WO2023040512A1 - Catalytic cracking unit simulation and prediction method based on molecular-level mechanism model and big data technology - Google Patents

Catalytic cracking unit simulation and prediction method based on molecular-level mechanism model and big data technology Download PDF

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WO2023040512A1
WO2023040512A1 PCT/CN2022/111033 CN2022111033W WO2023040512A1 WO 2023040512 A1 WO2023040512 A1 WO 2023040512A1 CN 2022111033 W CN2022111033 W CN 2022111033W WO 2023040512 A1 WO2023040512 A1 WO 2023040512A1
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steady
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元梦琪
涂文辉
何恺源
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广东辛孚科技有限公司
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    • GPHYSICS
    • G16INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR SPECIFIC APPLICATION FIELDS
    • G16CCOMPUTATIONAL CHEMISTRY; CHEMOINFORMATICS; COMPUTATIONAL MATERIALS SCIENCE
    • G16C10/00Computational theoretical chemistry, i.e. ICT specially adapted for theoretical aspects of quantum chemistry, molecular mechanics, molecular dynamics or the like
    • GPHYSICS
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    • G06F18/2135Feature extraction, e.g. by transforming the feature space; Summarisation; Mappings, e.g. subspace methods based on approximation criteria, e.g. principal component analysis
    • GPHYSICS
    • G06COMPUTING; CALCULATING OR COUNTING
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    • G06COMPUTING; CALCULATING OR COUNTING
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    • G16C20/30Prediction of properties of chemical compounds, compositions or mixtures
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    • G16CCOMPUTATIONAL CHEMISTRY; CHEMOINFORMATICS; COMPUTATIONAL MATERIALS SCIENCE
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    • G16C20/00Chemoinformatics, i.e. ICT specially adapted for the handling of physicochemical or structural data of chemical particles, elements, compounds or mixtures
    • G16C20/90Programming languages; Computing architectures; Database systems; Data warehousing

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  • the invention relates to the technical fields of petroleum refining and petrochemical production, in particular to a method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology.
  • Catalytic cracking is an important oil refining process. Its total processing capacity ranks first among various petroleum processing processes, and its technical complexity also ranks first among all kinds of oil refining processes. Therefore, catalytic cracking occupies a pivotal position in the oil refining industry.
  • the simulation of catalytic cracking process by traditional technology is mostly based on the method of lumped kinetics.
  • the lumped kinetics method divides the complex components in catalytic cracking into several lumped components according to the kinetic characteristics. In , each lump is considered as a virtual single component.
  • the traditional lumped kinetic model can usually only predict the yield of the product, but cannot predict the properties of the product, and the lumped kinetic model cannot reflect the change of the composition of the raw material, because there may be great differences between the composition of the oil products with the same properties. big difference.
  • the shortcomings of existing methods mainly include the following aspects: (1) The prediction accuracy and extension of traditional lumped models are not good, and the lack of control over the actual operation of the device makes it difficult to avoid deviations between prediction results and actual data. (2) The catalytic cracking process is complex, with many influencing variables, and it is difficult to construct a complete molecular-level mechanism model, which is difficult to apply to different devices, has poor practical applicability, and lacks control over the actual operation of the device. (3) The independent big data model does not consider the nature of the response, the causal relationship between the data does not correspond, and the extension of the model is poor. In addition, the causal correlation of variables and the time delay of causal response in the big data model are insufficiently considered, and the quality of data preprocessing seriously affects the accuracy of the model.
  • the present invention aims to provide a method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology.
  • the present invention can predict the product yield and product properties of the catalytic cracking process; the present invention Invented and established a molecular-level mechanism model of the catalytic cracking process.
  • the molecular-level mechanism model can not only improve the prediction accuracy, but also be applicable to different devices and has good extension; in addition, based on big data technology, the mechanism caused by the actual device operation Correction of model prediction deviations not only captures the essence of catalytic cracking reactions, but also reflects the characteristics of different catalytic devices, accurately predicts product yields and key product properties, and enables accurate process simulation of industrial-level devices.
  • the present invention achieves the above object through the following technical solutions: a method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology, comprising the following steps:
  • catalytic cracking unit model includes a raw material molecular analysis model, a molecular dynamics model, a riser reactor model, a product cutting model, and a physical property model;
  • step (3) Based on the processing results of step (2), a deviation compensation prediction model based on a machine learning algorithm is established; wherein, the input of the deviation compensation prediction model is the actual operating parameters of the device, and the output is the difference between the predicted value of the mechanism and the actual output value of the historical working condition The deviation of the actual working conditions is compensated to improve the prediction accuracy of the model;
  • a communication mechanism can be established with the real-time data of the catalytic cracking unit in the production process, and the device data can be read in real time and the model correction and deviation compensation prediction model can be updated to realize the prediction model Automatic updates.
  • step (1) the method of the raw material molecular analytical model that described step (1) establishes is specifically as follows:
  • Raw material molecular library construction carry out experimental analysis and characterization of the raw material, determine the core structure of the raw material molecule, add side chains, branch chains and methyl groups on the basis of the core molecular structure according to a certain strategy, and obtain the raw material molecular library;
  • Raw material molecular concentration analysis the initial value of the molecular concentration is set according to the composition characteristics of the raw material according to the probability distribution, and then the distribution parameters and molecular concentration are adjusted through the global optimization algorithm, so that the final molecular concentration distribution can meet the requirements of the raw material.
  • Macroscopic properties can be analyzed into detailed molecular composition according to the macroscopic physical properties of the feed such as density, carbon residue, sulfur content, nitrogen content, group composition, and distillation range; through the molecular concentration composition construction technology, according to various macroscopic properties that can be obtained through experimental analysis Properties Inversion analysis of molecular composition of FCC feedstock.
  • the method of the molecular-level dynamics model in the described step (1) is specifically as follows:
  • reaction rules and construct reaction network According to the carbenium ion mechanism of catalytic cracking reaction, reactant selection rules and product generation rules were established for different types of reactions, and a class of rule functions was written for each type of reaction , compiled a large class of reaction rules including cracking, ring-opening, isomerization, hydrogen transfer, and condensation, and used computer-aided technology to apply reaction rules to raw material molecules to automatically generate reaction networks; among them, the types of reaction rules are preferably within 10 pcs - 50 pcs.
  • the method of the riser reactor model in the described step (1) is specifically as follows:
  • (1.4) set up a reactor model, solve the model, and calculate the product molecular concentration distribution;
  • the built reactor model includes catalytic cracking processes such as single riser model, MIP double riser model, DCC main and auxiliary riser parallel model;
  • the network, stoichiometry, reaction rate equation and kinetic parameters are combined with the above reactor model to obtain a complete FCC reactor model.
  • the method of the product cutting model in described step (1) is specifically as follows:
  • Product cutting model For the product oil-gas mixture molecules coming out of the reactor, the mixed oil-gas is cut and separated into stream products of dry gas, liquefied gas, gasoline, diesel oil, oil slurry, and coke according to various product quality requirements; , the product cutting model can adopt a simple cutting model based on boiling point cutting, while considering the influence of overlapping factors;
  • the concrete method of the physical property model in described step (1) is as follows:
  • the specific method of parameter correction in the step (2) is: correct the parameters of the model through actual industrial data, and complete the molecular-level mechanism model; the industrial data include reactor structural size parameters, catalyst parameters, feed-in and discharge parameters, etc.
  • Property detection data LIMS data
  • DCS data device operating parameters
  • the concrete method of described step (3) is as follows:
  • Data preprocessing Extract data from the database for processing, including missing value interpolation processing, outlier processing, data smoothing and noise reduction, and data normalization processing;
  • Variable correlation analysis Calculate the correlation between variables through the correlation algorithm, and combine expert experience analysis to select the most relevant variables for modeling; specifically, the method of variable correlation analysis chooses Pearson correlation analysis One or more of , transfer entropy, Granger causality analysis, combined with expert experience analysis, select variables with strong correlation from many variables for modeling;
  • the missing value interpolation processing method in the step (3.2) selects any one of linear interpolation, cubic spline interpolation, mean value interpolation, and Lagrange interpolation;
  • the outlier identification method selects 3 ⁇ criterion method, box line Any one of the graph method and Grubbs test method;
  • the data noise reduction smoothing method selects the robust quadratic regression method to eliminate high-frequency noise signals and retain low-frequency data trends.
  • step (3.4) the method for the steady-state analysis in described step (3.4) is divided into univariate steady-state analysis and system steady-state analysis:
  • the steady state index ⁇ (t) is determined by the first derivative of the data trend f '(t 0 ) and the second derivative f”(t 0 ) are jointly determined according to the following criteria:
  • T s , T w , and Tu are the thresholds
  • the determination method is as follows: select a section of data in the historical database that is in a steady state as a reference, and extract the change trend of the process variable through wavelet transform to obtain the process variable at the sampling point.
  • is an adjustable parameter, which generally takes an integer between [2, 5]; through the above formula, the steady-state judgment threshold of the process variable can be obtained;
  • p is the number of key characteristic variables of the system
  • ⁇ i (t) is the steady-state index of the i-th variable
  • u i is the weight of the i-th variable.
  • the machine learning algorithm in the step (3.5) is selected from any one of a feedforward neural network, a recurrent neural network, a support vector machine, a least squares method, a least squares support vector machine, and an extreme learning machine regression algorithm.
  • the beneficial effects of the present invention are: (1) The present invention adopts the form of combining molecular-level mechanism model and big data technology, the molecular-level mechanism model describes the essential law of the catalytic cracking process, and the big data model makes full use of production history data, It can reflect the characteristics of different devices and the actual operating status of the device, and can efficiently process data sets with long time spans and huge data volumes; (2) the present invention calculates the yield and properties of products through the mechanism model, and uses the big data model to calculate the actual results The deviation from the mechanism prediction result, the mechanism model increases the data model to calculate the deviation between the actual result and the mechanism prediction result, and realizes the accurate prediction of product yield and product properties.
  • the present invention uses a molecular-level mechanism model based on structure-oriented lumping. Compared with the traditional lumped model, the molecular-level mechanism model has more accurate prediction accuracy and is more Wide forecast range.
  • Fig. 1 is a schematic flow sheet of the present invention
  • Fig. 2 is a schematic diagram of the reaction network of the present invention.
  • Fig. 3 is a schematic diagram of various physical properties that can be calculated by the physical property model of the present invention.
  • Fig. 4 is the schematic diagram of the univariate steady-state analysis result in the embodiment of the present invention.
  • Fig. 5 is the schematic diagram of the system steady-state analysis result in the implementation case of the present invention.
  • Fig. 6 is a schematic diagram of a multilayer neural network structure of the present invention.
  • Fig. 7 is a schematic diagram of the product yield prediction error of the dual-core drive model of the present invention.
  • Fig. 8 is a schematic diagram of the product property prediction error of the dual-core driver model of the present invention.
  • Embodiment The present invention will be described in further detail below through the specific implementation of the simulation of a catalytic cracking unit in a refining and chemical enterprise.
  • a method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology includes the following steps:
  • the accuracy of the molecular concentration of raw materials has a great influence on the calculation results of the mechanism model, and the molecular analysis algorithm is only a tool to obtain the molecular concentration, and the accuracy of the results depends more on the accuracy and completeness of the experimental analysis data.
  • reaction rules to construct the reaction network.
  • the reaction mechanism of catalytic cracking is very complicated, and the widely accepted mechanism is the carbanion mechanism. Under the action of the acidic center of the molecular sieve catalyst, the hydrocarbon molecules capture protons to form carbonium ions, and the carbonium ions undergo ⁇ -cleavage to generate olefins and new carbonium ions. Carbanions also undergo an isomerization reaction, which constitutes the main reaction in the catalytic cracking system.
  • the reaction rules are established for different types of reactions in turn.
  • the reaction rules include reactant selection rules and product production rules. A class of rule functions is written for each type of reaction.
  • reaction rules for the main reactions such as structure, hydrogen transfer, and condensation
  • computer-aided technology to apply the reaction rules to the raw material molecules to automatically generate a reaction network.
  • a reaction network containing 5216 reactions was generated (the reaction network diagram is shown in Figure 2 shown).
  • the types of reactions carried out on different catalysts will have some changes, so the reaction rules also need to be adjusted appropriately according to the experimental data.
  • the product is cut and separated. According to the typical distillation range range of each product, a simple cut model based on boiling point cut was adopted, and the influence of overlap factor was considered.
  • the present invention is based on the relevant physical property calculation model, adopts the group contribution method and the empirical correlation method, uses the molecular concentration of each product to calculate the properties of the product, and calculates the various physical properties of catalytic gasoline and catalytic diesel oil.
  • the calculable physical properties are shown in the figure 3.
  • Model parameter correction Collect the actual production data of the factory, including the property analysis data of the feed material and the product and the operating parameters of the device. The goal is to minimize the sum of squared errors between the predicted value and the actual output value, and the empirical value or experimental value is the initial value. Enable the global The optimization algorithm optimizes and solves the model parameters.
  • Wavelet transform has good time-frequency domain positioning and multi-resolution analysis capabilities. It can analyze the different frequency characteristic information contained in the historical data center, and analyze the measurement data by decomposing the signal into high-frequency noise and low-frequency band representing the signal trend. Finite continuous approximation to obtain an approximate function of the process variable.
  • Figure 4 and Figure 5 show the univariate steady-state analysis and the state of the system respectively judge. After judging the steady state of the system, extract the system data in the steady state. The average value of each segment of steady-state data is taken as the variable data representing the steady-state segment, and a database is established based on these variable data to facilitate subsequent analysis, extraction and use.
  • reaction system variables and raw oil property variables that have a greater impact on product yield and distribution are input from the first hidden layer after dimensionality reduction through principal component analysis, while the fractionation system and absorption system that have less impact on product yield and distribution
  • the variables of the stable system are input from the second hidden layer after dimensionality reduction by principal component analysis; a two-layer neural network containing 5 to 15 neurons is constructed, and the sample data is randomly divided into training set, verification set and test set, Parameter learning adopts the method of gradient descent and error backpropagation. After training, a predictive model of input and output is obtained. The error of the model is shown in Figure 7 and Figure 8.
  • Steps (7)-(12) can be combined with real-time data in the production process, and the real-time data of the device is used to perform parameter correction and automatic update of the deviation compensation model, thereby realizing automatic update of the model.

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Abstract

Provided is a catalytic cracking unit simulation and prediction method based on a molecular-level mechanism model and big data technology. The product yield and product properties of a catalytic cracking process are predicted; a molecular-level mechanism model for the catalytic cracking process is established; and furthermore, on the basis of big data technology, a mechanism model prediction deviation caused by an actual unit running state is corrected, thereby realizing the process simulation of an industrial-grade unit.

Description

一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法A simulation and prediction method for catalytic cracking unit based on molecular mechanism model and big data technology 技术领域technical field
本发明涉及石油炼制及石油化工生产技术领域,尤其涉及一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法。The invention relates to the technical fields of petroleum refining and petrochemical production, in particular to a method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology.
背景技术Background technique
催化裂化是一项重要的炼油工艺,其总加工能力已列各种石油加工工艺的前茅,其技术复杂程度也位居各类炼油工艺首位,因而催化裂化在炼油工业中占有举足轻重的地位。传统技术对催化裂化工艺的模拟多建立在集总动力学的方法上,集总动力学方法是按照动力学特性将催化裂化中复杂的组分划分为若干个集总组分,在动力学模拟中将每个集总作为虚拟的单一组分来考察。因此,传统的集总动力学模型通常只能预测产物的产量,无法预测产物的性质,并且集总动力学模型无法反映原料组成的改变,因为相同性质的油品的组成之间可能会有很大差异。Catalytic cracking is an important oil refining process. Its total processing capacity ranks first among various petroleum processing processes, and its technical complexity also ranks first among all kinds of oil refining processes. Therefore, catalytic cracking occupies a pivotal position in the oil refining industry. The simulation of catalytic cracking process by traditional technology is mostly based on the method of lumped kinetics. The lumped kinetics method divides the complex components in catalytic cracking into several lumped components according to the kinetic characteristics. In , each lump is considered as a virtual single component. Therefore, the traditional lumped kinetic model can usually only predict the yield of the product, but cannot predict the properties of the product, and the lumped kinetic model cannot reflect the change of the composition of the raw material, because there may be great differences between the composition of the oil products with the same properties. big difference.
随着对成品油质量要求越来越苛刻,迫切需要找到不仅能预测产物产量,还能准确预测产物性质的方法。分子级动力学模型的出现,为解决这个问题提供了可能性。通过解析原料分子组成,建立分子级反应动力学网络,计算反应物和产物分子在反应器内的转化规律,进而精准预测分子组成和产品性质。该方法比传统的集总方法预测更加准确,模型适应能力更加广泛。但是,因为模型复杂、参数多、计算量大,使得分子级机理模型在工业界还未有广泛应用。With the increasingly stringent requirements on the quality of refined oil, it is urgent to find a method that can not only predict the product yield, but also accurately predict the product properties. The emergence of molecular-level dynamics models provides the possibility to solve this problem. By analyzing the molecular composition of raw materials, a molecular-level reaction kinetic network is established, and the conversion laws of reactant and product molecules in the reactor are calculated, and then the molecular composition and product properties are accurately predicted. This method predicts more accurately than the traditional lumped method, and the model adaptability is more extensive. However, due to the complexity of the model, many parameters, and a large amount of calculation, the molecular-level mechanism model has not been widely used in the industry.
现有方法的不足,主要包括如下几个方面:(1)传统的集总模型预测精度、外延性不好,且缺少对装置实际运行情况的把控,难以避免预测结果与实际数据的偏差。(2)催化裂化过程复杂,影响变量多,完整的分子级机理模型构建难度大,难以适用于不同的装置,实际应用性差,也缺少对装置实际运行情况的把控。(3)独立的大数据模型,由于不考虑反应的本质,数据之间的因果关系不对应,模型的外延性差。并且大数据模型的变量因果关联性、因果响应的时间延迟等方面考虑不足,数据预处理的质量,严重影响模型准确度。The shortcomings of existing methods mainly include the following aspects: (1) The prediction accuracy and extension of traditional lumped models are not good, and the lack of control over the actual operation of the device makes it difficult to avoid deviations between prediction results and actual data. (2) The catalytic cracking process is complex, with many influencing variables, and it is difficult to construct a complete molecular-level mechanism model, which is difficult to apply to different devices, has poor practical applicability, and lacks control over the actual operation of the device. (3) The independent big data model does not consider the nature of the response, the causal relationship between the data does not correspond, and the extension of the model is poor. In addition, the causal correlation of variables and the time delay of causal response in the big data model are insufficiently considered, and the quality of data preprocessing seriously affects the accuracy of the model.
发明内容Contents of the invention
本发明为克服上述的不足之处,目的在于提供一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,本发明能够对催化裂化过程的产物收率和产品性质进行预测;本发明建立催化裂化过程的分子级机理模型,该分子级机理模型不仅可以提高预测精度,还可以适用于不同的装置,具有良好的外延性;另外,基于大数据技术对由实际装置运行状态造成机理模型预测偏差进行校正,不仅抓住催化裂化反应的本质,还能反映不同催化装置的特点,精准地预测产物收率以及关键产品性质,可实现工业级装置的准确过程模拟。In order to overcome the above shortcomings, the present invention aims to provide a method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology. The present invention can predict the product yield and product properties of the catalytic cracking process; the present invention Invented and established a molecular-level mechanism model of the catalytic cracking process. The molecular-level mechanism model can not only improve the prediction accuracy, but also be applicable to different devices and has good extension; in addition, based on big data technology, the mechanism caused by the actual device operation Correction of model prediction deviations not only captures the essence of catalytic cracking reactions, but also reflects the characteristics of different catalytic devices, accurately predicts product yields and key product properties, and enables accurate process simulation of industrial-level devices.
本发明是通过以下技术方案达到上述目的:一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,包括如下步骤:The present invention achieves the above object through the following technical solutions: a method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology, comprising the following steps:
(1)建立催化裂化装置模型,其中催化裂化装置模型包括原料分子解析模型、分子级动力学模型、提升管反应器模型、产物切割模型、物性模型;(1) Establish a catalytic cracking unit model, wherein the catalytic cracking unit model includes a raw material molecular analysis model, a molecular dynamics model, a riser reactor model, a product cutting model, and a physical property model;
(2)基于实际工业数据,对步骤(1)所建模型的参数进行校正;(2) based on actual industrial data, the parameters of the model built in step (1) are corrected;
(3)基于步骤(2)处理结果,建立基于机器学习算法的偏差补偿预测模型;其中,偏差补偿预测模型的输入是装置实际运行参数,输出是机理预测值与历史工况实际输出值之间的偏差,通过实际工况的偏差补偿,提升模型的预测精度;(3) Based on the processing results of step (2), a deviation compensation prediction model based on a machine learning algorithm is established; wherein, the input of the deviation compensation prediction model is the actual operating parameters of the device, and the output is the difference between the predicted value of the mechanism and the actual output value of the historical working condition The deviation of the actual working conditions is compensated to improve the prediction accuracy of the model;
(4)通过步骤(2)与步骤(3)可在生产过程中与催化裂化装置的实时数据建立通讯机制,实时读取装置数据并进行模型校正和偏差补偿预测模型的更新,实现预测模型的自动更新。(4) Through steps (2) and (3), a communication mechanism can be established with the real-time data of the catalytic cracking unit in the production process, and the device data can be read in real time and the model correction and deviation compensation prediction model can be updated to realize the prediction model Automatic updates.
作为优选,所述步骤(1)建立的原料分子解析模型的方法具体如下:As preferably, the method of the raw material molecular analytical model that described step (1) establishes is specifically as follows:
(1.1)原料分子库构建:对原料进行实验分析表征,确定原料分子的核心结构,在核心分子结构基础上按照一定策略添加侧链、支链和甲基,得到原料分子库;(1.1) Raw material molecular library construction: carry out experimental analysis and characterization of the raw material, determine the core structure of the raw material molecule, add side chains, branch chains and methyl groups on the basis of the core molecular structure according to a certain strategy, and obtain the raw material molecular library;
(1.2)原料分子浓度解析:分子浓度的初值根据原料组成特征按照概率分布进行设定,然后通过全局优化算法对分布参数和分子浓度进行调整,使最终的分子浓度分布能够满足原料的各项宏观性质,可以根据进料的宏观物性如密度、残炭、硫含量、氮含量、族组成、馏程解析成详细分子组成;通过分子浓度组成构建技术,根据各项可通过实验分析获取的宏观性质对催化裂化原料的分子组成进行反演分析。(1.2) Raw material molecular concentration analysis: the initial value of the molecular concentration is set according to the composition characteristics of the raw material according to the probability distribution, and then the distribution parameters and molecular concentration are adjusted through the global optimization algorithm, so that the final molecular concentration distribution can meet the requirements of the raw material. Macroscopic properties can be analyzed into detailed molecular composition according to the macroscopic physical properties of the feed such as density, carbon residue, sulfur content, nitrogen content, group composition, and distillation range; through the molecular concentration composition construction technology, according to various macroscopic properties that can be obtained through experimental analysis Properties Inversion analysis of molecular composition of FCC feedstock.
作为优选,所述步骤(1)中的分子级动力学模型的方法具体如下:As preferably, the method of the molecular-level dynamics model in the described step (1) is specifically as follows:
(1.3)编写反应规则,构建反应网络:根据催化裂化反应的正碳离子机理,对不同的类型的反应分别建立了反应物选择规则和产物生成规则,针对每一类反应各编写一类规则函数,编写了包含裂化、开环、异构、氢转移、缩合五类主要反应的大类反应规则,利用计算机辅助技术对原料分子应用反应规则,自动生成反应网络;其中反应规则的种类优选在10个-50个。(1.3) Write reaction rules and construct reaction network: According to the carbenium ion mechanism of catalytic cracking reaction, reactant selection rules and product generation rules were established for different types of reactions, and a class of rule functions was written for each type of reaction , compiled a large class of reaction rules including cracking, ring-opening, isomerization, hydrogen transfer, and condensation, and used computer-aided technology to apply reaction rules to raw material molecules to automatically generate reaction networks; among them, the types of reaction rules are preferably within 10 pcs - 50 pcs.
作为优选,所述步骤(1)中的提升管反应器模型的方法具体如下:As preferably, the method of the riser reactor model in the described step (1) is specifically as follows:
(1.4)建立反应器模型,求解模型,计算产物分子浓度分布;所建的反应器模型包括单提升管模型、MIP双提升管模型、DCC的主副提升管并联模型等催化裂化工艺;将反应网络、化学计量学、反应速率方程和动力学参数与上述反应器模型组合,即可得到完整的催化裂化反应器模型。(1.4) set up a reactor model, solve the model, and calculate the product molecular concentration distribution; the built reactor model includes catalytic cracking processes such as single riser model, MIP double riser model, DCC main and auxiliary riser parallel model; The network, stoichiometry, reaction rate equation and kinetic parameters are combined with the above reactor model to obtain a complete FCC reactor model.
作为优选,所述步骤(1)中的产物切割模型的方法具体如下:As preferably, the method of the product cutting model in described step (1) is specifically as follows:
(1.5)产物切割模型:对从反应器出来的产物油气混合分子,根据各项产品质量要求将混合油气切割分离成干气、液化气、汽油、柴油、油浆、焦炭各流股产品;其中,产物切割模型可采用基于沸点切割的简易切割模型,同时考虑重叠因子的影响;(1.5) Product cutting model: For the product oil-gas mixture molecules coming out of the reactor, the mixed oil-gas is cut and separated into stream products of dry gas, liquefied gas, gasoline, diesel oil, oil slurry, and coke according to various product quality requirements; , the product cutting model can adopt a simple cutting model based on boiling point cutting, while considering the influence of overlapping factors;
所述步骤(1)中的物性模型的具体方法如下:The concrete method of the physical property model in described step (1) is as follows:
(1.6)物性计算:通过物性计算模型,采用基团贡献法以及经验关联方法,用各项产物的分子浓度计算产物的性质,包括汽油和柴油的各项物性。(1.6) Calculation of physical properties: Through the physical property calculation model, the group contribution method and the empirical correlation method are used to calculate the properties of the products with the molecular concentration of each product, including the physical properties of gasoline and diesel.
作为优选,所述步骤(2)中的参数校正的具体方法为:通过实际工业数据对模型的参数进行校正,完成分子级机理模型;工业数据包括反应器结构尺寸参数、催化剂参数、进出料的性质检测数据(LIMS数据)、装置操作参数(DCS数据)。As preferably, the specific method of parameter correction in the step (2) is: correct the parameters of the model through actual industrial data, and complete the molecular-level mechanism model; the industrial data include reactor structural size parameters, catalyst parameters, feed-in and discharge parameters, etc. Property detection data (LIMS data), device operating parameters (DCS data).
作为优选,所述步骤(3)的具体方法如下:As preferably, the concrete method of described step (3) is as follows:
(3.1)数据采集及整理:读取装置的DCS、LIMS历史生产数据,建立数据库,规范格式并建立索引规则,方便后期查询和调用;(3.1) Data collection and arrangement: read the DCS and LIMS historical production data of the device, establish a database, standardize the format and establish indexing rules to facilitate later query and call;
(3.2)数据预处理:从数据库中抽取数据进行处理工作,包括缺失值插值处理、异常值处理、数据平滑降噪、数据归一化处理;(3.2) Data preprocessing: Extract data from the database for processing, including missing value interpolation processing, outlier processing, data smoothing and noise reduction, and data normalization processing;
(3.3)变量关联分析:通过相关性算法对各个变量间的相关性进行计算,并结合专家经验分析,选取最相关的变量进行建模;具体的,变量关联分析的方法选择皮尔逊相关性分析、传递熵、格兰杰因果分析中的一种或多种,并结合专家经验分析,从众多变量中挑选关联性强的变量进行建模;(3.3) Variable correlation analysis: Calculate the correlation between variables through the correlation algorithm, and combine expert experience analysis to select the most relevant variables for modeling; specifically, the method of variable correlation analysis chooses Pearson correlation analysis One or more of , transfer entropy, Granger causality analysis, combined with expert experience analysis, select variables with strong correlation from many variables for modeling;
(3.4)稳态分析:通过建立的稳态分析规则对系统进行稳态检测,并析取各个稳态下对应的工况,使用得到的稳态工况建立数据库,方便后续更新和使用;(3.4) Steady-state analysis: The steady-state detection of the system is carried out through the established steady-state analysis rules, and the corresponding working conditions in each steady state are extracted, and a database is established using the obtained steady-state working conditions to facilitate subsequent updates and use;
(3.5)建立偏差补偿预测模型:将历史工况对应的输入变量输入到建立的机理模型中,得到机理模型的预测值,然后计算机理预测值与历史工况实际输出值之间的偏差,通过主成分分析降低输入变量的输入维度,通过机器学习算法建立偏差补偿预测模型,机理模型预测值加偏差补偿得到最终的预测结果。(3.5) Establish a deviation compensation prediction model: input the input variables corresponding to the historical working conditions into the established mechanism model to obtain the predicted value of the mechanism model, and then calculate the deviation between the predicted value of the mechanism and the actual output value of the historical working condition, through The principal component analysis reduces the input dimension of the input variables, establishes the deviation compensation prediction model through the machine learning algorithm, and adds the deviation compensation to the predicted value of the mechanism model to obtain the final prediction result.
作为优选,所述步骤(3.2)中的缺失值插值处理方法选择线性插值、三次样条插值、均值插值、拉格朗日插值中的任意一种;异常值识别方法选择3σ准则法、箱线图法、格拉布斯检验法中的任意一种;数据降噪平滑方法选择稳健二次回归方法,消除高频噪音信号,保留低频的数据趋势。As preferably, the missing value interpolation processing method in the step (3.2) selects any one of linear interpolation, cubic spline interpolation, mean value interpolation, and Lagrange interpolation; the outlier identification method selects 3σ criterion method, box line Any one of the graph method and Grubbs test method; the data noise reduction smoothing method selects the robust quadratic regression method to eliminate high-frequency noise signals and retain low-frequency data trends.
作为优选,所述步骤(3.4)中的稳态分析的方法分为单变量稳态分析和系统稳态分析:As preferably, the method for the steady-state analysis in described step (3.4) is divided into univariate steady-state analysis and system steady-state analysis:
(i)单变量稳态分析:采用小波变换的方法对数据集进行趋势提取,通过将信号分解为高频段的噪声和代表信号趋势的低频段,来对测量数据进行有限连续的逼近,得到过程变量的近似函数f(t),建立了稳态指数β(0≤β≤1)来表示变量工况状态的稳定程度,当β=0时,过程变量处于非稳态,β=1时,过程变量处于稳态,0<β<1时,表示过程变量处于过渡态,并且β越接近于1,表示过程变量的状态越稳定;稳态指数β(t)由数据趋势的一阶导数f’(t 0)和二阶导数f”(t 0)根据以下准则共同决定: (i) Univariate steady-state analysis: use the wavelet transform method to extract the trend of the data set, and decompose the signal into the noise of the high frequency band and the low frequency band representing the trend of the signal to perform finite continuous approximation on the measured data, and obtain the process The approximate function f(t) of the variable establishes a steady-state index β (0≤β≤1) to represent the stability of the variable working condition. When β=0, the process variable is in an unsteady state. When β=1, The process variable is in a steady state. When 0<β<1, it means that the process variable is in a transition state, and the closer β is to 1, the more stable the state of the process variable is; the steady state index β(t) is determined by the first derivative of the data trend f '(t 0 ) and the second derivative f”(t 0 ) are jointly determined according to the following criteria:
θ(t)=|f′(t)|+γ|f″(t)|θ(t)=|f'(t)|+γ|f″(t)|
式中:In the formula:
Figure PCTCN2022111033-appb-000001
Figure PCTCN2022111033-appb-000001
Figure PCTCN2022111033-appb-000002
Figure PCTCN2022111033-appb-000002
其中T s、T w、T u为阈值,其确定方法如下:在历史数据库中选择过程处于稳态的一段数据作为参考基准,通过小波变换提取过程变量的变化趋势后,得到过程变量在采样点的一阶导数序列和二阶导数序列,通过分别求其百分位数,则:T s为一阶导数的百分位数,T w为二阶导数的百分位数,一般可选90%分位数或95%分位数,其中T u=αT s Among them, T s , T w , and Tu are the thresholds, and the determination method is as follows: select a section of data in the historical database that is in a steady state as a reference, and extract the change trend of the process variable through wavelet transform to obtain the process variable at the sampling point. The first-order derivative sequence and the second-order derivative sequence of , by calculating their percentiles respectively, then: T s is the percentile of the first-order derivative, T w is the percentile of the second-order derivative, generally 90 % quantile or 95% quantile, where T u = αT s
α为可调参数,一般取[2,5]之间的整数;通过以上公式,可得到过程变量的稳态判断阈值;α is an adjustable parameter, which generally takes an integer between [2, 5]; through the above formula, the steady-state judgment threshold of the process variable can be obtained;
(ii)系统稳态分析:采用单变量稳态检测规则得到各个变量的稳态指数β i,整个系统的稳态状况有各变量的稳态指数按下式加权决定: (ii) System steady-state analysis: The steady-state index β i of each variable is obtained by using the single-variable steady-state detection rule, and the steady-state condition of the entire system is determined by the weighting of the steady-state index of each variable according to the following formula:
Figure PCTCN2022111033-appb-000003
Figure PCTCN2022111033-appb-000003
其中,p为系统的关键特征变量个数,β i(t)为第i个变量的稳态指数,u i为第i个变量的权重。 Among them, p is the number of key characteristic variables of the system, β i (t) is the steady-state index of the i-th variable, and u i is the weight of the i-th variable.
作为优选,所述步骤(3.5)中的机器学习算法选择前馈神经网络、循环神经网络、支持向量机、最小二乘法、最小二乘支持向量机、极限学习机回归算法中的任意一种。As preferably, the machine learning algorithm in the step (3.5) is selected from any one of a feedforward neural network, a recurrent neural network, a support vector machine, a least squares method, a least squares support vector machine, and an extreme learning machine regression algorithm.
本发明的有益效果在于:(1)本发明采用了将分子级机理模型和大数据技术结合的形式,分子级机理模型描述了催化裂化过程的本质规律,大数据模型充分利用了生产历史数据,可以反映不同装置的特点以及装置实际的运行状态,可高效处理时间跨度长、数据量庞大的数据集;(2)本发明通过机理模型计算产物的收率和性质,利用大数据模型计算实际结果与机理预测结果的偏差,机理模型加大数据模型计算实际结果与机理预测结果的偏差,实现了对产物收率和产物性质的准确预测,同时在面对未知工况时,模型具有良好的外推性能,可以对未知工况进行探索;(3)本发明采用了基于结构导向集总的分子级机理模型,相比于传统的集总模型,分子级机理模型具有更加准确的预测精度,更加广泛的预测范围。The beneficial effects of the present invention are: (1) The present invention adopts the form of combining molecular-level mechanism model and big data technology, the molecular-level mechanism model describes the essential law of the catalytic cracking process, and the big data model makes full use of production history data, It can reflect the characteristics of different devices and the actual operating status of the device, and can efficiently process data sets with long time spans and huge data volumes; (2) the present invention calculates the yield and properties of products through the mechanism model, and uses the big data model to calculate the actual results The deviation from the mechanism prediction result, the mechanism model increases the data model to calculate the deviation between the actual result and the mechanism prediction result, and realizes the accurate prediction of product yield and product properties. At the same time, when facing unknown working conditions, the model has a good appearance (3) The present invention uses a molecular-level mechanism model based on structure-oriented lumping. Compared with the traditional lumped model, the molecular-level mechanism model has more accurate prediction accuracy and is more Wide forecast range.
附图说明Description of drawings
图1是本发明的流程示意图;Fig. 1 is a schematic flow sheet of the present invention;
图2是本发明的反应网络示意图;Fig. 2 is a schematic diagram of the reaction network of the present invention;
图3是本发明的物性模型可计算的各项物性示意图;Fig. 3 is a schematic diagram of various physical properties that can be calculated by the physical property model of the present invention;
图4是本发明实施案例中的单变量稳态分析结果示意图;Fig. 4 is the schematic diagram of the univariate steady-state analysis result in the embodiment of the present invention;
图5是本发明实施案例中的系统稳态分析结果示意图;Fig. 5 is the schematic diagram of the system steady-state analysis result in the implementation case of the present invention;
图6是本发明的多层神经网络结构示意图;Fig. 6 is a schematic diagram of a multilayer neural network structure of the present invention;
图7是本发明的双核驱动模型的产物收率预测误差示意图;Fig. 7 is a schematic diagram of the product yield prediction error of the dual-core drive model of the present invention;
图8是本发明的双核驱动模型的产品性质预测误差示意图。Fig. 8 is a schematic diagram of the product property prediction error of the dual-core driver model of the present invention.
具体实施方式Detailed ways
下面结合具体实施例对本发明进行进一步描述,但本发明的保护范围并不仅限于此:The present invention is further described below in conjunction with specific embodiment, but protection scope of the present invention is not limited thereto:
实施例:下面通过某炼化企业中催化裂化装置模拟的具体实施方式,对本发明作进一步详细描述。如图1所示,一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,包括如下步骤:Embodiment: The present invention will be described in further detail below through the specific implementation of the simulation of a catalytic cracking unit in a refining and chemical enterprise. As shown in Figure 1, a method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology includes the following steps:
(1)构建原料分子库。构成催化裂化原料的分子数目十分巨大,而构成这些分子的同系物核心结构数目则要少得多。在核心结构基础上按照一定的策略添加侧链、支链和甲基,得到一系列分子集,通过物性检索和分子物性计算模型计算各个分子的馏程密度等性 质,利用碳数和馏程约束对分子集进行进一步筛选,删除不合理的分子,得到最终的原料分子库,目前构建了包含48个核心2473个分子的原料分子库。(1) Construct the raw material molecular library. The number of molecules that make up FCC feedstock is enormous, and the number of homologue core structures that make up those molecules is much smaller. On the basis of the core structure, side chains, branch chains and methyl groups are added according to a certain strategy to obtain a series of molecular sets, and the properties such as the distillation range density of each molecule are calculated through the physical property search and molecular physical property calculation model, and the carbon number and distillation range constraints are used. The molecular set is further screened, unreasonable molecules are deleted, and the final raw material molecular library is obtained. Currently, a raw material molecular library containing 48 cores and 2473 molecules has been constructed.
(2)原料分子浓度解析。分子级反应机理模型需要输入分子浓度,通过不同的实验分析方法得到分子组成的某个碎片信息,通过对多个碎片的拼接,间接推断出原料完整的分子信息,分子浓度的初值根据原料组成特征按照一定的概率分布进行设定,然后通过特定的全局优化算法对分布参数和分子浓度进行调整,使最终的分子浓度分布能够满足原料的各项宏观性质。原料分子浓度的准确性对机理模型的计算结果有较大影响,而分子解析算法只是获取分子浓度的一种工具,结果的准确性更多依赖于实验分析数据的准确性和完备性。(2) Raw material molecular concentration analysis. The molecular-level reaction mechanism model needs to input the molecular concentration. The information of a certain fragment of the molecular composition is obtained through different experimental analysis methods. Through the splicing of multiple fragments, the complete molecular information of the raw material can be inferred indirectly. The characteristics are set according to a certain probability distribution, and then the distribution parameters and molecular concentration are adjusted through a specific global optimization algorithm, so that the final molecular concentration distribution can meet the macroscopic properties of the raw materials. The accuracy of the molecular concentration of raw materials has a great influence on the calculation results of the mechanism model, and the molecular analysis algorithm is only a tool to obtain the molecular concentration, and the accuracy of the results depends more on the accuracy and completeness of the experimental analysis data.
(3)编写反应规则构建反应网络。催化裂化反应机理十分复杂,被广泛接受的机理是正碳离子机理,在分子筛催化剂酸性中心作用下,烃类分子捕获质子形成正碳离子,正碳离子发生β断裂生成烯烃和新的正碳离子,正碳离子还会发生异构化反应,由此构成催化裂化系统的主要反应。针对催化裂化化学反应机理,对不同类型的反应依次建立反应规则,反应规则包括反应物选择规则和产物生产规则,针对每一类反应各编写一类规则函数,编写了包含裂化、开环、异构、氢转移、缩合等主要反应的25大类反应规则,然后利用计算机辅助技术对原料分子应用反应规则,自动生成反应网络,生成了了包含5216个反应的反应网络(反应网络示意图如图2所示)。不同的催化剂上进行的反应类型会有一些变化,因此反应规则也需要根据实验数据做适当的调整。(3) Write the reaction rules to construct the reaction network. The reaction mechanism of catalytic cracking is very complicated, and the widely accepted mechanism is the carbanion mechanism. Under the action of the acidic center of the molecular sieve catalyst, the hydrocarbon molecules capture protons to form carbonium ions, and the carbonium ions undergo β-cleavage to generate olefins and new carbonium ions. Carbanions also undergo an isomerization reaction, which constitutes the main reaction in the catalytic cracking system. According to the chemical reaction mechanism of catalytic cracking, the reaction rules are established for different types of reactions in turn. The reaction rules include reactant selection rules and product production rules. A class of rule functions is written for each type of reaction. 25 types of reaction rules for the main reactions such as structure, hydrogen transfer, and condensation, and then use computer-aided technology to apply the reaction rules to the raw material molecules to automatically generate a reaction network. A reaction network containing 5216 reactions was generated (the reaction network diagram is shown in Figure 2 shown). The types of reactions carried out on different catalysts will have some changes, so the reaction rules also need to be adjusted appropriately according to the experimental data.
(4)建立反应器模型。根据拟平推流反应器模型,建立质量平衡方程和热量平衡方程,将反应网络、化学计量学、反应速率方程和动力学参数与上述反应器模型组合,即可得到完整的催化裂化反应器模型,表示为一个庞大的微分方程组,通过求取该微分方程组即可计算反应器内各分子的浓度转化规律。(4) Build the reactor model. According to the pseudo-planar plug-flow reactor model, the mass balance equation and heat balance equation are established, and the reaction network, stoichiometry, reaction rate equation and kinetic parameters are combined with the above reactor model to obtain a complete catalytic cracking reactor model , which is expressed as a huge differential equation system, and the concentration conversion law of each molecule in the reactor can be calculated by obtaining the differential equation system.
(5)产物切割分离。根据各产物的典型馏程范围采用基于沸点切割的简易切割模型,同时考虑重叠因子的影响。(5) The product is cut and separated. According to the typical distillation range range of each product, a simple cut model based on boiling point cut was adopted, and the influence of overlap factor was considered.
(6)物性计算模型。本发明以相关的物性计算模型为基础,采用基团贡献法以及经验关联方法,用各项产物的分子浓度计算产物的性质,计算催化汽油和催化柴油的各项物性,可计算的物性如图3所示。(6) Physical property calculation model. The present invention is based on the relevant physical property calculation model, adopts the group contribution method and the empirical correlation method, uses the molecular concentration of each product to calculate the properties of the product, and calculates the various physical properties of catalytic gasoline and catalytic diesel oil. The calculable physical properties are shown in the figure 3.
(7)模型参数校正。采集工厂实际生产数据,包括进料和产品的性质分析数据以及装置的操作参数,以预测值与实际输出值之间的误差平方和最小为目标,以经验值或实验值为初值,启用全局优化算法对模型参数进行优化求解。(7) Model parameter correction. Collect the actual production data of the factory, including the property analysis data of the feed material and the product and the operating parameters of the device. The goal is to minimize the sum of squared errors between the predicted value and the actual output value, and the empirical value or experimental value is the initial value. Enable the global The optimization algorithm optimizes and solves the model parameters.
(8)数据采集及整理。本例中采集了某炼厂催化裂化装置DCS系统和LIMS检测约一年的完整历史生产数据,其中DCS系统的操作参数和状态参数每10分钟自动记录一次,装置系统进料物料性质检测数据每3天分析一次,装置系统产品出料物料性质每24小时分析一次。对采集到的DCS和LIMS数据进行整理,建立便于后续读取和检索的基础数据库。(8) Data collection and collation. In this example, the complete historical production data of the DCS system and LIMS of a catalytic cracking unit in a refinery were collected for about one year. The operating parameters and state parameters of the DCS system were automatically recorded every 10 minutes, and the detection data of the feed material properties of the device system were recorded every 10 minutes. Analyze once every 3 days, and analyze the properties of the output material of the device system every 24 hours. Organize the collected DCS and LIMS data, and establish a basic database for subsequent reading and retrieval.
(9)数据处理。对收集的DCS操作参数和状态参数以及LIMS的物料检测性质进行描述性统计分析,分析数据的分布规律及统计信息。对数据的缺失值和离群值进行处理,作为优选,选用百分位法对数据集的离群值进行判断。使用插值拟合方法对缺失值和离群值进行填补。使用二次回归函数对数据进行降噪处理,过滤高频噪音信号,得到更加符合数据变化趋势的数据集。(9) Data processing. Descriptive statistical analysis is carried out on the collected DCS operating parameters and state parameters and the material detection properties of LIMS, and the distribution rules and statistical information of the data are analyzed. The missing values and outliers of the data are processed, and as a preference, the percentile method is used to judge the outliers of the data set. Missing and outlier values are imputed using an interpolation fitting method. Use the quadratic regression function to denoise the data, filter high-frequency noise signals, and obtain a data set that is more in line with the trend of data changes.
(10)变量关联分析。采集得到542个DCS操作及状态变量,340项LIMS性质检测变量,为了能够简化输入的变量并尽可能多的保留有效信息,需要筛选出与预测模型最相关的一组变量。根据催化裂化生产装置的实际情况,结合专家的经验和专业知识,配合相应的相关性分析算法,对反应、分馏以及吸收稳定三大系统的变量进行分析,探索每个操作参数和状态参数间的相关性关系,选出对产物收率和性质影响较大的操作和状态参数作为后续建模的输入变量,其中相关性分析算法采用传递熵算法。(10) Variable correlation analysis. 542 DCS operation and state variables and 340 LIMS property detection variables were collected. In order to simplify the input variables and retain as much valid information as possible, it is necessary to filter out a group of variables most relevant to the prediction model. According to the actual situation of the catalytic cracking production unit, combined with the experience and professional knowledge of experts, and with the corresponding correlation analysis algorithm, the variables of the three major systems of reaction, fractionation and absorption stability are analyzed, and the relationship between each operating parameter and state parameter is explored. Correlation relationship, the operation and state parameters that have a greater impact on product yield and properties are selected as input variables for subsequent modeling, and the correlation analysis algorithm uses the transfer entropy algorithm.
(11)稳态分析。面对催化裂化这种复杂的非线性系统,采用基于趋势提取的小波分解法对系统进行稳态分析。小波变换具有良好的时频域定位和多分辨率分析能力,可以分析历史数据中心含有的不同频率特征信息,通过将信号分解为高频段的噪声和代表信号趋势的低频段,来对测量数据进行有限连续的逼近,从而得到过程变量的近似函数。通过建立的单变量稳态准则及系统稳态判断准则,先对所有变量单独进行稳态分析,然后对系统进行稳态判别,图4、图5分别展示了单变量稳态分析和系统的状态判断。对系统的稳态进行判定之后,对处于稳态的系统数据进行提取。取每一段稳态数据的平均值作为表征该稳态段的变量数据,并根据这些变量数据建立数据库,方便后续分析、提取和使用。(11) Steady-state analysis. Facing the complex nonlinear system of catalytic cracking, the steady-state analysis of the system is carried out by wavelet decomposition method based on trend extraction. Wavelet transform has good time-frequency domain positioning and multi-resolution analysis capabilities. It can analyze the different frequency characteristic information contained in the historical data center, and analyze the measurement data by decomposing the signal into high-frequency noise and low-frequency band representing the signal trend. Finite continuous approximation to obtain an approximate function of the process variable. Through the established univariate steady-state criterion and system steady-state judgment criterion, the steady-state analysis is performed on all variables separately, and then the steady-state judgment is performed on the system. Figure 4 and Figure 5 show the univariate steady-state analysis and the state of the system respectively judge. After judging the steady state of the system, extract the system data in the steady state. The average value of each segment of steady-state data is taken as the variable data representing the steady-state segment, and a database is established based on these variable data to facilitate subsequent analysis, extraction and use.
(12)建立基于机器学习的偏差补偿模型。通过变量关联分析以及稳态检测分析之后,确定了输入变量及对应的数据集,将输入变量的数据集输入到建立的机理模型中,可以得到机理模型的预测偏差,这些偏差将作为神经网络的输出变量。为了能够进一步区分不同变量对产物收率和产物性质的影响,同时提高模型的预测精度,采用双路输入的两层神经网络模型作为学习算法,网络结构如图6所示。将对产物收率和分布影响较大的反应系统变量和原料油性质变量经主成分分析降维后从第一个隐含层输入,而对产物收率和分布影响较小的分馏系统和吸收稳定系统的变量经主成分分析降维后从第二个隐含层输入;构建分别包含5到15个神经元的两层神经网络,将样本数据随机划分为训练集、验证集和测试集,参数学习采用梯度下降和误差反向传递的方法。经过训练后,得到输入输出的预测模型。模型的误差如图7、图8所示。(12) Establish a deviation compensation model based on machine learning. After variable correlation analysis and steady-state detection analysis, the input variables and corresponding data sets are determined, and the data sets of input variables are input into the established mechanism model to obtain the prediction deviation of the mechanism model, which will be used as the neural network. output variable. In order to further distinguish the influence of different variables on product yield and product properties, and improve the prediction accuracy of the model, a two-layer neural network model with dual input is used as the learning algorithm. The network structure is shown in Figure 6. The reaction system variables and raw oil property variables that have a greater impact on product yield and distribution are input from the first hidden layer after dimensionality reduction through principal component analysis, while the fractionation system and absorption system that have less impact on product yield and distribution The variables of the stable system are input from the second hidden layer after dimensionality reduction by principal component analysis; a two-layer neural network containing 5 to 15 neurons is constructed, and the sample data is randomly divided into training set, verification set and test set, Parameter learning adopts the method of gradient descent and error backpropagation. After training, a predictive model of input and output is obtained. The error of the model is shown in Figure 7 and Figure 8.
(13)模型自动更新。步骤(7)-(12)可在生产过程中与实时数据相结合,运用装置实时数据对模型进行参数校正和偏差补偿模型自动更新,从而实现模型的自动更新。(13) The model is automatically updated. Steps (7)-(12) can be combined with real-time data in the production process, and the real-time data of the device is used to perform parameter correction and automatic update of the deviation compensation model, thereby realizing automatic update of the model.
以上的所述乃是本发明的具体实施例及所运用的技术原理,若依本发明的构想所作的改变,其所产生的功能作用仍未超出说明书及附图所涵盖的精神时,仍应属本发明的保护范围。The above descriptions are the specific embodiments of the present invention and the technical principles used. If the changes made according to the conception of the present invention do not exceed the spirit covered by the description and accompanying drawings, they should still be Belong to the protection scope of the present invention.

Claims (10)

  1. 一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于,包括如下步骤:A method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology, characterized in that it includes the following steps:
    (1)建立催化裂化装置模型,其中催化裂化装置模型包括原料分子解析模型、分子级动力学模型、提升管反应器模型、产物切割模型、物性模型;(1) Establish a catalytic cracking unit model, wherein the catalytic cracking unit model includes a raw material molecular analysis model, a molecular dynamics model, a riser reactor model, a product cutting model, and a physical property model;
    (2)基于实际工业数据,对步骤(1)所建模型的参数进行校正;(2) based on actual industrial data, the parameters of the model built in step (1) are corrected;
    (3)基于步骤(2)处理结果,建立基于机器学习算法的偏差补偿预测模型;其中,偏差补偿预测模型的输入是装置实际运行参数,输出是机理预测值与历史工况实际输出值之间的偏差,通过实际工况的偏差补偿,提升模型的预测精度;(3) Based on the processing results of step (2), a deviation compensation prediction model based on a machine learning algorithm is established; wherein, the input of the deviation compensation prediction model is the actual operating parameters of the device, and the output is the difference between the predicted value of the mechanism and the actual output value of the historical working condition The deviation of the actual working conditions is compensated to improve the prediction accuracy of the model;
    (4)通过步骤(2)与步骤(3)可在生产过程中与催化裂化装置的实时数据建立通讯机制,实时读取装置数据并进行模型校正和偏差补偿预测模型的更新,实现预测模型的自动更新。(4) Through steps (2) and (3), a communication mechanism can be established with the real-time data of the catalytic cracking unit in the production process, and the device data can be read in real time and the model correction and deviation compensation prediction model can be updated to realize the prediction model Automatic updates.
  2. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于:所述步骤(1)建立的原料分子解析模型的方法具体如下:A method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology according to claim 1, characterized in that: the method of the raw material molecular analysis model established in the step (1) is specifically as follows:
    (1.1)原料分子库构建:对原料进行实验分析表征,确定原料分子的核心结构,在核心分子结构基础上按照一定策略添加侧链、支链和甲基,得到原料分子库;(1.1) Raw material molecular library construction: carry out experimental analysis and characterization of the raw material, determine the core structure of the raw material molecule, add side chains, branch chains and methyl groups on the basis of the core molecular structure according to a certain strategy, and obtain the raw material molecular library;
    (1.2)原料分子浓度解析:分子浓度的初值根据原料组成特征按照概率分布进行设定,然后通过全局优化算法对分布参数和分子浓度进行调整,使最终的分子浓度分布能够满足原料的各项宏观性质,可以根据进料的宏观物性如密度、残炭、硫含量、氮含量、族组成、馏程解析成详细分子组成;通过分子浓度组成构建技术,根据各项可通过实验分析获取的宏观性质对催化裂化原料的分子组成进行反演分析。(1.2) Raw material molecular concentration analysis: the initial value of the molecular concentration is set according to the composition characteristics of the raw material according to the probability distribution, and then the distribution parameters and molecular concentration are adjusted through the global optimization algorithm, so that the final molecular concentration distribution can meet the requirements of the raw material. Macroscopic properties can be analyzed into detailed molecular composition according to the macroscopic physical properties of the feed such as density, carbon residue, sulfur content, nitrogen content, group composition, and distillation range; through the molecular concentration composition construction technology, according to various macroscopic properties that can be obtained through experimental analysis Properties Inversion analysis of molecular composition of FCC feedstock.
  3. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于:所述步骤(1)中的分子级动力学模型的方法具体如下:A method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology according to claim 1, wherein the method of the molecular-level kinetic model in the step (1) is specifically as follows:
    (1.3)编写反应规则,构建反应网络:根据催化裂化反应的正碳离子机理,对不同的类型的反应分别建立了反应物选择规则和产物生成规则,针对每一类反应各编写一类规则函数,编写了包含裂化、开环、异构、氢转移、缩合五类主要反应的大类反应规则,利用计算机辅助技术对原料分子应用反应规则,自动生成反应网络;其中反应规则的种类优选在10个-50个。(1.3) Write reaction rules and construct reaction network: According to the carbenium ion mechanism of catalytic cracking reaction, reactant selection rules and product generation rules were established for different types of reactions, and a class of rule functions was written for each type of reaction , compiled a large class of reaction rules including cracking, ring-opening, isomerization, hydrogen transfer, and condensation, and used computer-aided technology to apply reaction rules to raw material molecules to automatically generate reaction networks; among them, the types of reaction rules are preferably within 10 pcs - 50 pcs.
  4. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于:所述步骤(1)中的提升管反应器模型的方法具体如下:A method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology according to claim 1, wherein the method for the riser reactor model in the step (1) is specifically as follows:
    (1.4)建立反应器模型,求解模型,计算产物分子浓度分布;所建的反应器模型包括单提升管模型、MIP双提升管模型、DCC的主副提升管并联模型等常见催化裂化工艺;将反应网络、化学计量学、反应速率方程和动力学参数与上述反应器模型组合,即可得到完整的催化裂化反应器模型。(1.4) Build a reactor model, solve the model, and calculate the product molecular concentration distribution; the built reactor model includes common catalytic cracking processes such as single riser model, MIP double riser model, DCC main and auxiliary riser parallel model; The reaction network, stoichiometry, reaction rate equation and kinetic parameters are combined with the above reactor model to obtain a complete FCC reactor model.
  5. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于:所述步骤(1)中的产物切割模型的方法具体如下:A method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology according to claim 1, wherein the method of the product cutting model in the step (1) is specifically as follows:
    (1.5)产物切割模型:对从反应器出来的产物油气混合分子,根据各项产品质量要求将混合油气切割分离成干气、液化气、汽油、柴油、油浆、焦炭各流股产品;其中,产物切割模型可采用基于沸点切割的简易切割模型,同时考虑重叠因子的影响;(1.5) Product cutting model: For the product oil-gas mixture molecules coming out of the reactor, the mixed oil-gas is cut and separated into stream products of dry gas, liquefied gas, gasoline, diesel oil, oil slurry, and coke according to various product quality requirements; , the product cutting model can adopt a simple cutting model based on boiling point cutting, while considering the influence of overlapping factors;
    所述步骤(1)中的物性模型的具体方法如下:The concrete method of the physical property model in described step (1) is as follows:
    (1.6)物性计算:通过物性计算模型,采用基团贡献法以及经验关联方法,用各项产物的分子浓度计算产物的性质,包括汽油和柴油的各项物性。(1.6) Calculation of physical properties: Through the physical property calculation model, the group contribution method and the empirical correlation method are used to calculate the properties of the products with the molecular concentration of each product, including the physical properties of gasoline and diesel.
  6. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于,所述步骤(2)中的参数校正的具体方法为:通过实际工业数据对模型的参数进行校正,完成分子级机理模型;工业数据包括反应器结构尺寸参数、催化剂参数、进出料的性质检测数据(LIMS数据)、装置操作参数(DCS数据)。A method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology according to claim 1, characterized in that, the specific method of parameter correction in the step (2) is: through actual industrial data to The parameters of the model are corrected to complete the molecular-level mechanism model; industrial data include reactor structure size parameters, catalyst parameters, property detection data of incoming and outgoing materials (LIMS data), and device operating parameters (DCS data).
  7. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于:所述步骤(3)的具体方法如下:A method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology according to claim 1, characterized in that: the specific method of the step (3) is as follows:
    (3.1)数据采集及整理:读取装置的DCS、LIMS历史生产数据,建立数据库,规范格式并建立索引规则,方便后期查询和调用;(3.1) Data collection and arrangement: read the DCS and LIMS historical production data of the device, establish a database, standardize the format and establish indexing rules to facilitate later query and call;
    (3.2)数据预处理:从数据库中抽取数据进行处理工作,包括缺失插值处理、异常值处理、数据平滑降噪、数据归一化处理;(3.2) Data preprocessing: Extract data from the database for processing, including missing interpolation processing, outlier processing, data smoothing and noise reduction, and data normalization processing;
    (3.3)变量关联分析:通过相关性算法对各个变量间的相关性进行计算,并结合专家经验分析,选取最相关的变量进行建模;具体的,变量关联分析的方法选择皮尔逊相关性分析、传递熵、格兰杰因果分析中的任意一种,并结合专家经验分析,从众多变量中挑选关联性强的变量进行建模;(3.3) Variable correlation analysis: Calculate the correlation between variables through the correlation algorithm, and combine expert experience analysis to select the most relevant variables for modeling; specifically, the method of variable correlation analysis chooses Pearson correlation analysis , transfer entropy, and Granger causality analysis, combined with expert experience analysis, select highly correlated variables from many variables for modeling;
    (3.4)稳态分析:通过建立的稳态分析规则对系统进行稳态检测,并析取各个稳态下对应的工况,使用得到的稳态工况建立数据库,方便后续更新和使用;(3.4) Steady-state analysis: The steady-state detection of the system is carried out through the established steady-state analysis rules, and the corresponding working conditions in each steady state are extracted, and a database is established using the obtained steady-state working conditions to facilitate subsequent updates and use;
    (3.5)建立偏差补偿预测模型:将历史工况对应的输入变量输入到建立的机理模型中,得到机理模型的预测值,然后计算机理预测值与历史工况实际输出值之间的偏差,通过主成分分析降低输入变量的输入维度,通过机器学习算法建立偏差补偿预测模型,机理模型预测值加偏差补偿得到最终的预测结果。(3.5) Establish a deviation compensation prediction model: input the input variables corresponding to the historical working conditions into the established mechanism model to obtain the predicted value of the mechanism model, and then calculate the deviation between the predicted value of the mechanism and the actual output value of the historical working condition, through The principal component analysis reduces the input dimension of the input variables, establishes the deviation compensation prediction model through the machine learning algorithm, and adds the deviation compensation to the predicted value of the mechanism model to obtain the final prediction result.
  8. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于:所述步骤(3.2)中的缺失插值处理方法选择线性插值、三次样条插值、均值插值、拉格朗日插值中的任意一种;异常值识别方法选择3σ准则法、箱线图法、格拉布斯检验法中的任意一种;数据降噪平滑方法选择稳健二次回归方法,消除高频噪音信号,保留低频的数据趋势。A method for simulating and predicting a catalytic cracking unit based on a molecular-level mechanism model and big data technology according to claim 1, characterized in that: the missing interpolation processing method in the step (3.2) selects linear interpolation and cubic spline interpolation Any one of , mean interpolation, and Lagrangian interpolation; the outlier identification method chooses any one of the 3σ criterion method, box plot method, and Grubbs test method; the data noise reduction smoothing method chooses robust quadratic regression method to eliminate high-frequency noise signals and retain low-frequency data trends.
  9. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于:所述步骤(3.4)中的稳态分析的方法分为单变量稳态分析和系统稳态分析:A method for simulating and predicting catalytic cracking units based on molecular-level mechanism models and big data technology according to claim 1, characterized in that: the steady-state analysis method in the step (3.4) is divided into univariate steady-state analysis and a steady-state analysis of the system:
    (i)单变量稳态分析:采用小波变换的方法对数据集进行趋势提取,通过将信号分解为高频段的噪声和代表信号趋势的低频段,来对测量数据进行有限连续的逼近,得到过程变量的近似函数f(t),建立了稳态指数β(0≤β≤1)来表示变量工况状态的稳定程度,当β=0时,过程变量处于非稳态,β=1时,过程变量处于稳态,0<β<1时,表示过程变量处于过渡态,并且β越接近于1,表示过程变量的状态越稳定;稳态指数β(t)由数据趋势的一阶导数f’(t 0)和二阶导数f”(t 0)根据以下准则共同决定: (i) Univariate steady-state analysis: use the wavelet transform method to extract the trend of the data set, and decompose the signal into the noise of the high frequency band and the low frequency band representing the trend of the signal to perform finite continuous approximation on the measured data, and obtain the process The approximate function f(t) of the variable establishes a steady-state index β (0≤β≤1) to represent the stability of the variable working condition. When β=0, the process variable is in an unsteady state. When β=1, The process variable is in a steady state. When 0<β<1, it means that the process variable is in a transition state, and the closer β is to 1, the more stable the state of the process variable is; the steady state index β(t) is determined by the first derivative of the data trend f '(t 0 ) and the second derivative f”(t 0 ) are jointly determined according to the following criteria:
    θ(t)=|f'(t)|+γ|f"(r)|θ(t)=|f'(t)|+γ|f"(r)|
    式中:In the formula:
    Figure PCTCN2022111033-appb-100001
    Figure PCTCN2022111033-appb-100001
    Figure PCTCN2022111033-appb-100002
    Figure PCTCN2022111033-appb-100002
    其中T s、T w、T u为阈值,其确定方法如下:在历史数据库中选择过程处于稳态的一段数据作为参考基准,通过小波变换提取过程变量的变化趋势后,得到过程变量在采样点的一阶导数序列和二阶导数序列,通过分别求其百分位数,则:T s为一阶导数的百分位数,T w为二阶导数的百分位数,一般可选90%分位数或95%分位数,其中 Among them, T s , T w , and Tu are the thresholds, and the determination method is as follows: select a section of data in the historical database that is in a steady state as a reference, and extract the change trend of the process variable through wavelet transform to obtain the process variable at the sampling point. The first-order derivative sequence and the second-order derivative sequence of , by calculating their percentiles respectively, then: T s is the percentile of the first-order derivative, T w is the percentile of the second-order derivative, generally 90 % quantile or 95% quantile, where
    T u=αT s T u =αT s
    α为可调参数,一般取[2,5]之间的整数;通过以上公式,可得到过程变量的稳态判断阈值;α is an adjustable parameter, which generally takes an integer between [2,5]; through the above formula, the steady-state judgment threshold of the process variable can be obtained;
    (ii)系统稳态分析:采用单变量稳态检测规则得到各个变量的稳态指数β i,整个系统的稳态状况有各变量的稳态指数按下式加权决定: (ii) System steady-state analysis: The steady-state index β i of each variable is obtained by using the single-variable steady-state detection rule, and the steady-state condition of the entire system is determined by the weighting of the steady-state index of each variable according to the following formula:
    Figure PCTCN2022111033-appb-100003
    Figure PCTCN2022111033-appb-100003
    其中,p为系统的关键特征变量个数,β i(t)为第i个变量的稳态指数,u i为第i个变量的权重。 Among them, p is the number of key characteristic variables of the system, β i (t) is the steady-state index of the i-th variable, and u i is the weight of the i-th variable.
  10. 根据权利要求1所述的一种基于分子级机理模型与大数据技术的催化裂化装置模拟预测方法,其特征在于:所述步骤(3.5)中的机器学习算法选择前馈神经网络、循环神经网络、支持向量机、最小二乘法、最小二乘支持向量机、极限学习机回归算法中的任意一种。A method for simulating and predicting catalytic cracking units based on molecular-level mechanism models and big data technology according to claim 1, characterized in that: the machine learning algorithm in the step (3.5) selects feedforward neural network and recurrent neural network , support vector machine, least squares method, least squares support vector machine, extreme learning machine regression algorithm.
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