A process regulation and control method and system based on production line co-production

Abstract

The present invention discloses a process regulation control method and system based on production line co-production, which relates to the technical field of new power systems, including completing full-load operation under load regulation according to the production line co-production, indirectly regulating the change of power generation load by adjusting the load of the ethanol production process; optimizing the load rate provided by the gas turbine in the production line co-production process through the fuel provided by the ethanol storage tank; and completing the process regulation control of the production line co-production through the mutual feedback mechanism of the sensor and the data acquisition model. The present invention realizes the process regulation control of the production line co-production, effectively solves the problems of slow response speed and insufficient regulation accuracy in the prior art, improves the automatic regulation capability of the production line, ensures efficient operation in a complex and changeable production environment, and thus provides a more intelligent and precise production control solution for the modern manufacturing industry.

Description

Technical Field

[0001] The present invention relates to the technical field of novel power systems, and in particular to a process regulation control method and system based on production line co-production. Background Art

[0002] With the rapid development of social economy and the continuous upgrading of manufacturing industry, new energy intelligent production lines have become one of the core driving forces of modern industry. While pursuing efficient production and quality control, enterprises are also facing increasingly complex production process management needs. Traditional production control methods are powerless in dealing with today's highly dynamic and changeable production environment. Therefore, society's demand for more intelligent and automated process regulation and control methods is increasingly urgent to ensure the improvement of production efficiency and the maximization of resource utilization, highlighting the importance of new energy technologies. Based on this social background, the present invention proposes a process regulation and control method and system suitable for joint production lines to better meet the needs of modern manufacturing industry for efficient and flexible production.

[0003] However, the existing production line joint production process control system has some shortcomings in the application process. For example, some systems have problems such as slow response speed and insufficient adjustment accuracy when dealing with complex production processes with multiple variables and multiple parameters. These technical defects have limited the overall efficiency and product quality of the production line to a certain extent. In response to these problems, the present invention proposes a process regulation control method and system based on production line joint production, which aims to effectively improve the automatic regulation capability of the production line and solve the deficiencies in the prior art by optimizing the control algorithm and enhancing the system integration capability. Summary of the invention

[0004] In view of the problems existing in the existing process regulation control method and system based on production line co-production, the present invention is proposed.

[0005] Therefore, the purpose of the present invention is to provide a process regulation and control method and system based on production line co-production. In view of the shortcomings of the existing production line co-production process control systems during application, the present invention proposes a process regulation and control method based on production line co-production, which aims to effectively improve the automation regulation capability of the production line by optimizing the control algorithm and enhancing the system integration capability.

[0006] In order to solve the above technical problems, the present invention provides the following technical solutions:

[0007] In a first aspect, an embodiment of the present invention provides a process regulation control method based on production line co-production, which includes, according to the production line co-production, completing full load operation under load regulation, indirectly regulating the change of power generation load by regulating the load of the ethanol production process;

[0008] In order to adjust the change of power generation load, based on the rate influence of production line co-production, the fuel provided by the ethanol storage tank is used to optimize the load rate provided by the gas turbine in the production line co-production process;

[0009] Based on the load regulation state of the production line joint production, the optimized load rate is adjusted, and the process regulation and control of the production line joint production is completed through the mutual feedback mechanism of the sensor and the data acquisition model.

[0010] As a preferred embodiment of the process regulation and control method based on production line co-production of the present invention, wherein: the full load state includes adjusting the load of the power generation device by reducing or increasing the load of the ethanol process in the case of production line co-production of ethanol;

[0011] The adjusting of the load of the power generation device comprises adjusting according to the synthetic gas distribution rule of the power generation device, the synthetic gas distribution rule comprises establishing a mathematical model of the system according to the operating characteristics of the ethanol production line under full load, the mathematical model comprises processing the load range, load change rate, inertia characteristics and production efficiency of the production line co-generation device and the power generation device, and pre-analyzing the mathematical model through a multi-objective optimization algorithm;

[0012] The multi-objective optimization algorithm includes optimizing the parameters of the synthesis gas distribution rule according to multiple objectives, and performing calculations based on the optimized parameters to obtain the synthesis gas distribution rule. The specific calculation formula of the parameters is:

[0013] ,

[0014] ,

[0015] in, Indicates the parameters, represents the total synthesis gas volume, represents the amount of synthesis gas for the power generation unit, It indicates the amount of synthesis gas in the co-generation unit of the ethanol production line.

[0016] As a preferred solution of the process regulation control method based on production line co-production of the present invention, wherein: the regulation of the change of power generation load includes decomposing the production line co-production under the full load state of load regulation, and the decomposition includes carrying out full load production of the production line co-production units according to air separation, gasification, purification and desulfurization, and adjusting the amplitude of the power generation device and the ethanol production line co-production device by calculating the parameters of the synthesis gas distribution rule;

[0017] When the system requires to increase the load of the power generation device, the system will detect the current load status of the ethanol production line co-generation device and reduce the amount of synthesis gas of the ethanol production line co-generation device through the intelligent control system. , increase the total synthesis gas volume , so that the power generation load increases;

[0018] When the system requires to reduce the load of the power generation device, the system will detect the current load status of the ethanol production line co-generation device and increase the synthesis gas volume of the ethanol production line co-generation device through the intelligent control system. , reducing the total syngas volume , so that the power generation load is reduced.

[0019] As a preferred solution of the process regulation control method based on production line co-production of the present invention, wherein: the load rate provided by the gas turbine during the optimization of the production line co-production process includes using the intelligent control system to monitor the current load status of the power generation device and the ethanol production line co-production device, and the specific calculation formula for the monitoring is:

[0020] ,

[0021] in, It indicates the load rate of the gas turbine after the change in the production line co-production process. Indicates the current load of the power generation device, It indicates the current load of the ethanol production line co-generation unit;

[0022] When the load rate of the gas turbine changes during the production line co-production process When the preset threshold range of the production line joint production is exceeded, the system triggers the load rate adjustment mechanism;

[0023] The preset threshold value includes setting safety parameters for the current load of the power generation device and the ethanol production line cogeneration device based on the safe operation of the system, and analyzing the operating status under different load conditions according to the simulation process of the mathematical model. The simulation process of the mathematical model includes taking into account the load range, load change rate, inertia characteristics and production efficiency of the production line cogeneration device and the power generation device in the form of a multivariable linear or nonlinear equation group;

[0024] The calculation formula of the simulation process of the mathematical model is:

[0025] ,

[0026] in, Indicates the preset threshold value, It indicates the maximum load value that the mathematical model simulation system can bear. It indicates the minimum load value that the mathematical model simulation system can bear. It represents the rate of load change in the system simulated by the mathematical model. It indicates the response speed of load changes in the mathematical model simulation system. Represents a multivariate function;

[0027] The preset threshold is optimized by using a multi-objective optimization algorithm, and the optimized preset threshold is calculated and obtained. The specific calculation formula is:

[0028] ,

[0029] in, represents the optimized preset threshold, Represents the functional form of multi-objective optimization, represents the weight coefficient, Indicates the number of items, Indicates from 1 to Sum the number of items;

[0030] At this time, when , the system triggers the load rate adjustment mechanism.

[0031] As a preferred solution of the process regulation and control method based on production line co-production of the present invention, wherein: the said adjusting the optimized load rate comprises calculating the syngas distribution ratio of the power generation device and the ethanol production line co-production device according to the syngas distribution rule, and adjusting the load rate of the gas engine based on the syngas distribution ratio through the fuel provided by the ethanol storage tank;

[0032] The calculation formula of the synthesis gas distribution ratio is:

[0033] ,

[0034] in, Indicates the distribution ratio of synthesis gas, Indicates the maximum syngas demand of the power generation unit;

[0035] when When the load rate increases, the current load state of the ethanol production line co-production device is detected. ;

[0036] like When the syngas volume of the ethanol production line co-generation unit is reduced, the syngas volume of the power generation unit is increased, so that the load of the ethanol production process is in a normal state. Indicates the minimum value of the current load of the ethanol production line co-production device. At this time, the load rate of the gas turbine is adjusted. The specific calculation formula for the adjustment is:

[0037] ,

[0038] in, Indicates the load rate of adjusting the gas turbine. represents the base load rate, Indicates the fuel regulation factor for the load rate, Indicates the amount of fuel provided by the ethanol tank;

[0039] when When the load rate decreases, the current load of the ethanol production line co-production unit is detected. ;

[0040] like When the syngas volume of the ethanol production line co-generation unit is increased, the syngas volume of the power generation unit is reduced, so that the load of the ethanol production process is in a normal state. It represents the minimum value of the current load of the ethanol production line co-generation unit;

[0041] At this time, adjust the secondary load rate of the gas turbine, and the specific calculation formula for the adjustment is:

[0042] ,

[0043] in, Indicates the secondary load rate of adjusting the gas turbine. Indicates the fuel adjustment factor for the secondary load rate.

[0044] As a preferred solution of the process regulation and control method based on production line co-production of the present invention, wherein: the mutual feedback mechanism includes the system deploying sensors in the process of production line co-production, and sending the data collected by the sensors to the data acquisition model;

[0045] If the system detects that the data collected by the sensor exceeds the set range of a certain parameter in the co-production process of the production line, the data acquisition model transmits the feedback information to the control system, and the control system automatically adjusts the distribution ratio of the synthesis gas amount according to the feedback information to obtain the secondary distribution ratio;

[0046] Transmitting the result of the secondary distribution ratio to the data acquisition model for analysis through the sensor to verify whether the result of the secondary distribution ratio achieves the expected effect of the synthesis gas distribution rule;

[0047] If the expected effect is not achieved, the mutual feedback mechanism will be triggered N times. If the expected effect is achieved, the system will adjust the load rate of the gas turbine for a second time according to the secondary distribution ratio result that achieves the expected effect.

[0048] As a preferred solution of the process regulation and control method based on production line co-production of the present invention, wherein: the secondary adjustment of the load rate of the gas engine includes adjusting the load rate of the gas engine again according to the secondary distribution ratio result;

[0049] like When the load rate of the gas turbine is adjusted again, the specific calculation formula for the adjustment is:

[0050] ,

[0051] in, The load rate of the adjusted gas turbine representing the result of the secondary distribution ratio, Indicates the fuel regulation coefficient of the secondary adjustment of the engine load rate, Indicates the amount of fuel provided by the ethanol tank of the secondary adjustment engine;

[0052] like When the load rate of the gas turbine is adjusted again, the specific calculation formula for the adjustment is:

[0053] ,

[0054] in, The secondary load rate of the adjusted gas turbine is expressed as a result of the secondary distribution ratio.

[0055] In a second aspect, an embodiment of the present invention provides a process regulation control system based on production line co-production, which includes: a regulation module, which operates at full load under load regulation according to the production line co-production, and indirectly regulates the change of power generation load by regulating the load of the ethanol production process;

[0056] An optimization module, which optimizes the load rate provided by the gas turbine during the co-production process of the production line through the fuel provided by the ethanol storage tank;

[0057] The control module completes the process regulation and control of the production line through the mutual feedback mechanism of sensors and data acquisition models.

[0058] In a third aspect, an embodiment of the present invention provides a computer device, including a memory and a processor, wherein the memory stores a computer program, wherein: when the processor executes the computer program, it implements any step of the above-mentioned process regulation and control method based on production line co-production.

[0059] In a fourth aspect, an embodiment of the present invention provides a computer-readable storage medium having a computer program stored thereon, wherein: when the computer program is executed by a processor, any step of the above-mentioned process regulation and control method based on production line co-production is implemented.

[0060] The beneficial effects of the present invention are as follows: the present invention successfully realizes the process regulation and control of the joint production of the production line by innovatively combining the mutual feedback mechanism of the sensor and the data acquisition model, effectively solving the problems of slow response speed and insufficient regulation accuracy in the prior art. By accurately allocating the amount of synthesis gas and optimizing the load rate of the gas turbine, the present invention significantly improves the automatic regulation capability of the production line and ensures efficient operation in a complex and changeable production environment. At the same time, based on the introduction of a multi-objective optimization algorithm, the present invention can flexibly respond to the changing needs of multi-variable production processes, ensuring the maximization of resource utilization and further improvement of production efficiency, thereby providing a more intelligent and precise production control solution for the modern manufacturing industry. BRIEF DESCRIPTION OF THE DRAWINGS

[0061] In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following briefly introduces the drawings required for describing the embodiments. Obviously, the drawings described below are only some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without creative work. Among them:

[0062] Figure 1 A specific flow chart of a process regulation control method and system based on production line co-production provided by an embodiment of the present invention.

[0063] Figure 2 A load data schematic diagram of a process regulation control method and system based on production line co-production provided by an embodiment of the present invention. DETAILED DESCRIPTION

[0064] In order to make the above-mentioned purposes, features and advantages of the present invention more obvious and easy to understand, the specific implementation methods of the present invention are described in detail below in conjunction with the drawings of the specification. Obviously, the described embodiments are part of the embodiments of the present invention, but not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary persons in the art without creative work should fall within the scope of protection of the present invention.

[0065] In the following description, many specific details are set forth to facilitate a full understanding of the present invention, but the present invention may also be implemented in other ways different from those described herein, and those skilled in the art may make similar generalizations without violating the connotation of the present invention. Therefore, the present invention is not limited to the specific embodiments disclosed below.

[0066] Secondly, the term "one embodiment" or "embodiment" as used herein refers to a specific feature, structure, or characteristic that may be included in at least one implementation of the present invention. The term "in one embodiment" that appears in different places in this specification does not necessarily refer to the same embodiment, nor does it refer to a separate or selective embodiment that is mutually exclusive with other embodiments.

[0067] The present invention is described in detail with reference to schematic diagrams. When describing the embodiments of the present invention, for the sake of convenience, the cross-sectional diagrams showing the device structure will not be partially enlarged according to the general scale, and the schematic diagrams are only examples, which should not limit the scope of protection of the present invention. In addition, in actual production, the three-dimensional dimensions of length, width and depth should be included.

[0068] At the same time, in the description of the present invention, it should be noted that the directions or positional relationships indicated by the terms "upper, lower, inner and outer" are based on the directions or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific direction, be constructed and operated in a specific direction, and therefore cannot be understood as limiting the present invention. In addition, the terms "first, second or third" are only used for descriptive purposes and cannot be understood as indicating or implying relative importance.

[0069] In the present invention, unless otherwise clearly specified and limited, the terms "install, connect, connect" should be understood in a broad sense, for example: it can be a fixed connection, a detachable connection or an integral connection; it can also be a mechanical connection, an electrical connection or a direct connection, or it can be indirectly connected through an intermediate medium, or it can be the internal communication of two components. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0070] Example 1

[0071] Reference Figure 1 and Figure 2 , which is the first embodiment of the present invention, provides a process regulation control method based on production line joint production, including:

[0072] S1: According to the joint production of the production line, the full load state operation is completed under load regulation, and the change of power generation load is indirectly adjusted by adjusting the load of the ethanol production process.

[0073] The full load state includes adjusting the load of the power generation device by reducing or increasing the load of the ethanol process when the production line is co-producing ethanol;

[0074] Adjusting the load of the power generation device includes adjusting it according to the synthetic gas distribution rule of the power generation device. The synthetic gas distribution rule includes establishing a mathematical model of the system according to the operating characteristics of the ethanol production line under full load. The mathematical model includes processing the load range, load change rate, inertia characteristics and production efficiency of the production line co-generation device and the power generation device, and pre-analyzing the mathematical model through a multi-objective optimization algorithm;

[0075] The multi-objective optimization algorithm includes optimizing the parameters of the synthesis gas allocation rule according to multiple objectives, and calculating based on the optimized parameters to obtain the synthesis gas allocation rule. The specific calculation formula of the parameters is:

[0076] ,

[0077] ,

[0078] in, Indicates the parameters, represents the total synthesis gas volume, represents the amount of synthesis gas for the power generation unit, It indicates the amount of synthesis gas in the co-generation unit of the ethanol production line.

[0079] Furthermore, in order to realize the full load and efficient operation of the production line cogeneration system under load regulation, the load of the ethanol production process is adjusted to indirectly adjust the change of the power generation load. Specifically, when the load of the ethanol production line changes, the system will dynamically adjust the amount of synthesis gas of the power generation device based on the current operating status and load characteristics of the ethanol production line to ensure that the entire system can operate stably and efficiently under different load conditions. To achieve this goal, the system has established a mathematical model that comprehensively considers factors such as load range, change rate, inertia characteristics, and production efficiency, and optimizes the parameters in the model through a multi-objective optimization algorithm. The system can reasonably allocate the amount of synthesis gas under complex conditions of multiple variables and multiple objectives, and realize precise regulation of the power generation device and the ethanol production line, thereby ensuring the optimal operation of the production line cogeneration system under different load conditions. This method not only improves the response speed and regulation accuracy of the system, but also significantly enhances the automatic regulation capability of the entire production line cogeneration system. The load data of the production line cogeneration system under load regulation are shown in Table 1 below:

[0080] Table 1 Load data of production line co-generation system under load regulation

[0081] ,

[0082] The load data of each device in the production line co-production system under different load adjustment conditions show that as the load of the power generation device gradually increases from 50% to 100%, the load of the ethanol device shows a gradual downward trend, from 100% to 40%, and drops to 0% when the load of the power generation device reaches 85% and above. At the same time, the load of the air separation and gasification devices is maintained at 100% when the load of the power generation device is 50% to 75%, fluctuates slightly after the load of the power generation device reaches 85%, and finally returns to 100% when the load of the power generation device reaches 100%. This table reflects the load distribution and adjustment relationship between each device in the process of load adjustment of the production line co-production system.

[0083] S2: In order to adjust the changes in power generation load, based on the impact of the rate of co-production of the production line, the fuel provided by the ethanol storage tank is used to optimize the load rate provided by the gas turbine during the co-production of the production line.

[0084] Among them, adjusting the change of power generation load includes decomposing the production line co-production under the full load state of load regulation, and the decomposition includes carrying out full load production of the production line co-production units according to air separation, gasification, purification and desulfurization, and adjusting the amplitude of the power generation device and the ethanol production line co-production device by calculating the parameters of the synthetic gas volume distribution rule;

[0085] When the system requires to increase the load of the power generation unit, the system will detect the current load status of the ethanol production line co-generation unit and reduce the amount of synthesis gas in the ethanol production line co-generation unit through the intelligent control system. , increase the total synthesis gas volume , so that the power generation load increases;

[0086] When the system requires to reduce the load of the power generation unit, the system will detect the current load status of the ethanol production line co-generation unit and increase the synthesis gas volume of the ethanol production line co-generation unit through the intelligent control system. , reducing the total syngas volume , so that the power generation load is reduced.

[0087] Furthermore, in the process of adjusting the changes in power generation load, the production line co-production system will optimize the load rate of the gas turbine according to the rate of the production line through the fuel provided by the ethanol storage tank. When the system detects that the load of the power generation unit needs to be increased, the system first analyzes the current load status of the ethanol production line. When the load of the power generation unit needs to be increased from 75% to 85%, the system will use the intelligent control system to gradually reduce the synthesis gas volume of the ethanol production line from 50% to 0%, and at the same time increase the total synthesis gas volume, so that the load of the power generation unit can be smoothly increased to 85%.

[0088] In the opposite case, if the load of the power generation unit needs to be reduced from 85% to 70%, the system will detect the current load status of the ethanol production line. At this time, the system will gradually increase the synthesis gas volume of the ethanol production line from 0% to 60%, so that the total synthesis gas volume is reduced, thereby reducing the load of the power generation unit to 70%. Through this series of operations, the production line co-production system can ensure reasonable load distribution of each unit under different load adjustment conditions, thereby optimizing overall production efficiency.

[0089] S2.1: Optimizing the load rate provided by the gas turbine during the production line co-production process includes using an intelligent control system to monitor the current load status of the power generation device and the ethanol production line co-production device. The specific calculation formula for monitoring is:

[0090] ,

[0091] in, It indicates the load rate of the gas turbine after the change in the production line co-production process. Indicates the current load of the power generation device, It indicates the current load of the ethanol production line co-generation unit;

[0092] When the load rate of the gas turbine changes during the production line co-production process When the preset threshold range of the production line joint production is exceeded, the system triggers the load rate adjustment mechanism;

[0093] The preset thresholds include setting safety parameters for the current loads of the power generation unit and the ethanol production line cogeneration unit based on the safe operation of the system, analyzing the operating status under different load conditions according to the simulation process of the mathematical model, and the simulation process of the mathematical model includes taking into account the load range, load change rate, inertia characteristics and production efficiency of the production line cogeneration unit and the power generation unit in the form of a multivariable linear or nonlinear equation system;

[0094] The calculation formula of the simulation process of the mathematical model is:

[0095] ,

[0096] in, Indicates the preset threshold value, It indicates the maximum load value that the mathematical model simulation system can bear. It indicates the minimum load value that the mathematical model simulation system can bear. It represents the rate of load change in the system simulated by the mathematical model. It indicates the response speed of load changes in the mathematical model simulation system. Represents a multivariate function;

[0097] The preset threshold is optimized by using a multi-objective optimization algorithm, and the optimized preset threshold is calculated. The specific calculation formula is:

[0098] ,

[0099] in, represents the optimized preset threshold, Represents the functional form of multi-objective optimization, represents the weight coefficient, Indicates the number of items, Indicates from 1 to Sum the number of items;

[0100] At this time, when When , the system triggers the load rate adjustment mechanism.

[0101] Furthermore, when optimizing the load rate of the gas turbine during the co-production process of the production line, the system monitors the current load status of the power generation unit and the ethanol production line through the intelligent control system. For example, if the current load of the power generation unit is 70% and the load of the ethanol production line is 60%, the system will calculate the load rate of the gas turbine. If the calculation result shows that the load rate of the gas turbine exceeds the system's preset threshold of 75%, the system will trigger the adjustment mechanism to ensure the safe and efficient operation of the entire production line co-production system.

[0102] S3: Based on the load regulation state of the production line joint production, the optimized load rate is adjusted, and the process regulation and control of the production line joint production is completed through the mutual feedback mechanism of the sensor and the data acquisition model.

[0103] The optimized load rate is adjusted by calculating the distribution ratio of the syngas between the power generation device and the ethanol production line co-generation device according to the syngas distribution rule, and adjusting the load rate of the gas engine based on the syngas distribution ratio and the fuel provided by the ethanol storage tank;

[0104] The calculation formula for the distribution ratio of synthesis gas is:

[0105] ,

[0106] in, Indicates the distribution ratio of synthesis gas, Indicates the maximum syngas demand of the power generation unit;

[0107] when When the load rate increases, the current load state of the ethanol production line co-production device is detected. ;

[0108] like When the syngas volume of the ethanol production line co-generation unit is reduced, the syngas volume of the power generation unit is increased, so that the load of the ethanol production process is in a normal state. Indicates the minimum value of the current load of the ethanol production line co-production device. At this time, the load rate of the gas turbine is adjusted. The specific calculation formula for the adjustment is:

[0109] ,

[0110] in, Indicates the load rate of adjusting the gas turbine. represents the base load rate, Indicates the fuel regulation factor for the load rate, Indicates the amount of fuel provided by the ethanol tank;

[0111] when When the load rate decreases, the current load of the ethanol production line co-production unit is detected. ;

[0112] like When the syngas volume of the ethanol production line co-production unit is increased, the syngas volume of the power generation unit is reduced, so that the load of the ethanol production process is in a normal state. At this time, the secondary load rate of the gas turbine is adjusted. The specific calculation formula for the adjustment is:

[0113] ,

[0114] in, Indicates the secondary load rate of adjusting the gas turbine. Indicates the fuel adjustment factor for the secondary load rate.

[0115] Furthermore, during the load regulation process of the production line, the system accurately adjusts the load rate of the gas turbine through the feedback mechanism of the sensor and data acquisition model. When the load of the power generation unit needs to increase from 75% to 85%, the system will reduce the syngas supply of the ethanol production line from 60% to 50%, and at the same time increase the syngas volume of the power generation unit to support higher power output. At the same time, the regulation amount of fuel oil is increased by 10% to ensure that the load rate of the gas turbine is increased to the required level. If the load of the power generation unit needs to be reduced to 70%, the syngas supply of the ethanol production line will be increased to 60% to maintain its production stability, and the load rate of the gas turbine will be reduced accordingly. By reasonably adjusting the amount of syngas and fuel oil, the system can ensure the stability and efficiency of the production line under different load conditions.

[0116] S3.1: The mutual feedback mechanism includes the system deploying sensors in the production line co-production process and sending the data collected by the sensors to the data acquisition model;

[0117] If the system detects that the data collected by the sensor exceeds the set range of a certain parameter in the co-production process of the production line, the data acquisition model transmits the feedback information to the control system, and the control system automatically adjusts the distribution ratio of the synthesis gas amount according to the feedback information to obtain the secondary distribution ratio;

[0118] The result of the secondary allocation ratio is transmitted to the data acquisition model for analysis through the sensor to verify whether the result of the secondary allocation ratio achieves the expected effect of the synthesis gas volume allocation rule;

[0119] If the expected effect is not achieved, the mutual feedback mechanism will be triggered N times. If the expected effect is achieved, the system will adjust the load rate of the gas turbine for a second time according to the secondary distribution ratio result that achieves the expected effect.

[0120] Furthermore, during the co-production process of the production line, the system uses sensors to monitor key parameters in real time. Assuming that the sensor detects that the distribution ratio of the synthesis gas volume deviates from the set range, the data acquisition model transmits this data to the control system. The control system then adjusts the distribution ratio of the synthesis gas volume based on the feedback information, from the initial 70% to 80%. The adjusted secondary distribution ratio result is sent back to the data acquisition model through the sensor for verification. If the secondary distribution ratio fails to achieve the expected effect, the mechanism will iterate multiple times (N times) for adjustment until it meets expectations. After three adjustments, the system reaches the expected ratio of 80%, and the control system adjusts the load rate of the gas turbine accordingly to maintain stable production.

[0121] S3.2: Secondary adjustment of the load rate of the gas turbine includes adjusting the load rate of the gas turbine again according to the secondary allocation ratio result;

[0122] like When the load rate of the gas turbine is adjusted again, the specific calculation formula for the adjustment is:

[0123] ,

[0124] in, The load rate of the adjusted gas turbine representing the result of the secondary distribution ratio, Indicates the fuel regulation coefficient of the secondary adjustment of the engine load rate, Indicates the amount of fuel provided by the ethanol tank of the secondary adjustment engine;

[0125] like When the load rate of the gas turbine is adjusted again, the specific calculation formula for the adjustment is:

[0126] ,

[0127] in, The secondary load rate of the adjusted gas turbine is expressed as a result of the secondary distribution ratio.

[0128] Preferably, during the process of production line co-production, if the initial adjustment fails to meet the expected effect, the system will make a secondary adjustment to the load rate of the gas engine. When the secondary distribution ratio initially set by the system is 80%, the control system will adjust the load rate of the gas engine according to this ratio. If the system detects that the load rate still needs to be further optimized, the load rate of the gas engine will be readjusted based on the new data. When it is detected that the actual load rate deviates from the expected 80%, the system will adjust the load rate of the gas engine by increasing or decreasing the amount of fuel from the ethanol tank for optimization. Assuming that the original fuel adjustment coefficient is 0.5 and the amount of fuel provided by the ethanol tank is 1000 liters, the system will make a secondary adjustment based on these data to ensure that the load rate accurately reaches the expected value. Finally, the load rate after the secondary adjustment will be verified again, and the operation of the gas engine will be further adjusted to ensure stable and efficient production line co-production.

[0129] In a preferred embodiment, a process regulation and control system based on production line co-production includes a regulation module, which operates at full load under load regulation according to the production line co-production, and indirectly regulates the change of power generation load by regulating the load of the ethanol production process; an optimization module, which optimizes the load rate provided by the gas turbine during the production line co-production process through the fuel provided by the ethanol storage tank; and a control module, which completes the process regulation and control of the production line co-production through the mutual feedback mechanism of sensors and data acquisition models.

[0130] The above-mentioned unit modules may be embedded in or independent of a processor in a computer device in the form of hardware, or may be stored in a memory in a computer device in the form of software, so that the processor can call and execute operations corresponding to the above-mentioned modules.

[0131] The computer device may be a terminal, and the computer device includes a processor, a memory, a communication interface, a display screen and an input device connected via a system bus. The processor of the computer device is used to provide computing and control capabilities. The memory of the computer device includes a non-volatile storage medium and an internal memory. The non-volatile storage medium stores an operating system and a computer program. The internal memory provides an environment for the operation of the operating system and the computer program in the non-volatile storage medium. The communication interface of the computer device is used to communicate with an external terminal in a wired or wireless manner, and the wireless manner can be achieved through WIFI, an operator network, NFC (near field communication) or other technologies. The display screen of the computer device may be a liquid crystal display screen or an electronic ink display screen, and the input device of the computer device may be a touch layer covering the display screen, or a key, trackball or touchpad provided on the housing of the computer device, or an external keyboard, touchpad or mouse, etc.

[0132] In summary, the present invention has successfully achieved process regulation and control of the joint production of production lines by innovatively combining the mutual feedback mechanism of sensors and data acquisition models, effectively solving the problems of slow response speed and insufficient regulation accuracy in the prior art. Through the precise allocation of the amount of synthesis gas and the optimization and regulation of the load rate of the gas turbine, the present invention has significantly improved the automatic regulation capability of the production line and ensured efficient operation in a complex and changeable production environment. At the same time, based on the introduction of a multi-objective optimization algorithm, the present invention can flexibly respond to the changing needs of multi-variable production processes, ensuring the maximization of resource utilization and further improvement of production efficiency, thereby providing a more intelligent and precise production control solution for the modern manufacturing industry.

[0133] Example 2

[0134] Reference Figure 1 and Figure 2 , which is the second embodiment of the present invention, and this embodiment provides a process regulation and control method based on production line co-production. In order to verify the beneficial effects of the present invention, scientific demonstration is carried out through simulation experiments.

[0135] During the experimental process to verify the present invention, multiple sensors were deployed in the production line co-production system to monitor the load status of the power generation unit and the ethanol production line co-production unit in real time. At the beginning of the experiment, the system set the load target of the power generation unit to 75% and the load of the ethanol production line co-production unit to 60%, and calculated the synthesis gas allocation ratio through the synthesis gas allocation rule and set it to 85%.

[0136] During the initial adjustment stage, the system automatically adjusted the load rate of the gas turbine according to the set ratio and set the amount of fuel provided by the ethanol tank to 1,200 liters. Experimental data showed that under this setting, the load rate of the power generation unit increased to 70%, but the system detected that the proportion of the synthesis gas volume deviated from the expected level and the actual load rate reached 67%, which was lower than the target load rate.

[0137] The system triggered the secondary adjustment mechanism. In the secondary adjustment stage, the control system adjusted the secondary distribution ratio to 82% according to the feedback, optimized the load rate of the gas turbine again, adjusted the fuel regulation coefficient to 0.6, and increased the amount of fuel provided by the ethanol tank to 1,300 liters. After the secondary adjustment, the load rate of the power generation unit increased to 74%, close to the expected target. After the secondary adjustment, the gap between the actual load rate and the target load rate was narrowed to 3%, which was in line with the expected effect of the system. The system ensured that the load rate reached the set value through the N-time mutual feedback mechanism and maintained a stable production line co-production effect throughout the experiment, thereby verifying the effectiveness and optimization ability of the technical solution. The experimental data adjustment record data is shown in Table 2 below:

[0138] Table 2 Experimental data adjustment record table

[0139] ,

[0140] During the experiment, the load adjustment of the power generation unit and the ethanol production line was tested, and the table shows the load changes of the ethanol unit and the air separation and gasification units at different power generation unit load percentages from 50% to 100%. When the load of the power generation unit gradually increases, the load of the ethanol unit gradually decreases from 100% to 0%, while the load of the air separation and gasification units is maintained at 100% when the load of the power generation unit is low, and gradually decreases to 85% as the power generation load increases. The data reflects the dynamic changes in the load of each device during the load adjustment process, and verifies the effectiveness of the optimized load adjustment mechanism. The comparison between the present invention and the prior art is shown in Table 3 below:

[0141] Table 3 Comparison between the present invention and the prior art

[0142] ,

[0143] The present invention is superior to the existing technology in load regulation, and has the advantages of real-time precise adjustment, high flexibility and dynamic optimization. Through the intelligent control system and data feedback mechanism, the present invention can quickly adapt to load changes and adjust the load rate of the gas turbine through ethanol storage tank fuel to ensure effective regulation under full load conditions, thereby improving the efficiency and accuracy of load regulation.

[0144] It should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention rather than to limit it. Although the present invention has been described in detail with reference to the preferred embodiments, those skilled in the art should understand that the technical solutions of the present invention may be modified or replaced by equivalents without departing from the spirit and scope of the technical solutions of the present invention, which should all be included in the scope of the claims of the present invention.

Claims

1. A process regulation and control method based on production line joint production, characterized in that: include, According to the joint production of the production line, the full load state operation is completed under load regulation, and the change of power generation load is indirectly regulated by adjusting the load of the ethanol production process; In order to adjust the change of power generation load, based on the rate influence of production line co-production, the fuel provided by the ethanol storage tank is used to optimize the load rate provided by the gas turbine in the production line co-production process; Based on the load regulation state of the production line joint production, the optimized load rate is adjusted, and the process regulation and control of the production line joint production is completed through the mutual feedback mechanism of the sensor and the data acquisition model; Adjusting the optimized load rate includes calculating the syngas distribution ratio of the power generation device and the ethanol production line co-generation device according to the syngas distribution rule, and adjusting the load rate of the gas engine based on the syngas distribution ratio through the fuel provided by the ethanol storage tank; The calculation formula of the synthesis gas distribution ratio is: in, Indicates the distribution ratio of synthesis gas, Indicates the maximum syngas demand of the power generation unit; when When the load rate increases, the current load state of the ethanol production line co-production device is detected. ; like When the syngas volume of the ethanol production line co-generation unit is reduced, the syngas volume of the power generation unit is increased, so that the load of the ethanol production process is in a normal state. Indicates the minimum value of the current load of the ethanol production line co-production device. At this time, the load rate of the gas turbine is adjusted. The specific calculation formula for the adjustment is: in, Indicates the load rate of adjusting the gas turbine. represents the base load rate, Indicates the fuel regulation factor for the load rate, Indicates the amount of fuel provided by the ethanol tank; when When the load rate decreases, the current load of the ethanol production line co-production unit is detected. ; like When the syngas volume of the ethanol production line co-production unit is increased, the syngas volume of the power generation unit is reduced, so that the load of the ethanol production process is in a normal state. At this time, the secondary load rate of the gas turbine is adjusted. The specific calculation formula for the adjustment is: in, Indicates the secondary load rate of adjusting the gas turbine. Indicates the fuel adjustment factor for the secondary load rate.

2. The process regulation and control method based on production line joint production as claimed in claim 1, characterized in that: The full load state includes adjusting the load of the power generation device by reducing or increasing the load of the ethanol process in the case of co-production of ethanol based on the production line; The adjusting of the load of the power generation device comprises adjusting according to the synthetic gas distribution rule of the power generation device, the synthetic gas distribution rule comprises establishing a mathematical model of the system according to the operating characteristics of the ethanol production line under full load, the mathematical model comprises processing the load range, load change rate, inertia characteristics and production efficiency of the production line co-generation device and the power generation device, and pre-analyzing the mathematical model through a multi-objective optimization algorithm; The multi-objective optimization algorithm includes optimizing the parameters of the synthesis gas distribution rule according to multiple objectives, and performing calculations based on the optimized parameters to obtain the synthesis gas distribution rule. The specific calculation formula of the parameters is: in, Indicates the parameters, represents the total synthesis gas volume, represents the amount of synthesis gas for the power generation unit, It indicates the amount of synthesis gas in the co-generation unit of the ethanol production line.

3. The process regulation and control method based on production line joint production as claimed in claim 2, characterized in that: The adjustment of the change of the power generation load includes decomposing the production line co-production under the full load state of the load adjustment, wherein the decomposition includes carrying out full load production of the production line co-production units according to air separation, gasification, purification and desulfurization, and adjusting the amplitude of the power generation device and the ethanol production line co-production device by calculating the parameters of the synthetic gas distribution rule; When the system requires to increase the load of the power generation device, the system will detect the current load status of the ethanol production line co-generation device and reduce the amount of synthesis gas of the ethanol production line co-generation device through the intelligent control system. , increase the total synthesis gas volume , so that the power generation load increases; When the system requires to reduce the load of the power generation device, the system will detect the current load status of the ethanol production line co-generation device and increase the synthesis gas volume of the ethanol production line co-generation device through the intelligent control system. , reducing the total syngas volume , so that the power generation load is reduced.

4. The process regulation and control method based on production line joint production as claimed in claim 3, characterized in that: The load rate provided by the gas engine during the optimization of the production line co-production process includes using the intelligent control system to monitor the current load status of the power generation device and the ethanol production line co-production device. The specific calculation formula for the monitoring is: in, It indicates the load rate of the gas turbine after the change in the production line co-production process. Indicates the current load of the power generation device, It indicates the current load of the ethanol production line co-generation unit; When the load rate of the gas turbine changes during the production line co-production process When the preset threshold range of the production line joint production is exceeded, the system triggers the load rate adjustment mechanism; The preset threshold value includes setting safety parameters for the current load of the power generation device and the ethanol production line cogeneration device based on the safe operation of the system, and analyzing the operating status under different load conditions according to the simulation process of the mathematical model. The simulation process of the mathematical model includes taking into account the load range, load change rate, inertia characteristics and production efficiency of the production line cogeneration device and the power generation device in the form of a multivariable linear or nonlinear equation group; The calculation formula of the simulation process of the mathematical model is: in, Indicates the preset threshold value, It indicates the maximum load value that the mathematical model simulation system can bear. It indicates the minimum load value that the mathematical model simulation system can bear. It represents the rate of load change in the mathematical model simulation system. It indicates the response speed of load changes in the mathematical model simulation system. Represents a multivariate function; The preset threshold is optimized by using a multi-objective optimization algorithm, and the optimized preset threshold is calculated and obtained. The specific calculation formula is: in, represents the optimized preset threshold, Represents the functional form of multi-objective optimization, represents the weight coefficient, Indicates the number of items, Indicates from 1 to Sum the number of items; At this time, when , the system triggers the load rate adjustment mechanism.

5. The process regulation and control method based on production line joint production as claimed in claim 4, characterized in that: The mutual feedback mechanism includes the system deploying sensors in the production line co-production process and sending the data collected by the sensors to the data acquisition model; If the system detects that the data collected by the sensor exceeds the set range of a certain parameter in the co-production process of the production line, the data acquisition model transmits the feedback information to the control system, and the control system automatically adjusts the distribution ratio of the synthesis gas amount according to the feedback information to obtain the secondary distribution ratio; Transmitting the result of the secondary distribution ratio to the data acquisition model for analysis through the sensor to verify whether the result of the secondary distribution ratio achieves the expected effect of the synthesis gas distribution rule; If the expected effect is not achieved, the mutual feedback mechanism will be triggered N times. If the expected effect is achieved, the system will adjust the load rate of the gas turbine for a second time according to the secondary distribution ratio result that achieves the expected effect.

6. The process regulation and control method based on production line joint production as claimed in claim 5, characterized in that: The second adjustment of the load rate of the fuel engine includes adjusting the load rate of the fuel engine again according to the result of the second distribution ratio; like When the load rate of the gas turbine is adjusted again, the specific calculation formula for the adjustment is: in, The load rate of the adjusted gas turbine representing the result of the secondary distribution ratio, Indicates the fuel regulation coefficient of the secondary adjustment of the engine load rate, Indicates the amount of fuel provided by the ethanol tank of the secondary adjustment engine; like When the load rate of the gas turbine is adjusted again, the specific calculation formula for the adjustment is: in, The secondary load rate of the adjusted gas turbine is expressed as a result of the secondary distribution ratio.

7. A process regulation and control system based on production line co-production, based on the process regulation and control method based on production line co-production according to any one of claims 1 to 6, characterized in that: include, A regulating module, which operates at full load under load regulation according to the co-production of the production line, and indirectly regulates the change of the power generation load by regulating the load of the ethanol production process; An optimization module, which optimizes the load rate provided by the gas turbine during the co-production process of the production line through the fuel provided by the ethanol storage tank; The control module completes the process regulation and control of the production line through the mutual feedback mechanism of sensors and data acquisition models.

8. A computer device comprising a memory and a processor, wherein the memory stores a computer program, wherein: When the processor executes the computer program, the steps of the process regulation and control method based on production line co-production described in any one of claims 1 to 6 are implemented.

9. A computer-readable storage medium having a computer program stored thereon, characterized in that: When the computer program is executed by a processor, the steps of the process regulation and control method based on production line co-production according to any one of claims 1 to 6 are implemented.

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