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  • Tutorial: Simulation of Transitional Flow over an Aerospatiale-A Airfoil

    Introduction

    Transitional boundary layer flows are important in many CFD applications of engineering

    interest such as airfoils, wind turbines, ship hulls and turbomachinery blade rows. An ANSYS

    proprietary empirical correlation (Langtry and Menter) has been developed to predict standard

    bypass transition as well as flows in low free-stream turbulence environments. The transition

    model is based on the coupling of the SST k- model transport equations with two other

    transport equations, one for the intermittency and one for the transition onset criteria, in terms of

    momentum-thickness Reynolds number.

    This tutorial will teach you the basic setup and solution procedures for transitional flow over

    the Aerospatiale-A airfoil. The objective of this tutorial is to perform a validation study that

    examines the accuracy of ANSYS Fluent 15.0 for computation of two-dimensional transitional

    flows

    In this tutorial you will learn how to:

    Use the Fluent 15.0 GUI Model compressible flow (using the ideal gas law for density)

    Set boundary conditions for external flows

    Use the Transition SST turbulence model

    Use Full Multigrid (FMG) initialization to obtain better initial field values

    Post-process the results and compare them with experimental data

    Do an additional exercise comparing the results against the (fully turbulent) SST

    k- model

    Prerequisites

    This tutorial assumes that you are familiar with the FLUENT interface and that you have

    a good understanding of the basic setup and solution procedures. This is an advanced

    tutorial and should only be attempted after you have mastered the introductory tutorials.

    Problem Description

    The problem considers flow around the Aerospatiale-A airfoil at 13.1 and 13.3 angles of

    attack with free stream Reynolds numbers of 2.07 x 106 and 2.10 x 10

    6, respectively. The

    chord length is 1 m. The geometry of the airfoil is shown in Figure 1

  • Figure 1: Problem Description

    A 2D domain is created for the problem. The leading edge of the airfoil is located at the origin of

    the global coordinate system. The computational domain extends from -18 m to 25 m in the x-

    direction and from -18 m to 21.56m in the y-direction. A quadrilateral mesh is created, with very

    fine mesh spacing close to the airfoil surface. The total mesh count is 65,536 quadrilateral cells.

    Mesh Requirements

    The recommended mesh guidelines for predicting boundary layer transitional flow are a

    maximum y+ value of 1 in the wall adjacent cell, an expansion ratio no greater than 1.1 for the

    wall normal mesh spacing and sufficient grid points in the streamwise direction. These

    requirements are needed to ensure proper resolution of the flow in the viscous sublayer and

    proper resolution of streamwise changes in geometry, for instance where there is high surface

    curvature, or flow, for instance near separation or reattachment points.

    Setup

    Start the 2D, double precision version of FLUENT. If multiple cores are available, start the

    parallel version of Fluent

    Step 1: Mesh

    1.1 Read the mesh file

    File --> Read --> Mesh

    Select the file a_airfoil.msh.gz by clicking on it under Files and then clicking on OK

    1.2 Check the grid.

    Mesh -->Check Fluent will perform various checks on the mesh and will report the progress in the console. A

    message will appear warning of potential problems that might result from high aspect ratio

    cells near the surface of the airfoil. In this case, the warnings can be ignored as the wall

    distance calculation is unaffected by the high aspect ratio cells but in general it is

    recommended to confirm the wall distance is correct by displaying contours of Cell Wall Distance as suggested by the warning message.

  • 1.3 Display the mesh (Figure 2)

    Display --> Mesh Make sure that all the surfaces are selected and click Display

    Figure 2: Mesh Display

    You can use the middle mouse button to zoom into the area around the airfoil and view the mesh

    around the pressure and suction sides more closely.

  • Step 2: Materials

    2.1 Define the Materials

    Define -->Materials

    In Properties, select Ideal-Gas for Density, specify the other material properties as shown in

    Figure 3 and click on Change/Create and Close the panel. The selection of the ideal gas model

    will automatically enable the energy equation.

    Figure 3: Materials Panel

    Step 3: Models

    3.1 Select the Pressure-Based solver

    Define --> General

    In Solver, select Pressure-Based under Type, Absolute under Velocity-Formulation, Steady

    under Time, and Planar under 2D Space as shown in Figure 4.

  • Figure 4: General Panel

    3.2 Specify the turbulence model. This tutorial will be solved using the Transition SST

    turbulence model

    Define -->Models -->Viscous

    Select Transition SST (4 eqn) under Model and Viscous Heating under Options as shown in

    Figure 5. Keep the default settings for the other options.

    Figure 5: Viscous Model Panel

  • Note: The transition model is based on coupling of the SST k-omega transport equations with

    two other transport equations, one for the intermittency, and one for the transition onset criteria,

    in terms of momentum thickness Reynolds number. Because the model requires the solution of

    these additional equations, there are additional CPU costs associated with using it.

    Step 4: Opera t ing Condit ions

    Define --> Operating Conditions

    Set the Operating Pressure to 59607.1 Pascals.

    Step 5: Boundary Condit ions

    Define --> Boundary Conditions

    The inputs in Table 1 will be specified at the inlet boundary for the simulation

    Free Stream Conditions F1 wind tunnel data F2 wind tunnel data

    Angle of attack 13.1 13.3

    Static pressure (Pa) 59607.1 59607.1

    Static temperature (K) 273 273

    Mach number 0.148 0.150

    Cos (AoA) 0.97398 0.97318

    Sin (AoA) 0.22665 0.23005

    Intermittency 1 1

    Turbulent intensity 1 1

    Turbulent viscosity ratio 15 15

    Table 1. Inputs for Inlet Boundary Conditions

    Specifying Inlet Turbulence Levels

    It has been observed that the turbulence intensity specified at an inlet can decay quite rapidly

    depending on the inlet turbulent viscosity ratio. As a result, the local turbulence intensity

    downstream of the inlet can be much smaller than the inlet value. Typically, larger values of inlet

    turbulent viscosity ratio result in a smaller turbulent decay rate. However, if the specified

    turbulent viscosity ratio is too large (i.e. greater than 100), the skin friction on the airfoil surface

    can deviate significantly from the laminar value. For this reason, it can be desirable to have a

    relatively low (i.e. 1 -10) inlet turbulent viscosity ratio and set the turbulence intensity value at

    the inlet such that it decays to reach the actual experimental value at the leading edge of the

    airfoil.

    5.1 Specify the inputs for the F2 wind tunnel data

    Select inlet under Zone, select pressure-far-field under Type and click on Edit. Specify the

    inputs as shown in Figure 6 below. In the Thermal tab, specify a temperature of 273 K. If the

    inlet temperature is not specified correctly, the results will not match the data.

  • Figure 6. Inlet Boundary Condition Settings

    5.2 Set the Boundary Condition for outlet by selecting it in Zone, select pressure-outlet as the

    Type and click on Edit. Enter values in the panel as shown in Figure 7 below. In the Thermal

    tab, specify a value of 273 K for Backflow Total Temperature.

    Figure 7. Outlet Boundary Condition Settings

  • 5.3 The boundaries bottom-airfoil and top-airfoil are walls. They require no changes to be made

    from the default wall boundary condition settings.

    Step 6: Solut ion Methods/Cont rols

    6.1 Set the Solution Methods

    Solve --> Methods

    Set up the parameters as shown in Figure 8 below. Select Coupled under Scheme, Least Squares

    Cell Based under Gradient, Second Order under Pressure, and Second Order Upwind for all

    other equations. Be sure to scroll down below what is shown in the figure to get all equations.

    Figure 8. Solution Methods Panel Settings

    6.2 Set the solution controls

    Solve --> Controls

    Enter the values shown in Figure 9. For the equations that do not appear in the figure, use values

    of 0.8 for Momentum Thickness Re, and 1.0 for both Turbulent Viscosity and Energy.

  • Figure 9. Solution Controls Settings

    Step 7: Solut ion Monitors

    7.1 Residual Monitoring

    Solve --> Monitors --> Residuals --> Edit

    Enable Plot under Options. Change Convergence Criterion from absolute to none.

    Figure 10. Residual Monitors Panel

  • 7.2 Drag Coefficient Monitoring

    We will monitor the drag coefficient on the bottom-airfoil and top-airfoil wall zones.

    Solve --> Monitors then click Create > Drag below Residuals, Statistic and Force Monitors

    Select both walls under Wall Zones. Turn on Print to Console and Plot under Options. Select

    2 under Window. Under Force Vector enter x=0.97318 and y=0.23005.

    Figure 11. Drag Monitor Panel

    Step 8: In it ia lizing the Solut ion

    8.1 Initialize the solution

    Solve --> Initialization

    Select Standard Initialization and use the inlet boundary conditions to initialize the flow. Select

    inlet under Compute From and then click on Initialize. The individual variable fields will

    automatically populate with the inlet values.

  • Figure 12. Solution Initialization Panel. Values will be automatically populated after selecting

    inlet under Compute From.

    8.2 Apply FMG initialization (Text User Interface command)

    /solve/initialize/fmg-initialization yes

    Note: The Full Multigrid (FMG) initialization can provide a better initial solution for complex

    problems at a minimal cost compared to the overall computational expense. The use of FMG

    initialization will accelerate the convergence of the problem.

    8.3 Set the reference values used to compute the coefficients of drag, pressure and skin friction

    Report --> Reference Values

    In the Compute From drop-down list, select inlet. FLUENT will update the Reference Values

    based on the inlet boundary conditions.

  • Figure 13. Reference Values Panel.

    Note: The default value of 1 m2 is kept for Area. In reality, one should calculate the appropriate

    area (typically the projected area) for accurate computation of the drag coefficient, Cd. In this

    tutorial, Cd is used only to monitor the convergence.

    Step 9: Save Case and Data

    File --> Write --> Case & Data

    Enter a_airfoilf2_transition_fmg.cas.gz under Case/Data File and click OK.

    Step 10: Itera te

    10.1 Start the solution

    Solve --> Run Calculation After the requested 250 iterations, execute the TUI command /solve/monitors/force/clear-

    monitor, then request another 1750 iterations.

  • Figure 14: Run Calculation Panel

    Monitor the scaled residuals (Figure 15) and the drag convergence history (Figure 16). The drag

    is converged within one drag count (1e-4).

    Figure 15: Scaled Residuals History

  • Figure 16: Drag Convergence History

    10.2 Save case and data files

    File --> Write --> Case & Data

    Save the case and data files as a_airfoil_f2_transition_2000.cas.gz

    Step 11: Post-processing

    11.1 Display contours of Mach Number, Static Pressure, and Intermittency

    Display --> Graphics and Animations --> Contours

    Select Filled under Options and Velocity/Mach Number under Contours of. It will be necessary to zoom to a smaller region close to the airfoil.

  • Figure 17: Contours of Mach Number

  • Figure 18: Contours of Static Pressure

    Figure 19: Contours of Intermittency

  • Figure 20: Velocity Vectors Colored by Velocity Magnitude (m/s)

    Observation: Transition on the suction surface is triggered by a laminar separation bubble which

    results in a turbulent boundary layer downstream. If difficulties are experienced locating the

    separation bubble shown in the figure, open the Camera panel ( Display --> Views --> Camera)

    and enter the values (3.702,1.183,118.4) for Position, (0.122,0.088,0) for Target, (0,1,0) for Up

    Vector, (0.005,0.005) for Field and increase the value of Scale in the Vectors panel from 1 to 10.

    11.4 Experimental F2 wind tunnel data is available for the skin friction coefficient on the top-

    airfoil surface

    Display --> Plots --> XY Plot

    Figure 21: Solution XY Plot Panel

  • Deselect Node Values under Options.

    Select Wall Fluxes/Skin Friction Coefficient in Y Axis Function.

    Select top-airfoil under Surfaces.

    Click on Load File to load the experimental data file Exp-F2-CF.xy.

    Click on Plot to plot both the simulation and experimental results.

    Figure 22: Comparison of Skin Friction Coefficient with F2 Wind Tunnel Data

    11.5 The pressure coefficient from the experimental F2 wind tunnel data is available

    Display --> Plots --> XY Plot

    Deselect Node Values under Options

    Select Pressure/Pressure Coefficient in Y Axis Function

    Select top-airfoil and bottom-airfoil under Surfaces

    Click on Free Data to unload the skin friction coefficient data file, then click Load File and load the experimental data file Exp-F2-Cp.xy.

    Click on Plot to plot both the simulation results and the experimental data

  • Figure 23: Comparison of Pressure Coefficient with F2 Wind Tunnel Data

    Step 12: Additional Exercise

    A comparison has been made between CFD results obtained using the Transition SST turbulence

    model and the experimental F2 wind tunnel data. Next we will make the following additional

    comparisons

    12.1 Comparison of results from the SST k-omega model with the Transition SST model results

    and the F2 wind tunnel data.

    12.2 Comparison of results from the Transition SST and SST k-omega models with experimental

    F1 wind tunnel test data

    12.1.1 Enable the SST k-omega turbulence model.

    Define --> Models --> Viscous

    Select k-omega under Model, SST under k-omega Model and Viscous Heating under Options.

    Be sure Compressibility Effects is not selected in k-omega Options.

  • Figure 24: Viscous Model Panel After Activating SST k-omega Model

    12.1.2 Repeat the operations described in Steps 8-10 of this tutorial, then save the case and data

    files as a_airfoil_f2_sst_2000.cas.gz.

    12.1.3 Quantitative comparison with F2 wind tunnel data

  • Figure 25: Skin Friction Coefficient Predictions with SST k-omega and Transition SST Models

    Compared with Experimental F2 Wind Tunnel Data

    Figure 26: Pressure Coefficient Predictions with SST k-omega and Transition SST Models

    Compared with Experimental F2 Wind Tunnel Data

  • 12.2 Comparison of results from the SST k-omega model with the Transition SST model results

    and the F1 wind tunnel data.

    Open a_airfoil_f2_transition.2000.cas.gz, change the inlet boundary conditions to reflect the F1

    experimental conditions that were reported in Table 1.

    After changing the inlet boundary conditions, repeat Steps 8 10 and save the case and data files as a_airfoil_f1_transition_2000.cas.gz.

    Change the turbulence model to SST k-omega, repeat Step 12.1.2, and save the case and data files

    as a_airfoil_f1_sst_2000.cas.gz.

    Figure 27: Comparison of Transition SST and SST k-omega Model Skin Friction Coefficient

    Predictions with Experimental F1 Wind Tunnel Data

  • Figure 28: Comparison of Transition SST and SST k-omega Model Pressure Coefficient

    Predictions

    References:

    Chaput, E., Chapter 3: Application-Oriented Synthesis of Work Presented in Chapter II, Notes on Numerical Fluid Mechanics, Vol. 58, Vieweg Braunschweig, Wiesbaden, 1997, pp. 327-346

    Langtry, R.B. and Menter, F.R., Transition Modeling for General CFD Applications in Aeronautics, AIAA 2005-522.