CN117548053B - Adjustable reaction kettle, control method thereof and related equipment - Google Patents
Adjustable reaction kettle, control method thereof and related equipment Download PDFInfo
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 158
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- 238000012544 monitoring process Methods 0.000 claims abstract description 25
- 238000003756 stirring Methods 0.000 claims abstract description 25
- 238000011217 control strategy Methods 0.000 claims description 39
- 238000004364 calculation method Methods 0.000 claims description 25
- 238000004590 computer program Methods 0.000 claims description 14
- 238000007781 pre-processing Methods 0.000 claims description 14
- 238000003860 storage Methods 0.000 claims description 8
- 238000013500 data storage Methods 0.000 claims description 7
- 238000005070 sampling Methods 0.000 claims description 5
- 230000004044 response Effects 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 5
- 238000006555 catalytic reaction Methods 0.000 abstract description 4
- 230000001276 controlling effect Effects 0.000 description 9
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- 230000002159 abnormal effect Effects 0.000 description 4
- 238000013461 design Methods 0.000 description 4
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
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- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D27/00—Simultaneous control of variables covered by two or more of main groups G05D1/00 - G05D25/00
- G05D27/02—Simultaneous control of variables covered by two or more of main groups G05D1/00 - G05D25/00 characterised by the use of electric means
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
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Abstract
The application relates to an adjustable reaction kettle, a control method thereof and related equipment, wherein the adjustable reaction kettle comprises a kettle body, a stirring assembly, a temperature control assembly, an air pressure assembly and an adjusting control system, wherein the stirring assembly is arranged on the kettle body, and the temperature control assembly and the air pressure assembly are communicated with the kettle body; the stirring assembly, the temperature control assembly and the air pressure assembly are electrically connected with the adjusting and controlling system; the stirring assembly is used for stirring reactants in the kettle body; the temperature control component is used for monitoring and adjusting the temperature in the kettle body; the air pressure component is used for monitoring and adjusting the air pressure in the kettle body; the adjusting and controlling system is used for controlling the stirring assembly, the temperature control assembly and the air pressure assembly to work. The application has the effect of improving the reaction catalysis of the reaction kettle.
Description
Technical Field
The application relates to the technical field of chemical engineering, in particular to an adjustable reaction kettle, a control method thereof and related equipment.
Background
The reactor typically consists of a reaction vessel, which is a sealed vessel, for containing reactants and catalyst. The reaction vessel is typically made of a high temperature, corrosion resistant material (e.g., stainless steel) to ensure the safety and durability of the reaction.
In the prior art, when the reaction kettle is used, the reactants are added into the reaction kettle to be stirred according to the proportion of the reactants, so that the reactants added into the reaction kettle react to form a required composition, or the reactants are catalyzed.
With respect to the related art in the above, there are the following drawbacks: in the reaction process, the temperature in the reaction kettle is possibly changed along with the progress of the reaction, so that the reaction efficiency is reduced, and the reaction catalysis effect of the reaction kettle is reduced.
Disclosure of Invention
In order to improve the reaction catalysis effect of the reaction kettle, the application provides an adjustable reaction kettle, a control method thereof and related equipment.
In a first aspect, the above object of the present application is achieved by the following technical solutions:
an adjustable reaction kettle control method comprises the following steps:
acquiring type data of reactants, and inputting the type data into a preset reactant database;
the reactant database matches the optimal reaction parameters of the reaction kettle corresponding to the reactant according to the type data of the reactant, and sets an optimal reaction threshold according to the optimal reaction parameters of the reaction kettle;
generating an adjustment control strategy according to the optimal reaction threshold by a preset adjustment control strategy model;
the temperature control component and the air pressure component execute control commands according to a strategy.
By adopting the technical scheme, the key parameters in the reaction process can be monitored in real time by acquiring and processing the reaction parameter data, and accurate reaction state information is provided; the control strategy is designed based on the processed reaction parameter data, so that an execution component of the reaction kettle can be accurately regulated, and the accurate control of the reaction process is realized; the stability of the reaction can be improved and the influence of fluctuation and instability factors can be reduced by controlling the design and execution of the strategy; the method adopts an automatic control mode, reduces the requirement of manual operation, and reduces the workload of operators and the risk of human errors.
The present application may be further configured in a preferred example to: the step of generating the regulation control strategy according to the optimal reaction parameters of the reaction kettle comprises the following steps:
acquiring real-time parameter data of the reaction kettle, and inputting the real-time parameter data into a preset monitoring model;
comparing the parameters of the real-time parameter data with the optimal response threshold value, and judging whether an adjustment control strategy is needed to be generated;
if the parameters in the real-time parameter data exceed the optimal reaction threshold, an adjustment control strategy needs to be generated.
By adopting the technical scheme, whether an adjustment control strategy is needed to be generated or not is judged by comparing the parameters of the real-time parameter data with the optimal reaction threshold value, and the adjustment is timely carried out on the reaction kettle, so that the reaction catalysis effect of the reaction kettle is optimized.
The present application may be further configured in a preferred example to: after the step of generating the adjustment control strategy when the real-time parameter exceeds the optimal reaction threshold, the method comprises the following steps:
inputting the real-time parameter data into a preset adjustment calculation model;
the adjustment calculation model calculates a parameter adjustment value based on the real-time parameter data and the optimal reaction threshold;
an adjustment control strategy is generated based on the parameter adjustment value.
By adopting the technical scheme, the control strategy is designed based on the processed reaction parameter data, the execution component of the reaction kettle can be accurately regulated, and the accurate control of the reaction process is realized.
The present application may be further configured in a preferred example to: the method comprises the following steps of:
preprocessing the acquired real-time parameter data;
and carrying out data sampling on the obtained reaction parameter data.
By adopting the technical scheme, the interference of noise and abnormal values on a control algorithm is reduced; the data volume and the demand of calculation resources are reduced, and the calculation efficiency is improved; key characteristics in the reaction process are captured, and a basis is provided for the design of a control strategy and the judgment of the reaction state.
In a second aspect, the above object of the present application is achieved by the following technical solutions:
the adjustable reaction kettle comprises a kettle body, a stirring assembly, a temperature control assembly, an air pressure assembly and an adjusting control system, wherein the stirring assembly is arranged on the kettle body, and the temperature control assembly and the air pressure assembly are communicated with the kettle body; the stirring assembly, the temperature control assembly and the air pressure assembly are electrically connected with the adjusting and controlling system;
the stirring assembly is used for stirring reactants in the kettle body;
the temperature control component is used for monitoring and adjusting the temperature in the kettle body;
the air pressure component is used for monitoring and adjusting the air pressure in the kettle body;
the adjusting and controlling system is used for controlling the stirring assembly, the temperature control assembly and the air pressure assembly to work.
Optionally, the regulation control system comprises a reactant data storage module and a regulation control strategy generation module; the reactant data storage module is used for presetting a reactant database; the adjustment control strategy generation module is used for presetting an adjustment control strategy model.
Optionally, the adjusting control system further comprises a monitoring module, an adjusting calculation module and a data preprocessing module, wherein the monitoring module is used for presetting a monitoring model; the adjusting calculation module is used for presetting an adjusting calculation model; the data preprocessing module is used for preprocessing data.
In a third aspect, the above object of the present application is achieved by the following technical solutions:
an electronic device comprising a memory, a processor and a computer program stored in the memory and executable on the processor, wherein the processor implements the steps of the above-mentioned adjustable reactor control method when executing the computer program.
The fourth object of the present application is achieved by the following technical solutions:
a computer readable storage medium storing a computer program which when executed by a processor performs the steps of a method of controlling an adjustable reactor as described above.
In summary, the present application includes at least one of the following beneficial technical effects:
1. by acquiring and processing the reaction parameter data, key parameters in the reaction process can be monitored in real time, and accurate reaction state information is provided; the control strategy is designed based on the processed reaction parameter data, so that an execution component of the reaction kettle can be accurately regulated, and the accurate control of the reaction process is realized; the stability of the reaction can be improved and the influence of fluctuation and instability factors can be reduced by controlling the design and execution of the strategy;
2. the method adopts an automatic control mode, reduces the requirement of manual operation, and reduces the workload of operators and the risk of human errors;
3. providing more stable reaction parameter data, and reducing the interference of noise and abnormal values to a control algorithm; the data volume and the demand of calculation resources are reduced, and the calculation efficiency is improved; key characteristics in the reaction process are captured, and a basis is provided for the design of a control strategy and the judgment of the reaction state.
Drawings
FIG. 1 is a schematic flow chart of the steps of an adjustable reactor control method of the present application;
FIG. 2 is a schematic flow chart of the step S30 in the control method of the adjustable reaction kettle;
FIG. 3 is a schematic flow chart of step S31 in an adjustable reactor control method according to the present application;
FIG. 4 is a schematic flow chart of the adjustable reactor control method according to the present application after step S32;
FIG. 5 is a schematic view of a structural module of an adjustable reactor of the present application;
FIG. 6 is a block diagram of the electronic device of the present application;
reference numerals illustrate:
1. a stirring assembly; 2. a temperature control assembly; 3. a pneumatic assembly; 4. adjusting a control system; 41. a reactant data storage module; 42. a regulation control strategy generation module; 43. a monitoring module; 44. an adjustment calculation module; 45. and a data preprocessing module.
Detailed Description
The present application is described in further detail below with reference to the accompanying drawings.
In one embodiment, as shown in fig. 1-4, the application discloses an adjustable reaction kettle control method, which specifically comprises the following steps:
an adjustable reaction kettle control method comprises the following steps:
s10: acquiring type data of reactants, and inputting the type data into a preset reactant database;
specifically, the type of the reactant is selected by a worker, the type data of the reactant is input to the reaction kettle, the system receives the type data of the reactant selected by the worker, and the type data of the reactant is input to a preset reactant database.
S20: the reactant database matches the optimal reaction parameters of the reaction kettle corresponding to the reactant according to the type data of the reactant, and sets an optimal reaction threshold according to the optimal reaction parameters of the reaction kettle;
the preset reactant database is provided with optimal reaction parameters of the reaction kettle, the optimal reaction parameters of the reaction kettle in the reactant database correspond to different types of reactants, namely, the optimal reaction parameters of different reactants in the reaction kettle, and in the embodiment of the application, the optimal reaction parameters comprise basic values and values optimized after self-learning through big data, wherein the basic values are set based on reaction rules.
The optimal reaction parameters of the reaction kettle comprise an optimal reaction temperature, an optimal reaction air pressure and an optimal reaction ph value, the optimal reaction parameters of the reaction kettle are fixed values, a section threshold value is set according to the fixed values of the optimal reaction parameters of the reaction kettle, and the set section threshold value is used as the optimal reaction threshold value.
S30: generating an adjustment control strategy according to the optimal reaction threshold by a preset adjustment control strategy model;
s40: the temperature control component and the air pressure component execute control commands according to a strategy.
At S30: the step of generating the regulation control strategy according to the optimal reaction parameters of the reaction kettle comprises the following steps:
s31, acquiring real-time parameter data of the reaction kettle, and inputting the real-time parameter data into a preset monitoring model;
and analyzing real-time parameter data of the reaction kettle by a monitoring model, wherein the monitoring model analyzes the reaction temperature, the reaction air pressure and the reaction ph value in the real-time parameter data.
S32, comparing the parameters of the real-time parameter data with the optimal response threshold value, and judging whether an adjustment control strategy is needed to be generated;
specifically, the parameters of the real-time parameter data are compared with the optimal reaction threshold, and whether the parameters of the real-time parameter data are located in the optimal reaction threshold or not is judged, namely whether the reaction temperature, the reaction air pressure and the reaction ph value are located in the optimal reaction threshold or not is judged.
S33, if the parameters in the real-time parameter data exceed the optimal response threshold, an adjustment control strategy is needed to be generated;
specifically, if the reaction temperature, the reaction air pressure and the reaction ph value are not located at the optimal reaction threshold, that is, the reaction state corresponding to the parameters in the real-time parameter data is not located at the optimal reaction state.
At S31: the method comprises the steps of obtaining real-time parameter data of the reaction kettle, and inputting the real-time parameter data into a preset monitoring model, wherein the method comprises the following steps of:
s311: preprocessing the acquired real-time parameter data;
specifically, preprocessing is performed on the obtained real-time parameter data to improve accuracy and stability of the data, and noise and abnormal values in the obtained real-time parameter data are values of abrupt change of the data values and are automatically removed, because in an actual production process, temperature, air pressure and ph values in a kettle body are difficult to abrupt change, specifically, among more than three continuous data values, parameter values in the middle are difficult to abrupt change in order of time stamps, and whether the values are abnormal values is judged.
S312: sampling the obtained reaction parameter data;
specifically, in the embodiment of the present application, data sampling refers to sampling acquired reaction parameter data to reduce data volume and increase calculation speed; feature extraction is also included in embodiments of the present application,
feature extraction refers to extracting key features from the processed reaction parameter data, such as the rate of change of temperature, the rate of change of ph, the degree of fluctuation of pressure, and the like.
After the step of generating the adjustment control strategy if the real-time parameter exceeds the optimal reaction threshold in S32, the method comprises the following steps:
s321: inputting the real-time parameter data into a preset adjustment calculation model;
specifically, the parameters of the real-time parameter data are compared with the optimal reaction threshold by adjusting the calculation model, and whether the parameters of the real-time parameter data are located in the optimal reaction threshold or not is judged, namely whether the reaction temperature, the reaction air pressure and the reaction ph value are located in the optimal reaction threshold or not is judged.
S322: the adjustment calculation model calculates a parameter adjustment value based on the real-time parameter data and the optimal reaction threshold;
specifically, the adjustment calculation model carries out differential transportation on the parameters of the real-time parameter data and the optimal reaction parameters of the reaction kettle, calculates the differential value of the parameters to be adjusted, synthesizes the volume, the temperature, the ph value and the air pressure of reactants in the reaction kettle, and carries out comprehensive adjustment to generate parameter adjustment values, namely specific temperature differential value, ph differential value and air pressure differential value to be adjusted.
S323: generating an adjustment control strategy based on the parameter adjustment value;
in the regulation calculation model, subtracting the parameter of the real-time parameter data from the optimal parameter value of the reaction kettle, and determining the specific control during regulation positively and negatively, taking the temperature as an example, if the temperature value of the optimal reaction parameter of the reaction kettle is larger than the temperature of the real-time parameter data, the result of the difference calculation is a positive number, and the optimal temperature is larger than the real-time temperature, and then, the temperature rise control is performed; otherwise, the optimal temperature is smaller than the real-time temperature, and the temperature is reduced at the moment.
It should be understood that the sequence number of each step in the foregoing embodiment does not mean that the execution sequence of each process should be determined by the function and the internal logic of each process, and should not limit the implementation process of the embodiment of the present application in any way.
In one embodiment, an adjustable reaction kettle is provided, and the adjustable reaction kettle corresponds to one of the adjustable reaction kettle control methods in the above embodiment. As shown in fig. 5, the adjustable reaction kettle comprises a kettle body, a stirring assembly 1, a temperature control assembly 2, an air pressure assembly 3 and an adjusting control system 4, wherein the stirring assembly 1 is arranged on the kettle body, and the temperature control assembly 2 and the air pressure assembly 3 are communicated with the kettle body; the stirring assembly 1, the temperature control assembly 2 and the air pressure assembly 3 are electrically connected with the adjusting and controlling system 4;
the stirring assembly 1 is used for stirring reactants in the kettle body;
the temperature control assembly 2 is used for monitoring and adjusting the temperature in the kettle body;
the air pressure component 3 is used for monitoring and adjusting the air pressure in the kettle body;
the adjusting and controlling system 4 is used for controlling the stirring assembly 1, the temperature control assembly 2 and the air pressure assembly 3 to work.
Wherein the regulatory control system 4 comprises a reactant data storage module 41 and a regulatory control strategy generation module 42; the reactant data storage module 41 is used for presetting a reactant database; the adjustment control strategy generation module 42 is configured to preset an adjustment control strategy model, the adjustment control system 4 further includes a monitoring module 43, an adjustment calculation module 44, and a data preprocessing module 45, where the monitoring module 43 is configured to preset a monitoring model; the adjustment calculation module 44 is configured to preset an adjustment calculation model; the data preprocessing module 45 is used for preprocessing data.
For specific limitations of an adjustable reactor, reference is made to the above limitations of an adjustable reactor control method, and no further description is given here. Each module in the adjustable reaction kettle can be fully or partially realized by software, hardware and a combination thereof. The above modules may be embedded in hardware or independent of a processor in the electronic device, or may be stored in software in a memory in the electronic device, so that the processor may call and execute operations corresponding to the above modules.
In one embodiment, an electronic device is provided, which may be a server, and the internal structure of which may be as shown in fig. 6. The electronic device includes a processor, a memory, a network interface, and a database connected by a system bus. Wherein the processor of the electronic device is configured to provide computing and control capabilities. The memory of the electronic device includes a nonvolatile storage medium and an internal memory. The non-volatile storage medium stores an operating system, computer programs, and a database. The internal memory provides an environment for the operation of the operating system and computer programs in the non-volatile storage media. The network interface of the electronic device is used for communicating with an external terminal through a network connection. The computer program when executed by the processor is used for realizing an adjustable reaction kettle control method.
In one embodiment, an electronic device is provided that includes a memory, a processor, and a computer program stored on the memory and executable on the processor, the processor implementing the following steps when executing the computer program:
acquiring type data of reactants, and inputting the type data into a preset reactant database;
the reactant database matches the optimal reaction parameters of the reaction kettle corresponding to the reactant according to the type data of the reactant, and sets an optimal reaction threshold according to the optimal reaction parameters of the reaction kettle;
generating an adjustment control strategy according to the optimal reaction threshold by a preset adjustment control strategy model;
the temperature control component and the air pressure component execute control commands according to a strategy.
In one embodiment, a computer readable storage medium is provided having a computer program stored thereon, which when executed by a processor, performs the steps of:
acquiring type data of reactants, and inputting the type data into a preset reactant database;
the reactant database matches the optimal reaction parameters of the reaction kettle corresponding to the reactant according to the type data of the reactant, and sets an optimal reaction threshold according to the optimal reaction parameters of the reaction kettle;
generating an adjustment control strategy according to the optimal reaction threshold by a preset adjustment control strategy model;
the temperature control component and the air pressure component execute control commands according to a strategy.
Those skilled in the art will appreciate that implementing all or part of the above described methods may be accomplished by way of a computer program stored on a non-transitory computer readable storage medium, which when executed, may comprise the steps of the embodiments of the methods described above. Any reference to memory, storage, database, or other medium used in the various embodiments provided herein may include non-volatile and/or volatile memory. The nonvolatile memory can include Read Only Memory (ROM), programmable ROM (PROM), electrically Programmable ROM (EPROM), electrically Erasable Programmable ROM (EEPROM), or flash memory. Volatile memory can include Random Access Memory (RAM) or external cache memory. By way of illustration and not limitation, RAM is available in a variety of forms such as Static RAM (SRAM), dynamic RAM (DRAM), synchronous DRAM (SDRAM), double Data Rate SDRAM (DDRSDRAM), enhanced SDRAM (ESDRAM), synchronous Link DRAM (SLDRAM), memory bus direct RAM (RDRAM), direct memory bus dynamic RAM (DRDRAM), and memory bus dynamic RAM (RDRAM), among others.
It will be apparent to those skilled in the art that, for convenience and brevity of description, only the above-described division of the functional units and modules is illustrated, and in practical application, the above-described functional distribution may be performed by different functional units and modules according to needs, i.e. the internal structure of the apparatus is divided into different functional units or modules to perform all or part of the above-described functions.
The above embodiments are only for illustrating the technical solution of the present application, and are not limiting; although the present application has been described in detail with reference to the foregoing embodiments, it should be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit and scope of the technical solutions of the embodiments of the present application, and are intended to be included in the scope of the present application.
Claims (6)
1. An adjustable reaction kettle control method is characterized in that: the method comprises the following steps:
acquiring type data of reactants, and inputting the type data into a preset reactant database;
matching a preset reactant matching model with optimal reaction parameters of a reaction kettle corresponding to the reactant according to the type data of the reactant in the reactant database, and setting an optimal reaction threshold according to the optimal reaction parameters of the reaction kettle;
the preset regulation control strategy model generates a regulation control strategy according to the optimal reaction threshold, and the method comprises the following steps:
acquiring real-time parameter data of the reaction kettle, and inputting the real-time parameter data into a preset monitoring model;
comparing the parameters of the real-time parameter data with the optimal response threshold by using a preset monitoring model, and judging whether an adjustment control strategy needs to be generated or not;
if the parameters in the real-time parameter data exceed the optimal reaction threshold, generating an adjustment control strategy;
inputting the real-time parameter data into a preset adjustment calculation model, wherein the method comprises the following steps of:
preprocessing the acquired real-time parameter data;
carrying out data sampling on the preprocessed real-time parameter data;
the adjustment calculation model calculates a parameter adjustment value based on the real-time parameter data and the optimal reaction threshold;
generating an adjustment control strategy based on the parameter adjustment value;
the temperature control component and the air pressure component execute control commands according to a strategy.
2. An adjustable reaction kettle, which is characterized in that: the adjustable reaction kettle control method applied to the claim 1 comprises a kettle body, a stirring assembly (1), a temperature control assembly (2), a pneumatic assembly (3) and an adjusting control system (4), wherein the stirring assembly (1) is arranged in the kettle body, and the temperature control assembly (2) and the pneumatic assembly (3) are communicated with the kettle body; the stirring assembly (1), the temperature control assembly (2) and the air pressure assembly (3) are electrically connected with the adjusting and controlling system (4); the stirring assembly (1) is used for stirring reactants in the kettle body; the temperature control component (2) is used for monitoring and adjusting the temperature in the kettle body; the air pressure component (3) is used for monitoring and adjusting the air pressure in the kettle body; the adjusting control system (4) is used for controlling the stirring assembly (1), the temperature control assembly (2) and the air pressure assembly (3) to work.
3. An adjustable reactor according to claim 2, wherein: the regulation control system (4) comprises a reactant data storage module (41) and a regulation control strategy generation module (42), wherein the reactant data storage module (41) is used for presetting a reactant database; the regulation control strategy generation module (42) is used for presetting a regulation control strategy model.
4. An adjustable reactor according to claim 3, wherein: the regulation control system (4) further comprises a monitoring module (43), a regulation calculation module (44) and a data preprocessing module (45), wherein the monitoring module (43) is used for presetting a monitoring model; the adjustment calculation module (44) is used for presetting an adjustment calculation model; the data preprocessing module (45) is used for preprocessing data.
5. An electronic device comprising 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 steps of a method for controlling an adjustable reactor according to claim 1.
6. A computer readable storage medium storing a computer program, characterized in that the computer program when executed by a processor implements the steps of a method for controlling an adjustable reactor according to claim 1.
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