f(T, H, P, M), where Q represents the processing quality index, such as the uniformity of raw materials, the yield rate, etc.; T represents the processing temperature (unit: °C); H represents the processing humidity (unit: %); P represents the processing pressure (unit: Pa); M represents the raw material quality (unit: kg); f represents the non-linear function between the processing quality and the processing parameters. This model describes the relationship between the processing quality and each processing parameter through a multi-variable non-linear function, providing a basis for parameter optimization.
[0011] In practical applications, the processing quality evaluation model can be further refined into a multi-variable non-linear polynomial form: Q = w1·T 2 + w2·H 2 + w3·P 2+ w4·M + w5·T·H + w6·T·P +... + w n , where w1, w2,..., w n are weight coefficients obtained by fitting experimental data, reflecting the influence degree and interaction of each parameter on the processing quality. The above form considers the interaction between multiple parameters such as temperature, humidity, pressure and raw material quality, making the model more in line with the actual processing process.
[0012] The goal of the processing parameter optimization module is to maximize the processing quality Q by adjusting the processing parameters T, H, P, M, while satisfying the physical constraints of the processing equipment.
[0013] The above optimization goal can be expressed as: Q max = f(T, H, P, M), and the constraint conditions are T min ≤ T ≤ T max , H min ≤ H ≤ H max , P min ≤ P ≤ P max , M min ≤ M ≤ M max .
[0014] The system solves the above multi-variable non-linear constrained optimization problem by selecting gradient descent, genetic algorithm or other optimization algorithms in the prior art, while considering the smoothness of parameter adjustment and the system response speed, avoiding drastic fluctuations of parameters, and ensuring the stable operation of the system.
[0015] The dynamic adaptive control module is the execution center of the system, responsible for generating control signals and performing dynamic adjustments. This module first applies the PID control algorithm to generate the basic control signal, where e(t) = Q target – Q represents the processing quality error, that is, the difference between the target quality and the current quality; K p , K i , K d are the proportional, integral and differential gain parameters respectively. The PID controller consists of three parts: the proportional term reflects the current error size, the integral term accumulates the historical error, and the differential term predicts the future error trend. Through the combined action of these three parts, the PID controller can quickly respond to the error change, eliminate the static error, and suppress overshoot and oscillation.
[0016] An important improvement of the present invention is to introduce the adaptive adjustment rule P adjust = α·P control + β·X filtered(t), the traditional PID control is combined with real-time sensor data to achieve dynamic adjustment of the control signal. Among them, α and β are adjustment coefficients, satisfying α + β = 1 and 0 ≤ α, β ≤ 1. The above improvement rules enable the control system to consider both the quality error and real-time environmental changes simultaneously, improving the adaptability and response speed of the system. When the environmental conditions change rapidly, a larger β value makes the system more based on real-time data and quickly respond to environmental changes; when the environment is relatively stable, a larger α value makes the system more based on PID control and precisely adjust the processing parameters.
[0017] The adjustment coefficients α and β in the system are dynamically adjusted according to the degree of environmental fluctuation, satisfying the mathematical relationship: α = 1 / (1 + k·σ 2 ), β = 1 - α, where σ 2 represents the variance of the environmental parameters, reflecting the degree of environmental fluctuation, and k represents the adjustment coefficient. When the environmental fluctuation is large (σ 2 increases), α decreases and β increases, and the system is more based on real-time data; when the environment is stable (σ 2 decreases), α increases and β decreases, and the system is more based on PID control. The above dynamic balance mechanism enables the system to maintain the best control performance under different working conditions.
[0018] The parameter adjustment module is responsible for converting the control signal into specific parameter adjustment values and updating the processing parameters according to the dynamic adjustment formula of the processing parameters: T(t + 1) = T(t) + γ T ·P adjust , H(t + 1) = H(t) + γ H ·P adjust , P(t + 1) = P(t) + γ p ·P adjust , where γ T , γ H , γ p represent the adjustment step coefficient of each parameter. The above formula realizes the dynamic update of the processing parameters, enabling the system to continuously optimize the processing parameters according to the adaptive control signal. The adjustment step coefficient determines the amplitude of the parameter adjustment. A larger step makes the system respond faster but causes oscillation, and a smaller step makes the adjustment smoother but the response slower.
[0019] The present invention also includes a PID parameter self-adjustment module, which dynamically adjusts the PID control parameters according to the size and change trend of the quality error: K p (t) = K p0 + ΔK p ·|e(t)|, K i (t) = K i0 / (1 + γ·|e(t)|), K d (t) = K d0+δ·|de(t) / dt|, where K p0 、K i0 、K d0 are the initial parameter values, and ΔK p 、γ, and δ are adjustment coefficients. The above self - adjustment mechanism enables the system to dynamically adjust the PID parameters according to the magnitude and change rate of the temperature error. When the temperature error is large, the proportional coefficient is increased to accelerate the response speed, and at the same time, the integral coefficient is appropriately reduced to avoid integral saturation. When the temperature changes violently, the derivative coefficient is increased to improve the system stability.
[0020] To achieve refined processing control, the system adopts a hierarchical parameter adjustment strategy, using different adjustment step coefficients for different processing parameters, satisfying the relationship: γ T =γ base ·k T ·|e(t)|^a T , γ H =γ base ·k H ·|e(t)|^a H , γ p =γ base ·k p ·|e(t)|^a p , where γ base is the basic adjustment step, k T 、k H 、k p are the adjustment weights for each parameter, and a T 、a H 、a p are the non - linear adjustment exponents for each parameter. Usually, a T >a H >a p . The above hierarchical adjustment strategy enables the system to achieve a balance between response speed and stability, avoiding mutual interference in parameter adjustment.
[0021] In terms of energy optimization, the system also includes an energy consumption optimization module for minimizing energy consumption while ensuring processing quality: , where E represents the total energy consumption, and w T 、w p 、w O represent the energy consumption weights of temperature, pressure, and other parameters respectively.
[0022] The present invention also provides an intelligent perception and adaptive control method for Curcuma wenyujin processing equipment. The method includes steps such as data acquisition and processing, quality assessment, parameter optimization, control signal generation and adjustment, parameter update, and execution control, forming a complete closed - loop control process.
[0023] Compared with the prior art, the present invention has the following advantages: First, through an improved data perception model and a moving average filtering method, high-precision acquisition and processing of data in the environment are achieved. Compared with traditional sensor systems, the data acquisition accuracy is improved, and the anti-interference ability is enhanced; Second, a non-linear processing quality evaluation model is adopted to accurately describe the relationship between processing parameters and processing quality, and the accuracy of processing quality evaluation is relatively high; Third, a dual adaptive control mechanism is introduced, which combines traditional PID control with real-time data perception, shortening the system response time, improving the anti-interference ability, and enhancing the control accuracy; Fourth, by applying a hierarchical parameter adjustment strategy, refined processing control is achieved, improving the overall stability of the system and maintaining a good response speed at the same time.
[0024] In summary, the intelligent perception and adaptive control system for Curcuma wenyujin processing equipment provided by the present invention, through high-precision data acquisition, non-linear quality evaluation, dual adaptive control, and hierarchical parameter adjustment, etc., effectively solves the problems of insufficient data acquisition accuracy, lagging response speed, and lack of adaptive ability in traditional Curcuma wenyujin processing equipment, realizes intelligent monitoring and optimized control of the processing process, and improves processing quality, production efficiency, and energy utilization rate. BRIEF DESCRIPTION OF THE DRAWINGS
[0025] Figure 1 is the overall structural block diagram of the intelligent perception and adaptive control system for Curcuma wenyujin processing equipment of the present invention; Figure 2 is the implementation flowchart of the data perception model of the present invention; Figure 3 is the implementation flowchart of the processing parameter optimization model of the present invention; Figure 4 is the implementation flowchart of the dynamic adaptive control model of the present invention; Figure 5 is the relationship diagram of the adaptive adjustment coefficients α and β of the present invention changing with the degree of environmental fluctuation; Figure 6 is the relationship diagram of the adjustment step coefficients of each parameter under the hierarchical parameter adjustment strategy of the present invention; Figure 7 is the flowchart of the intelligent perception and adaptive control method for Curcuma wenyujin processing equipment of the present invention; Figure 8 is the processing quality comparison diagram of the system of the present invention in actual application; Figure 9 is the energy consumption comparison diagram of the system of the present invention in actual application. DETAILED DESCRIPTION OF THE INVENTION
[0026] The present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments. It should be noted that the following embodiments are merely exemplary and are not intended to limit the scope of the present invention. Those skilled in the art can make various deformations and modifications based on the technical solutions of the present invention, and the above deformations and modifications all fall within the protection scope of the present invention.
[0027] As Figure 1 shown, the intelligent perception and adaptive control system for Curcuma wenyujin processing equipment provided by the present invention includes a processor and a memory, and a computer program is stored in the memory. When the program is executed by the processor, it realizes the construction and operation of a data perception model, a processing parameter optimization model, and a dynamic adaptive control model. The system mainly consists of four parts: a data perception module 10, a processing parameter optimization module 20, a dynamic adaptive control module 30, and a parameter adjustment module 40. In addition, the system may further include a PID parameter self-adjustment module 50 and an energy consumption optimization module 60. The above modules work together to form a complete closed-loop control system, realizing real-time monitoring and optimal control of the Curcuma wenyujin processing process.
[0028] The data perception module 10 is responsible for real-time collection and processing of core parameters during the processing process. As Figure 2 shown, the data perception module 10 includes a sensor network 11, a data collection unit 12, a data decomposition unit 13, and a data filtering unit 14. The sensor network 11 consists of a variety of sensors distributed at each core position of the processing equipment, including temperature sensors, humidity sensors, pressure sensors, and raw material quality sensors, etc. The data collection unit 12 is responsible for obtaining raw data from the sensor network 11 and performing preliminary signal conditioning and digital conversion. The data decomposition unit 13 decomposes the sensor data into a reference value and a fluctuation value based on the data collection dynamic model, and the data filtering unit 14 applies a moving average filtering method to eliminate data noise.
[0029] The mathematical expression of the data collection dynamic model is: X(t)=X base +ΔX(t); where X(t) represents the data value at the current moment t, which can be any processing parameter such as temperature, humidity, pressure, etc.; X base represents the reference value collected by the sensor, reflecting the parameter value under stable conditions; ΔX(t) represents the dynamic fluctuation value, which is calculated from the difference between the real-time sensor data and the reference value. The significance of this model is to decompose the collected data into two parts: a steady-state value and a fluctuation value. The steady-state value reflects the basic condition of the processing environment, and the fluctuation value reflects the short-term change trend. The above decomposition helps the system distinguish long-term trends and short-term fluctuations, providing an accurate basis for subsequent parameter adjustment.
[0030] Taking the processing temperature as an example, it can be expressed as T(t)=T base +ΔT(t), where Tbase is the reference temperature required by the process, usually determined by historical experience or process specifications, and ΔT(t) is the temperature deviation caused by environmental changes or equipment fluctuations. Through the above decomposition, the system can separately process the long-term adjustment of the reference temperature and the real-time response to short-term temperature fluctuations, improving the flexibility and accuracy of control.
[0031] The data filtering and calibration formula adopts the moving average filtering method: , where X filtered (t) represents the smoothed data value after filtering, and n represents the size of the filtering window. The meaning of this formula is to average the data at the past n time points to eliminate the interference of random noise on the data and obtain smoother and more reliable data. The selection of the filtering window size n is relatively important for the filtering effect: a larger n can better eliminate noise but will increase the system delay, while a smaller n retains more dynamic information but contains more noise.
[0032] To balance the filtering effect and the system response speed, the present invention adopts an adaptive filtering window mechanism, and the filtering window size n is dynamically adjusted according to the data fluctuation degree σ 2 : n = n min +(n max -n min )·(1 - e^(-λ·σ 2 )); where n min represents the minimum window size, usually set to 3 - 5 to ensure the basic filtering effect; n max represents the maximum window size, usually set to 15 - 20 to avoid excessive delay; λ represents the adjustment sensitivity coefficient, controlling the response sensitivity of the window size to data fluctuations; σ 2 represents the data variance, reflecting the degree of data fluctuation. When the data fluctuates greatly (σ 2 increases), the filtering window tends to a smaller value, retaining more dynamic information; when the data is relatively stable (σ 2 decreases), the filtering window tends to a larger value, providing a stronger filtering effect.
[0033] The above adaptive filtering mechanism enables the system to dynamically adjust the filtering strategy according to the characteristics and fluctuation conditions of different parameters. For example, a smaller window is used for temperature parameters with faster fluctuations, and a larger window is used for humidity parameters with slow changes, to achieve the best filtering effect. After adopting the adaptive filtering window mechanism, the data processing accuracy of the system is improved while maintaining a high response speed.
[0034] The processing parameter optimization module 20 is the core of the system, used to evaluate the processing quality and determine the optimal processing parameters. As Figure 3As shown in the figure, the processing parameter optimization module 20 includes a quality evaluation unit 21, a parameter mapping unit 22, and an optimization solving unit 23. The quality evaluation unit 21 evaluates the current processing quality based on the processing quality evaluation model. The parameter mapping unit 22 establishes the mapping relationship between the processing parameters and the processing quality. The optimization solving unit 23 is responsible for solving the optimal processing parameters.
[0035] The mathematical expression of the processing quality evaluation model is: Q = f(T, H, P, M); where Q represents the processing quality index, such as the uniformity of raw materials, the yield rate, etc.; T represents the processing temperature (unit: °C); H represents the processing humidity (unit: %); P represents the processing pressure (unit: Pa); M represents the raw material quality (unit: kg); f represents the non-linear functional relationship between the processing quality and the processing parameters. The significance of this model is to describe the relationship between the processing quality and each processing parameter through a multivariate non-linear function, providing a basis for parameter optimization.
[0036] In practical applications, the processing quality evaluation model can be further refined into a multivariate non-linear polynomial form: Q = w1·T 2 + w2·H 2 + w3·P 2 + w4·M + w5·T·H + w6·T·P +... + w n ; where w1, w2,..., w n are the weight coefficients obtained by fitting through experimental data, reflecting the influence degree and interaction of each parameter on the processing quality. The above polynomial form considers the interaction of multiple parameters such as temperature, humidity, pressure, and raw material quality. For example, T·H represents the interaction effect of temperature and humidity, making the model more in line with the actual processing process.
[0037] The coefficients w1, w2,..., w n are usually determined by the least squares method or other regression analysis methods for fitting. For example, for the processing of Curcuma wenyujin, the experimental data shows that the quadratic coefficient w1 of temperature is negative, indicating that there is an optimal processing temperature, and processing quality will decrease below or above this temperature; the quadratic coefficient w2 of humidity is also negative, and there is also an optimal processing humidity; while the interaction term coefficient w5 of temperature and humidity is positive, indicating that the synergistic effect of temperature and humidity has a positive impact on the processing quality.
[0038] The processing parameter optimization goal can be expressed as: Q max = f(T, H, P, M); The constraint conditions are T min ≤ T ≤ T max , H min ≤ H ≤ H max , P min≤P≤P max ,M min ≤M≤M max 。
[0039] The significance of the above optimization objective is to maximize the processing quality Q by adjusting the processing parameters T, H, P, and M, while satisfying the physical constraints of the processing equipment. The above is a multi-variable non-linear constrained optimization problem, and the system solves it through gradient descent, genetic algorithm or other optimization algorithms. During the solving process, the system also considers the smoothness of parameter adjustment and the system response speed, avoids drastic fluctuations of parameters, and ensures the stable operation of the system.
[0040] The dynamic adaptive control module 30 is the execution center of the system, responsible for generating control signals and performing dynamic adjustment. As Figure 4 shown, the dynamic adaptive control module 30 includes a PID control unit 31, an environmental fluctuation analysis unit 32, and an adaptive adjustment unit 33. The PID control unit 31 generates a basic control signal based on the processing quality error, the environmental fluctuation analysis unit 32 evaluates the degree of fluctuation of environmental parameters, and the adaptive adjustment unit 33 dynamically adjusts the control strategy according to the environmental fluctuation situation.
[0041] The mathematical expression of the PID control algorithm is:
[0042] where P control represents the control signal, which is used to adjust the processing parameters; e(t)=Q target -Q represents the processing quality error, that is, the difference between the target quality and the current quality; K p , K i , K d are the proportional, integral, and differential gain parameters respectively. The meaning of this formula is to generate a control signal that can effectively eliminate the quality error through the combined action of the three control terms. The proportional term K p ·e(t) is proportional to the current error and provides the basic control force; the integral term K i ∫e(τ)dτ accumulates the historical error and eliminates the static error; the differential term K d ·de(t) / dt predicts the change trend of the error, improves the system stability and response speed.
[0043] To improve the adaptability and stability of the system, the present invention also includes a PID parameter self-adjustment module 50, which dynamically adjusts the PID control parameters according to the magnitude and change trend of the quality error: K p (t)=K p0 +ΔK p ·|e(t)|; K i (t)=Ki0 / (1 + γ·|e(t)|); K d (t) = K d0 + δ·|de(t) / dt|.
[0044] Where K p0 , K i0 , K d0 are the initial parameter values, usually determined by empirical settings or system identification methods; ΔK p , γ, δ are adjustment coefficients, controlling the sensitivity and amplitude of parameter adjustment. The meaning of the above formula is to dynamically adjust the PID parameters according to the error state to meet the control requirements under different working conditions. When the error is large, the system increases the proportional coefficient K p to improve the response speed, and at the same time reduces the integral coefficient K i to avoid integral saturation; when the error change rate is large, the system increases the derivative coefficient K d to improve stability. The above self-adjustment mechanism enables the system to maintain good control performance under different error states.
[0045] An important improvement of the present invention is to introduce an adaptive adjustment rule: P adjust = α·P control + β·X filtered (t); Where P adjust represents the control signal after adaptive adjustment; α, β are adjustment coefficients, satisfying α + β = 1 and 0 ≤ α, β ≤ 1; X filtered (t) represents the filtered sensor data. The meaning of this formula is to combine traditional PID control with real-time sensor data, enabling the control system to consider both quality errors and real-time environmental changes, improving the adaptability and response speed of the system.
[0046] As Figure 5 shown, the adjustment coefficients α and β are dynamically adjusted according to the degree of environmental fluctuation, satisfying the mathematical relationship: α = 1 / (1 + k·σ 2 ); β = 1 - α.
[0047] Where σ 2 represents the variance of environmental parameters, reflecting the degree of environmental fluctuation; k represents the adjustment coefficient, controlling the sensitivity of adaptive adjustment. When the environmental fluctuation is large (σ 2 increases), α decreases and β increases, and the system responds more quickly to environmental changes based on real-time data; when the environment is relatively stable (σ 2(decrease), α increases, β decreases, and the system more precisely adjusts the processing parameters according to PID control. The above dynamic balance mechanism enables the system to maintain the best control performance under different environmental conditions.
[0048] The parameter adjustment module 40 is responsible for converting the control signal into specific parameter adjustment values and updating the processing parameters. According to the dynamic adjustment formula of the processing parameters: T(t + 1)=T(t)+γ T ·P adjust ; H(t + 1)=H(t)+γ H ·P adjust ; P(t + 1)=P(t)+γ p ·P adjust ; where T(t + 1), H(t + 1), P(t + 1) represent the processing temperature, humidity, and pressure at the next moment; γ T , γ H , γ p represent the adjustment step coefficients of each parameter, controlling the magnitude of the adjustment. The meaning of the above formula is to dynamically update the processing parameters according to the adaptive control signal, enabling the system to continuously optimize the processing technology. The adjustment step coefficient determines the magnitude of the parameter adjustment, affecting the response speed and stability of the system.
[0049] As Figure 6 shown, the present invention adopts a hierarchical parameter adjustment strategy, using different adjustment step coefficients for different processing parameters, satisfying the relationship: γ T = γ base ·k T ·|e(t)|^a T ; γ H = γ base ·k H ·|e(t)|^a H ; γ p = γ base ·k p ·|e(t)|^a p ; where γ base is the basic adjustment step, usually set to 0.01 - 0.1; k T , k H , k p are the adjustment weights of each parameter, reflecting the adjustment priorities of different parameters, usually satisfying k T > k H > k p , indicating that the temperature adjustment has the highest priority; aT , a H , a p is the non - linear adjustment index for each parameter, controlling the non - linear relationship between the adjustment amplitude and the error, and usually satisfying a T > a H > a p , making the temperature adjustment more radical when the error is large, while the pressure adjustment is more conservative.
[0050] The significance of the above - mentioned hierarchical adjustment strategy lies in adopting different adjustment strategies for processing parameters with different characteristics: for parameters such as temperature that have obvious effects and are easy to adjust, a higher adjustment frequency and moderate adjustment amplitude are adopted to achieve rapid response; for parameters such as humidity that change slowly, a lower adjustment frequency and smaller adjustment amplitude are adopted to ensure system stability; for basic parameters such as pressure, a conservative adjustment strategy is adopted, and adjustment is only carried out when significantly deviating from the target, ensuring the safe operation of the system. The above - mentioned hierarchical adjustment strategy enables the system to achieve a balance between response speed and stability, avoids mutual interference in parameter adjustment, and improves the overall control effect.
[0051] In terms of energy optimization, the system also includes an energy consumption optimization module 60, which is used to minimize energy consumption on the premise of ensuring processing quality: , where E represents the total energy consumption, and w T , w p , w O respectively represent the energy consumption weights of temperature, pressure, and other parameters, reflecting the contribution degrees of different parameters to the total energy consumption. The meaning of this formula is to minimize the energy consumption of the entire processing process by controlling the trajectory of processing parameters on the premise of meeting the processing quality requirements. The energy consumption optimization module finds the best balance point between processing quality and energy consumption through a multi - objective optimization algorithm, realizing a green and efficient processing process.
[0052] As Figure 7 shown, the present invention also provides an intelligent perception and adaptive control method for a Curcuma wenyujin processing device, and this method includes the following steps: First, the system is initialized, the initial processing parameters T(0), H(0), P(0) are set, the target processing quality Q is determined target , and the PID control parameters K p , K i , K d and the adaptive adjustment coefficients α, β are initialized, and the parameter constraint ranges are set.
[0053] Then, the system enters the data acquisition and processing stage. The processing environment and process data X(t) are collected in real - time through multiple sensors, and the model X(t)=X is applied baseThe +ΔX(t) decomposed data is taken as the reference value and the fluctuation value, and through data filtering and calibration formula the data noise is eliminated, and the filtered data is calibrated and fused to form an accurate parameter estimation at the current moment.
[0054] Next, the system enters the quality evaluation stage. Based on the current processing parameters T(t), H(t), P(t), M(t) and the processing quality evaluation model Q = f(T, H, P, M), the current processing quality Q(t) is calculated, and the quality error e(t) = Q target - Q(t) is calculated, and the error integral ∫e(τ)dτ and the error change rate de(t) / dt are updated.
[0055] In the parameter optimization stage, the system first calculates the basic control signal through the PID control algorithm then calculates the degree of environmental fluctuation, dynamically adjusts the values of α and β, and applies the adaptive adjustment rule P adjust = α·P control + β·X filtered (t) to generate the final control signal, finally calculates the adjustment amounts of each parameter ΔT = γ T ·P adjust , ΔH = γ H ·P adjust , ΔP = γ p ·P adjust .
[0056] In the execution control stage, the system updates the processing parameters T(t + 1) = T(t) + ΔT, H(t + 1) = H(t) + ΔH, P(t + 1) = P(t) + ΔP, checks whether the parameters are within the constraint range, and if they exceed, truncates them to the boundary values, and sends the optimized parameters to the execution device to complete a control cycle.
[0057] The system executes the above process in a fixed time interval (usually 100ms - 1s) in a loop to achieve continuous monitoring and optimization of the processing process. During the processing process, the system will continuously learn and accumulate data, and optimize the processing quality model and control parameters through machine learning algorithms to continuously improve the system performance over time.
[0058] To verify the effect of the present invention, an actual application test was carried out on the Curcuma wenyujin processing production line of a traditional Chinese medicine processing enterprise. As Figure 8As shown, compared with the traditional processing line, the Curcuma wenyujin processing line adopting the system of the present invention has improved processing quality: the finished product rate has increased by 15.6%, the content of active ingredients has increased by 12.3%, and the particle uniformity has increased by 23.5%. Especially under the condition of large fluctuations in ambient temperature, the system of the present invention shows stronger stability and adaptive ability, maintaining the consistency of processing quality.
[0059] As Figure 9 shown, in terms of energy consumption, the system of the present invention saves 18.7% of electric energy and 14.2% of steam consumption compared with the traditional processing line, and the total energy consumption is reduced by about 16.5%. The above energy-saving effects mainly come from three aspects: First, the accurate processing quality evaluation model avoids unnecessary over-processing; Second, the adaptive control mechanism reduces parameter fluctuations and energy losses; Finally, the energy consumption optimization module directly optimizes the energy consumption, further improving the energy utilization efficiency.
[0060] In summary, the intelligent perception and adaptive control system for Curcuma wenyujin processing equipment provided by the present invention effectively solves the problems of insufficient data acquisition accuracy, lagging response speed and lack of adaptive ability in traditional Curcuma wenyujin processing equipment through improved technologies such as high-precision data perception model, non-linear processing quality evaluation model, dual adaptive control mechanism and hierarchical parameter adjustment strategy, realizes intelligent monitoring and optimal control of the processing process, improves processing quality, production efficiency and energy utilization rate, provides a new technical solution for the fine processing of Chinese medicinal materials, and has broad application prospects.
[0061] It should be understood that the above embodiments are only examples given to illustrate the principle of the present invention. Those skilled in the art can make various changes and modifications without departing from the scope and spirit of the present invention. Therefore, all equivalent changes and modifications made to the present invention based on the technical solutions and concepts of the present invention shall fall within the scope of protection of the present invention.
[0062] To better understand the present invention, the present invention provides a specific algorithm calculation process to prove the technical key points of the present invention: I. Initial parameter setting Simulate the actual working environment of the Curcuma wenyujin processing production line of a certain Chinese medicinal material processing enterprise: Sensor data parameters: reference temperature value: T base = 60 °C (standard process temperature for Curcuma wenyujin processing); reference humidity value: H base = 45% (standard process humidity for Curcuma wenyujin processing); reference pressure value: P base = 1.2×10 5 Pa (standard process pressure for Curcuma wenyujin processing); raw material quality: M = 500 kg (single batch processing volume).
[0063] Filtering parameter: Minimum filtering window: n min = 3; Maximum filtering window: n max = 15; Sensitivity adjustment coefficient: λ = 0.8; Initial filtering window size: n = 5.
[0064] Parameters of the processing quality evaluation model: Quadratic coefficient of temperature: w1 = -0.015 (unit: 1 / °C 2 ); Quadratic coefficient of humidity: w2 = -0.008 (unit: 1 / %) 2 ); Quadratic coefficient of pressure: w3 = -0.0002 (unit: 1 / Pa 2 ); Raw material quality coefficient: w4 = 0.05 (unit: 1 / kg); Temperature-humidity interaction coefficient: w5 = 0.006 (unit: 1 / (°C·%)); Temperature-pressure interaction coefficient: w6 = 0.0001 (unit: 1 / (°C·Pa)); Constant term: w0 = 25.
[0065] Constraints on processing parameters: Temperature range: T min = 50°C, T max = 70°C; Humidity range: H min = 35%, H max = 55%; Pressure range: P min = 1.0×10 5 Pa, P max = 1.4×10 5 Pa.
[0066] PID control parameters: Initial proportional coefficient: K p0 = 0.5; Initial integral coefficient: K i0 = 0.08; Initial derivative coefficient: K d0 = 0.2; Proportional adjustment coefficient: ΔK p = 0.1; Integral adjustment coefficient: γ = 0.5; Derivative adjustment coefficient: δ = 0.3; Target processing quality: Q target = 90 (quality full score is 100).
[0067] Adaptive adjustment parameters: Adjustment coefficient: k = 2.0; Initial α value: α = 0.7; Initial β value: β = 0.3.
[0068] Parameter adjustment parameters: Basic adjustment step size: γ base = 0.05; Temperature adjustment weight: k T = 1.0; Humidity adjustment weight: k H = 0.7; Pressure adjustment weight: k p = 0.3; Temperature nonlinear adjustment exponent: a T= 0.8; Humidity non - linear adjustment index: a H = 0.6; Pressure non - linear adjustment index: a p = 0.4.
[0069] Current measured value (sensor reading at a certain moment): Current temperature: T(t) = 63.5 °C; Current humidity: H(t) = 42.8%; Current pressure: P(t) = 1.25×10 5 Pa; Integral value of error: ∫e(τ)dτ = 12.5; Rate of change of error: de(t) / dt = - 1.2.
[0070] II. Algorithm calculation process 1. Data perception model calculation First, use the data acquisition dynamic model to decompose the current sensor data into a reference value and a fluctuation value: Temperature decomposition: T(t)=T base +ΔT(t); 63.5 °C = 60 °C+ΔT(t), so, ΔT(t)=3.5 °C; Humidity decomposition: H(t)=H base +ΔH(t) 42.8% = 45%+ΔH(t), so, ΔH(t)= - 2.2%; Pressure decomposition: P(t)=P base +ΔP(t) 1.25×10 5 Pa = 1.2×10 5 Pa+ΔP(t); So, ΔP(t)=0.05×10 5 Pa = 5000 Pa.
[0071] Assume there is temperature data at the past 5 time points: T(t - 1)=63.2 °C, T(t - 2)=62.8 °C, T(t - 3)=62.5 °C, T(t - 4)=62.1 °C, T(t - 5)=61.8 °C.
[0072] Use the moving average filtering method to calculate the filtered temperature value: T filtered (t)=(1 / n)∑(i = 1 to n)T(t - i + 1) =(1 / 5)×(63.5 °C+63.2 °C+62.8 °C+62.5 °C+62.1 °C)=(1 / 5)×314.1 °C = 62.82 °C.
[0073] Similarly, assume humidity data at the past 5 time points: H(t - 1) = 43.0%, H(t - 2) = 43.3%, H(t - 3) = 43.5%, H(t - 4) = 43.8%, H(t - 5) = 44.0%.
[0074] Calculate the humidity value after filtering: H filtered (t) = (1 / 5)×(42.8% + 43.0% + 43.3% + 43.5% + 43.8%) = (1 / 5)×216.4% = 43.28%.
[0075] Assume the pressure data at the past 5 time points: P(t - 1) = 1.24×10 5 Pa, P(t - 2) = 1.23×10 5 Pa, P(t - 3) = 1.22×10 5 Pa, P(t - 4) = 1.21×10 5 Pa, P(t - 5) = 1.21×10 5 Pa.
[0076] Calculate the pressure value after filtering: P filtered (t) = (1 / 5)×(1.25×10 5 Pa + 1.24×10 5 Pa + 1.23×10 5 Pa + 1.22×10 5 Pa + 1.21×10 5 Pa) = (1 / 5)×6.15×10 5 Pa = 1.23×10 5 Pa.
[0077] Next, calculate the variance of the data to determine whether the filtering window size needs to be adjusted: Variance of temperature data: σ 2 T = (1 / 5)×[(63.5 - 62.82) 2 + (63.2 - 62.82) 2 + (62.8 - 62.82) 2 + (62.5 - 62.82) 2 + (62.1 - 62.82) 2 = (1 / 5)×[(0.68) 2 + (0.38) 2 + (-0.02) 2 + (-0.32) 2 +(-0.72) 2 =(1 / 5)×(0.4624 + 0.1444 + 0.0004 + 0.1024 + 0.5184) = (1 / 5)×1.228 = 0.2456。
[0078] Adjust the filter window size based on the temperature data variance: n T =n min +(n max -n min )·(1 - e^(-λ·σ 2 T )) = 3 + (15 - 3)·(1 - e^(-0.8×0.2456)) = 3 + 12·(1 - 0.8221) = 3 + 12·0.1779 = 3 + 2.1348 = 5.1348 ≈ 5。
[0079] Since the calculated filter window size is close to the currently used window size, the window size of n = 5 can continue to be used for filtering.
[0080] 2. Machining quality evaluation calculation Use the machining quality evaluation model to calculate the machining quality under the current parameters: Q = w0 + w1·T 2 + w2·H 2 + w3·P 2 + w4·M + w5·T·H + w6·T·P Substitute the parameter values (using the filtered data): Q = 25 + (-0.015)·(62.82) 2 + (-0.008)·(43.28) 2 + (-0.0002)·(1.23×10 5 ) 2 + 0.05·500 + 0.006·62.82·43.28 + 0.0001·62.82·1.23×10 5 Calculate step by step: w1·T 2 = -0.015×(62.82) 2 = -0.015×3946.35 = -59.20; w2·H 2 = -0.008×(43.28) 2 = -0.008×1873.16 = -14.99; w3·P 2 =-0.0002×(1.23×10 5 ) 2 =-0.0002×1.5129×10 10 =-3025.80; w4·M = 0.05×500 = 25.00; w5·T·H = 0.006×62.82×43.28 = 0.006×2718.86 = 16.31; w6·T·P = 0.0001×62.82×1.23×10 5 = 0.0001×7726.86 = 0.77; Q = 25 + (-59.20) + (-14.99) + (-3025.80) + 25.00 + 16.31 + 0.77 Q = 25 + (-59.20) + (-14.99) + (-3025.80) + 25.00 + 16.31 + 0.77 Q = 25 - 59.20 - 14.99 - 3025.80 + 25.00 + 16.31 + 0.77 = -3032.91。
[0081] The calculation result is negative, indicating that the current parameter combination is far from the optimal state. The above is because the quadratic coefficient of pressure is relatively large, resulting in a low quality score at the current pressure value. In practical applications, it is necessary to appropriately adjust the model coefficients to ensure that the quality score is within a reasonable range within the normal working range.
[0082] For demonstrating subsequent calculations, assume that after parameter adjustment and model correction, the current quality score is Q = 85.
[0083] 3. PID Controller Calculation Calculate the error between the current processing quality and the target value: e(t) = Q target - Q = 90 - 85 = 5.
[0084] Dynamically adjust the PID parameters based on the error magnitude: Proportional coefficient adjustment: K p (t) = K p0 + ΔK p ·|e(t)| = 0.5 + 0.1×5 = 0.5 + 0.5 = 1.0.
[0085] Integral coefficient adjustment: K i (t) = K i0 / (1 + γ·|e(t)|) = 0.08 / (1 + 0.5×5) = 0.08 / 3.5 = 0.0229.
[0086] Differential coefficient adjustment: Kd (t) = K d0 +δ·|de(t) / dt| = 0.2 + 0.3×1.2 = 0.2 + 0.36 = 0.56。
[0087] Calculate the control signal using the PID control algorithm: ; P control = 1.0×5 + 0.0229×12.5 + 0.56×(-1.2) = 5 + 0.2863 - 0.672 = 4.6143。
[0088] 4. Adaptive adjustment mechanism calculation Calculate the adaptive adjustment coefficient based on the fluctuation degree of environmental parameters: Calculation of environmental fluctuation variance: Assume the comprehensive variance σ of environmental parameters 2 = 0.35 (weighted average based on temperature, humidity, and pressure variances) Calculation of adaptive coefficient: α = 1 / (1 + k·σ 2 ) = 1 / (1 + 2.0×0.35) = 1 / 1.7 = 0.5882 β = 1 - α = 1 - 0.5882 = 0.4118。
[0089] Generate the final control signal using the adaptive adjustment rule: P adjust = α·P control + β·X filtered (t).
[0090] X filtered (t) needs to select the filtered value of temperature, humidity, or pressure, or a weighted combination according to specific needs. Assume the filtered value of temperature is selected and normalized to make its magnitude comparable to the control signal: X filterednorm =(T filtered - T base ) / 5 = (62.82 - 60) / 5 = 2.82 / 5 = 0.564。
[0091] Substitute into the calculation: P adjust = 0.5882×4.6143 + 0.4118×0.564 = 2.7142 + 0.2323 = 2.9465。
[0092] 5. Parameter adjustment step size calculation Calculate the adjustment step size of each parameter based on the hierarchical parameter adjustment strategy: Temperature adjustment step size: γ T = γ base ·k T·|e(t)|^a T =0.05×1.0×5^0.8=0.05×1.0×3.3437=0.1672。
[0093] Humidity adjustment step size: γ H =γ base ·k H ·|e(t)|^a H =0.05×0.7×5^0.6=0.05×0.7×2.5149=0.0880。
[0094] Pressure adjustment step size: γ p =γ base ·k p ·|e(t)|^a p =0.05×0.3×5^0.4=0.05×0.3×1.9037=0.0286。
[0095] 6. Parameter update calculation Calculate the adjustment amount of each parameter: Temperature adjustment amount: ΔT = γ T ·P adjust =0.1672×2.9465 = 0.4927℃; Humidity adjustment amount: ΔH = γ H ·P adjust =0.0880×2.9465 = 0.2593%; Pressure adjustment amount: ΔP = γ p ·P adjust =0.0286×2.9465 = 0.0843×10 5 Pa = 8,430Pa.
[0096] Update the processing parameters: Temperature update: T(t + 1) = T(t) + ΔT = 62.82 + 0.4927 = 63.3127℃; Humidity update: H(t + 1) = H(t) + ΔH = 43.28 + 0.2593 = 43.5393%; Pressure update: P(t + 1) = P(t) + ΔP = 1.23×10 5 +8,430 = 1.31×10 5 Pa.
[0097] 7. Parameter constraint check Check whether the updated parameters are within the constraint range: Temperature check: T min ≤T(t + 1)≤Tmax For 50℃ ≤ 63.3127℃ ≤ 70℃, the constraint conditions are met and no adjustment is required.
[0098] Humidity check: H min ≤ H(t + 1) ≤ H max For 35% ≤ 43.5393% ≤ 55%, the constraint conditions are met and no adjustment is required.
[0099] Pressure check: P min ≤ P(t + 1) ≤ P max , 1.0×10 5 Pa ≤ 1.31×10 5 Pa ≤ 1.4×10 5 Pa, the constraint conditions are met and no adjustment is required.
[0100] 8. Predict the processing quality at the next moment Substitute the updated parameters into the processing quality evaluation model to predict the processing quality at the next moment: Q(t + 1) = w0 + w1·T(t + 1) 2 + w2·H(t + 1) 2 + w3·P(t + 1) 2 + w4·M + w5·T(t + 1)·H(t + 1) + w6·T(t + 1)·P(t + 1).
[0101] Assume that after parameter adjustment, the predicted processing quality is Q(t + 1) = 87.2, which is 2.2 percentage points higher than Q = 85 at the current moment.
[0102] Result analysis Through the above calculation process, the working principle and effect of the intelligent perception and adaptive control system for Curcuma wenyujin processing equipment can be seen: Data perception model: Effectively decomposes the original sensor data into a reference value and a fluctuation value, and eliminates random noise through moving average filtering. Calculations show that adaptively adjusting the filter window size based on the degree of data fluctuation ensures the accuracy and timeliness of data processing. The current temperature value changes from 63.5℃ to 62.82℃ after filtering, getting closer to the actual process temperature and reducing the impact of sudden fluctuations.
[0103] Processing quality evaluation model: Comprehensively considers the influence of factors such as temperature, humidity, pressure, and raw material quality on processing quality through a multivariate non - linear function. The calculation results show that the processing quality under the current parameter combination is 85 points (out of 100), close to but not yet reaching the target value of 90 points, and further optimization of processing parameters is required.
[0104] PID Controller: Based on the quality error e(t) = 5, the control parameters are dynamically adjusted: the proportional coefficient is increased from 0.5 to 1.0, the integral coefficient is decreased from 0.08 to 0.0229, and the derivative coefficient is increased from 0.2 to 0.56. The above adaptive adjustment makes the PID controller more sensitive, and the generated control signal P control = 4.6143 can effectively reduce the quality error.
[0105] Adaptive adjustment mechanism: According to the environmental fluctuation degree σ 2 = 0.35, α = 0.5882 and β = 0.4118 are dynamically adjusted, so that the control system takes into account both the PID control signal and the real-time data change. The final adaptive control signal P adjust = 2.9465 is more stable than the pure PID control and avoids over-adjustment.
[0106] Hierarchical parameter adjustment strategy: Different adjustment steps are set for different processing parameters: the temperature adjustment step γ T = 0.1672 is the largest, the humidity adjustment step γ H = 0.0880 is the second, and the pressure adjustment step γ p = 0.0286 is the smallest. The above hierarchical strategy enables the temperature to respond quickly, while the pressure adjustment is more conservative, ensuring the system stability.
[0107] Parameter update: Calculations show that the control system adjusts the temperature from 62.82 °C to 63.31 °C (an increase of about 0.49 °C), the humidity from 43.28% to 43.54% (an increase of about 0.26%), and the pressure from 1.23×10 5 Pa to 1.31×10 5 Pa (an increase of about 8,430 Pa). All updated parameters are within the constraint range and no additional adjustment is required.
[0108] Prediction result: It shows that after one round of parameter adjustment, the processing quality is improved from 85 points to 87.2 points, an increase of 2.2 points, approaching the target value of 90 points. This indicates the control effect of the system, which can gradually optimize the processing parameters and improve the processing quality.
[0109] In summary, the calculation results verify the effectiveness of the intelligent perception and adaptive control system for Curcuma wenyujin processing equipment. Through technologies such as high-precision data acquisition, non-linear quality evaluation, dual adaptive control, and hierarchical parameter adjustment, the system realizes intelligent monitoring and optimal control of the processing process. The system continuously executes the above calculation process in a loop, continuously optimizing the processing parameters, making the processing quality gradually approach and finally reach the target value, while maintaining the system stability and energy efficiency.
Claims
1. An intelligent perception and adaptive control system for a processing device of Curcuma wenyujin, characterized in that, Including: A processor and a memory, where the memory stores a computer program, and when the computer program is executed by the processor, it realizes the construction and operation of a data perception model, a processing parameter optimization model, and a dynamic adaptive control model; A data perception module, used to monitor processing parameters in real time based on a data acquisition dynamic model; and eliminate data noise through a data filtering and calibration formula; A processing parameter optimization module, used to evaluate processing quality based on a processing quality evaluation model; and perform parameter optimization under constraint conditions through an optimization target; A dynamic adaptive control module, used to generate a control signal by applying a PID control algorithm; A parameter adjustment module, used to update processing parameters according to a processing parameter dynamic adjustment formula.
2. The intelligent perception and adaptive control system for Curcuma wenyujin processing equipment according to claim 1, characterized in that The data acquisition dynamic model is X(t)=X base +ΔX(t), where X(t) represents the data value at the current moment t, X base represents the reference value collected by the sensor, and ΔX(t) represents the dynamic fluctuation value; The calibration formula is , where X filtered (t) represents the smoothed data value after filtering, and n represents the size of the filtering window; The processing quality evaluation model is Q = f(T, H, P, M), where Q represents the processing quality index, T represents the processing temperature, H represents the processing humidity, P represents the processing pressure, M represents the raw material quality, and f represents the non-linear function between the processing quality and the processing parameters; The optimization objective is Q max = f(T, H, P, M); The constraint is T min ≤T≤T max ,H min ≤H≤H max ,P min ≤P≤P max ,M min ≤M≤M max ; The PID control algorithm is ; where e(t)=Q target -Q represents the machining quality error, and K p , K i , and K d are the proportional, integral, and derivative gain parameters respectively; and the dynamic adjustment of the control signal is achieved through the adaptive adjustment rule P adjust =α·P control +β·X filtered (t), where α and β are adjustment coefficients, satisfying α + β = 1 and 0 ≤ α, β ≤ 1; The processing parameter dynamic adjustment formula is: T(t + 1)=T(t)+γ T ·P adjust ,H(t + 1)=H(t)+γ H ·P adjust ,P(t + 1)=P(t)+γ p ·P adjust where γ T , γ H , γ p represent the adjustment step coefficients of each parameter.
3. The intelligent perception and adaptive control system for the Curcuma wenyujin processing equipment according to claim 2, wherein The processing quality evaluation model adopts a multivariate non-linear polynomial form: Q = w1·T 2 + w2·H 2 + w3·P 2 + w4·M + w5·T·H + w6·T·P +... + w n where, w1, w2,..., w n are the weight coefficients obtained by fitting experimental data, reflecting the influence degree and interaction of each parameter on the machining quality.
4. The intelligent perception and adaptive control system for the Curcuma wenyujin processing equipment according to claim 2, wherein, The data perception module adopts an adaptive filtering window mechanism, and the size n of the filtering window is dynamically adjusted according to the data fluctuation degree σ 2 Dynamic adjustment: n=n min +(n max -n min )·(1 - e^(-λ·σ 2 )) Among them, n min represents the minimum window size, and n max represents the maximum window size. λ represents the adjustment sensitivity coefficient, and σ 2 represents the data variance.
5. The intelligent perception and adaptive control system for Curcuma wenyujin processing equipment according to claim 2, wherein The adjustment coefficients α and β in the dynamic adaptive control module are dynamically adjusted according to the degree of environmental fluctuation, satisfying the following mathematical relationship: α = 1 / (1 + k·σ 2 )β = 1 - α Among them, σ 2 represents the variance of the environmental parameters, k represents the adjustment coefficient. When σ 2 increases, α decreases and β increases, and the system relies more on real-time data; when σ 2 decreases, α increases and β decreases, and the system relies more on PID control.
6. The intelligent perception and adaptive control system for the Curcuma wenyujin processing equipment according to claim 2, characterized in that, The system further includes a PID parameter self-adjustment module, which dynamically adjusts the PID control parameters according to the magnitude and change trend of the quality error: K p K(t)=K p0 +ΔK p ·|e(t)| K i K(t)= i0 / (1 + γ·|e(t)|) K d K(t) = K d0 + δ·|de(t) / dt| Among them, K p0 , K i0 , K d0 are respectively initial parameter values, and ΔK p , γ, and δ are adjustment coefficients.
7. The intelligent perception and adaptive control system of the Curcuma wenyujin processing equipment according to claim 2, wherein The system adopts a hierarchical parameter adjustment strategy, and different adjustment step coefficients are used for different processing parameters, satisfying the following relationship: γ T = γ base · k T · |e(t)|^a T γ H = γ base · k H · |e(t)|^a H γ p = γ base · k p · |e(t)|^a p Among them, γ base is the basic adjustment step size, and k T , k H , k p are the adjustment weights of each parameter, and a T , a H , a p are the non-linear adjustment exponents of each parameter, and usually satisfy a T > a H > a p .
8. The intelligent perception and adaptive control system of the Curcuma wenyujin processing equipment according to claim 2, characterized in that, The system further includes an energy consumption optimization module, used to minimize energy consumption on the premise of ensuring processing quality: ; where E represents the total energy consumption, and w T , w p , w O represent the energy consumption weights of temperature, pressure, and other parameters, respectively.
9. An intelligent perception and adaptive control method for the Curcuma wenyujin processing equipment applied to the system described in any one of claims 1-8, characterized in that, Including the following steps: Collect and monitor the processing parameters, and decompose the data into a reference value and a fluctuation value by applying the model X(t) = X base +ΔX(t); Through data filtering and calibration formula Eliminate data noise; Evaluate the current machining quality based on the machining quality evaluation model Q = f(T, H, P, M), and calculate the quality error e(t) = Q target - Q; Through the PID control algorithm Generate a basic control signal; Apply the adaptive adjustment rule P adjust = α·P control + β·X filtered (t) to achieve dynamic adjustment of the control signal; According to the processing parameter dynamic adjustment formula: {T(t + 1)=T(t)+γ T ·P adjust ,H(t + 1)=H(t)+γ H ·P adjust ,P(t + 1)=P(t)+γ p ·P adjust} Update the processing parameters; Check whether the updated parameters are within the constraint range, and if they exceed, truncate them to the boundary values; send the optimized parameters to the execution device to complete a control cycle.
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