CN114036670A - Method for optimizing separation performance of liquid-solid hydrocyclone based on transfer learning - Google Patents

Method for optimizing separation performance of liquid-solid hydrocyclone based on transfer learning Download PDF

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CN114036670A
CN114036670A CN202111323572.XA CN202111323572A CN114036670A CN 114036670 A CN114036670 A CN 114036670A CN 202111323572 A CN202111323572 A CN 202111323572A CN 114036670 A CN114036670 A CN 114036670A
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hydrocyclone
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鄂殿玉
崔佳鑫
范海瀚
许光泰
苏中方
黄发源
李政权
翁凌熠
谭聪
郑奇军
焦璐璐
邹瑞萍
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Nanjing Aobo Industrial Intelligent Technology Research Institute Co ltd
Jiangxi University of Science and Technology
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Abstract

The invention provides a method for optimizing the separation performance of a liquid-solid hydrocyclone based on transfer learning, which comprises the following steps: training and establishing a data source domain of the liquid-solid hydrocyclone under each working condition, and modeling the working condition under an unknown mode through transfer learning to determine characteristic parameters of the liquid-solid hydrocyclone; acquiring empirical characteristic parameters of the liquid-solid hydrocyclone; performing numerical simulation according to the characteristic parameters of the liquid-solid hydrocyclone and the acquired empirical characteristic parameters; determining and obtaining a geometric model of the liquid-solid hydrocyclone determined by transfer learning through numerical simulation; calculating the flow characteristic, the air column characteristic and the solid phase flow characteristic of the gas-liquid two-phase flow and the simulated separation efficiency of the liquid-solid hydrocyclone; and then calculating to obtain the optimal separation efficiency value of the liquid-solid hydrocyclone. The invention can efficiently realize the improvement of the separation performance of the liquid-solid separation hydrocyclone.

Description

Method for optimizing separation performance of liquid-solid hydrocyclone based on transfer learning
Technical Field
The invention relates to the technical field of design of hydrocyclones, in particular to a method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning.
Background
The hydrocyclone is a commonly used two-phase separation device in industrial production and has the advantages of simple structure, convenient operation, high production capacity, high separation efficiency, small occupied area and the like. The application of the hydrocyclone comprises solid-liquid separation, liquid-gas separation, solid-solid separation, liquid-liquid separation, liquid-gas-solid three-phase simultaneous separation and the like. The hydrocyclone is used as a separation and classification device, the basic working principle is based on the centrifugal sedimentation effect, when two-phase mixed liquid to be separated enters a device from an inlet of the hydrocyclone under certain pressure, strong rotary motion is generated, because the density difference exists between a light phase and a heavy phase, the centrifugal force, the centripetal buoyancy and the fluid drag force are different, under the centrifugal sedimentation effect, most of the heavy phase is discharged through a bottom flow port of the hydrocyclone, and most of the light phase is discharged from an overflow port, so that the separation purpose is achieved.
At present, the hydrocyclone is widely used in the fields of petroleum, chemical industry, mining industry, food, environmental protection and the like. For example, classification, sorting, product concentration, paint washing clarification and the like in mining and metallurgy engineering; oil-water separation in petrochemical industry; grading coarse and fine particles, removing impurities, washing paint of starch and the like in the food industry; preparation of paper coating in the paper industry, treatment of paper-making wastewater and the like; industrial and domestic wastewater treatment in environmental engineering, and the like.
Hydrocyclones are generally used for industrial scale production, and the performance of hydrocyclones has an important influence on the production capacity, economic benefit and product quality thereof. In practical applications, hydrocyclones are usually selected according to production capacity, classification particle size or existing products, or preliminary design of basic diameters and related structural parameters of the hydrocyclones is carried out by an empirical method, and the hydrocyclones determined according to the modes are difficult to realize the optimal performance under specific production requirements. Therefore, the method has important engineering significance for further optimization of the hydrocyclone.
At present, the optimization research of the hydrocyclone is more specific to the engineering application problem. (1) The influence of each factor on the performance of the hydrocyclone is quantitatively analyzed through a single-factor test method, and then the selection of key parameters of the hydrocyclone is realized. The method can intuitively obtain the influence rule of each factor on the performance of the hydrocyclone, but the test quantity is huge, and meanwhile, the influence of the interaction among the factors is ignored; (2) and (3) designing a test scheme by using a test design method, and performing statistical analysis on test results to realize parameter optimization. The method is also limited by the test cost and workload, the selection of the number of test factors is greatly limited, and only part of parameters can be optimized; (3) and the other method is to apply a numerical simulation method and analyze the influence of each influencing factor on the internal flow field characteristic and the performance of the hydrocyclone through single-factor numerical simulation. The method can perform approximate quantitative analysis on the partial performance of the hydrocyclone by selecting a proper turbulence model and simulation parameters, and simultaneously obtains the influence rule of each factor on the internal flow field, thereby analyzing the separation mechanism of the hydrocyclone. However, the numerical simulation method is greatly influenced by model selection and grid division methods, and the current numerical simulation method is mostly used for researching the influence rule of each factor on the flow field characteristics in the hydrocyclone, has a certain theoretical guidance effect on the structural design and process formulation of the hydrocyclone, but is difficult to be directly used in engineering application. (4) And the other method is to analyze the internal flow field of the hydrocyclone through numerical simulation, so as to improve the structure of the hydrocyclone according to the existing hydrocyclone separation mechanism. Obviously, the improvement is still obtained by a qualitative method, the optimization capability is limited, meanwhile, the pertinence is strong, and the reference of other engineering application problems is inconvenient.
Specifically, the separation performance of hydrocyclones is affected by a number of factors including: physical property parameters, operational parameters, and structural parameters. Wherein, the physical property parameters comprise 2 items of particle density and particle granularity; the operation parameters comprise 2 items of ore pulp concentration and inlet speed; the structural parameters comprise 8 items of basic diameter of the hydrocyclone, length of a column section, cone angle, inlet diameter, overflow port diameter, underflow port diameter, insertion depth of the overflow pipe, wall thickness of the overflow pipe and the like. In addition, the installation inclination angle of the hydrocyclone and the external environment pressure can also influence the separation performance.
In theory, the performance of a hydrocyclone can be analyzed and described by its internal flow field. However, the structure and operation of the hydrocyclone seem simple, the internal flow field of the hydrocyclone is extremely complex, and although scholars at home and abroad carry out a great deal of research on the internal flow field of the hydrocyclone and put forward a plurality of theories, methods and empirical models for designing and optimizing the hydrocyclone, various defects still exist. For example, lack of generality, based on certain specific conditions; or the accuracy is low due to the removal of various influencing factors and the interaction influence among the factors; or simply analyzing the optimization from a qualitative perspective results in a more comprehensive result; or rely on a large amount of tests to cause the problems of huge workload and cost and low working efficiency. Based on this, there is a need to provide a new method for optimizing the separation performance of a liquid-solid hydrocyclone based on migration learning, so as to solve the above technical problems.
Disclosure of Invention
Based on this, the invention aims to provide a method for optimizing the separation performance of a liquid-solid hydrocyclone based on transfer learning, so as to solve the technical problems.
The invention provides a method for optimizing the separation performance of a liquid-solid hydrocyclone based on transfer learning, wherein the method comprises the following steps:
the method comprises the following steps: training and establishing a data source domain of the liquid-solid hydrocyclone under each working condition, and modeling the working condition under an unknown mode through transfer learning to determine characteristic parameters of the liquid-solid hydrocyclone;
step two: acquiring empirical characteristic parameters of the liquid-solid hydrocyclone;
step three: respectively carrying out numerical simulation by adopting a quadratic orthogonal rotation combined test method according to the characteristic parameters of the liquid-solid hydrocyclone and the acquired empirical characteristic parameters;
step four: respectively determining and obtaining a geometric model of the liquid-solid hydrocyclone determined through transfer learning and a geometric model of the liquid-solid hydrocyclone determined through the empirical characteristic parameters through numerical simulation in the third step;
step five: by utilizing a computational fluid dynamics principle, the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of the gas-liquid two-phase flow corresponding to the geometric model of the liquid-solid hydrocyclone determined by transfer learning are calculated in a simulation mode, and the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of the gas-liquid two-phase flow corresponding to the geometric model of the liquid-solid hydrocyclone determined by empirical characteristic parameters are calculated in a simulation mode;
step six: and determining to obtain the optimal separation efficiency value of the liquid-solid hydrocyclone according to the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of each gas-liquid two-phase flow.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning comprises the following steps of:
training and establishing a data source domain of the liquid-solid hydrocyclone under each working condition, wherein data samples in the data source domain are provided with labels;
and taking a new working condition needing to be tested in an unknown mode as a target field, and constructing a feature subspace according to data source domain and data in the target field based on a transfer learning principle.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning is characterized in that in the step one, the characteristic parameters comprise physical property parameters, geometric parameters, operation parameters and separation efficiency;
wherein the physical property parameters comprise inlet flow rate, particle size, inlet density difference and particle concentration; the geometric parameters comprise the diameter of the feeding pipe, the diameter of the cylindrical section, the length of the cylindrical section, the upper diameter of the conical section, the lower diameter of the conical section, the cone angle, the diameter of the overflow pipe, the length of the overflow pipe, the diameter of the underflow pipe and the length of the underflow pipe; the operating parameters include inlet speed and reflux ratio.
In the fifth step, when performing simulation calculation, the corresponding simulation condition setting includes:
adopting pressure coupling; carrying out simulation calculation based on an implicit equation and an unsteady algorithm; constructing a fluid volume function model and a gas-liquid two-phase environment; the inlet adopts a speed inlet, and the overflow port and the low flow port both adopt pressure outlets; the pressure-velocity coupling is performed by pressure correction, and the discrete format is performed by PRESTO! And (4) format.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning is characterized in that after the sixth step, the method further comprises the following steps:
and inputting the obtained optimal separation efficiency value of the liquid-solid hydrocyclone into the data source domain so as to reduce the error when data migration calculation iteration is carried out.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning comprises the following steps of constructing a feature subspace according to data of a data source domain and data of a target domain based on the transfer learning principle:
and constructing the relation between the data source domain and the target domain by using an Euclidean distance formula, a cosine similarity formula, a probability mutual information formula, an information divergence formula, a JS distance formula, a maximum mean difference formula and a greedy distance formula.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning is characterized in that the Euclidean distance formula is expressed as follows:
Figure BDA0003345512380000041
wherein d isEuclideanExpressing the Euclidean distance, wherein x and y respectively express coordinates corresponding to a point x and a point y on a space model, and T is a transposed matrix operation;
the cosine similarity formula is expressed as:
Figure BDA0003345512380000051
wherein cos (x, y) represents the cosine similarity between point x and point y, | x |, | y | are the absolute value operations of point x and point y, respectively.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning is characterized in that the probability mutual information formula is as follows:
Figure BDA0003345512380000052
wherein I (X; Y) represents the probability mutual reliability between the point X and the point Y, p (X, Y) represents the probability that the point X and the point Y have a common feature subspace, p (X) represents the probability that the point X has an independent subspace, and p (Y) represents the probability that the point Y has an independent subspace;
the information divergence formula is expressed as:
Figure BDA0003345512380000053
wherein D isKL(P | | Q) represents the divergence of information between region P and region Q, P (x) represents the probability distribution of point x at region P, and Q (x) represents the probability distribution of point x at region Q.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning is characterized in that the JS distance formula is expressed as follows:
Figure BDA0003345512380000054
wherein JSD (P | | Q) represents JS distance, DKL(P M) represents the divergence of information between region P and region M, DKL(Q | | M) represents the divergence of information between region Q and region M;
the maximum mean difference formula is expressed as:
Figure BDA0003345512380000061
wherein, MMD2(X, Y) represents the maximum mean difference,
Figure BDA0003345512380000062
representing the set of mappings for point x,
Figure BDA0003345512380000063
represents the set of mappings to which point y corresponds,
Figure BDA0003345512380000065
representing the regenerated nuclear hilbert space.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning is characterized in that the greedy distance formula is expressed as follows:
Figure BDA0003345512380000064
wherein, Wp(P, Q) represents a greedy distance, ρ (x, y) represents a distance function between a point x and a point y in the set M, Γ (P, Q) represents a joint distribution of all points in the set M × M, the joint distribution having the region P and the region Q as an edge distribution, and d μ (x, y) represents a differential value of the distance function between the point x and the small number of points.
The method for optimizing the separation performance of the liquid-solid hydrocyclone based on the transfer learning has the following beneficial effects:
1. according to the method, based on the principle of transfer learning, according to the design theory and the empirical method of the liquid-solid hydrocyclone, the relevant structural parameters and efficiency comparison of the liquid-solid hydrocyclone are specifically and rapidly given, and according to the actual engineering situation, the structural parameters of the hydrocyclone to be optimized are determined, so that a foundation is laid for the parameter optimization of the liquid-solid hydrocyclone;
2. in the invention, a numerical simulation method is utilized, and the optimization of the operation parameters and the structural parameters is carried out step by step for optimizing the performance of the liquid-solid hydrocyclone, thereby effectively solving the problems of complex design, huge cost and low efficiency of the existing hydrocyclone. The separation performance of the liquid-solid separation hydrocyclone can be simply, economically and efficiently improved;
3. by adopting the migration data provided by the invention, the experimental method of orthogonal numerical simulation parameters is combined with the empirical data, so that the consistency of the numerical simulation result and the test result can be effectively ensured, and the feasibility of replacing the test result with the numerical simulation result is ensured; meanwhile, the influence of errors existing in numerical simulation results on optimization results can be effectively avoided by processing the orthogonal parameter test design method;
4. according to the invention, the structural design and parameter optimization of the liquid-solid hydrocyclone can be rapidly realized by using data migration according to the actual engineering requirements, the separation performance of the hydrocyclone is obviously improved, the production efficiency is improved, the production cost is reduced, and the product quality is improved; and the data optimized by the experiment is fed back to the source field, so that the accuracy and the efficiency of data migration under different working conditions can be continuously improved. The test proves that: according to the optimization result obtained by the method, high-purity overflow concentrate can be obtained while energy consumption is reduced and the concentration of the concentrate in overflow is improved.
Additional features and advantages of the disclosure will be set forth in the description which follows, or in part may be learned by the practice of the above-described techniques of the disclosure, or may be learned by practice of the disclosure.
In order to make the aforementioned and other objects, features and advantages of the present invention comprehensible, preferred embodiments accompanied with figures are described in detail below.
Drawings
FIG. 1 is a schematic block diagram of a method for optimizing the separation performance of a liquid-solid hydrocyclone based on transfer learning according to the present invention;
FIG. 2 is a flow chart of a method for optimizing the separation performance of a liquid-solid hydrocyclone based on transfer learning according to the present invention;
FIG. 3 is a schematic structural view of a liquid-solid hydrocyclone in the present invention;
FIG. 4 is a basic geometric model of a liquid-solid hydrocyclone in accordance with the present invention;
FIG. 5 is a top view of an orthogonal optimized inlet configuration for a liquid-solid hydrocyclone in accordance with the present invention;
FIG. 6 is a comparison of separation efficiency curves for a liquid-solid hydrocyclone in accordance with the present invention.
Detailed Description
To facilitate an understanding of the invention, the invention will now be described more fully with reference to the accompanying drawings. Preferred embodiments of the present invention are shown in the drawings. This invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
Referring to fig. 1 and fig. 2, the present invention provides a method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning, wherein the method comprises the following steps:
s101, training and establishing a data source domain of the liquid-solid hydrocyclone under each working condition, and modeling the working condition under an unknown mode through transfer learning to determine characteristic parameters of the liquid-solid hydrocyclone.
In this step, the characteristic parameters include physical parameters, geometric parameters, operational parameters and separation efficiency.
Wherein, the physical parameters comprise inlet flow rate, particle size, inlet density difference and particle concentration. The geometric parameters include feed pipe diameter, cylinder section length, cone section upper diameter, cone section lower diameter, cone angle, overflow pipe diameter, overflow pipe length, underflow pipe diameter, and underflow pipe length. Further, the operating parameters include inlet speed and reflux ratio.
Specifically, in this step, the method for training and establishing the data source domain of the liquid-solid hydrocyclone under each working condition and modeling the working condition under the unknown mode through transfer learning specifically includes the following steps:
s1011, training and establishing a data source domain of the liquid-solid hydrocyclone under each working condition, wherein data samples in the data source domain are provided with labels.
And S1012, taking the new working condition to be tested in the unknown mode as a target field, and constructing a feature subspace according to the data source domain and the data of the target field based on the transfer learning principle.
In the step of constructing the feature subspace according to the data of the data source domain and the data of the target domain, a relation between the data source domain and the target domain needs to be constructed by using an Euclidean distance formula, a cosine similarity formula, a probability mutual information formula, an information divergence formula, a JS distance formula, a maximum mean difference formula and a greedy distance formula.
Wherein, the Euclidean distance formula is expressed as:
Figure BDA0003345512380000081
wherein d isEuclideanAnd expressing the Euclidean distance, wherein x and y respectively express coordinates corresponding to a point x and a point y on the space model, and T is a transposed matrix operation.
Meanwhile, the cosine similarity formula is expressed as:
Figure BDA0003345512380000091
wherein cos (x, y) represents the cosine similarity between the point x and the point y, and | x |, | y | are the absolute value operations of the point x and the point y, respectively.
Further, in this embodiment, the two probability distributions X and Y are defined, where X belongs to X and Y belongs to Y, and the mutual probability information formula is expressed as:
Figure BDA0003345512380000092
wherein I (X; Y) represents the probability mutual reliability between the point X and the point Y, p (X, Y) represents the probability that the point X and the point Y have a common feature subspace, p (X) represents the probability that the point X has an independent subspace, and p (Y) represents the probability that the point Y has an independent subspace.
Further, the information divergence formula is expressed as:
Figure BDA0003345512380000093
wherein D isKL(P | | Q) represents the divergence of information between region P and region Q, P (x) represents the probability distribution of point x at region P, and Q (x) represents the probability distribution of point x at region Q. It should be noted that D isKL(P | Q) is used to represent the distance between probability distribution P (x) and probability distribution Q (x).
Further, the JS distance formula is expressed as:
Figure BDA0003345512380000094
wherein JSD (P | | Q) represents JS distance, DKL(P M) represents the divergence of information between region P and region M, DKL(Q | | M) represents the divergence of information between region Q and region M.
Further, the maximum mean difference formula is as follows:
Figure BDA0003345512380000101
wherein, MMD2(X, Y) represents the maximum mean difference,
Figure BDA0003345512380000102
representing the set of mappings for point x,
Figure BDA0003345512380000103
represents the set of mappings to which point y corresponds,
Figure BDA0003345512380000105
representing the regenerated nuclear hilbert space.
Further, the greedy Distance (Wasserstein Distance) formula is expressed as:
Figure BDA0003345512380000104
wherein, Wp(P, Q) represents a greedy distance, ρ (x, y) represents a distance function between the point x and the point y in the set M, Γ (P, Q) represents a joint distribution of all the points in the set M × M, the joint distribution having the region P and the region Q as an edge distribution, and d μ (x, y) represents a differential value of the distance function between the point x and the point y.
S102, acquiring empirical characteristic parameters of the liquid-solid hydrocyclone.
In this step, it should be noted that the empirical characteristic parameters are calculated by a conventional empirical calculation method.
S103, respectively carrying out numerical simulation by adopting a quadratic orthogonal rotation combined test method according to the characteristic parameters of the liquid-solid hydrocyclone and the acquired empirical characteristic parameters.
In the step, the characteristic parameters of the liquid-solid hydrocyclone determined by the secondary orthogonal rotation combined test transfer learning and the traditional method are adopted, and the parameters of the scheme are operated to carry out numerical simulation and test optimization. As described in step S101, the characteristic parameters include physical property parameters, geometric parameters, and operation parameters.
And S104, respectively determining and obtaining a geometric model of the liquid-solid hydrocyclone determined through transfer learning and a geometric model of the liquid-solid hydrocyclone determined through the empirical characteristic parameters through numerical simulation in the third step.
And S105, by utilizing the computational fluid dynamics principle, performing simulation calculation on the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of the gas-liquid two-phase flow corresponding to the geometric model of the liquid-solid hydrocyclone determined by the transfer learning, and performing simulation calculation on the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of the gas-liquid two-phase flow corresponding to the geometric model of the liquid-solid hydrocyclone determined by the empirical characteristic parameters.
In this step, when performing simulation calculation, the corresponding simulation condition setting includes:
adopting pressure coupling; carrying out simulation calculation based on an implicit equation and an unsteady algorithm; constructing a fluid volume function model and a gas-liquid two-phase environment; the inlet adopts a speed inlet, and the overflow port and the low flow port both adopt pressure outlets; the pressure-velocity coupling is performed by pressure correction, and the discrete format is performed by PRESTO! And (4) format.
Further, after the conditions are set, the pressure drop, the tangential velocity, the axial velocity and the radial velocity of the gas-liquid two-phase flow and the gas-liquid-solid three-phase flow of the liquid-solid hydrocyclone can be calculated and determined.
And S106, determining and obtaining the optimal separation efficiency value of the liquid-solid hydrocyclone according to the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of each gas-liquid two-phase flow.
In this step, it specifically includes:
and inputting the obtained optimal separation efficiency value of the liquid-solid hydrocyclone into a data source domain to reduce the error when data migration calculation iteration is carried out.
It should be added to the description here that characteristic parameters of the operating condition liquid-solid hydrocyclone, including physical property parameters, geometric parameters, operating parameters and separation efficiency, are fed back to the data source domain, so that the richness of data, the accuracy of migration learning and the richness of the data source domain are further improved, and finally, the error during data migration is reduced through continuous learning, so that the effect that an optimal solution can be obtained only through one migration is achieved.
In the present invention, please refer to fig. 3 and 4, for the liquid-solid hydrocyclone proposed in the present invention, wherein 1 is the length of the cylindrical section of the hydrocyclone, 2 is the insertion depth of the overflow pipe of the hydrocyclone, 3 is the diameter of the overflow port, 4 is the wall thickness of the overflow pipe, 5 is the inlet width of the hydrocyclone, 6 is the basic diameter of the hydrocyclone, 7 is the taper angle, 8 is the diameter of the underflow port, and 9 is the inlet length of the hydrocyclone.
Meanwhile, as shown in fig. 5 and fig. 6, it can be known that the method for optimizing the separation performance of the liquid-solid hydrocyclone based on the migration learning provided by the present invention has the following beneficial effects:
1. according to the method, based on the principle of transfer learning, according to the design theory and the empirical method of the liquid-solid hydrocyclone, the relevant structural parameters and efficiency comparison of the liquid-solid hydrocyclone are specifically and rapidly given, and according to the actual engineering situation, the structural parameters of the hydrocyclone to be optimized are determined, so that a foundation is laid for the parameter optimization of the liquid-solid hydrocyclone;
2. in the invention, a numerical simulation method is utilized, and the optimization of the operation parameters and the structural parameters is carried out step by step for optimizing the performance of the liquid-solid hydrocyclone, thereby effectively solving the problems of complex design, huge cost and low efficiency of the existing hydrocyclone. The separation performance of the liquid-solid separation hydrocyclone can be simply, economically and efficiently improved;
3. by adopting the migration data provided by the invention, the experimental method of orthogonal numerical simulation parameters is combined with the empirical data, so that the consistency of the numerical simulation result and the test result can be effectively ensured, and the feasibility of replacing the test result with the numerical simulation result is ensured; meanwhile, the influence of errors existing in numerical simulation results on optimization results can be effectively avoided by processing the orthogonal parameter test design method;
4. according to the invention, the structural design and parameter optimization of the liquid-solid hydrocyclone can be rapidly realized by using data migration according to the actual engineering requirements, the separation performance of the hydrocyclone is obviously improved, the production efficiency is improved, the production cost is reduced, and the product quality is improved; and the data optimized by the experiment is fed back to the source field, so that the accuracy and the efficiency of data migration under different working conditions can be continuously improved. The test proves that: according to the optimization result obtained by the method, high-purity overflow concentrate can be obtained while energy consumption is reduced and the concentration of the concentrate in overflow is improved.
Finally, it should be noted that: the above-mentioned embodiments are only specific embodiments of the present invention, which are used for illustrating the technical solutions of the present invention and not for limiting the same, and the protection scope of the present invention is not limited thereto, although the present invention is described in detail with reference to the foregoing embodiments, those skilled in the art should understand that: any person skilled in the art can modify or easily conceive the technical solutions described in the foregoing embodiments or equivalent substitutes for some technical features within the technical scope of the present disclosure; such modifications, changes or substitutions do not depart from the spirit and scope of the embodiments of the present invention, and they should be construed as being included therein. Therefore, the protection scope of the present invention shall be subject to the protection scope of the appended claims.

Claims (10)

1. A method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning is characterized by comprising the following steps:
the method comprises the following steps: training and establishing a data source domain of the liquid-solid hydrocyclone under each working condition, and modeling the working condition under an unknown mode through transfer learning to determine characteristic parameters of the liquid-solid hydrocyclone;
step two: acquiring empirical characteristic parameters of the liquid-solid hydrocyclone;
step three: respectively carrying out numerical simulation by adopting a quadratic orthogonal rotation combined test method according to the characteristic parameters of the liquid-solid hydrocyclone and the acquired empirical characteristic parameters;
step four: respectively determining and obtaining a geometric model of the liquid-solid hydrocyclone determined through transfer learning and a geometric model of the liquid-solid hydrocyclone determined through the empirical characteristic parameters through numerical simulation in the third step;
step five: by utilizing a computational fluid dynamics principle, the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of the gas-liquid two-phase flow corresponding to the geometric model of the liquid-solid hydrocyclone determined by transfer learning are calculated in a simulation mode, and the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of the gas-liquid two-phase flow corresponding to the geometric model of the liquid-solid hydrocyclone determined by empirical characteristic parameters are calculated in a simulation mode;
step six: and determining to obtain the optimal separation efficiency value of the liquid-solid hydrocyclone according to the flow characteristic, the air column characteristic, the solid phase flow characteristic and the simulated separation efficiency of the liquid-solid hydrocyclone of each gas-liquid two-phase flow.
2. The method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning of claim 1, wherein in the step one, a data source domain of the liquid-solid hydrocyclone under each working condition is trained and established, and the method for modeling the working condition under the unknown mode through transfer learning specifically comprises the following steps:
training and establishing a data source domain of the liquid-solid hydrocyclone under each working condition, wherein data samples in the data source domain are provided with labels;
and taking a new working condition needing to be tested in an unknown mode as a target field, and constructing a feature subspace according to data source domain and data in the target field based on a transfer learning principle.
3. The method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning of claim 2, wherein in the first step, the characteristic parameters include physical property parameters, geometric parameters, operation parameters and separation efficiency;
wherein the physical property parameters comprise inlet flow rate, particle size, inlet density difference and particle concentration; the geometric parameters comprise the diameter of the feeding pipe, the diameter of the cylindrical section, the length of the cylindrical section, the upper diameter of the conical section, the lower diameter of the conical section, the cone angle, the diameter of the overflow pipe, the length of the overflow pipe, the diameter of the underflow pipe and the length of the underflow pipe; the operating parameters include inlet speed and reflux ratio.
4. The method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning of claim 2, wherein in the step five, when performing simulation calculation, the corresponding simulation condition setting includes:
adopting pressure coupling; carrying out simulation calculation based on an implicit equation and an unsteady algorithm; constructing a fluid volume function model and a gas-liquid two-phase environment; the inlet adopts a speed inlet, and the overflow port and the low flow port both adopt pressure outlets; the pressure-velocity coupling is performed by pressure correction, and the discrete format is performed by PRESTO! And (4) format.
5. The method for optimizing liquid-solid hydrocyclone separation performance based on transfer learning according to claim 2, wherein after the sixth step, the method further comprises:
and inputting the obtained optimal separation efficiency value of the liquid-solid hydrocyclone into the data source domain so as to reduce the error when data migration calculation iteration is carried out.
6. The method for optimizing separation performance of the liquid-solid hydrocyclone based on the transfer learning of claim 2, wherein in the step of constructing the feature subspace based on the transfer learning principle according to the data of the data source domain and the data of the target domain, the method comprises:
and constructing the relation between the data source domain and the target domain by using an Euclidean distance formula, a cosine similarity formula, a probability mutual information formula, an information divergence formula, a JS distance formula, a maximum mean difference formula and a greedy distance formula.
7. The method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning of claim 6, wherein the Euclidean distance formula is expressed as:
Figure FDA0003345512370000021
wherein d isEuclideanExpressing the Euclidean distance, wherein x and y respectively express coordinates corresponding to a point x and a point y on a space model, and T is a transposed matrix operation;
the cosine similarity formula is expressed as:
Figure FDA0003345512370000031
wherein cos (x, y) represents the cosine similarity between the point x and the point y, and | x |, | y | are the absolute value operations of the point x and the point y, respectively.
8. The method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning of claim 7, wherein the probability mutual information formula is expressed as:
Figure FDA0003345512370000032
wherein I (X; Y) represents the probability mutual reliability between the point X and the point Y, p (X, Y) represents the probability that the point X and the point Y have a common feature subspace, p (X) represents the probability that the point X has an independent subspace, and p (Y) represents the probability that the point Y has an independent subspace;
the information divergence formula is expressed as:
Figure FDA0003345512370000033
wherein D isKL(P | | Q) represents the divergence of information between region P and region Q, P (x) represents the probability distribution of point x at region P, and Q (x) represents the probability distribution of point x at region Q.
9. The method for optimizing liquid-solid hydrocyclone separation performance based on transfer learning of claim 8, wherein the JS distance formula is expressed as:
Figure FDA0003345512370000034
wherein JSD (P | | Q) represents JS distance, DKL(P M) represents the divergence of information between region P and region M, DKL(Q | | M) represents the divergence of information between region Q and region M;
the maximum mean difference formula is expressed as:
Figure FDA0003345512370000041
wherein, MMD2(X, Y) represents the maximum mean difference,
Figure FDA0003345512370000042
representing the set of mappings for point x,
Figure FDA0003345512370000043
represents the set of mappings to which point y corresponds,
Figure FDA0003345512370000044
representing the regenerated nuclear hilbert space.
10. The method for optimizing separation performance of a liquid-solid hydrocyclone based on transfer learning of claim 9, wherein the greedy distance formula is expressed as:
Figure FDA0003345512370000045
wherein, Wp(P, Q) represents a greedy distance, ρ (x, y) represents a distance function between the point x and the point y in the set M, Γ (P, Q) represents a joint distribution of all the points in the set M × M, the joint distribution having the region P and the region Q as an edge distribution, and d μ (x, y) represents a differential value of the distance function between the point x and the point y.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160312552A1 (en) * 2015-04-27 2016-10-27 Baker Hughes Incorporated Integrated modeling and monitoring of formation and well performance
CN112517258A (en) * 2020-11-05 2021-03-19 上海明罗石油天然气工程有限公司 Novel liquid-liquid separation hydrocyclone
CN113011114A (en) * 2021-03-25 2021-06-22 赣江新区澳博颗粒科技研究院有限公司 Numerical simulation method for optimizing separation performance of liquid-solid hydrocyclone
US20210190882A1 (en) * 2019-12-10 2021-06-24 Wuhan University Transformer failure identification and location diagnosis method based on multi-stage transfer learning

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160312552A1 (en) * 2015-04-27 2016-10-27 Baker Hughes Incorporated Integrated modeling and monitoring of formation and well performance
US20210190882A1 (en) * 2019-12-10 2021-06-24 Wuhan University Transformer failure identification and location diagnosis method based on multi-stage transfer learning
CN112517258A (en) * 2020-11-05 2021-03-19 上海明罗石油天然气工程有限公司 Novel liquid-liquid separation hydrocyclone
CN113011114A (en) * 2021-03-25 2021-06-22 赣江新区澳博颗粒科技研究院有限公司 Numerical simulation method for optimizing separation performance of liquid-solid hydrocyclone

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