Control method, system and equipment of reaction tower and medium

Abstract

The invention provides a control method, system and equipment of a reaction tower and a medium, and relates to the technical field of reaction towers. The target reaction parameters comprise an introduction parameter of a target reactant, an external temperature of a target reaction tower, an internal temperature of the target reaction tower, a thickness of a thermal insulation layer of the target reaction tower, a thermal insulation coefficient of the thermal insulation layer of the target reaction tower, a reaction space of the target reaction tower and a conversion rate of a target reaction; the target reaction parameters are input into a reaction tower control parameter model, reaction tower prediction control parameters are obtained, and the reaction tower control parameter model is obtained based on training of the sample reaction parameters and the reaction tower sample control parameters. According to the method, the steam introduction amount of the reaction tower can be set.

Description

Technical Field

[0001] The present application relates to the technical field of reaction towers, and in particular to a control method, system, equipment and medium for a reaction tower. Background Art

[0002] A reaction tower is a device used to hold reactants and conduct chemical reactions during chemical reactions. In chemical reactions, the temperature in the reaction tower is an important factor affecting the conversion rate of reactants. In order to increase the conversion rate of reactants, the temperature of the reaction tower needs to be controlled within a suitable range. Usually, the temperature of the reaction tower is increased by introducing steam into the reaction tower. The higher the amount of steam introduced, the higher the temperature in the reaction tower.

[0003] In the prior art, the amount of steam introduced is set manually, but the manual setting method mainly relies on subjective experience, which makes it difficult to maintain the temperature in the reaction tower within an appropriate range. If too much steam is introduced, the temperature in the reaction tower exceeds the appropriate range. If too little steam is introduced, the temperature in the reaction tower does not reach the appropriate range, thereby affecting the chemical reaction rate of the reaction. Summary of the invention

[0004] The purpose of the present application is to address the above problems and to provide a control method, system, equipment and medium for a reaction tower, which can improve the chemical reaction rate in the reaction tower to a certain extent.

[0005] In a first aspect, the present application provides a control method for a reaction tower, comprising: Obtaining target reaction parameters, the target reaction parameters including the target reactant feed parameters, the target reaction tower external temperature, the target reaction tower internal temperature, the target reaction tower insulation layer thickness, the target reaction tower insulation layer insulation coefficient, the target reaction tower reaction space and the target reaction conversion rate; Inputting the target reaction parameters into a reaction tower control parameter model to obtain reaction tower prediction control parameters, the reaction tower prediction control parameters include prediction parameters for steam introduction and prediction parameters for reactants, wherein the reaction tower control parameter model is trained based on sample reaction parameters and reaction tower sample control parameters, the sample reaction parameters include sample reactant introduction parameters, sample reaction tower external temperature, sample reaction tower internal temperature, sample reaction tower insulation layer thickness, sample reaction tower insulation layer insulation coefficient, sample reaction tower reaction space and sample reaction conversion rate, the reaction tower sample control parameters include sample steam introduction parameters and reactant introduction parameters; The target reaction tower is controlled according to the predicted introduction parameters of the steam and the predicted introduction parameters of the reactants.

[0006] In some possible implementations, the method further includes: Determine the predicted steam flow rate sequence according to the predicted steam flow rate parameters, and determine the predicted reactant flow rate sequence according to the predicted reactant flow rate parameters, wherein the predicted flow rate sequence includes a plurality of consecutive predicted time points and the predicted flow rate value corresponding to each predicted time point; Acquire the actual flow rate sequence of the steam, and acquire the actual flow rate sequence of the reactant, wherein the actual flow rate sequence includes a plurality of consecutive actual time points and a predicted flow rate value corresponding to each actual time point; Comparing the predicted flow rate of the steam with the actual flow rate of the steam in real time to obtain a first comparison result, and comparing the predicted flow rate of the reactant with the actual flow rate of the reactant to obtain a second comparison result; If the first comparison result and / or the second comparison result are inconsistent, a first prompt message is generated, wherein the first prompt message is used to prompt adjustment of the actual flow rate of the steam and / or the actual flow rate of the reactant.

[0007] In some possible implementations, the method further includes: Obtaining a product of the target reaction tower reaction; If the purity of the product is lower than a preset threshold, a second prompt information is generated, and the second prompt information is used to prompt to update the reaction tower control parameter model.

[0008] In some possible implementations, the predicted input parameters of the reactant include the predicted concentration of the reactant, the predicted pressure of the reactant, and the predicted flow rate of the reactant, and the sample input parameters of the reactant include the sample concentration of the reactant, the sample pressure of the reactant, and the sample flow rate of the reactant.

[0009] In some possible implementations, the target reaction tower internal temperature includes a target reaction tower inner wall temperature and a target reaction tower internal hollow region temperature.

[0010] In a second aspect, the present application provides a control system for a reaction tower, comprising: An acquisition module is used to acquire target reaction parameters, wherein the target reaction parameters include the input parameters of the target reactant, the external temperature of the target reaction tower, the internal temperature of the target reaction tower, the thickness of the insulation layer of the target reaction tower, the insulation coefficient of the insulation layer of the target reaction tower, the reaction space of the target reaction tower, and the conversion rate of the target reaction; A prediction module, used for inputting the target reaction parameters into a reaction tower control parameter model to obtain reaction tower prediction control parameters, wherein the reaction tower prediction control parameters include prediction input parameters of steam and prediction input parameters of reactants, wherein the reaction tower control parameter model is trained based on sample reaction parameters and reaction tower sample control parameters, wherein the sample reaction parameters include input parameters of sample reactants, sample reaction tower external temperature, sample reaction tower internal temperature, sample reaction tower insulation layer thickness, sample reaction tower insulation layer insulation coefficient, sample reaction tower reaction space and sample reaction conversion rate, and the reaction tower sample control parameters include sample steam input parameters and sample reactant input parameters; A control module is used to control the target reaction tower according to the predicted introduction parameters of the steam and the predicted introduction parameters of the reactants.

[0011] In some possible implementations, the system also includes a monitoring module, which is used to determine a predicted steam input flow sequence based on the predicted steam input parameters, and determine a predicted input flow sequence of the reactant based on the predicted input parameters of the reactant; obtain the actual steam input flow sequence, and obtain the actual input flow sequence of the reactant; compare the predicted steam input flow value and the actual steam input flow value in real time to obtain a first comparison result, and compare the predicted input flow value of the reactant with the actual input flow value of the reactant to obtain a second comparison result; if the first comparison result and / or the second comparison result are inconsistent, generate a first prompt message, and the first prompt message is used to prompt the adjustment of the actual steam input flow value and / or the actual input flow value of the reactant.

[0012] In some possible implementations, the system also includes an update module, which is used to obtain the product of the target reaction tower reaction; if the purity of the product is lower than a preset threshold, a second prompt information is generated, and the second prompt information is used to prompt the update of the reaction tower control parameter model.

[0013] In some possible implementations, the predicted input parameters of the reactant include the predicted concentration of the reactant, the predicted pressure of the reactant, and the predicted flow rate of the reactant, and the sample input parameters of the reactant include the sample concentration of the reactant, the sample pressure of the reactant, and the sample flow rate of the reactant.

[0014] In some possible implementations, the target reaction tower internal temperature includes a target reaction tower inner wall temperature and a target reaction tower internal hollow region temperature.

[0015] In a third aspect, the present application provides 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 method described above when executing the computer program.

[0016] In a fourth aspect, the present application provides a computer-readable storage medium having a computer program stored thereon, and the computer program implements the method described above when executed by a processor.

[0017] Compared with the prior art, the beneficial effects of the present application are as follows: first, sample reaction parameters and reaction tower sample control parameters are obtained to train the initial reaction tower control parameter model to obtain a reaction tower control parameter model, then the target reaction parameters are input into the reaction tower control parameter model to obtain the reaction tower prediction control parameters, and finally the reaction tower is controlled according to the reaction tower prediction control parameters, wherein the reaction tower prediction control parameters include the prediction of steam input parameters and the prediction of reactant input parameters, the target reaction parameters include the target reactant input parameters, the target reaction tower external temperature, the target reaction tower internal temperature, the target reaction tower insulation layer thickness, the insulation coefficient of the target reaction tower insulation layer, the reaction space of the target reaction tower and the conversion rate of the target reaction, and these parameters have been proven in practice to have a great influence on the amount of steam input into the reaction tower and the amount of reactant input, so these parameters can be used as influencing factors, and the present application directly obtains the prediction of steam input parameters and the prediction of reactant input parameters through the reaction tower control parameter model, and this method controls the temperature of the reaction tower within a suitable range while obtaining an accurate steam input, reduces dependence on experienced personnel, and improves the chemical reaction rate.

[0018] It should be understood that the description of technical features, technical solutions, beneficial effects or similar language in this application does not imply that all features and advantages can be realized in any single embodiment. On the contrary, it is understood that the description of features or beneficial effects means that specific technical features, technical solutions or beneficial effects are included in at least one embodiment. Therefore, the description of technical features, technical solutions or beneficial effects in this specification does not necessarily refer to the same embodiment. Furthermore, the technical features, technical solutions and beneficial effects described in the present embodiment can also be combined in any appropriate manner. Those skilled in the art will understand that the embodiment can be realized without one or more specific technical features, technical solutions or beneficial effects of a specific embodiment. In other embodiments, additional technical features and beneficial effects can also be identified in a specific embodiment that does not embody all embodiments. BRIEF DESCRIPTION OF THE DRAWINGS

[0019] In order to more clearly illustrate the technical solution in this embodiment, the drawings required for use in the description of the embodiment will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present application. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative work.

[0020] Figure 1 A flow chart of a control method for a reaction tower provided in an embodiment of the present application; Figure 2 A flowchart of a model training method provided in an embodiment of the present application; Figure 3 A schematic diagram of a control system of a reaction tower provided in an embodiment of the present application; Figure 4 A schematic diagram of the structure of a computing device provided in an embodiment of the present application. DETAILED DESCRIPTION

[0021] In order to enable those skilled in the art to better understand the technical solution of the present application, the technical solution in the embodiments of the present application will be clearly and completely described below in conjunction with the accompanying drawings. The description in this section is only exemplary and explanatory and should not have any limiting effect on the protection scope of the present application. Specifically, the described embodiments are only embodiments of a part of the present application, not all embodiments. Based on the embodiments in the present application, all other embodiments obtained by ordinary technicians in the field without making creative work should fall within the scope of protection of the present application.

[0022] It should be noted that similar reference numerals and letters represent similar items in the following figures, so once an item is defined in one figure, it does not need to be further defined and explained in subsequent figures. In addition, the terms "including" and "having" and any variations thereof are intended to cover non-exclusive inclusions, for example, a process, method, system, product or device that includes a series of steps or units is not necessarily limited to those steps or units clearly listed, but may include other steps or units that are not clearly listed or inherent to these processes, methods, products or devices.

[0023] In order to facilitate the understanding of this application, a brief introduction to the related technology is first given: A reaction tower is a vertical cylindrical device used to hold solutions or gases for chemical reactions. The tower body of the reaction tower is a multi-layer structure. The inner layer is in contact with the medium and is made of corrosion-resistant, high-temperature-resistant and high-pressure-resistant composite steel plates. The outer layer is made of pressure vessel steel plates. In order to maintain the temperature required for the chemical reaction, an insulation layer is provided between the inner and outer layers. Different insulation materials have different insulation effects. Usually, the temperature of the reaction tower is increased by introducing steam into the reaction tower. The higher the amount of steam introduced, the higher the temperature in the reaction tower.

[0024] The setting of steam input currently relies on the subjective experience and intuition of operators. However, since the chemical reaction process is inevitably accompanied by heat absorption and heat release, it is difficult to maintain the temperature in the reaction tower continuously and stably within the ideal range. In actual operation, the steam input is often excessive or insufficient, which affects the chemical reaction rate. For example, the temperature of the reaction tower is set to 80C°-90C°. Under normal circumstances, the steam input in winter is much higher than that in summer, but since heat may be released in the chemical reaction, a small amount of steam needs to be introduced instead.

[0025] In view of this, an embodiment of the present application provides a control method for a reaction tower, the method comprising: First, sample reaction parameters and reaction tower sample control parameters are obtained to train the initial reaction tower control parameter model to obtain the reaction tower control parameter model, and then the target reaction parameters are input into the reaction tower control parameter model to obtain the reaction tower prediction control parameters, and finally the reaction tower is controlled according to the reaction tower prediction control parameters, wherein the reaction tower prediction control parameters include the prediction of steam input parameters and the prediction of reactant input parameters, and the target reaction parameters include the target reactant input parameters, the target reaction tower external temperature, the target reaction tower internal temperature, the target reaction tower insulation layer thickness, the insulation coefficient of the target reaction tower insulation layer, the reaction space of the target reaction tower and the conversion rate of the target reaction. These parameters have been proven in practice to have a great influence on the amount of steam input to the reaction tower and the amount of reactant input, so these parameters can be used as influencing factors. The present application directly obtains the prediction of steam input parameters and the prediction of reactant input parameters through the reaction tower control parameter model. This method controls the temperature of the reaction tower within a suitable range while obtaining an accurate steam input, reduces dependence on experienced personnel, and improves the chemical reaction rate.

[0026] like Figure 1 As shown, the figure is a flow chart of a control method for a reaction tower provided in an embodiment of the present application, the method comprising: S101. Obtain target reaction parameters.

[0027] Reaction refers to the chemical reaction carried out in the reaction tower. During this process, reactants need to be introduced into the reaction tower, and steam needs to be introduced to control the temperature of the reaction. Reaction parameters refer to the parameters that affect the amount of steam and reactants introduced during the chemical reaction. The amount of steam introduced affects the internal temperature of the reaction tower. Since the chemical reaction process is accompanied by endothermic and exothermic phenomena, the amount of reactant introduced also directly affects the internal temperature of the reaction tower. In order to control the temperature in the reaction tower within a certain range, it is necessary to control the amount of steam introduced and the amount of reactants introduced during the target chemical reaction. The target reaction parameters refer to the influencing factors of the amount of steam introduced and the amount of reactants introduced during the target chemical reaction.

[0028] The influencing factors of the steam input amount and the reactant input amount provided in the present application include the input parameters of the target reactant, the external temperature of the target reaction tower, the internal temperature of the target reaction tower, the thickness of the insulation layer of the target reaction tower, the insulation coefficient of the insulation layer of the target reaction tower, the reaction space of the target reaction tower and the conversion rate of the target reaction.

[0029] Among them, the introduction parameters of the target reactant include the concentration of the target reactant, the flow rate of the target reactant and the pressure of the target reactant. The target reactant refers to the substance participating in the target chemical reaction. The concentration of the reactant will affect the reaction rate, and then affect the amount of heat absorption and heat release of the chemical reaction. The greater the pressure of the reactant, the higher the concentration, which affects the reaction rate, and then affects the amount of heat absorption and heat release. The flow rate of the reactant also affects the reaction rate through the concentration, and then affects the amount of heat absorption and heat release. The introduction parameters of the target reactant are the influencing factors of the amount of steam introduced and the amount of reactant introduced.

[0030] The target external temperature of the reaction tower refers to the temperature of the environment around the reaction tower. In extremely cold or hot weather, the ambient temperature will affect the internal temperature of the reaction tower. For example, if the tower is not well insulated in winter, the internal temperature of the reaction tower may drop rapidly. To maintain the internal temperature of the reaction tower, more steam will be required. The target external temperature of the reaction tower is an influencing factor of the steam and reactant inputs.

[0031] In some embodiments, the target reaction tower internal temperature includes the target reaction tower inner wall temperature and the target reaction tower internal hollow area temperature. The inner wall refers to the inner layer structure of the reaction tower body in contact with the reactants, and the target reaction tower inner wall temperature refers to the temperature of the inner layer structure. In order to make the temperature of the inner wall of the reaction tower more accurate, the inner wall of the reaction tower can be divided into three parts: the upper part, the middle part, and the lower part, and the temperature of the upper part of the inner wall, the middle part of the inner wall, and the lower part of the inner wall is obtained. In actual operation, the inner wall can also be divided into finer areas, which is not limited in this application. The internal hollow area refers to the area where the reactants undergo chemical reactions. The internal hollow area can also be divided into areas, which will not be repeated here.

[0032] The inner wall is in direct contact with the reactants, and the chemical reaction takes place in the hollow area. Therefore, the inner wall temperature of the target reaction tower and the hollow area inside the target reaction tower are influencing factors of the amount of steam and reactants introduced.

[0033] The insulation layer refers to the structure between the inner layer and the outer layer of the reaction tower for insulation. The main function of the insulation layer is to reduce the loss of heat from the inside of the reaction tower to the external environment. When the thickness of the insulation layer increases, its thermal resistance also increases accordingly, thereby more effectively blocking the transfer of heat and maintaining the stability of the temperature inside the reaction tower. Therefore, the thickness of the insulation layer of the target reaction tower can be used as an influencing factor of the amount of steam and reactants introduced. The thickness of the insulation layer of the target reaction tower can also divide the insulation layer into regions, which will not be repeated here.

[0034] Different materials of the insulation layer have different insulation coefficients. The smaller the insulation coefficient, the better the insulation performance of the material. The insulation effect of the material is affected by the insulation coefficient of the insulation layer. Therefore, the insulation coefficient of the insulation layer of the target reaction tower is an influencing factor of the steam input amount and the reactant input amount.

[0035] For reactants of the same mass or molar amount, the smaller the reaction space of the reaction tower, the greater the concentration of the reactants in the reaction tower, the faster the rate of the chemical reaction, and the greater the amount of heat absorption and heat release. Therefore, the reaction space of the target reaction tower is an influencing factor of the amount of steam and reactants introduced.

[0036] The conversion rate of a reaction is the percentage of reactants converted into products. The higher the conversion rate, the higher the utilization rate of the reactants. For the same chemical reaction, the higher the utilization rate of the reactants, the greater the amount of heat absorbed and released during the chemical reaction. Therefore, the target reaction conversion rate is an influencing factor of the amount of steam input and the amount of reactants input.

[0037] The concentration of the target reactant, the flow rate of the target reactant, the pressure of the target reactant, the external temperature of the target reaction tower and the internal temperature of the target reaction tower are monitored and controlled by a distributed control system (DCS). DCS is an instrument control system used to monitor and control various parameters in industrial production processes.

[0038] S102, inputting the target reaction parameters into the reaction tower control parameter model to obtain the reaction tower prediction control parameters.

[0039] First, obtain the sample reaction parameters and the sample control parameters of the reaction tower, wherein the sample reaction parameters include the introduction parameters of the sample reactants, the external temperature of the sample reaction tower, the internal temperature of the sample reaction tower, the thickness of the insulation layer of the sample reaction tower, the insulation coefficient of the insulation layer of the sample reaction tower, the reaction space of the sample reaction tower and the conversion rate of the sample reaction; the sample control parameters of the reaction tower include the sample introduction parameters of steam and the sample introduction parameters of the reactants; the steam introduction amount and the reactant introduction control parameters determine the temperature range of the reaction tower.

[0040] Then, the sample reaction parameters and the reaction tower sample control parameters are used to train the initial reaction tower control parameter model to obtain the reaction tower control parameter model, which refers to a prediction model.

[0041] Finally, the target reaction parameters are input into the reaction tower control parameter model to obtain the reaction tower prediction control parameters. The reaction tower prediction control parameters are used to control the reaction tower. The reaction tower prediction control parameters include the predicted steam introduction parameters and the predicted reactant introduction parameters. The amount of steam introduction and the reactant introduction control parameters determine the temperature range inside the reaction tower.

[0042] In some embodiments, the predicted input parameters of the reactants are predicted by a reaction tower control parameter model, and the predicted input parameters of the reactants include the predicted concentration of the reactants, the predicted pressure of the reactants, and the predicted flow rate of the reactants. Similarly, the sample input parameters of the reactants include the sample concentration of the reactants, the sample pressure of the reactants, and the sample flow rate of the reactants.

[0043] In some embodiments, the target reaction parameters also include the reactant temperature of the target reaction. The reactant temperature refers to the temperature of the reactant before it participates in the reaction. The product of a chemical reaction may be the reactant of other chemical reactions. Therefore, the reactant temperature of the chemical reactions will be different. The target reactant temperature directly affects the amount of steam input and the amount of reactant input. Correspondingly, the sample reaction parameters also include the reactant temperature of the sample reaction.

[0044] S103, controlling the target reaction tower according to the predicted steam introduction parameters and the predicted reactant introduction parameters.

[0045] The predicted reactant introduction parameters, i.e., predicted reactant concentration, predicted reactant pressure and predicted reactant flow rate, are input into the distributed control system DCS to ensure that the target reaction tower can control the introduction of reactants according to the predicted reactant concentration, pressure and flow rate. At the same time, the introduction of steam is controlled according to the predicted steam introduction parameters, so that the target reaction tower can control the introduction of steam according to the predicted steam introduction parameters, thereby maintaining the temperature of the target reaction tower within an appropriate range.

[0046] In some embodiments, after controlling the reaction tower for a period of time according to the reaction tower prediction control parameter, the flow rates of steam and reactants in the reaction tower are monitored in real time to adjust the control of the reaction tower, wherein the predicted input flow sequence includes a plurality of consecutive predicted time points and a predicted input flow value corresponding to each predicted time point, and the actual input flow sequence includes a plurality of consecutive actual time points and a predicted input flow value corresponding to each actual time point, and the predicted input flow sequence A is set to: A=

[0047] in, represents the inflow flow value at the i-th prediction time point. The prediction time point can be selected at intervals of a few seconds, a few minutes, or a few hours, etc., and this application does not limit this. For example, Indicates the inflow flow value at the first prediction time point, It represents the inflow flow value at the second prediction time point, and so on.

[0048] The actual inflow flow sequence B is set as: B=

[0049] in, represents the inflow flow value at the jth actual time point. The actual time point can be selected at intervals of a few seconds, a few minutes, or a few hours, etc., and the present application does not limit this. It should be noted that the number of elements in the predicted inflow flow sequence A can be greater than that in the actual inflow flow sequence B. For example, Indicates the inflow flow value at the first actual time point, Indicates the inflow flow value at the second actual time point, and so on.

[0050] Specifically, firstly, the predicted steam flow rate sequence is determined according to the predicted steam flow rate parameters, and then the predicted reactant flow rate sequence is determined according to the predicted reactant flow rate parameters.

[0051] Then, the actual flow rate sequence of steam is obtained, and the actual flow rate sequence of reactants is obtained; The predicted steam flow rate and the actual steam flow rate are compared in real time to obtain a first comparison result, and the predicted reactant flow rate and the actual reactant flow rate are compared to obtain a second comparison result. For example, if the elements of the obtained actual flow rate sequence are b1-b6, then the elements are compared with the predicted flow rate sequence a1-a6. If the elements of the obtained actual flow rate sequence are b1-b6, then the predicted flow rate sequence a1-a6 is compared. 7，It is then compared with the predicted input flow sequence a1-a7; finally, as long as one of the first comparison result and the second comparison result is inconsistent, the user is prompted to make timely adjustments, that is, if the first comparison result and / or the second comparison result are inconsistent, a first prompt message is generated to prompt the user to adjust the actual input flow value of the steam and / or the actual input flow value of the reactant.

[0052] In some embodiments, the predicted input flow value of the x-th steam and the actual input flow value of the x-th steam are obtained, the predicted input flow value of the y-th reactant and the actual input flow value of the y-th reactant are obtained, the predicted input flow value of the x-th steam and the actual input flow value of the x-th steam are compared to obtain the x-th first difference between the predicted input flow value of the x-th steam and the actual input flow value of the x-th steam, the predicted input flow value of the y-th reactant and the actual input flow value of the y-th reactant are compared to obtain the y-th second difference, if the absolute value of the first difference is less than or equal to the first threshold value and / or the absolute value of the second difference is less than or equal to the second threshold value, then a first prompt message is generated for prompting adjustment of the actual input flow value of the steam and / or the actual input flow value of the reactant.

[0053] For example, the actual steam flow sequence is , the actual flow rate sequence of the reactants is , the predicted steam inlet flow sequence is , the predicted flow rate sequence of the reactants is , the first threshold is set to 5, the second threshold is set to 1, and each flow value in the actual steam flow sequence is compared with the corresponding value in the predicted steam flow sequence. It can be seen that each flow value in the actual steam flow sequence satisfies that the absolute value of the first difference is less than the first threshold. Specifically, ; Compare each flow value in the actual flow sequence of the reactant with the corresponding value in the predicted flow sequence of the reactant in turn, the first value in the actual flow sequence of the reactant satisfies that the absolute value of the second difference is less than the second threshold value, and the second value and the third value do not satisfy that the absolute value of the second difference is less than or equal to the second threshold value, specifically, 1, therefore, the first prompt information generated is: adjust the actual inlet flow value of the reactant.

[0054] In some embodiments, during the reaction or after the reaction is completed, in order to evaluate the accuracy of the reaction tower control parameter model so as to adjust and update the reaction tower control parameter model, the product of the target reaction tower is first obtained, and then the target reaction tower is controlled according to the predicted steam input parameters and the predicted reactant input parameters. If the purity of the product is lower than a preset threshold, a second prompt message is generated to prompt the reaction tower control parameter model to be updated. Specifically, the method for re-updating the reaction tower control parameter model may be to re-acquire the sample reaction parameters and the reaction tower control parameters to train and update the reaction tower control parameter model, thereby improving the accuracy of the reaction tower control parameter model.

[0055] In some embodiments, different chemical reactions require different reaction tower control parameter models.

[0056] In some embodiments, the internal temperature of the reaction tower is obtained. If the internal temperature of the reaction tower is not within a preset interval, a second prompt message is generated, and the second prompt message is used to adjust the steam supply or cool the reaction tower. The preset interval range includes a minimum value and a maximum value. If the temperature of the reaction tower exceeds the maximum value of the preset interval range, a prompt message for cooling the reaction tower is generated. If the temperature of the reaction tower is lower than the minimum value of the preset range, a prompt message for adjusting the steam supply is generated.

[0057] Combination of the above Figure 1 A control method for a reaction tower provided in an embodiment of the present application is introduced in detail. Hereinafter, a model training method, a control system, equipment and medium of a reaction tower provided in an embodiment of the present application will be introduced in conjunction with the accompanying drawings.

[0058] Figure 2 A flowchart of a model training method provided in an embodiment of the present application is shown in FIG. Figure 2 As shown, the method includes: S201. Obtain sample reaction parameters and reaction tower sample control parameters.

[0059] The sample reaction parameters include the sample reactant introduction parameters, the sample reaction tower external temperature, the sample reaction tower internal temperature, the sample reaction tower insulation layer thickness, the sample reaction tower insulation layer insulation coefficient, the sample reaction tower reaction space and the sample reaction conversion rate.

[0060] S202: training an initial reaction tower control parameter model using sample reaction parameters and reaction tower sample control parameters to obtain a reaction tower control parameter model.

[0061] The reaction tower control parameter model is used to predict the reaction tower prediction control parameters corresponding to the target reaction parameters.

[0062] The specific training process of a model training method provided in an embodiment of the present application has been described in detail in the aforementioned embodiments and will not be repeated here for the sake of brevity.

[0063] Figure 3 A control system for a reaction tower provided in an embodiment of the present application, such as Figure 3 As shown, this figure is a schematic diagram of a control system of a reaction tower provided by the present application, and the system includes: An acquisition module 301 is used to acquire target reaction parameters, wherein the target reaction parameters include the input parameters of the target reactant, the external temperature of the target reaction tower, the internal temperature of the target reaction tower, the thickness of the insulation layer of the target reaction tower, the insulation coefficient of the insulation layer of the target reaction tower, the reaction space of the target reaction tower, and the conversion rate of the target reaction; Prediction module 302, used for inputting the target reaction parameter into the reaction tower control parameter model to obtain the reaction tower prediction control parameter, wherein the reaction tower prediction control parameter includes the prediction input parameter of steam and the prediction input parameter of reactant, wherein the reaction tower control parameter model is obtained by training based on sample reaction parameters and reaction tower sample control parameters, wherein the sample reaction parameters include the input parameter of sample reactant, the external temperature of the sample reaction tower, the internal temperature of the sample reaction tower, the thickness of the insulation layer of the sample reaction tower, the insulation coefficient of the insulation layer of the sample reaction tower, the reaction space of the sample reaction tower and the conversion rate of the sample reaction, and the reaction tower sample control parameters include the sample input parameter of steam and the sample input parameter of reactant; The control module 303 is used to control the target reaction tower according to the predicted introduction parameters of the steam and the predicted introduction parameters of the reactants.

[0064] In some embodiments, the system also includes a monitoring module, which is used to determine a predicted steam flow sequence according to the predicted steam flow parameters, and determine a predicted flow sequence of the reactant according to the predicted flow parameters of the reactant, wherein the predicted flow sequence includes multiple consecutive predicted time points and corresponding predicted flow values ​​at each predicted time point; obtain the actual flow sequence of the steam, and obtain the actual flow sequence of the reactant, wherein the actual flow sequence includes multiple consecutive actual time points and corresponding predicted flow values ​​at each actual time point; compare the predicted flow value of the steam with the actual flow value of the steam in real time to obtain a first comparison result, and compare the predicted flow value of the reactant with the actual flow value of the reactant to obtain a second comparison result; if the first comparison result and / or the second comparison result are inconsistent, generate a first prompt message, and the first prompt message is used to prompt the adjustment of the actual flow value of the steam and / or the actual flow value of the reactant.

[0065] In some embodiments, the system also includes an update module, which is used to obtain the product of the target reaction tower reaction; if the purity of the product is lower than a preset threshold, a second prompt information is generated, and the second prompt information is used to prompt the update of the reaction tower control parameter model.

[0066] In some embodiments, the predicted input parameters of the reactant include the predicted concentration of the reactant, the predicted pressure of the reactant, and the predicted flow rate of the reactant, and the sample input parameters of the reactant include the sample concentration of the reactant, the sample pressure of the reactant, and the sample flow rate of the reactant.

[0067] In some embodiments, the target reaction tower internal temperature includes the target reaction tower inner wall temperature and the target reaction tower internal hollow area temperature.

[0068] The control system of a reaction tower provided in the embodiment of the present application may correspond to executing a control method of a reaction tower described in the embodiment of the present application, and the above functions of each module of the system correspond to realizing Figure 1 For the sake of brevity, the corresponding process of the method shown will not be repeated here.

[0069] like Figure 4 As shown, this figure is a schematic diagram of the structure of a computing device provided in an embodiment of the present application, such as Figure 4 As shown, computing device 800 includes bus 801, processor 802, communication interface 803 and memory 804. Processor 802, memory 804 and communication interface 803 communicate with each other via bus 801.

[0070] The bus 801 may be a peripheral component interconnect (PCI) bus or an extended industry standard architecture (EISA) bus. The bus may be divided into an address bus, a data bus, a control bus, etc. For ease of representation, Figure 4 Only one thick line is used in the diagram, but this does not mean that there is only one bus or only one type of bus.

[0071] The processor 802 may be any one or more of a central processing unit (CPU), a graphics processing unit (GPU), a microprocessor (MP), or a digital signal processor (DSP).

[0072] The communication interface 803 is used for communicating with the outside.

[0073] The memory 804 may include a volatile memory, such as a random access memory (RAM). The memory 804 may also include a non-volatile memory, such as a read-only memory (ROM), a flash memory, a hard disk drive (HDD), or a solid state drive (SSD).

[0074] The memory 804 stores executable codes, and the processor 802 executes the executable codes to perform the aforementioned control method of the reaction tower.

[0075] Specifically, in implementing Figure 3 In the case of the embodiment shown, and Figure 3 When each module or unit of the reaction tower control system described in the embodiment is implemented by software, the execution Figure 3 The software or program code required for the functions of each module / unit in the reactor may be partially or completely stored in the memory 804. The processor 802 executes the program code corresponding to each unit stored in the memory 804 to execute the aforementioned reaction tower control method.

[0076] The embodiment of the present application also provides a computer-readable storage medium. The computer-readable storage medium can be any available medium that can be stored by a computing device or a data storage device such as a data center containing one or more available media. The available medium can be a magnetic medium (such as a floppy disk, a hard disk, a tape), an optical medium (such as a DVD), or a semiconductor medium (such as a solid-state hard disk). The computer-readable storage medium includes instructions that instruct the computing device to execute the above-mentioned reaction tower control method applied to the reaction tower control system.

[0077] The embodiment of the present application further provides a computer program product, which includes one or more computer instructions. When the computer instructions are loaded and executed on a computing device, the process or function described in the embodiment of the present application is generated in whole or in part.

[0078] The computer instructions may be stored in a computer-readable storage medium or transmitted from one computer-readable storage medium to another computer-readable storage medium. For example, the computer instructions may be transmitted from one website, computer or data center to another website, computer or data center via wired (e.g., coaxial cable, optical fiber, digital subscriber line (DSL)) or wireless (e.g., infrared, wireless, microwave, etc.) means.

[0079] When the computer program product is executed by a computer, the computer executes any of the aforementioned control methods for the reaction tower. The computer program product may be a software installation package, and when any of the aforementioned control methods for the reaction tower needs to be used, the computer program product may be downloaded and executed on the computer.

[0080] The descriptions of the processes or structures corresponding to the above-mentioned figures have different emphases. For parts that are not described in detail in a certain process or structure, please refer to the relevant descriptions of other processes or structures.

[0081] The above description is only a specific implementation of the present application, but the protection scope of the present application is not limited thereto. Any changes or substitutions within the technical scope disclosed in the present application should be included in the protection scope of the present application.

Claims

1. A control method for a reaction tower, characterized in that: include: Obtaining target reaction parameters, the target reaction parameters including the target reactant feed parameters, the target reaction tower external temperature, the target reaction tower internal temperature, the target reaction tower insulation layer thickness, the target reaction tower insulation layer insulation coefficient, the target reaction tower reaction space and the target reaction conversion rate; Inputting the target reaction parameters into a reaction tower control parameter model to obtain reaction tower prediction control parameters, the reaction tower prediction control parameters include prediction parameters for steam introduction and prediction parameters for reactants, wherein the reaction tower control parameter model is trained based on sample reaction parameters and reaction tower sample control parameters, the sample reaction parameters include sample reactant introduction parameters, sample reaction tower external temperature, sample reaction tower internal temperature, sample reaction tower insulation layer thickness, sample reaction tower insulation layer insulation coefficient, sample reaction tower reaction space and sample reaction conversion rate, the reaction tower sample control parameters include sample steam introduction parameters and reactant introduction parameters; The target reaction tower is controlled according to the predicted introduction parameters of the steam and the predicted introduction parameters of the reactants.

2. The method according to claim 1, characterized in that The method further comprises: Determine a predicted steam flow rate sequence according to the predicted steam flow rate parameters, and determine a predicted reactant flow rate sequence according to the predicted reactant flow rate parameters; Obtaining the actual flow rate sequence of the steam and the actual flow rate sequence of the reactants; Comparing the predicted flow rate of the steam with the actual flow rate of the steam in real time to obtain a first comparison result, and comparing the predicted flow rate of the reactant with the actual flow rate of the reactant to obtain a second comparison result; If the first comparison result and / or the second comparison result are inconsistent, a first prompt message is generated, wherein the first prompt message is used to prompt adjustment of the actual flow rate of the steam and / or the actual flow rate of the reactant.

3. The method according to claim 1, characterized in that The method further comprises: Obtaining a product of the target reaction tower reaction; If the purity of the product is lower than a preset threshold, a second prompt information is generated, and the second prompt information is used to prompt to update the reaction tower control parameter model.

4. The method according to any one of claims 1 to 3, characterized in that: The predicted parameters for the introduction of reactants include the predicted concentration of reactants, the predicted pressure of reactants and the predicted flow rate of reactants, and the sample parameters for the introduction of reactants include the sample concentration of reactants, the sample pressure of reactants and the sample flow rate of reactants.

5. The method according to claim 1, characterized in that The target reaction tower internal temperature includes the target reaction tower inner wall temperature and the target reaction tower internal hollow area temperature.

6. A control system for a reaction tower, characterized in that: include: An acquisition module is used to acquire target reaction parameters, wherein the target reaction parameters include the input parameters of the target reactant, the external temperature of the target reaction tower, the internal temperature of the target reaction tower, the thickness of the insulation layer of the target reaction tower, the insulation coefficient of the insulation layer of the target reaction tower, the reaction space of the target reaction tower, and the conversion rate of the target reaction; A prediction module, used for inputting the target reaction parameters into a reaction tower control parameter model to obtain reaction tower prediction control parameters, wherein the reaction tower prediction control parameters include prediction input parameters of steam and prediction input parameters of reactants, wherein the reaction tower control parameter model is trained based on sample reaction parameters and reaction tower sample control parameters, wherein the sample reaction parameters include input parameters of sample reactants, sample reaction tower external temperature, sample reaction tower internal temperature, sample reaction tower insulation layer thickness, sample reaction tower insulation layer insulation coefficient, sample reaction tower reaction space and sample reaction conversion rate, and the reaction tower sample control parameters include sample steam input parameters and sample reactant input parameters; A control module is used to control the target reaction tower according to the predicted introduction parameters of the steam and the predicted introduction parameters of the reactants.

7. The system according to claim 6, characterized in that The system further includes a monitoring module, which is used to determine a predicted steam flow rate sequence according to the predicted steam flow rate parameters, and to determine a predicted reactant flow rate sequence according to the predicted reactant flow rate parameters; to obtain an actual steam flow rate sequence, and to obtain an actual reactant flow rate sequence; The predicted flow rate value of the steam and the actual flow rate value of the steam are compared in real time to obtain a first comparison result, and the predicted flow rate value of the reactant and the actual flow rate value of the reactant are compared to obtain a second comparison result; if the first comparison result and / or the second comparison result are inconsistent, a first prompt message is generated, and the first prompt message is used to prompt the adjustment of the actual flow rate value of the steam and / or the actual flow rate value of the reactant.

8. The system according to claim 6, characterized in that The system also includes a monitoring module, which is used to obtain the product of the target reaction tower reaction; if the purity of the product is lower than a preset threshold, a second prompt information is generated, and the second prompt information is used to prompt the update of the reaction tower control parameter model.

9. An electronic device comprising a memory, a processor, and a computer program stored in the memory and executable on the processor, characterized in that: When the processor executes the computer program, the method according to any one of claims 1 to 5 is implemented.

10. A computer-readable storage medium having a computer program stored thereon, characterized in that: When the computer program is executed by a processor, the method according to any one of claims 1 to 5 is implemented.

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