A dynamic regulation method of microwave sterilization system based on distributed photovoltaic driving

CN122526017APending Publication Date: 2026-08-07CHENGJUN TECHNOLOGY (BEIJING) CO LTD
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Patent Information

Application Number
CN202610389428.2
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2026-03-27
Publication Date
2026-08-07

AI Technical Summary

Technical Problem

第一,能源消耗与碳排放问题

Benefits of technology

[0011] The beneficial effects of this invention are as follows: by acquiring the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system, and dynamically calculating the target operating parameters, including the target microwave power and/or the target material processing time, based on the real-time power generation and the preset sterilization energy requirements, and then adjusting the current operating parameters, including the current microwave power and/or the current material processing time, based on the target operating parameters, the microwave energy input to the material by the microwave sterilization system per unit time is matched with the real-time power of the photovoltaic power generation, thereby achieving a dynamic balance between the energy consumption and photovoltaic output of the microwave sterilization system, maximizing the absorption of green electricity while ensuring the stability and effectiveness of the sterilization process.

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Abstract

The application provides a kind of microwave sterilization system dynamic regulation method based on distributed photovoltaic drive, it is related to microwave sterilization and renewable energy utilization technical field.The method comprises: obtaining the real-time power generation of distributed photovoltaic power generation unit;According to the real-time power generation and the preset sterilization energy demand, dynamically calculate target microwave power and / or target material processing time;According to the target operating parameter, adjust the current microwave power and / or the current material processing time, so that the microwave energy input to the material per unit time of microwave sterilization system matches the real-time power generation.The application realizes the dynamic adjustment of microwave power following the change of photovoltaic power generation, maximizes the consumption of green power while ensuring the stability of sterilization effect, avoids the sterilization deficiency or overkill caused by photovoltaic fluctuation, and ensures the stability of microbial agent activity in microbial-containing materials.
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Description

Technical Field

[0001] This invention relates to the fields of microwave sterilization technology and renewable energy utilization technology. Specifically, this invention relates to a dynamic control method for a microwave sterilization system based on distributed photovoltaic drive. Background Technology

[0002] With increasing environmental awareness, the biomass product industry is undergoing a transformation from chemical processing to biotechnology. In the production of biomass products containing active microorganisms (such as microbial activated cat litter and agricultural biological agents), sterilization is typically required to control the growth of contaminating microorganisms while ensuring the activity of the encapsulated microorganisms. Existing sterilization technologies have the following main drawbacks: First, the issue of energy consumption and carbon emissions.

[0003] Traditional production lines are often equipped with high-power microwave sterilization or drying equipment, which typically operate at constant power, resulting in huge energy consumption and increased carbon emissions. If renewable energy sources such as distributed photovoltaic power generation are used for power supply, the intermittent and fluctuating nature of photovoltaic power generation often necessitates drawing power from the grid or curtailing solar power to ensure stable production, making it impossible to maximize the use of green electricity and truly achieve zero-carbon production.

[0004] Second, it is difficult to balance the bactericidal effect with the microbial activity.

[0005] Microwave sterilization systems require a certain energy input to ensure sterilization effectiveness; however, excessively high energy input may damage the activity of encapsulated microorganisms, while insufficient energy input will fail to meet sterilization requirements. Current technologies struggle to dynamically adjust energy input based on supply conditions, leading to inconsistent product quality.

[0006] Third, the utilization rate of renewable energy is low.

[0007] Distributed photovoltaic power generation on factory rooftops is intermittent and volatile. Existing production lines often use grid connection or energy storage to smooth out these fluctuations, failing to achieve dynamic matching between photovoltaic power and production equipment, resulting in low utilization of "green electricity" and high production costs.

[0008] In summary, there is an urgent need for a technical solution that can combine the energy demand for sterilization with the dynamic regulation of green energy, so as to achieve efficient utilization of photovoltaic power, ensure sterilization effect and microbial activity, and produce high-quality biomass products with active biodegradation function. Summary of the Invention

[0009] The technical problem to be solved by the present invention is to provide a dynamic control method for a microwave sterilization system based on distributed photovoltaic drive, which aims to solve at least one of the above-mentioned technical problems.

[0010] In a first aspect, the technical solution of the present invention to solve the above-mentioned technical problems is as follows: a dynamic control method for a microwave sterilization system based on distributed photovoltaic drive, the method comprising: Obtain the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system; Based on the real-time power generation and the preset sterilization energy requirements, the target operating parameters of the microwave sterilization system are dynamically calculated. The target operating parameters include the target microwave power and / or the target material processing time. Based on the target operating parameters, adjust the current operating parameters of the microwave sterilization system to match the microwave energy supply rate of the microwave sterilization system with the real-time power generation. The current operating parameters include the current microwave power and / or the current material processing time. The microwave energy supply rate is the microwave energy input to the material by the microwave sterilization system per unit time.

[0011] The beneficial effects of this invention are as follows: by acquiring the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system, and dynamically calculating the target operating parameters, including the target microwave power and / or the target material processing time, based on the real-time power generation and the preset sterilization energy requirements, and then adjusting the current operating parameters, including the current microwave power and / or the current material processing time, based on the target operating parameters, the microwave energy input to the material by the microwave sterilization system per unit time is matched with the real-time power of the photovoltaic power generation, thereby achieving a dynamic balance between the energy consumption and photovoltaic output of the microwave sterilization system, maximizing the absorption of green electricity while ensuring the stability and effectiveness of the sterilization process.

[0012] Based on the above technical solution, the present invention can be further improved as follows.

[0013] Furthermore, the target operating parameters of the microwave sterilization system are dynamically calculated based on the real-time power generation and the preset sterilization energy requirements, including: The energy density threshold range required for sterilization is determined based on the material characteristics. The energy density threshold range includes the minimum energy density threshold and the maximum energy density threshold. Calculate the required microwave power based on the current batch material quality and the preset energy density setting value determined from the energy density threshold range; The required microwave power is compared with the real-time power generation, and the target operating parameters are determined based on the comparison results.

[0014] Furthermore, the required microwave power is compared with the real-time power generation, and the target operating parameters are determined based on the comparison results, including: If the real-time power generation is greater than or equal to the required microwave power, the required microwave power is determined as the target microwave power, and the standard processing time is determined as the target material processing time. If the real-time power generation is less than the required microwave power, the real-time power generation is determined as the target microwave power. Based on the preset energy density setting, the current batch material quality, and the real-time power generation, the extended processing time is determined and used as the target material processing time.

[0015] Furthermore, the above-mentioned adjustment of the current operating parameters of the microwave sterilization system according to the target operating parameters includes: If the target operating parameters include the target microwave power, then adjust the operating parameters of the microwave power generator of the microwave sterilization system to adjust the current microwave power to the target microwave power. The operating parameters include the anode voltage and / or duty cycle. If the target operating parameters include the target material processing time, then adjust the operating speed of the material conveying device of the microwave sterilization system to adjust the current material processing time to the target material processing time. The operating speed includes the conveyor belt speed.

[0016] Furthermore, the method also includes: Obtain the current material flow rate of the material entering the microwave sterilization system; Calculate the current energy density value based on the current material flow rate and real-time power generation. Determine whether the current energy density value is between the minimum energy density threshold and the maximum energy density threshold; If the current energy density value is lower than the minimum energy density threshold, then power is supplemented from the energy storage unit or the grid so that the actual energy density after supplementing the power reaches the minimum energy density threshold. If the current energy density value is higher than the maximum energy density threshold, reduce the microwave power of the microwave sterilization system or activate the backup load to reduce the adjusted actual energy density to below the maximum energy density threshold.

[0017] Furthermore, the aforementioned material characteristics include the moisture content of the material entering the microwave sterilization system and the content of microorganisms in the material. Based on these material characteristics, the energy density threshold range required for sterilization is determined, including: Based on the moisture content of the material entering the microwave sterilization system, the content of microorganisms in the material, and the kill rate of target bacteria, the minimum energy density threshold and the maximum energy density threshold required for sterilization are determined.

[0018] Furthermore, the extended processing time is determined based on the preset energy density setting, the current batch material quality, and real-time power generation, including: Calculate the total sterilization energy required based on the preset energy density setting and the current batch material mass; The extended processing time is calculated based on the total required sterilization energy and real-time power generation.

[0019] Secondly, to solve the above-mentioned technical problems, the present invention also provides a dynamic control device for a microwave sterilization system based on distributed photovoltaic drive, the device comprising: The acquisition module is used to acquire the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system; The target operating parameter determination module is used to dynamically calculate the target operating parameters of the microwave sterilization system based on the real-time power generation and the preset sterilization energy requirements. The target operating parameters include the target microwave power and / or the target material processing time. The control module is used to adjust the current operating parameters of the microwave sterilization system according to the target operating parameters, so that the microwave energy supply rate of the microwave sterilization system matches the real-time power generation. The current operating parameters include the current microwave power and / or the current material processing time. The microwave energy supply rate is the microwave energy input to the material by the microwave sterilization system per unit time.

[0020] Thirdly, in order to solve the above-mentioned technical problems, the present invention also provides an electronic device, which includes a memory, a processor, and a computer program stored in the memory and executable on the processor. When the processor executes the computer program, it implements the dynamic control method of the microwave sterilization system based on distributed photovoltaic drive of the present application.

[0021] Fourthly, in order to solve the above-mentioned technical problems, the present invention also provides a computer-readable storage medium storing a computer program, which, when executed by a processor, implements the dynamic control method of the microwave sterilization system based on distributed photovoltaic drive of the present application.

[0022] Additional aspects and advantages of this application will be set forth in part in the description which follows, and will become apparent from the description or may be learned by practice of this application. Attached Figure Description

[0023] To more clearly illustrate the technical solutions in the embodiments of the present invention, the accompanying drawings used in the description of the embodiments of the present invention will be briefly introduced below.

[0024] Figure 1 A flowchart illustrating a dynamic control method for a microwave sterilization system based on distributed photovoltaic drive, provided in one embodiment of the present invention; Figure 2 A schematic diagram of the structure of a dynamic control device for a microwave sterilization system based on distributed photovoltaic drive, provided in one embodiment of the present invention; Figure 3 This is a schematic diagram of the structure of an electronic device provided in one embodiment of the present invention. Detailed Implementation

[0025] The principles and features of the present invention are described below. The examples given are only for explaining the present invention and are not intended to limit the scope of the present invention.

[0026] The technical solution of the present invention and how the technical solution of the present invention solves the above-mentioned technical problems are described in detail below with specific embodiments. These specific embodiments can be combined with each other, and the same or similar concepts or processes may not be described again in some embodiments. The embodiments of the present invention will now be described with reference to the accompanying drawings.

[0027] The data acquisition process involved in this invention follows the principles of legality, legitimacy, and necessity. Based on obtaining the explicit authorization and consent of the user, only the minimum necessary information required to achieve the purpose is collected, and data security protection obligations are fulfilled in accordance with the law.

[0028] The solution provided in this invention can be applied to any application scenario that requires dynamic control of a microwave sterilization system based on distributed photovoltaic drive.

[0029] This invention provides a possible implementation, such as... Figure 1 The diagram shows a flowchart of a dynamic control method for a microwave sterilization system based on distributed photovoltaic drive. This method can be executed by any electronic device, such as an intelligent control unit built into the microwave sterilization system. For ease of description, the method provided in this embodiment will be described below using the intelligent control unit as the execution subject. Figure 1 The flowchart shown indicates that the method may include the following steps: S10, Obtain the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system; S20, dynamically calculates the target operating parameters of the microwave sterilization system based on the real-time power generation and the preset sterilization energy requirements. The target operating parameters include the target microwave power and / or the target material processing time. S30, adjust the current operating parameters of the microwave sterilization system according to the target operating parameters so that the microwave energy supply rate of the microwave sterilization system matches the real-time power generation. The current operating parameters include the current microwave power and / or the current material processing time. The microwave energy supply rate is the microwave energy input to the material by the microwave sterilization system per unit time.

[0030] The method of this invention obtains the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system, and dynamically calculates target operating parameters, including target microwave power and / or target material processing time, based on the real-time power generation and preset sterilization energy requirements. Then, it adjusts the current operating parameters, including the current microwave power and / or current material processing time, based on the target operating parameters, so that the microwave energy input to the material by the microwave sterilization system per unit time matches the real-time power of the photovoltaic power generation. This achieves a dynamic balance between the energy consumption and photovoltaic output of the microwave sterilization system, maximizing the utilization of green electricity while ensuring the stability and effectiveness of the sterilization process.

[0031] The following specific embodiments further illustrate the solution of the present invention. In this embodiment, the dynamic control method for a microwave sterilization system based on distributed photovoltaic drive may include the following steps: S10, Obtain the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system; In this step, distributed photovoltaic (PV) power generation units are installed on the roof of the factory (a factory producing biomass products containing live microorganisms). These units include PV modules, inverters, and smart meters, used to collect real-time PV power generation data. The smart meters upload the real-time power generation P_PV(t) to the PLC controller of the intelligent control unit via communication protocols such as Modbus TCP, providing basic data for subsequent dynamic control. Real-time power generation refers to the actual output power of the distributed PV power generation unit at the current moment, exhibiting intermittent and fluctuating characteristics.

[0032] Among them, the microwave sterilization system refers to a tunnel-type microwave processing device used to sterilize the final product after the embedding carrier is mixed with the substrate of biomass products (such as cat litter) containing active microorganisms. The microwave sterilization system is equipped with a power controller and the microwave power is adjustable. By penetrating the material through microwave energy, the final product is sterilized, the growth of miscellaneous bacteria is controlled, and the survival of the embedded microorganisms is ensured.

[0033] S20, dynamically calculates the target operating parameters of the microwave sterilization system based on the real-time power generation and the preset sterilization energy requirements. The target operating parameters include the target microwave power and / or the target material processing time. In this step, the intelligent control unit dynamically calculates the target operating parameters of the microwave sterilization system based on the collected real-time power generation and the preset sterilization energy requirements using a built-in algorithm.

[0034] Optionally, in S20 above, the target operating parameters of the microwave sterilization system are dynamically calculated based on the real-time power generation and the preset sterilization energy requirement, including: S201, Determine the energy density threshold range required for sterilization based on the material characteristics. The energy density threshold range includes the minimum energy density threshold and the maximum energy density threshold. Optionally, if the aforementioned material characteristics include the moisture content and microbial content of the material entering the microwave sterilization system, then one implementation of S201 is as follows: Based on the moisture content, microbial content, and target microbial kill rate of the material entering the microwave sterilization system, determine the minimum energy density threshold and the maximum energy density threshold required for sterilization. The minimum energy density threshold D_min is the minimum energy density required to ensure sterilization effectiveness; below this threshold, sterilization is insufficient. The maximum energy density threshold D_max is the maximum energy density required to ensure microbial survival; above this threshold, the activity of the encapsulated microorganisms may be damaged.

[0035] S202, Calculate the required microwave power based on the current batch material quality and the preset energy density setting value determined from the energy density threshold range; Based on the current batch material mass M and the preset energy density setpoint D_set selected between the lowest and highest energy density thresholds, the required microwave power P_req is calculated using the formula: P_req = D_set × M / T_proc, where T_proc is the standard processing time. The preset energy density setpoint D_set is determined based on the material's moisture content, microbial content, and the target bacteria kill rate, ensuring that the preset energy density setpoint satisfies both the sterilization effect and the microbial survival rate.

[0036] The standard processing time refers to the baseline processing time required to sterilize the current batch of materials with the required microwave power, provided that the preset energy density setting value is met. The required microwave power is calculated based on the preset energy density setting value and the mass of the current batch of materials. The standard processing time is determined by dividing the mass of the current batch of materials by the material flow rate.

[0037] S203 compares the required microwave power with the real-time power generation and determines the target operating parameters based on the comparison results.

[0038] Alternatively, one implementation of S203 above is as follows: S2031, if the real-time power generation is greater than or equal to the required microwave power, the required microwave power is determined as the target microwave power and the standard processing time is determined as the target material processing time. If the real-time power generation is greater than or equal to the required microwave power, it indicates that the photovoltaic power is sufficient. At this time, the microwave sterilization system operates at the required microwave power, and the remaining photovoltaic power is connected to the grid or supplied to other loads.

[0039] S2032, if the real-time power generation is less than the required microwave power, determine the real-time power generation as the target microwave power, and determine the extended processing time based on the preset energy density setting value, the current batch material quality and the real-time power generation, and use the extended processing time as the target material processing time.

[0040] Optionally, in the above S2032, one way to determine the extended processing time based on the preset energy density setting, the current batch material quality, and the real-time power generation is as follows: S20321, Calculate the total sterilization energy required based on the preset energy density setting value and the current batch material mass; The total sterilization energy required is E_need = D_set × M, where D_set is the preset energy density setting value and M is the mass of the current batch of materials.

[0041] S20322, based on the total required sterilization energy and real-time power generation, calculates the extended processing time.

[0042] The extended processing time is calculated as T_adj = E_need / P_PV = (D_set×M) / P_PV, where P_PV is the real-time power generation. The extended processing time is greater than the standard processing time, ensuring that the total sterilization energy received per unit mass of material remains consistent with that obtained using the required microwave power and standard processing time.

[0043] S30, adjust the current operating parameters of the microwave sterilization system according to the target operating parameters so that the microwave energy supply rate of the microwave sterilization system matches the real-time power generation. The current operating parameters include the current microwave power and / or the current material processing time. The microwave energy supply rate is the microwave energy input to the material by the microwave sterilization system per unit time.

[0044] In this step, the intelligent control unit can dynamically adjust the microwave sterilization system through the actuator based on the target operating parameters calculated in S20, so that the microwave energy supply rate is matched with the real-time power generation of the distributed photovoltaic power generation unit, thereby realizing the local consumption of photovoltaic power.

[0045] Furthermore, in the above S30, one way to adjust the current operating parameters of the microwave sterilization system according to the target operating parameters is as follows: S301, If ​​the target operating parameters include the target microwave power, then adjust the operating parameters of the microwave power generator of the microwave sterilization system to adjust the current microwave power to the target microwave power. The operating parameters include the anode voltage and / or duty cycle. By adjusting the magnetron anode voltage or duty cycle, the microwave output power can be changed to achieve the target microwave power.

[0046] S302, if the target operating parameters include the target material processing time, then adjust the operating speed of the material conveying device of the microwave sterilization system to adjust the current material processing time to the target material processing time. The operating speed includes the conveyor belt speed.

[0047] By adjusting the conveyor belt speed, the residence time of the material in the microwave field is changed, thus enabling the current material processing time to reach the target processing time. Decreasing the conveyor belt speed increases the processing time, while increasing the conveyor belt speed shortens the processing time.

[0048] Optionally, the method further includes: Obtain the current material flow rate of the material entering the microwave sterilization system; wherein, the material flow rate Q(t) entering the tunnel microwave sterilization system can be monitored in real time by a material flow sensor.

[0049] The current energy density value is calculated based on the current material flow rate and real-time power generation; the current energy density value D_curr is calculated based on the current material flow rate and real-time power generation, reflecting the actual microwave energy received per unit mass of material.

[0050] Determine whether the current energy density value is between the minimum energy density threshold and the maximum energy density threshold; If the current energy density value is lower than the minimum energy density threshold, power will be supplemented from the energy storage unit or the grid to bring the actual energy density after the power supplementation to the minimum energy density threshold. In particular, when the photovoltaic power is too low and the sterilization energy is insufficient, a small amount of power will be automatically supplemented from the energy storage unit or the grid to ensure the sterilization effect and ensure stable product quality.

[0051] If the current energy density value is higher than the maximum energy density threshold, the microwave power of the microwave sterilization system will be reduced or a backup load will be activated to bring the adjusted actual energy density down below the maximum energy density threshold. Specifically, if excessive photovoltaic power may damage microorganisms, the microwave power will be reduced or a backup load (such as a water heater) will be activated to protect the equipment and maintain microbial activity, avoiding over-sterilization.

[0052] By repeating the above steps, this invention enables microwave power to follow changes in photovoltaic power generation while ensuring sterilization effect, maximizing the use of green electricity, reducing carbon emissions from production, and meeting the access requirements for low-carbon products in the Middle East and European and American markets.

[0053] The solution of the present invention has the following beneficial effects: First, it enables dynamic consumption of photovoltaic power, reducing carbon emissions from production. This invention acquires the power output of distributed photovoltaic power generation units in real time and dynamically adjusts the operating parameters of the microwave sterilization system based on the photovoltaic output. This ensures that the microwave energy supply rate matches the renewable energy supply, maximizing the local consumption of green electricity, reducing curtailment and grid dependence, significantly reducing carbon emissions in the production process, and meeting the low-carbon product access requirements of high-end markets in the Middle East, Europe, and the United States.

[0054] Secondly, it ensures a balance between sterilization effectiveness and microbial activity. Based on material characteristics (moisture content, microbial content), this invention presets an energy density threshold range. When photovoltaic power fluctuates, it dynamically adjusts microwave power and / or material processing time to maintain the energy density of the actual input material between the lowest and highest thresholds. This ensures that the kill rate of miscellaneous bacteria meets the standard while avoiding excessive sterilization that could damage the activity of encapsulated microorganisms, thus guaranteeing product quality stability.

[0055] Third, in scenarios with insufficient power, the invention extends the processing time to compensate for energy. When the real-time power generation is lower than the required microwave power, the invention automatically adjusts the microwave power to the current available photovoltaic power. By calculating the ratio of the required total sterilization energy to the real-time power, the material processing time is extended accordingly, ensuring that the total sterilization energy received per unit mass of material is consistent with that under standard operating conditions, thus solving the problem of insufficient sterilization caused by the intermittency of photovoltaic power generation.

[0056] Fourth, multiple safety protection mechanisms ensure stable system operation. This invention monitors the current energy density value in real time. When it falls below the minimum threshold, it automatically replenishes power from the energy storage unit or the power grid to ensure the sterilization effect. When it exceeds the maximum threshold, it automatically reduces microwave power or activates backup load to protect microbial activity and avoid equipment overload, forming a complete photovoltaic-microwave coordinated control closed loop.

[0057] Based on and Figure 1 Based on the same principle as the method shown, this embodiment of the invention also provides a dynamic control device 20 for a microwave sterilization system driven by distributed photovoltaics, such as... Figure 2 As shown, the dynamic control device 20 of the microwave sterilization system based on distributed photovoltaic drive may include an acquisition module 210, a target operating parameter determination module 220, and a control module 230, wherein: The acquisition module 210 is used to acquire the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system; The target operating parameter determination module 220 is used to dynamically calculate the target operating parameters of the microwave sterilization system based on the real-time power generation and the preset sterilization energy requirements. The target operating parameters include the target microwave power and / or the target material processing time. The control module 230 is used to adjust the current operating parameters of the microwave sterilization system according to the target operating parameters, so that the microwave energy supply rate of the microwave sterilization system matches the real-time power generation. The current operating parameters include the current microwave power and / or the current material processing time. The microwave energy supply rate is the microwave energy input to the material by the microwave sterilization system per unit time.

[0058] Furthermore, when the aforementioned target operating parameter determination module 220 dynamically calculates the target operating parameters of the microwave sterilization system based on the real-time power generation and the preset sterilization energy requirements, it is specifically used for: The energy density threshold range required for sterilization is determined based on the material characteristics. The energy density threshold range includes the minimum energy density threshold and the maximum energy density threshold. Calculate the required microwave power based on the current batch material quality and the preset energy density setting value determined from the energy density threshold range; The required microwave power is compared with the real-time power generation, and the target operating parameters are determined based on the comparison results.

[0059] Furthermore, when the aforementioned target operating parameter determination module 220 compares the required microwave power with the real-time power generation and determines the target operating parameters based on the comparison results, it is specifically used for: If the real-time power generation is greater than or equal to the required microwave power, the required microwave power is determined as the target microwave power, and the standard processing time is determined as the target material processing time. If the real-time power generation is less than the required microwave power, the real-time power generation is determined as the target microwave power. Based on the preset energy density setting, the current batch material quality, and the real-time power generation, the extended processing time is determined and used as the target material processing time.

[0060] Furthermore, when adjusting the current operating parameters of the microwave sterilization system according to the target operating parameters, the aforementioned control module 230 is specifically used for: If the target operating parameters include the target microwave power, then adjust the operating parameters of the microwave power generator of the microwave sterilization system to adjust the current microwave power to the target microwave power. The operating parameters include the anode voltage and / or duty cycle. If the target operating parameters include the target material processing time, then adjust the operating speed of the material conveying device of the microwave sterilization system to adjust the current material processing time to the target material processing time. The operating speed includes the conveyor belt speed.

[0061] Furthermore, the device also includes an adjustment module for performing the following steps: Obtain the current material flow rate of the material entering the microwave sterilization system; Calculate the current energy density value based on the current material flow rate and real-time power generation. Determine whether the current energy density value is between the minimum energy density threshold and the maximum energy density threshold; If the current energy density value is lower than the minimum energy density threshold, then power is supplemented from the energy storage unit or the grid so that the actual energy density after supplementing the power reaches the minimum energy density threshold. If the current energy density value is higher than the maximum energy density threshold, reduce the microwave power of the microwave sterilization system or activate the backup load to reduce the adjusted actual energy density to below the maximum energy density threshold.

[0062] Furthermore, the aforementioned material characteristics include the moisture content of the material entering the microwave sterilization system and the content of microorganisms in the material. When determining the energy density threshold range required for sterilization based on the material characteristics, the target operating parameter determination module 220 is specifically used for: Based on the moisture content of the material entering the microwave sterilization system, the content of microorganisms in the material, and the kill rate of target bacteria, the minimum energy density threshold and the maximum energy density threshold required for sterilization are determined.

[0063] Furthermore, when determining the extended processing time based on the preset energy density setting, the current batch material quality, and real-time power generation, the aforementioned target operating parameter determination module 220 is specifically used for: Calculate the total sterilization energy required based on the preset energy density setting and the current batch material mass; The extended processing time is calculated based on the total required sterilization energy and real-time power generation.

[0064] The distributed photovoltaic-driven microwave sterilization system dynamic control device of the present invention can execute the distributed photovoltaic-driven microwave sterilization system dynamic control method provided in the present invention. The implementation principle is similar. The actions performed by each module and unit in the distributed photovoltaic-driven microwave sterilization system dynamic control device of the present invention correspond to the steps in the distributed photovoltaic-driven microwave sterilization system dynamic control method of the present invention. For detailed functional descriptions of each module of the distributed photovoltaic-driven microwave sterilization system dynamic control device, please refer to the descriptions in the corresponding distributed photovoltaic-driven microwave sterilization system dynamic control methods shown above, which will not be repeated here.

[0065] The aforementioned dynamic control device for a microwave sterilization system based on distributed photovoltaic drive can be a computer program (including program code) running on a computer device. For example, the dynamic control device for a microwave sterilization system based on distributed photovoltaic drive is an application software. The device can be used to execute the corresponding steps in the method provided in the embodiments of the present invention.

[0066] In some embodiments, the dynamic control device for a microwave sterilization system based on distributed photovoltaic drive provided in this invention can be implemented using a combination of hardware and software. As an example, the dynamic control device for a microwave sterilization system based on distributed photovoltaic drive provided in this invention can be a processor in the form of a hardware decoding processor, which is programmed to execute the dynamic control method for a microwave sterilization system based on distributed photovoltaic drive provided in this invention. For example, the processor in the form of a hardware decoding processor can be one or more application-specific integrated circuits (ASICs), DSPs, programmable logic devices (PLDs), complex programmable logic devices (CPLDs), field-programmable gate arrays (FPGAs), or other electronic components.

[0067] In other embodiments, the dynamic control device for the microwave sterilization system based on distributed photovoltaic drive provided in this invention can be implemented in software. Figure 2 A dynamic control device for a microwave sterilization system based on distributed photovoltaic drive, stored in a memory, is shown. It can be software in the form of programs and plug-ins, and includes a series of modules, including an acquisition module 210, a target operating parameter determination module 220, and a control module 230, for implementing the dynamic control method for a microwave sterilization system based on distributed photovoltaic drive provided in the embodiments of the present invention.

[0068] The modules described in the embodiments of the present invention can be implemented in software or hardware. The names of the modules are not, in some cases, limiting the scope of the module itself.

[0069] Based on the same principles as the methods shown in the embodiments of the present invention, the embodiments of the present invention also provide an electronic device, which may include, but is not limited to: a processor and a memory; the memory for storing computer programs; and the processor for executing the methods shown in any embodiment of the present invention by invoking the computer programs.

[0070] In one alternative embodiment, an electronic device is provided, such as Figure 3 As shown, Figure 3The illustrated electronic device 4000 includes a processor 4001 and a memory 4003. The processor 4001 and the memory 4003 are connected, for example, via a bus 4002. Optionally, the electronic device 4000 may further include a transceiver 4004, which can be used for data interaction between the electronic device and other electronic devices, such as sending and / or receiving data. It should be noted that in practical applications, the transceiver 4004 is not limited to one type, and the structure of the electronic device 4000 does not constitute a limitation on the embodiments of the present invention.

[0071] Processor 4001 may be a CPU (Central Processing Unit), a general-purpose processor, a DSP (Digital Signal Processor), an ASIC (Application Specific Integrated Circuit), an FPGA (Field Programmable Gate Array), or other programmable logic devices, transistor logic devices, hardware components, or any combination thereof. It can implement or execute the various exemplary logic blocks, modules, and circuits described in conjunction with the disclosure of this invention. Processor 4001 may also be a combination that implements computational functions, such as including one or more microprocessor combinations, a combination of a DSP and a microprocessor, etc.

[0072] Bus 4002 may include a pathway for transmitting information between the aforementioned components. Bus 4002 may be a PCI (Peripheral Component Interconnect) bus or an EISA (Extended Industry Standard Architecture) bus, etc. Bus 4002 can be divided into address bus, data bus, control bus, etc. For ease of representation, Figure 3 The bus is represented by a single thick line, but this does not mean that there is only one bus or one type of bus.

[0073] The memory 4003 may be ROM (Read Only Memory) or other types of static storage devices capable of storing static information and instructions, RAM (Random Access Memory) or other types of dynamic storage devices capable of storing information and instructions, or EEPROM (Electrically Erasable Programmable Read Only Memory), CD-ROM (Compact Disc Read Only Memory) or other optical disc storage, optical disc storage (including compressed optical discs, laser discs, optical discs, digital universal optical discs, Blu-ray discs, etc.), magnetic disk storage media or other magnetic storage devices, or any other medium capable of carrying or storing desired program code in the form of instructions or data structures and accessible by a computer, but not limited thereto.

[0074] The memory 4003 stores application code (computer program) for executing the present invention, and its execution is controlled by the processor 4001. The processor 4001 executes the application code stored in the memory 4003 to implement the content shown in the foregoing method embodiments.

[0075] Among these, electronic devices can also be terminal devices. Figure 3 The electronic device shown is merely an example and should not be construed as limiting the functionality and scope of use of the embodiments of the present invention.

[0076] This invention provides a computer-readable storage medium storing a computer program that, when run on a computer, enables the computer to execute the corresponding content in the aforementioned method embodiments.

[0077] According to another aspect of the present invention, a computer program product or computer program is also provided, comprising computer instructions stored in a computer-readable storage medium. A processor of a computer device reads the computer instructions from the computer-readable storage medium and executes the computer instructions, causing the computer device to perform the methods provided in the various embodiments described above.

[0078] Computer program code for performing the operations of this invention can be written in one or more programming languages ​​or a combination thereof, including object-oriented programming languages ​​such as Java, Smalltalk, and C++, and conventional procedural programming languages ​​such as C or similar languages. The program code can be executed entirely on the user's computer, partially on the user's computer, as a standalone software package, partially on the user's computer and partially on a remote computer, or entirely on a remote computer or server. In cases involving remote computers, the remote computer can be connected to the user's computer via any type of network—including a local area network (LAN) or a wide area network (WAN)—or can be connected to an external computer (e.g., via the Internet using an Internet service provider).

[0079] It should be understood that the flowcharts and block diagrams in the accompanying drawings illustrate the architecture, functionality, and operation of possible implementations of methods and computer program products according to various embodiments of the present invention. In this regard, each block in a flowchart or block diagram may represent a module, segment, or portion of code containing one or more executable instructions for implementing the specified logical function. It should also be noted that in some alternative implementations, the functions indicated in the blocks may occur in a different order than those indicated in the drawings. For example, two consecutively indicated blocks may actually be executed substantially in parallel, and they may sometimes be executed in reverse order, depending on the functions involved. It should also be noted that each block in the block diagrams and / or flowcharts, and combinations of blocks in the block diagrams and / or flowcharts, may be implemented using a dedicated hardware-based system that performs the specified function or operation, or using a combination of dedicated hardware and computer instructions.

[0080] The computer-readable storage medium provided in this invention can be, for example, but not limited to, an electrical, magnetic, optical, electromagnetic, infrared, or semiconductor system, apparatus, or device, or any combination thereof. More specific examples of a computer-readable storage medium may include, but are not limited to: an electrical connection having one or more wires, a portable computer disk, a hard disk, random access memory (RAM), read-only memory (ROM), erasable programmable read-only memory (EPROM or flash memory), optical fiber, portable compact disk read-only memory (CD-ROM), optical storage device, magnetic storage device, or any suitable combination thereof. In this invention, a computer-readable storage medium can be any tangible medium containing or storing a program that can be used by or in conjunction with an instruction execution system, apparatus, or device.

[0081] The aforementioned computer-readable storage medium carries one or more programs, which, when executed by the electronic device, cause the electronic device to perform the method shown in the above embodiments.

[0082] The above description is merely a preferred embodiment of the present invention and an explanation of the technical principles employed. Those skilled in the art should understand that the scope of disclosure in this invention is not limited to technical solutions formed by specific combinations of the above-described technical features, but should also cover other technical solutions formed by arbitrary combinations of the above-described technical features or their equivalents without departing from the above-disclosed concept. For example, technical solutions formed by substituting the above features with (but not limited to) technical features with similar functions disclosed in this invention.

Claims

1. A dynamic control method for a microwave sterilization system based on distributed photovoltaic drive, characterized in that, include: Obtain the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system; Based on the real-time power generation and the preset sterilization energy requirement, the target operating parameters of the microwave sterilization system are dynamically calculated, including the target microwave power and / or the target material processing time. According to the target operating parameters, the current operating parameters of the microwave sterilization system are adjusted so that the microwave energy supply rate of the microwave sterilization system matches the real-time power generation. The current operating parameters include the current microwave power and / or the current material processing time. The microwave energy supply rate is the microwave energy input to the material by the microwave sterilization system per unit time.

2. The method according to claim 1, characterized in that, The step of dynamically calculating the target operating parameters of the microwave sterilization system based on the real-time power generation and the preset sterilization energy requirement includes: The energy density threshold range required for sterilization is determined based on the material characteristics, and the energy density threshold range includes a minimum energy density threshold and a maximum energy density threshold. Calculate the required microwave power based on the current batch material quality and the preset energy density setting value determined from the energy density threshold range; The required microwave power is compared with the real-time power generation, and the target operating parameters are determined based on the comparison results.

3. The method according to claim 2, characterized in that, The step of comparing the required microwave power with the real-time power generation and determining the target operating parameters based on the comparison result includes: If the real-time power generation is greater than or equal to the required microwave power, the required microwave power is determined as the target microwave power and the standard processing time is determined as the target material processing time. If the real-time power generation is less than the required microwave power, the real-time power generation is determined as the target microwave power. Based on the preset energy density setting, the current batch material quality, and the real-time power generation, the extended processing time is determined, and the extended processing time is used as the target material processing time.

4. The method according to claim 3, characterized in that, The step of adjusting the current operating parameters of the microwave sterilization system according to the target operating parameters includes: If the target operating parameters include the target microwave power, then the operating parameters of the microwave power generator of the microwave sterilization system are adjusted to adjust the current microwave power to the target microwave power. The operating parameters include anode voltage and / or duty cycle. If the target operating parameters include the target material processing time, then the operating speed of the material conveying device of the microwave sterilization system is adjusted to adjust the current material processing time to the target material processing time. The operating speed includes the conveyor belt speed.

5. The method according to any one of claims 1 to 4, characterized in that, The method further includes: Obtain the current material flow rate of the material entering the microwave sterilization system; Calculate the current energy density value based on the current material flow rate and the real-time power generation. Determine whether the current energy density value is between the minimum energy density threshold and the maximum energy density threshold; If the current energy density value is lower than the minimum energy density threshold, then power is supplemented from the energy storage unit or the grid so that the actual energy density after supplementing the power reaches the minimum energy density threshold. If the current energy density value is higher than the maximum energy density threshold, the microwave power of the microwave sterilization system is reduced or a backup load is activated, so that the adjusted actual energy density is reduced to below the maximum energy density threshold.

6. The method according to claim 2, characterized in that, The material characteristics include the moisture content of the material entering the microwave sterilization system and the content of microorganisms in the material. Determining the energy density threshold range required for sterilization based on the material characteristics includes: Based on the moisture content of the material entering the microwave sterilization system, the content of microorganisms in the material, and the kill rate of target bacteria, the minimum energy density threshold and the maximum energy density threshold required for sterilization are determined.

7. The method according to claim 3, characterized in that, The step of determining the extended processing time based on a preset energy density setting, the current batch material quality, and the real-time power generation includes: Calculate the total sterilization energy required based on the preset energy density setting and the current batch material mass; The extended processing time is calculated based on the total required sterilization energy and the real-time power generation.

8. A dynamic control device for a microwave sterilization system based on distributed photovoltaic drive, characterized in that, include: The acquisition module is used to acquire the real-time power generation of the distributed photovoltaic power generation unit that powers the microwave sterilization system; The target operating parameter determination module is used to dynamically calculate the target operating parameters of the microwave sterilization system based on the real-time power generation and the preset sterilization energy requirements. The target operating parameters include the target microwave power and / or the target material processing time. The control module is used to adjust the current operating parameters of the microwave sterilization system according to the target operating parameters, so that the microwave energy supply rate of the microwave sterilization system matches the real-time power generation. The current operating parameters include the current microwave power and / or the current material processing time. The microwave energy supply rate is the microwave energy input to the material by the microwave sterilization system per unit time.

9. An electronic device, characterized in that, It includes a memory, a processor, and a computer program stored in the memory and executable on the processor, wherein the processor, when executing the computer program, implements the method of any one of claims 1-7.

10. A computer-readable storage medium, characterized in that, The computer-readable storage medium stores a computer program that, when executed by a processor, implements the method of any one of claims 1-7.