Assessment of Turbulence Modeling for Compressible Flow...

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Assessment of Turbulence Modeling for Compressible Flow Around Stationary and Oscillating Cylinders by Alejandra Uranga Supervisors: Drs Nedjib Djilali and Afzal Suleman Dept. of Mechanical Engineering - University of Victoria August 21, 2006 A p p l i e d V e h i c l e Technologies

Transcript of Assessment of Turbulence Modeling for Compressible Flow...

Page 1: Assessment of Turbulence Modeling for Compressible Flow ...auranga/presentations/uranga2006...Assessment of Turbulence Modeling for Compressible Flow Around Stationary and Oscillating

Assessment of Turbulence Modeling for Compressible Flow

Around Stationary and Oscillating Cylinders

by Alejandra Uranga

Supervisors: Drs Nedjib Djilali and Afzal Suleman Dept. of Mechanical Engineering - University of Victoria

August 21, 2006

A p p l i e d V e h i c l e

Technologies

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Outline

  Introduction

  Simulation Methodology

  Stationary Cylinder

  Oscillating Cylinder

  Conclusions

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Introduction

Periodic pattern of counter-rotating vortices caused by unsteady separation from a bluff body

Kármán Vortex Street

Introduction Methodology Stationary Oscillating Conclusions

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Introduction

Periodic pattern of counter-rotating vortices caused by unsteady separation from a bluff body

Kármán Vortex Street

Introduction Methodology Stationary Oscillating Conclusions

NASA satellite image 1999

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Introduction

  Interaction between 3 shear layers -  Boundary layer -  Free shear layer -  Wake

Flow Around a Circular Cylinder

Introduction Methodology Stationary Oscillating Conclusions

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Introduction

  Interaction between 3 shear layers -  Boundary layer -  Free shear layer -  Wake

Flow Around a Circular Cylinder

Introduction Methodology Stationary Oscillating Conclusions

  Transition to turbulence in -  Wake ReD 200 → 400 -  Free Shear layer ReD 400 → 150x103 -  Boundary layer ReD 150x103 → 8x106

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Introduction

  Simulation of turbulent flow around circular cylinders - Stationary ReD = 3900 - Oscillating ReD = 3600

  Compare accuracy of turbulence models using same numerical procedure with respect to experiments

and other simulations

Scope

Introduction Methodology Stationary Oscillating Conclusions

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Methodology

Numerical Simulation of Turbulent Flows

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Methodology

Example: Incompressible Momentum Equation

Applying an average or filter operator (overbar) to the momentum equation yields

The terms , , are solved for

The cross terms are unknown closure problem

Introduction Methodology Stationary Oscillating Conclusions

The Need for Turbulence Models

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Methodology

Introduction Methodology Stationary Oscillating Conclusions

Simulation of Turbulence

DNS Direct Numerical

Simulation

Solve all Scales

very thin grid required €

ui

URANS Unsteady

Reynolds Averaged Navier-Stokes

(One-point closure)

mean fluctuating

Solve mean quantities

Model Reynolds stresses

u i

LES Large Eddy Simulation

large scale Subgrid-Scale

Solve large scale eddies

Model subgrid-scale stress €

u i

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Methodology

  URANS - One equation Spalart-Allmaras - K-tau Speziale et al.

  Large Eddy Simulation (LES) - Smagorinsky-Lilly

  Very Large Eddy Simulation (VLES) - Adaptive k-tau Magagnato & Gabi (uses a URANS type subgrid-scale model)

Introduction Methodology Stationary Oscillating Conclusions

Turbulence Models Considered

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Methodology

  SPARC Structured PArallel Research Code

  Finite Volume, Cell Centered, Block-Structured, Multigrid

  Simulations are 3D Unsteady Compressible Viscous

Introduction Methodology Stationary Oscillating Conclusions

Computational Code

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Stationary Cylinder

Stationary Circular Cylinder in a Uniform Flow

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Stationary Cylinder

  Cylinder diameter D = 1m   Flow velocity U0 = 68.63m/s   Mach number Mach 0.2   Reynolds number ReD = 3900

Problem Setup

Introduction Methodology Stationary Oscillating Conclusions

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Stationary Cylinder

2D figures: x-y plane at span center

Computational Domain

Introduction Methodology Stationary Oscillating Conclusions

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Stationary Cylinder URANS : Average Fields

Introduction Methodology Stationary Oscillating Conclusions

SA Sp

u/U0

ωzD/U0

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Stationary Cylinder URANS : Average Streamlines

Introduction Methodology Stationary Oscillating Conclusions

SA Sp

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Stationary Cylinder URANS : Average Profiles

Introduction Methodology Stationary Oscillating Conclusions

u/U0 at x/D = 1.54

cp around cylinder

cf around cylinder

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Stationary Cylinder LES-VLES : Streamlines

Introduction Methodology Stationary Oscillating Conclusions

LES VLES

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Stationary Cylinder LES-VLES : Average Fields

Introduction Methodology Stationary Oscillating Conclusions

LES VLES

u/U0

ωzD/U0

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Stationary Cylinder LES-VLES : Average Profiles

Introduction Methodology Stationary Oscillating Conclusions

u/U0 at x/D=1.54

cp around cylinder

cf around cylinder

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Stationary Cylinder 3-Dimensionality

Streamwise velocity iso-surfaces

Introduction Methodology Stationary Oscillating Conclusions

URANS Sp LES

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Stationary Cylinder Comparison

Introduction Methodology Stationary Oscillating Conclusions

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Oscillating Cylinder

Circular Cylinder in Cross-Flow Oscillations

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Oscillating Cylinder

  Vertical sinusoidal motion

  2D URANS k-tau Speziale

  Reynolds number 3600

  Lock-in: vortex shedding frequency matches cylinder motion frequency

Motion and Cases

Introduction Methodology Stationary Oscillating Conclusions

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Oscillating Cylinder URANS Sp Fields

Introduction Methodology Stationary Oscillating Conclusions

ωzD/U0 u/U0

Case IV fc / f0 = 0.800

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Oscillating Cylinder Lock-in

Introduction Methodology Stationary Oscillating Conclusions

46%

40% 2%

1%

63%

32%

motion frequency fc/f0

sheddi

ng f

requ

ency

fS/f

0

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Conclusions

Summary and Further Work

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Conclusions

  comparison of results from different turbulence models with same numerical procedure

  Spalart-Allmaras model -  error in separation point flow remains attached too long small recirculation zone low back pressure large drag

-  Accurate Strouhal number

Introduction Methodology Stationary Oscillating Conclusions

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Conclusions

  K-tau Speziale model -  Good mean global quantities Strouhal number, drag, back pressure, separation point velocity profiles along the wake

  LES and VLES -  reveal secondary eddies -  LES resolves dynamics in boundary layer

  Oscillating Cylinder

-  No other numerical results in same regime

-  Lock-in over large range of motion frequencies

-  Further investigation required

Introduction Methodology Stationary Oscillating Conclusions

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Conclusions

  Better averages on LES and VLES

  LES with Dynamic and Dynamic Mixed subgrid-scale models

  LES of oscillating cylinder

Further Work

Introduction Methodology Stationary Oscillating Conclusions

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Questions