CN112182922A - Calculation method of flow field around square bridge pier scour problem - Google Patents

Calculation method of flow field around square bridge pier scour problem Download PDF

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CN112182922A
CN112182922A CN202010929328.7A CN202010929328A CN112182922A CN 112182922 A CN112182922 A CN 112182922A CN 202010929328 A CN202010929328 A CN 202010929328A CN 112182922 A CN112182922 A CN 112182922A
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洪锋
张帆
胡涛
肖仁政
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China Three Gorges University CTGU
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Abstract

本发明公开了方形桥墩冲刷问题的绕流流场计算方法,包括:构建方形桥墩及其冲刷水流的物理模型,即绕流模型;对步骤1的物理模型进行网格划分,对桥墩表面附近区域划分边界层网格;将步骤2得到的网格文件导入流体有限元软件,建立方形桥墩的数值模型;设置方形桥墩数值模型的控制方程求解格式和数值计算精度;利用数值模型计算得到方形桥墩的绕流流场,利用后处理软件对计算结果进行提取。本发明的绕流流场计算方法,实现了对实际工程桥梁冲刷问题的绕流流场进行高精度数值计算,获取流场详细的特征参数及非定常流动结构,为揭示桥梁局部冲刷机理提供理论支撑。

Figure 202010929328

The invention discloses a method for calculating a flow field around a square bridge pier scouring problem, which includes: constructing a physical model of a square bridge pier and its scouring water flow, that is, a flow model; Divide the boundary layer mesh; import the mesh file obtained in step 2 into the fluid finite element software to establish the numerical model of the square pier; set the governing equation solution format and numerical calculation accuracy of the numerical model of the square pier; use the numerical model to calculate the The flow field around the flow is extracted by post-processing software. The surrounding flow field calculation method of the invention realizes high-precision numerical calculation of the surrounding flow field of the actual engineering bridge scour problem, obtains the detailed characteristic parameters of the flow field and the unsteady flow structure, and provides a theory for revealing the local scour mechanism of the bridge. support.

Figure 202010929328

Description

Method for calculating streaming flow field of square pier scouring problem
Technical Field
The invention belongs to the field of bridge monitoring, and particularly relates to a method for calculating a flow-around flow field of a square pier scouring problem.
Background
In recent years, with the rapid development of the transportation industry, the number of bridges is increasing, and square piers are widely applied to the construction of viaducts along the trend of rivers. However, natural disasters caused by severe scours generated at piers and abutments are frequent, which has a great influence on national economy. Under the condition of complex incoming flow, the streaming of the square pier comprises complex flowing phenomena such as backflow, impact, separation, reattachment, vortex shedding and the like. Particularly, the water flow structure is changed by the water blocking effect of the square pier, and a horseshoe vortex system in front of the pier, a submerged water flow and a wake vortex system are generated, so that the local shear stress of the bed surface around the square pier is increased, and finally local scouring is formed. Currently, most bridge instability and collapse are caused by serious local scouring around the bridge pier. Therefore, the method has very important engineering significance for researching the local scouring problem of the square pier under the condition of complex incoming flow.
At present, the research aiming at the problem of local scouring mainly comprises three methods, namely semi-theoretical and semi-empirical, reduced-proportion hydraulic model test and numerical calculation. The three methods have advantages and disadvantages respectively, and the first two methods belong to the traditional methods, have the advantages of reality, intuition and high data reliability, but need a large amount of manpower and material resources, advanced measuring equipment and testing means. In this case, the numerical calculation can completely overcome the disadvantages of the conventional method, and the microscopic flow phenomenon and more detailed physical parameters can be obtained by the numerical calculation, but the requirement of the numerical calculation method on the theoretical level and the numerical model of the user is high. In terms of numerical models, in practical engineering application cases, most of the numerical models are calculation frameworks based on the reynolds time mean square range RANS, and the method is poor in calculation accuracy and relatively insufficient in capture capacity of micro-flow details. Therefore, it is necessary to develop an efficient numerical calculation method applied to the problem of local scour of piers.
Disclosure of Invention
The invention aims to solve the problems, and provides a method for calculating a streaming flow field of a square pier scouring problem.
The technical scheme of the invention is a method for calculating the flow-around flow field of the square pier scouring problem, which comprises the following steps:
step 1: constructing a physical model of the square pier and the scouring water flow of the square pier, namely a streaming model;
step 2: carrying out mesh division on the physical model in the step 1, and dividing boundary layer meshes in the area near the surface of the pier;
and step 3: importing the grid file obtained in the step 2 into fluid finite element software, and establishing a numerical model of the square pier;
and 4, step 4: setting conditions of a numerical model of the square pier, a solving format of a control method and numerical calculation precision;
and 5: calculating by using a numerical model to obtain a streaming flow field of the square pier, and extracting a calculation result by using post-processing software to obtain non-steady characteristics of the streaming flow field of the square pier;
step 6: and (3) establishing an entity model of the square pier, performing a water flow scouring experiment under the same condition in the step (3), comparing the water flow scouring experiment result with the calculation result of the streaming flow field in the step (5), and correcting the numerical model of the square pier according to the comparison result.
Further, in the step 1, a physical model of the square pier and the scouring water flow of the square pier is built, and the three-dimensional drawing software UG is adopted to model the square pier and the area near the surface of the pier.
Further, in step 4, all physical meters are setCalculating convergence residual error criterion to be 1 × 10-5And taking the convergence result of the constant calculation as the initial value of the unsteady calculation to accelerate the convergence efficiency.
Further, step 2 comprises the following substeps:
step 2.1: importing the physical model file in the step 1 into network partitioning software ANSYS ICEM, and defining the flow field region boundary;
step 2.2: and dividing the paste blocks into a flow field calculation domain, setting the number of nodes of each edge on each block according to the side length of the physical model, placing the first layer of grids inside the laminar flow bottom layer, repeating the operation to obtain four grids with different densities, which are named as a coarse grid, a medium grid, a fine grid and a superfine grid respectively, and outputting four grid files.
Further, step 3 comprises the following substeps:
step 3.1: using ANSYS FLUENT software to read the grid file obtained in the step 2 and checking whether the grid quality meets the requirement;
step 3.2: establishing a turbulence model of the square pier, and compiling;
step 3.3: setting the working medium as liquid water, setting the density and viscosity of the working medium, and calculating the boundary of a domain inlet as a speed inlet, the boundary of an outlet as a pressure outlet and the rest boundaries as solid wall surfaces;
step 3.4: setting a pressure-speed coupling equation and adopting a SIMPLEC algorithm; the pressure interpolation adopts a Standard format; the momentum equation, the turbulent kinetic energy, the dissipation rate and the cavitation volume fraction control equation adopt a second-order windward format; the non-fixed item selects bound Second order identifier format.
Preferably, in step 3.2, the turbulence model of the square pier adopts a separation vortex model based on grid scale correction, and on the basis of the existing separation vortex model, the kinetic energy dissipation term Y of turbulence caused by turbulence is calculatedkThe correction is carried out, and the control equation is as follows:
Figure BDA0002669650280000031
in the formula, the symbol < represents the mean value of the variables in the calculation domain; rho is density; k is the turbulence energy; u. ofjIs the velocity component; μ is the molecular viscosity; mu.stIs a turbulent viscosity; sigmakTurbulence prandtl number, which is the turbulence energy; gkGenerating a term for the kinetic energy of the turbulence; y iskA turbulent kinetic energy dissipation term; skCustom items for turbulence energy users; sigmaωA turbulent prandtl number that is the specific dissipation ratio; y isωIs the specific dissipation ratio dissipation term; gωGenerating terms for the specific dissipation ratio; sωCustomizing an item for a specific dissipation rate user; fAdaptive-DESIs a masking function; Δ is a sub-lattice scale; v is the first layer grid cell volume; l istThe turbulence scale of the two-stroke model; fSSTIs a mixing function; r isdIs a characteristic distance; climIs CDESA lower critical value; cdynIs CDESAn upper critical value; cDESSeparating vortex model coefficients; l iskIs the kolmogorov scale; ζ is the dissipation ratio; upsilon is a kinematic viscosity coefficient; f. ofdIs a delay function; Ω is strain rate tensor; s is a rotation rate tensor; h ismaxThe maximum side length of the wall surface grid is; h isminThe minimum side length of the wall surface grid is; v istIs turbulent kinematic viscosity; ν is the molecular kinematic viscosity; dw
The height of the grid from the wall surface;
Figure BDA0002669650280000041
is a decay function; r is the attenuation coefficient; gamma is the maximum grid transverse-longitudinal ratio; the power factor is used for representing filtering; u shapei,jIs the velocity gradient tensor; constant α 25, β 0.05, λ 0.61, Cμ=0.09,Cd1=80,Cd2=3,K=0.41。
Further, step 6 comprises:
1) obtaining predicted values of horizontal component velocity and vertical component velocity at different positions under the same Reynolds number condition through data processing, and comparing the predicted values with water flow scouring experiment values under the same condition;
2) obtaining the predicted values of the vertical component velocity root mean square at different positions under the same Reynolds number condition through data processing, and comparing the predicted values with the water flow scouring experiment values under the same condition;
3) and verifying the accuracy and the feasibility of the numerical model of the square pier according to the comparison result, and correcting the numerical model of the square pier.
Compared with the prior art, the invention has the beneficial effects that:
1) the calculation method of the flow bypassing flow field realizes high-precision numerical calculation of the flow field of the actual engineering bridge scouring problem, obtains detailed characteristic parameters and unsteady flow structure of the flow field, and provides theoretical support for revealing a local scouring mechanism of the bridge;
2) the separation vortex model based on grid scale correction is adopted for numerical calculation, compared with the existing separation vortex model, the calculation precision is higher, and the problems of modeling stress loss and grid induced separation of the existing model are solved;
3) the method provided by the invention utilizes an experimental method to verify and correct the calculation result of the numerical model of the square pier, so that the accuracy of the calculation result of the numerical model is better guaranteed.
Drawings
The invention is further illustrated by the following figures and examples.
Fig. 1 is a schematic flow chart of a method for calculating a flow field of a bypass flow according to an embodiment of the present invention.
Fig. 2 is a schematic view of a square pier bypass flow model according to an embodiment of the invention.
Fig. 3 is a schematic grid view of a flow field around a square pier according to an embodiment of the present invention.
Fig. 4(a) is a schematic diagram showing the comparison between the calculated horizontal component velocity and the experimental value of the water flow in the cross section of the flow field with the x/D of the flow field around 1.0.
Fig. 4(b) is a schematic diagram showing the comparison between the calculated vertical velocity component and the experimental value of the water flow in the cross section of the flow field x/D of the circumferential flow of 1.0.
Fig. 4(c) is a schematic diagram showing the comparison between the calculated vertical velocity component and the experimental value of the water flow in the cross section of the flow field x/D3.0.
Fig. 4(D) is a schematic diagram showing the comparison between the calculated horizontal component velocity and the experimental value of the water flow in the cross section of 8.0 around the flow field x/D.
Fig. 5 is a schematic diagram of the comparison between the calculated vertical component velocity root mean square value and the experimental value of the water flow with the section of the streaming flow field y being 0.
Detailed Description
The embodiment adopts the experiment models of the river-crossing bridge and the bridge piers thereof which are reduced in equal proportion to carry out experiments and verification on the method.
As shown in fig. 1, the method for calculating the flow-around flow field of the square pier scouring problem comprises the following steps:
step 1: constructing a physical model of the square pier and the scouring water flow of the square pier, namely a streaming model;
as shown in FIG. 2, the bypass flow model of the square pier comprises an Inlet Inlet, an Outlet Outlet, a wall surface Solid boundary and the square pier located in the calculation domain. The side length D of the square pier is 40mm, the total length of the calculation domain is 25D, the width of the calculation domain is 14D, the distance from the left side face of the square pier to an inlet is 5D, and in the center of the vertical direction, the center point of the square pier is used as the origin of coordinates, and an XOY coordinate axis is established. And modeling the overcurrent area by adopting three-dimensional drawing software UG, and storing the final physical model as an igs format file.
Step 2: performing mesh division on the physical model in the step 1, dividing boundary layer meshes with sufficient precision in a region near the surface of the pier, and performing mesh independence analysis to obtain flow field calculation meshes as shown in FIG. 3;
step 2.1: importing the igs file in the step 1 into mesh division software ANSYS ICEM, defining the flow field region boundary, and respectively defining a calculation region inlet, an outlet and a solid wall surface;
step 2.2: based on the topology idea, a patch block is divided into a flow field calculation domain, then the number of nodes of each edge on the block is set according to the side length of a physical model, a first layer of grids is arranged in a laminar flow bottom layer, four grids with different densities are obtained through repeated operation and named as a coarse grid, a medium grid, a fine grid and a fine grid respectively, and four msh files are output.
And step 3: importing the msh file obtained in the step 2 into ANSYS FLUENT v16.0, and establishing a numerical model of the square pier; step 3.1: reading the grid file obtained in the step 2 by using ANSYS FLUENT v16.0 software, and checking whether the grid quality meets the requirement;
step 3.2: establishing a turbulence model of a square pier, and adopting a separation vortex model based on grid scale correction;
step 3.3: setting the entrance boundary of the calculation domain as a speed entrance, wherein the size of the entrance boundary is U-0.535 m/s; the outlet boundary is a pressure outlet, the size of the outlet boundary is standard atmospheric pressure, and the rest boundaries are solid wall surfaces; the working medium is liquid water, and the density and the viscosity of the working medium are set, wherein the density rho is 1000kg/m3The kinetic viscosity coefficient [ mu ] is 1.139 × 10-3Pa.s;
Step 3.4: setting a pressure-speed coupling equation and adopting a SIMPLEC algorithm; the pressure interpolation adopts a Standard format; the momentum equation, the turbulent kinetic energy, the dissipation rate and the cavitation volume fraction control equation adopt a second-order windward format; the non-fixed item selects bound Second order identifier format.
And 4, step 4: and setting a solving format of a control equation and numerical calculation precision. And solving the format setting of the pressure-velocity coupling mode, the pressure item, the momentum, the turbulence energy, the dissipation rate and the non-constant item. Setting the convergence residual error standard of all physical quantity calculation as 1 × 10-5And taking the convergence result of the constant calculation as the initial value of the unsteady calculation to accelerate the convergence efficiency.
And 5: and calculating by using a numerical model to obtain a flow-around flow field of the square pier, and extracting a calculation result by using post-processing software. Step 6: and (3) establishing an entity model of the square pier, performing a water flow scouring test under the same condition in the step (3), comparing the water flow scouring test result with the calculation result of the streaming flow field in the step (5), and correcting the numerical model of the square pier according to the comparison result.
3.2, based on the Mesh-adaptive DES, the Mesh-adaptive DES is used for solving the problem that the original DES method is used, and the Mesh-adaptive DES dissipates the turbulent kinetic energy Y caused by the turbulent flowkAnd (6) correcting. In the original DES model, model coefficients CDES0.61 and the filter size is close to the wallThe maximum side length of the planar grid cell, i.e., Δ ═ max (Δ x, Δ y, Δ z). When the original DES model is applied to a complex grid, the conversion process from Reynolds average RANS to large vortex simulation LES is advanced due to the empirical coefficients, so that problems of modeling stress loss, grid induced separation and the like are caused in sequence, and finally simulation distortion is caused. The Mesh-adaptive DES can avoid the above problems, and the control equation of the Mesh-adaptive DES is as follows:
Figure BDA0002669650280000061
in the formula, the symbol < represents the mean value of the variables in the calculation domain; rho is density; k is the turbulence energy; u. ofjIs the velocity component; μ is the molecular viscosity; mu.stIs a turbulent viscosity; sigmakTurbulence prandtl number, which is the turbulence energy; gkGenerating a term for the kinetic energy of the turbulence; y iskA turbulent kinetic energy dissipation term; skCustom items for turbulence energy users; sigmaωA turbulent prandtl number that is the specific dissipation ratio; y isωIs the specific dissipation ratio dissipation term; gωGenerating terms for the specific dissipation ratio; sωCustomizing an item for a specific dissipation rate user; fAdaptive-DESIs a masking function; Δ is a sub-lattice scale; v is the first layer grid cell volume; l istThe turbulence scale of the two-stroke model; fSSTIs a mixing function; r isdIs a characteristic distance; climIs CDESA lower critical value; cdynIs CDESAn upper critical value; cDESSeparating vortex model coefficients; l iskIs the kolmogorov scale; ζ is the dissipation ratio; upsilon is a kinematic viscosity coefficient; f. ofdIs a delay function; Ω is strain rate tensor; s is a rotation rate tensor; h ismaxThe maximum side length of the wall surface grid is; h isminThe minimum side length of the wall surface grid is; v istIs turbulent kinematic viscosity; ν is the molecular kinematic viscosity; dwThe height of the grid from the wall surface;
Figure BDA0002669650280000071
is a decay function; r is the attenuation coefficient; gamma is the maximum grid transverse-longitudinal ratio; the power factor is used for representing filtering; u shapei,jIs the velocity gradient tensor; constant α 25, β 0.05, λ 0.61, Cμ=0.09,Cd1=80,Cd2=3,K=0.41。
In step 6, the numerical calculation results of the horizontal component velocity and the vertical component velocity at different positions of the flow-surrounding flow field under the same reynolds number are obtained through data processing, and are compared with the experimental values, as shown in fig. 4(a), 4(b), 4(c), and 4(D), where fig. 4(a) shows the calculated values and the experimental values of the horizontal component velocity of the water flow at different vertical coordinates where x/D is 1.0 on the abscissa, fig. 4(b) shows the calculated values and the experimental values of the vertical component velocity of the water flow at different vertical coordinates where x/D is 1.0 on the abscissa, fig. 4(c) shows the calculated values and the experimental values of the vertical component velocity of the water flow at different vertical coordinates where x/D is 3.0 on the abscissa, and fig. 4(D) shows the calculated values and the experimental values of the horizontal component velocity of the water flow at different vertical coordinates where x/D is 8.0 on the abscissa. The numerical calculation results and experimental values of the root-mean-square of the vertical component velocities at different positions on the transverse section of the central axis of the square pier are shown in fig. 5. Therefore, the numerical calculation result is well matched with the experimental value, and the accuracy and the feasibility of the numerical method are verified.
The above detailed description is intended to illustrate the objects, aspects and advantages of the present invention, and it should be understood that the above detailed description is only exemplary of the present invention and is not intended to limit the scope of the present invention, and any modifications, equivalents, improvements and the like made within the spirit and principle of the present invention should be included in the scope of the present invention.

Claims (7)

1.方形桥墩冲刷问题的绕流流场计算方法,其特征在于,包括以下步骤,1. the calculation method of the flow field around the square pier scour problem, is characterized in that, comprises the following steps, 步骤1:构建方形桥墩及其冲刷水流的物理模型,即绕流模型;Step 1: Build the physical model of the square pier and its scouring water flow, that is, the surrounding flow model; 步骤2:对步骤1的物理模型进行网格划分,对桥墩表面附近区域划分边界层网格;Step 2: Mesh the physical model of Step 1, and divide the boundary layer mesh for the area near the surface of the bridge pier; 步骤3:将步骤2得到的网格文件导入流体有限元软件,建立方形桥墩的数值模型;Step 3: Import the mesh file obtained in Step 2 into the fluid finite element software to establish the numerical model of the square pier; 步骤4:设置方形桥墩数值模型的控制方程求解格式和数值计算精度;Step 4: Set the governing equation solution format and numerical calculation accuracy of the numerical model of the square pier; 步骤5:利用数值模型计算得到方形桥墩的绕流流场,利用后处理软件对计算结果进行提取。Step 5: Calculate the flow field around the square pier by using the numerical model, and use the post-processing software to extract the calculation results. 2.根据权利要求1所述的方形桥墩冲刷问题的绕流流场计算方法,其特征在于,还包括步骤6:建立方形桥墩的实体模型,并在步骤3相同的条件下进行水流冲刷试验,将水流冲刷试验结果与步骤5的绕流流场的计算结果进行对比,根据对比结果对方形桥墩的数值模型进行校正。2. The method for calculating the flow field around the square pier scouring problem according to claim 1, further comprising step 6: establishing a solid model of the square pier, and carrying out a water scouring test under the same conditions as in step 3, The results of the water scouring test are compared with the calculation results of the flow field around the flow field in step 5, and the numerical model of the square pier is corrected according to the comparison results. 3.根据权利要求1所述的方形桥墩冲刷问题的绕流流场计算方法,其特征在于,步骤1中,所述构建方形桥墩及其冲刷水流的物理模型,采用三维绘图软件对方形桥墩及桥墩表面附近区域进行建模。3. The method for calculating the flow field around the square pier scouring problem according to claim 1, wherein in step 1, the described construction of the square pier and the physical model of the scour water flow, adopts three-dimensional drawing software to analyze the square pier and the scour water flow. Model the area near the pier surface. 4.根据权利要求1所述的方形桥墩冲刷问题的绕流流场计算方法,其特征在于,步骤2包括以下子步骤:4. The method for calculating the flow field around the square pier scour problem according to claim 1, wherein step 2 comprises the following sub-steps: 步骤2.1:将步骤1的物理模型文件导入到网络划分软件ANSYS ICEM中,对流场区域边界进行定义;Step 2.1: Import the physical model file of Step 1 into the network division software ANSYS ICEM to define the boundary of the flow field area; 步骤2.2:对流场计算域划分贴体块,然后依据物理模型边长大小设置块上每条边的节点数,使第一层网格置于层流底层内部,重复操作获得四种不同密度的网格,分别命名为粗网格、中等网格、细网格及极细网格,输出四个网格文件。Step 2.2: Divide the body-fitted block for the flow field calculation domain, and then set the number of nodes on each edge of the block according to the side length of the physical model, so that the first-layer mesh is placed inside the laminar flow bottom layer, and repeat the operation to obtain four different densities The meshes are named as coarse mesh, medium mesh, fine mesh and very fine mesh, and output four mesh files. 5.根据权利要求1所述的方形桥墩冲刷问题的绕流流场计算方法,其特征在于,步骤3包括以下子步骤:5. The method for calculating the flow field around the square pier scour problem according to claim 1, wherein step 3 comprises the following sub-steps: 步骤3.1:使用ANSYS FLUENT软件读取步骤2得到的网格文件,并检查网格质量是否满足要求;Step 3.1: Use the ANSYS FLUENT software to read the mesh file obtained in step 2, and check whether the mesh quality meets the requirements; 步骤3.2:建立方形桥墩的湍流模型,并进行编译;Step 3.2: Establish the turbulence model of the square pier and compile it; 步骤3.3:设置工质为液态水,并对其密度与粘度进行设定;Step 3.3: Set the working medium to liquid water, and set its density and viscosity; 步骤3.4:选择设置压力-速度耦合方程的算法;设置压力插值、动量方程、湍动能、耗散率参数。Step 3.4: Select the algorithm for setting the pressure-velocity coupling equation; set the parameters of pressure interpolation, momentum equation, turbulent kinetic energy, and dissipation rate. 6.根据权利要求5所述的方形桥墩冲刷问题的绕流流场计算方法,其特征在于,步骤3.2中,方形桥墩的湍流模型采用基于网格尺度修正的分离涡模型,控制方程如下:6. The calculation method of the flow field around the square pier scouring problem according to claim 5, is characterized in that, in step 3.2, the turbulence model of the square pier adopts the separation vortex model based on grid scale correction, and the control equation is as follows:
Figure FDA0002669650270000021
Figure FDA0002669650270000021
式中符号〈〉表示计算域内变量的均值;ρ为密度;k为湍动能;uj为速度分量;μ为分子粘度;μt为湍流粘度;σk为湍动能的湍流普朗特数;Gk为湍动能生成项;Yk为湍动能耗散项;Sk为湍动能用户自定义项;σω为比耗散率的湍流普朗特数;Yω为比耗散率耗散项;Gω为比耗散率生成项;Sω为比耗散率用户自定义项;FAdaptive-DES为屏蔽函数;Δ为亚格子尺度;V为第一层网格单元体积;Lt为双方程模型的湍流尺度;FSST为混合函数;rd为特征距离;Clim为CDES下临界值;Cdyn为CDES上临界值;CDES为分离涡模型系数;Lk为柯莫格罗夫尺度;ζ为耗散率;υ为运动粘度系数;fd为延迟函数;Ω为应变率张量;S为旋转率张量;hmax为壁面网格最大边长;hmin为壁面网格最小边长;νt为湍流运动粘度;ν为分子运动粘度;dw为网格距离壁面的高度;
Figure FDA0002669650270000031
为衰减函数;r为衰减系数;γ为最大网格横纵比;^表示滤波;Ui,j为速度梯度张量;α、β、λ、Cμ、Cd1、Cd2、K分别为常数。
where the symbol 〈〉 represents the mean value of the variables in the computational domain; ρ is the density; k is the turbulent kinetic energy; u j is the velocity component; μ is the molecular viscosity; μ t is the turbulent viscosity; σ k is the turbulent Prandtl number of the turbulent kinetic energy; G k is the turbulent kinetic energy generation term; Y k is the turbulent kinetic energy dissipation term; Sk is the turbulent kinetic energy user-defined term; σ ω is the turbulent Prandtl number of the specific dissipation rate; Y ω is the specific dissipation rate dissipation term; G ω is the generation term of the specific dissipation rate; S ω is the user-defined item of the specific dissipation rate; F Adaptive -DES is the masking function; Δ is the sub-grid scale; is the turbulence scale of the two-equation model; F SST is the mixing function; r d is the characteristic distance; C lim is the lower critical value of C DES ; C dyn is the upper critical value of C DES ; C DES is the separation eddy model coefficient ; Mogrove scale; ζ is the dissipation rate; υ is the kinematic viscosity coefficient; f d is the delay function; Ω is the strain rate tensor; S is the rotation rate tensor; h max is the maximum side length of the wall mesh; h min is the minimum side length of the wall mesh; ν t is the turbulent kinematic viscosity; ν is the molecular kinematic viscosity; d w is the height of the mesh from the wall;
Figure FDA0002669650270000031
is the attenuation function; r is the attenuation coefficient; γ is the maximum grid aspect ratio; ^ represents filtering; U i,j is the velocity gradient tensor ; constant.
7.根据权利要求1-6任意一项所述的方形桥墩冲刷问题的绕流流场计算方法,其特征在于,步骤4中,设置所有物理量计算收敛残差标准为1×10-5,将定常计算的收敛结果作为非定常计算的初始值,以加快收敛效率。7. The method for calculating the flow field around a square bridge pier scour problem according to any one of claims 1 to 6, wherein in step 4, set the convergence residual standard of all physical quantity calculations to 1×10 -5 , and set the The convergence result of the steady calculation is used as the initial value of the unsteady calculation to speed up the convergence efficiency.
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