- •ANSYS Fluent Tutorial Guide
- •Table of Contents
- •Using This Manual
- •1. What’s In This Manual
- •2. How To Use This Manual
- •2.1. For the Beginner
- •2.2. For the Experienced User
- •3. Typographical Conventions Used In This Manual
- •Chapter 1: Fluid Flow in an Exhaust Manifold
- •1.1. Introduction
- •1.2. Prerequisites
- •1.3. Problem Description
- •1.4. Setup and Solution
- •1.4.1. Preparation
- •1.4.2. Meshing Workflow
- •1.4.3. General Settings
- •1.4.4. Solver Settings
- •1.4.5. Models
- •1.4.6. Materials
- •1.4.7. Cell Zone Conditions
- •1.4.8. Boundary Conditions
- •1.4.9. Solution
- •1.4.10. Postprocessing
- •1.5. Summary
- •Chapter 2: Fluid Flow and Heat Transfer in a Mixing Elbow
- •2.1. Introduction
- •2.2. Prerequisites
- •2.3. Problem Description
- •2.4. Setup and Solution
- •2.4.1. Preparation
- •2.4.2. Launching ANSYS Fluent
- •2.4.3. Reading the Mesh
- •2.4.4. Setting Up Domain
- •2.4.5. Setting Up Physics
- •2.4.6. Solving
- •2.4.7. Displaying the Preliminary Solution
- •2.4.8. Adapting the Mesh
- •2.5. Summary
- •Chapter 3: Postprocessing
- •3.1. Introduction
- •3.2. Prerequisites
- •3.3. Problem Description
- •3.4. Setup and Solution
- •3.4.1. Preparation
- •3.4.2. Reading the Mesh
- •3.4.3. Manipulating the Mesh in the Viewer
- •3.4.4. Adding Lights
- •3.4.5. Creating Isosurfaces
- •3.4.6. Generating Contours
- •3.4.7. Generating Velocity Vectors
- •3.4.8. Creating an Animation
- •3.4.9. Displaying Pathlines
- •3.4.10. Creating a Scene With Vectors and Contours
- •3.4.11. Advanced Overlay of Pathlines on a Scene
- •3.4.12. Creating Exploded Views
- •3.4.13. Animating the Display of Results in Successive Streamwise Planes
- •3.4.14. Generating XY Plots
- •3.4.15. Creating Annotation
- •3.4.16. Saving Picture Files
- •3.4.17. Generating Volume Integral Reports
- •3.5. Summary
- •Chapter 4: Modeling Periodic Flow and Heat Transfer
- •4.1. Introduction
- •4.2. Prerequisites
- •4.3. Problem Description
- •4.4. Setup and Solution
- •4.4.1. Preparation
- •4.4.2. Mesh
- •4.4.3. General Settings
- •4.4.4. Models
- •4.4.5. Materials
- •4.4.6. Cell Zone Conditions
- •4.4.7. Periodic Conditions
- •4.4.8. Boundary Conditions
- •4.4.9. Solution
- •4.4.10. Postprocessing
- •4.5. Summary
- •4.6. Further Improvements
- •Chapter 5: Modeling External Compressible Flow
- •5.1. Introduction
- •5.2. Prerequisites
- •5.3. Problem Description
- •5.4. Setup and Solution
- •5.4.1. Preparation
- •5.4.2. Mesh
- •5.4.3. Solver
- •5.4.4. Models
- •5.4.5. Materials
- •5.4.6. Boundary Conditions
- •5.4.7. Operating Conditions
- •5.4.8. Solution
- •5.4.9. Postprocessing
- •5.5. Summary
- •5.6. Further Improvements
- •Chapter 6: Modeling Transient Compressible Flow
- •6.1. Introduction
- •6.2. Prerequisites
- •6.3. Problem Description
- •6.4. Setup and Solution
- •6.4.1. Preparation
- •6.4.2. Reading and Checking the Mesh
- •6.4.3. Solver and Analysis Type
- •6.4.4. Models
- •6.4.5. Materials
- •6.4.6. Operating Conditions
- •6.4.7. Boundary Conditions
- •6.4.8. Solution: Steady Flow
- •6.4.9. Enabling Time Dependence and Setting Transient Conditions
- •6.4.10. Specifying Solution Parameters for Transient Flow and Solving
- •6.4.11. Saving and Postprocessing Time-Dependent Data Sets
- •6.5. Summary
- •6.6. Further Improvements
- •Chapter 7: Modeling Flow Through Porous Media
- •7.1. Introduction
- •7.2. Prerequisites
- •7.3. Problem Description
- •7.4. Setup and Solution
- •7.4.1. Preparation
- •7.4.2. Mesh
- •7.4.3. General Settings
- •7.4.4. Models
- •7.4.5. Materials
- •7.4.6. Cell Zone Conditions
- •7.4.7. Boundary Conditions
- •7.4.8. Solution
- •7.4.9. Postprocessing
- •7.5. Summary
- •7.6. Further Improvements
- •Chapter 8: Modeling Radiation and Natural Convection
- •8.1. Introduction
- •8.2. Prerequisites
- •8.3. Problem Description
- •8.4. Setup and Solution
- •8.4.1. Preparation
- •8.4.2. Reading and Checking the Mesh
- •8.4.3. Solver and Analysis Type
- •8.4.4. Models
- •8.4.5. Defining the Materials
- •8.4.6. Operating Conditions
- •8.4.7. Boundary Conditions
- •8.4.8. Obtaining the Solution
- •8.4.9. Postprocessing
- •8.4.10. Comparing the Contour Plots after Varying Radiating Surfaces
- •8.4.11. S2S Definition, Solution, and Postprocessing with Partial Enclosure
- •8.5. Summary
- •8.6. Further Improvements
- •Chapter 9: Using a Single Rotating Reference Frame
- •9.1. Introduction
- •9.2. Prerequisites
- •9.3. Problem Description
- •9.4. Setup and Solution
- •9.4.1. Preparation
- •9.4.2. Mesh
- •9.4.3. General Settings
- •9.4.4. Models
- •9.4.5. Materials
- •9.4.6. Cell Zone Conditions
- •9.4.7. Boundary Conditions
- •9.4.8. Solution Using the Standard k- ε Model
- •9.4.9. Postprocessing for the Standard k- ε Solution
- •9.4.10. Solution Using the RNG k- ε Model
- •9.4.11. Postprocessing for the RNG k- ε Solution
- •9.5. Summary
- •9.6. Further Improvements
- •9.7. References
- •Chapter 10: Using Multiple Reference Frames
- •10.1. Introduction
- •10.2. Prerequisites
- •10.3. Problem Description
- •10.4. Setup and Solution
- •10.4.1. Preparation
- •10.4.2. Mesh
- •10.4.3. Models
- •10.4.4. Materials
- •10.4.5. Cell Zone Conditions
- •10.4.6. Boundary Conditions
- •10.4.7. Solution
- •10.4.8. Postprocessing
- •10.5. Summary
- •10.6. Further Improvements
- •Chapter 11: Using Sliding Meshes
- •11.1. Introduction
- •11.2. Prerequisites
- •11.3. Problem Description
- •11.4. Setup and Solution
- •11.4.1. Preparation
- •11.4.2. Mesh
- •11.4.3. General Settings
- •11.4.4. Models
- •11.4.5. Materials
- •11.4.6. Cell Zone Conditions
- •11.4.7. Boundary Conditions
- •11.4.8. Operating Conditions
- •11.4.9. Mesh Interfaces
- •11.4.10. Solution
- •11.4.11. Postprocessing
- •11.5. Summary
- •11.6. Further Improvements
- •Chapter 12: Using Overset and Dynamic Meshes
- •12.1. Prerequisites
- •12.2. Problem Description
- •12.3. Preparation
- •12.4. Mesh
- •12.5. Overset Interface Creation
- •12.6. Steady-State Case Setup
- •12.6.1. General Settings
- •12.6.2. Models
- •12.6.3. Materials
- •12.6.4. Operating Conditions
- •12.6.5. Boundary Conditions
- •12.6.6. Reference Values
- •12.6.7. Solution
- •12.7. Unsteady Setup
- •12.7.1. General Settings
- •12.7.2. Compile the UDF
- •12.7.3. Dynamic Mesh Settings
- •12.7.4. Report Generation for Unsteady Case
- •12.7.5. Run Calculations for Unsteady Case
- •12.7.6. Overset Solution Checking
- •12.7.7. Postprocessing
- •12.7.8. Diagnosing an Overset Case
- •12.8. Summary
- •Chapter 13: Modeling Species Transport and Gaseous Combustion
- •13.1. Introduction
- •13.2. Prerequisites
- •13.3. Problem Description
- •13.4. Background
- •13.5. Setup and Solution
- •13.5.1. Preparation
- •13.5.2. Mesh
- •13.5.3. General Settings
- •13.5.4. Models
- •13.5.5. Materials
- •13.5.6. Boundary Conditions
- •13.5.7. Initial Reaction Solution
- •13.5.8. Postprocessing
- •13.5.9. NOx Prediction
- •13.6. Summary
- •13.7. Further Improvements
- •Chapter 14: Using the Eddy Dissipation and Steady Diffusion Flamelet Combustion Models
- •14.1. Introduction
- •14.2. Prerequisites
- •14.3. Problem Description
- •14.4. Setup and Solution
- •14.4.1. Preparation
- •14.4.2. Mesh
- •14.4.3. Solver Settings
- •14.4.4. Models
- •14.4.5. Boundary Conditions
- •14.4.6. Solution
- •14.4.7. Postprocessing for the Eddy-Dissipation Solution
- •14.5. Steady Diffusion Flamelet Model Setup and Solution
- •14.5.1. Models
- •14.5.2. Boundary Conditions
- •14.5.3. Solution
- •14.5.4. Postprocessing for the Steady Diffusion Flamelet Solution
- •14.6. Summary
- •Chapter 15: Modeling Surface Chemistry
- •15.1. Introduction
- •15.2. Prerequisites
- •15.3. Problem Description
- •15.4. Setup and Solution
- •15.4.1. Preparation
- •15.4.2. Reading and Checking the Mesh
- •15.4.3. Solver and Analysis Type
- •15.4.4. Specifying the Models
- •15.4.5. Defining Materials and Properties
- •15.4.6. Specifying Boundary Conditions
- •15.4.7. Setting the Operating Conditions
- •15.4.8. Simulating Non-Reacting Flow
- •15.4.9. Simulating Reacting Flow
- •15.4.10. Postprocessing the Solution Results
- •15.5. Summary
- •15.6. Further Improvements
- •Chapter 16: Modeling Evaporating Liquid Spray
- •16.1. Introduction
- •16.2. Prerequisites
- •16.3. Problem Description
- •16.4. Setup and Solution
- •16.4.1. Preparation
- •16.4.2. Mesh
- •16.4.3. Solver
- •16.4.4. Models
- •16.4.5. Materials
- •16.4.6. Boundary Conditions
- •16.4.7. Initial Solution Without Droplets
- •16.4.8. Creating a Spray Injection
- •16.4.9. Solution
- •16.4.10. Postprocessing
- •16.5. Summary
- •16.6. Further Improvements
- •Chapter 17: Using the VOF Model
- •17.1. Introduction
- •17.2. Prerequisites
- •17.3. Problem Description
- •17.4. Setup and Solution
- •17.4.1. Preparation
- •17.4.2. Reading and Manipulating the Mesh
- •17.4.3. General Settings
- •17.4.4. Models
- •17.4.5. Materials
- •17.4.6. Phases
- •17.4.7. Operating Conditions
- •17.4.8. User-Defined Function (UDF)
- •17.4.9. Boundary Conditions
- •17.4.10. Solution
- •17.4.11. Postprocessing
- •17.5. Summary
- •17.6. Further Improvements
- •Chapter 18: Modeling Cavitation
- •18.1. Introduction
- •18.2. Prerequisites
- •18.3. Problem Description
- •18.4. Setup and Solution
- •18.4.1. Preparation
- •18.4.2. Reading and Checking the Mesh
- •18.4.3. Solver Settings
- •18.4.4. Models
- •18.4.5. Materials
- •18.4.6. Phases
- •18.4.7. Boundary Conditions
- •18.4.8. Operating Conditions
- •18.4.9. Solution
- •18.4.10. Postprocessing
- •18.5. Summary
- •18.6. Further Improvements
- •Chapter 19: Using the Multiphase Models
- •19.1. Introduction
- •19.2. Prerequisites
- •19.3. Problem Description
- •19.4. Setup and Solution
- •19.4.1. Preparation
- •19.4.2. Mesh
- •19.4.3. Solver Settings
- •19.4.4. Models
- •19.4.5. Materials
- •19.4.6. Phases
- •19.4.7. Cell Zone Conditions
- •19.4.8. Boundary Conditions
- •19.4.9. Solution
- •19.4.10. Postprocessing
- •19.5. Summary
- •Chapter 20: Modeling Solidification
- •20.1. Introduction
- •20.2. Prerequisites
- •20.3. Problem Description
- •20.4. Setup and Solution
- •20.4.1. Preparation
- •20.4.2. Reading and Checking the Mesh
- •20.4.3. Specifying Solver and Analysis Type
- •20.4.4. Specifying the Models
- •20.4.5. Defining Materials
- •20.4.6. Setting the Cell Zone Conditions
- •20.4.7. Setting the Boundary Conditions
- •20.4.8. Solution: Steady Conduction
- •20.5. Summary
- •20.6. Further Improvements
- •Chapter 21: Using the Eulerian Granular Multiphase Model with Heat Transfer
- •21.1. Introduction
- •21.2. Prerequisites
- •21.3. Problem Description
- •21.4. Setup and Solution
- •21.4.1. Preparation
- •21.4.2. Mesh
- •21.4.3. Solver Settings
- •21.4.4. Models
- •21.4.6. Materials
- •21.4.7. Phases
- •21.4.8. Boundary Conditions
- •21.4.9. Solution
- •21.4.10. Postprocessing
- •21.5. Summary
- •21.6. Further Improvements
- •21.7. References
- •22.1. Introduction
- •22.2. Prerequisites
- •22.3. Problem Description
- •22.4. Setup and Solution
- •22.4.1. Preparation
- •22.4.2. Structural Model
- •22.4.3. Materials
- •22.4.4. Cell Zone Conditions
- •22.4.5. Boundary Conditions
- •22.4.6. Solution
- •22.4.7. Postprocessing
- •22.5. Summary
- •23.1. Introduction
- •23.2. Prerequisites
- •23.3. Problem Description
- •23.4. Setup and Solution
- •23.4.1. Preparation
- •23.4.2. Solver and Analysis Type
- •23.4.3. Structural Model
- •23.4.4. Materials
- •23.4.5. Cell Zone Conditions
- •23.4.6. Boundary Conditions
- •23.4.7. Dynamic Mesh Zones
- •23.4.8. Solution Animations
- •23.4.9. Solution
- •23.4.10. Postprocessing
- •23.5. Summary
- •Chapter 24: Using the Adjoint Solver – 2D Laminar Flow Past a Cylinder
- •24.1. Introduction
- •24.2. Prerequisites
- •24.3. Problem Description
- •24.4. Setup and Solution
- •24.4.1. Step 1: Preparation
- •24.4.2. Step 2: Define Observables
- •24.4.3. Step 3: Compute the Drag Sensitivity
- •24.4.4. Step 4: Postprocess and Export Drag Sensitivity
- •24.4.4.1. Boundary Condition Sensitivity
- •24.4.4.2. Momentum Source Sensitivity
- •24.4.4.3. Shape Sensitivity
- •24.4.4.4. Exporting Drag Sensitivity Data
- •24.4.5. Step 5: Compute Lift Sensitivity
- •24.4.6. Step 6: Modify the Shape
- •24.5. Summary
- •25.1. Introduction
- •25.2. Prerequisites
- •25.3. Problem Description
- •25.4. Setup and Solution
- •25.4.1. Preparation
- •25.4.2. Reading and Scaling the Mesh
- •25.4.3. Loading the MSMD battery Add-on
- •25.4.4. NTGK Battery Model Setup
- •25.4.4.1. Specifying Solver and Models
- •25.4.4.2. Defining New Materials for Cell and Tabs
- •25.4.4.3. Defining Cell Zone Conditions
- •25.4.4.4. Defining Boundary Conditions
- •25.4.4.5. Specifying Solution Settings
- •25.4.4.6. Obtaining Solution
- •25.4.5. Postprocessing
- •25.4.6. Simulating the Battery Pulse Discharge Using the ECM Model
- •25.4.7. Using the Reduced Order Method (ROM)
- •25.4.8. External and Internal Short-Circuit Treatment
- •25.4.8.1. Setting up and Solving a Short-Circuit Problem
- •25.4.8.2. Postprocessing
- •25.5. Summary
- •25.6. Appendix
- •25.7. References
- •26.1. Introduction
- •26.2. Prerequisites
- •26.3. Problem Description
- •26.4. Setup and Solution
- •26.4.1. Preparation
- •26.4.2. Reading and Scaling the Mesh
- •26.4.3. Loading the MSMD battery Add-on
- •26.4.4. Battery Model Setup
- •26.4.4.1. Specifying Solver and Models
- •26.4.4.2. Defining New Materials
- •26.4.4.3. Defining Cell Zone Conditions
- •26.4.4.4. Defining Boundary Conditions
- •26.4.4.5. Specifying Solution Settings
- •26.4.4.6. Obtaining Solution
- •26.4.5. Postprocessing
- •26.5. Summary
- •Chapter 27: In-Flight Icing Tutorial Using Fluent Icing
- •27.1. Fluent Airflow on the NACA0012 Airfoil
- •27.2. Flow Solution on the Rough NACA0012 Airfoil
- •27.3. Droplet Impingement on the NACA0012
- •27.3.1. Monodispersed Calculation
- •27.3.2. Langmuir-D Distribution
- •27.3.3. Post-Processing Using Quick-View
- •27.4. Fluent Icing Ice Accretion on the NACA0012
- •27.5. Postprocessing an Ice Accretion Solution Using CFD-Post Macros
- •27.6. Multi-Shot Ice Accretion with Automatic Mesh Displacement
- •27.7. Multi-Shot Ice Accretion with Automatic Mesh Displacement – Postprocessing Using CFD-Post
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29.Go to the Data tab and change the color range to Spectrum 2 –16.
30.Align the view angle with the Z-symmetry plane and zoom in to capture the following image:
Figure 27.16: Lwc Distribution and Shadow Zones for 44.4 Micron Droplets (Left) and 6.2 Micron Droplets (Right)
Observe the difference in the shadow zones. The smallest droplets follow the airfoil very closely but avoiding it while the largest droplets barely change their path and hit almost straight on, leaving a larger shadow zone.
27.4. Fluent Icing Ice Accretion on the NACA0012
The objective of this tutorial is to compute ice accretion and water runback on the NACA0012 airfoil at different icing temperatures. Icing temperature refers to the free stream of air temperature at which the icing is to be computed. Inside Ice, this temperature can be different than what was used for the airflow free stream temperature. Indeed, the formulation of the heat fluxes in Ice allows to use an air solution obtained at a temperature different than the intended icing temperature. In this manner, several icing temperatures can be investigated using the same airflow solution.
Note
The option to change icing air temperature in icing parameters is provided as a quick method to obtain different ice shapes with different ambient temperatures. It should be understood that this method is not identical in terms of accuracy to running air and droplet flows independently for each of those temperatures. Change in ambient air temperature
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Fluent Icing Ice Accretion on the NACA0012 |
would result in a proportional change in air density which would change the momentum transfer between air and particles. This would ultimately affect particle flow paths and collection efficiency. For internal flows, where particle thermal equation and/or vapor transport is enabled, icing air temperature should be kept the same as the reference air temperature.
You are invited to read Set-up → Ice and Set-up User's Guide for more information on how to set
→ Boundary Conditions → Wall within the Fluent up the input parameters of the Ice module.
1.Launch Fluent Icing from your working directory, FLUENT_ICING_NACA0012.
2.Go to File → Preferences…. Select Icing on the left hand-side of the Preferences window. Assign a number of CPUs, 2 to 4 CPUs, next to Default Fluent CPU and set Default work folder to the location of your working directory.
3.Go to File → Open case…. Browse to and select the file naca0012_rough_mvd.cas, created in Monodispersed Calculation (p. 896).
4.A message window will ask you to launch Fluent, click Yes. A new simulation tree appears under naca0012_rough_mvd.cas(loaded) in the Outline View window. All airflow and droplet conditions and solutions previously configured and computed in the previous simulation are automatically imported under that .CAS.
5.Select Set-up under naca0012_rough_mvd.cas(loaded). In its Properties window, make sure that Airflow,
Particles and Ice are checked.
6.Under Set-up → Ice,
•In Ice accretion conditions,
–Set the Recovery factor to 0.9.
–Check Specify Icing air temperature to simulate an icing temperature that is different than the ref- erence/far-field air temperature.
–Set the Icing air temperature to 248.15 K (-25 °C).
•In Model,
–Make sure that Icing model is set to Glaze.
•Leave the other settings as default.
7.In general, there is nothing to set in the Boundary Conditions of Ice unless icing is to be turned off on certain surfaces to reduce computational effort or sink boundaries are to be declared. Examine the options available at each wall without performing any changes.
8.Go to Solve and inside the Properties window, change Log verbosity to Complete to output extra execution and post-processed data in the Console Window.
9.Right-click Particles under Solve, and select Load. A window appears to specify a *.droplet file to load. Select naca0012_rough_mvd.droplet since we will use the monodispersed cloud solution computed in Monodispersed Calculation (p. 896) to accrete ice over the NACA0012.
10.Go to Solve → Ice,
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•Under Time, keep the Total time of ice accretion [s] at 420 seconds and the Automatic time step option checked. The Ice feature in Fluent Icing is an explicit time-accurate code where the stability of
the solution strongly depends on the value of the time step. The automatic time stepping option calculates the optimal stable time step at every iteration, which can change greatly depending on the size of the geometry and the mesh density.
•Under Output, keep the option for grid displacement unchecked to skip the morphing of the volume mesh due to ice displacement.
11.Right-click Ice under Solve and choose Calculate to run the calculation.
12.After the simulation is complete, save the solution by selecting File → Save Case as… and name it naca0012_rough_mvd_m25C.
Look through the Console window of Fluent Icing. The accumulated time, value of the time step, total impingement, film, and mass of ice are printed at selected iterations. Heat flux and ice mass per wall boundary condition are listed in the following two tables. Finally, energy and mass conservation tables are printed. Most of the items in these tables are self-explanatory except perhaps mass of clipped film and runback flux. Clipped film refers to any film that is removed by sink boundaries and on certain nodes which collect and shed water (trailing edges, wing and blade tips, etc.) that are detected automatically. Runback flux is the sum of all edge fluxes in the domain which will be equal to the film removed by sink boundaries, or close to zero (mass conservation).
Figure 27.17: Mass Conservation Table Printed in the Log File of Fluent Icing
13.Cycle through the Graphs window. You will observe the progress of the total mass of ice in a sub-window and the change in instantaneous ice growth, water film thickness, and ice surface temperature with time in the next sub-window. Since the input flow and droplet solutions are steady-state solutions, the icing solutions will eventually reach a steady-state where instantaneous ice growth, water film thickness, and ice surface temperature do not change after a while.
14.Go to Ribbon menu and select View. In Quick-view, click Ice cover → Ice over - Viewmerical to see the ice shape and the original surface in Viewmerical. You can change the Metallic + Smooth option to other choices in the Object box to see the wireframe profiles and the surface meshes. In the Data panel, you can adjust the Ice thickness threshold based on ice growth to reduce display interlacing due to the overlapping of iced and clean surfaces.
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Figure 27.18: Ice View in Viewmerical Showing Shaded + Wireframe, -25 °C
At -25 °C (248.15 K), the result is a pure rime ice shape.
15.Do not close the Fluent Icing session and run two more calculations at warmer temperatures.
16.Right-click Ice under Solve and select Reset to delete the previous ice solution.
17.Select Set-up → Ice and set the Icing air temperature value to 263.15 K (-10 °C) in Ice accretion conditions.
18.Right-click Ice under Solve and click Calculate to run the calculation.
19.After the simulation is complete, save the ice solution by selecting File → Save Case as… and name it naca0012_rough_mvd_m10C.
20.Repeat steps 16 to 19. This time with an Icing air temperature value of 265.67 K (-7.48 °C), same as the airflow Temperature [K] in Set-up → Airflow → Conditions. After the simulation is complete, save the ice solution and name it naca0012_rough_mvd_m7p5C.
21.Now that there are 3 different ice shapes computed, we will analyze them using Quick-View.
22.Go to Ribbon menu and select View. In Quick-view, click Ice cover → Ice cover – Viewmerical. This opens the ice solution calculated in the previous simulation.
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Figure 27.19: Ice View in Viewmerical Showing Metallic + Smooth, , -7.5 °C
23.Rename this object by double-clicking on its original name in the Object window and enter Ice -7.5C in the window Rename dataset.
24.To load the -10 °C and -25 °C solutions, click on the button located at the right corner of the Object panel. A window appears to load a pair of files, a grid file and its solution file.
25.Click on the folder icon of Grid file and select the naca0012_rough_mvd_m10C.ice.grid file located inside your working directory.
26.Do not specify a solution file as you will only compare ice shapes.
27.Press the Load button. A new data set is added to the Object panel.
28.Rename this new object by double-clicking on its original name in the Object window and enter Ice - 10C in the window Rename dataset.
29.Repeat steps 23 to 27 for the remaining ice shape, file naca0012_rough_mvd_m25C.ice.grid.
30.Click the lock button at the bottom right of the data set list window located in the Objects panel to enable all the grids in the 2D plot.
31.Go to Query panel and enable the 2D plot. Change the Cutting plane to Z and the horizontal axis to X. All four data sets should be plotted in Geometry mode. Change the color and thickness of the curves by right-clicking on the cube menu on the top right and then by choosing the Curve Settings menu.
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Fluent Icing Ice Accretion on the NACA0012 |
Figure 27.20: Ice Shapes at -25, -10, and -7.5 C |
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At -25 °C (248.15 K), the cooling effects are large and all droplets freeze almost instantly producing a rime ice shape. This shape generally resembles the original airfoil profile and can be considered somewhat aerodynamic. As the icing temperature increases, more water can run back away from the stagnation zone and freeze where cooling effects become more predominant. This mechanism
initiates the growth of ice horns on the upper and lower sides of the airfoil. These geometric features are common in glaze icing conditions and induce flow separation therefore they dramatically change the aerodynamic performance of the airfoil.
To properly capture the shape of the horns, a multishot computation is recommended where the grid, air and droplet solutions are updated at certain time intervals.
32.Finally, we will compare the film height of the three solutions. Uncheck all Ice* objects.
33.Click on button located at the right corner of the Object panel. A window appears to load a pair of files, a grid file and its solution file.
34.Click on the folder icon of Grid file and select the naca0012_rough_mvd_m7p5C.map.grid file located inside your working directory.
35.Click on the folder icon of Solution file (optional) and select the naca0012_rough_mvd_m7p5C.swimsol file located inside your working directory.
36.Press the Load button. A new data set is added to the Object panel. Rename this dataset by double-clicking on its original name and enter -7.5C in the window Rename dataset.
37.Repeat steps 32 to 35 for the remaining pairs of *.map.grid and *.swimsol files of -10 °C and -25 °C cases.
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38.In the Data panel, inside Files, choose Film Thickness as the Data field. Click Shared inside Color range.
39.Go to the Query panel and activate the 2D plot. Set the Mode to Data and Cutting plane to Z. Set the horizontal axis to Y. The three curves showing the film height for the 3 different temperatures should be visible. Change the curve colors and thickness using the Curve Settings in the cube menu located at the top right.
Figure 27.21: Film Height Variation over the Ice at -25, -10, and -7.5 C
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Release 2019 R1 - © ANSYS,Inc.All rights reserved.- Contains proprietary and confidential information |
918 |
of ANSYS, Inc. and its subsidiaries and affiliates. |