DNS Study on Small Length Scale in Turbulent Flow

Similar documents
J. Szantyr Lecture No. 4 Principles of the Turbulent Flow Theory The phenomenon of two markedly different types of flow, namely laminar and

AER1310: TURBULENCE MODELLING 1. Introduction to Turbulent Flows C. P. T. Groth c Oxford Dictionary: disturbance, commotion, varying irregularly

Lecture 7. Turbulence

Before we consider two canonical turbulent flows we need a general description of turbulence.

LES of Turbulent Flows: Lecture 3

Applied Computational Fluid Dynamics

Engineering. Spring Department of Fluid Mechanics, Budapest University of Technology and Economics. Large-Eddy Simulation in Mechanical

B.1 NAVIER STOKES EQUATION AND REYNOLDS NUMBER. = UL ν. Re = U ρ f L μ

Turbulent Rankine Vortices

Turbulence (January 7, 2005)

Exercises in Combustion Technology

Chapter 7. Basic Turbulence

Nonequilibrium Dynamics in Astrophysics and Material Science YITP, Kyoto

Computational Fluid Dynamics 2

Turbulence Instability

FLUID MECHANICS. Atmosphere, Ocean. Aerodynamics. Energy conversion. Transport of heat/other. Numerous industrial processes

Turbulence Modeling I!

Chapter 7 The Time-Dependent Navier-Stokes Equations Turbulent Flows

Introduction to Turbulence Modeling

Turbulence and its modelling. Outline. Department of Fluid Mechanics, Budapest University of Technology and Economics.

Modeling of turbulence in stirred vessels using large eddy simulation

Introduction to Turbulence and Turbulence Modeling

Tutorial School on Fluid Dynamics: Aspects of Turbulence Session I: Refresher Material Instructor: James Wallace

Note the diverse scales of eddy motion and self-similar appearance at different lengthscales of the turbulence in this water jet. Only eddies of size

Lecture 2. Turbulent Flow

Eddy viscosity. AdOc 4060/5060 Spring 2013 Chris Jenkins. Turbulence (video 1hr):

Project Topic. Simulation of turbulent flow laden with finite-size particles using LBM. Leila Jahanshaloo

Numerical Heat and Mass Transfer

FLUID MECHANICS. ! Atmosphere, Ocean. ! Aerodynamics. ! Energy conversion. ! Transport of heat/other. ! Numerous industrial processes

Turbulence: Basic Physics and Engineering Modeling

The Atmospheric Boundary Layer. The Surface Energy Balance (9.2)

Numerical Study of Natural Unsteadiness Using Wall-Distance-Free Turbulence Models

ESCI 485 Air/sea Interaction Lesson 2 Turbulence Dr. DeCaria

Lecture 14. Turbulent Combustion. We know what a turbulent flow is, when we see it! it is characterized by disorder, vorticity and mixing.

Explicit algebraic Reynolds stress models for internal flows

BOUNDARY LAYER ANALYSIS WITH NAVIER-STOKES EQUATION IN 2D CHANNEL FLOW

Process Chemistry Toolbox - Mixing

Turbulence - Theory and Modelling GROUP-STUDIES:

Masters in Mechanical Engineering Aerodynamics 1 st Semester 2015/16

ROLE OF THE VERTICAL PRESSURE GRADIENT IN WAVE BOUNDARY LAYERS

Detailed Outline, M E 320 Fluid Flow, Spring Semester 2015

A dynamic global-coefficient subgrid-scale eddy-viscosity model for large-eddy simulation in complex geometries

Mass Transfer in Turbulent Flow

Comparison of Turbulence Models in the Flow over a Backward-Facing Step Priscila Pires Araujo 1, André Luiz Tenório Rezende 2

On the aeroacoustic tonal noise generation mechanism of a sharp-edged. plate

Chapter 6 An introduction of turbulent boundary layer

FLOW-NORDITA Spring School on Turbulent Boundary Layers1

1. Introduction, tensors, kinematics

Fundamentals of Fluid Dynamics: Elementary Viscous Flow

Masters in Mechanical Engineering. Problems of incompressible viscous flow. 2µ dx y(y h)+ U h y 0 < y < h,

Chuichi Arakawa Graduate School of Interdisciplinary Information Studies, the University of Tokyo. Chuichi Arakawa

Aerodynamic force analysis in high Reynolds number flows by Lamb vector integration

Simulating Drag Crisis for a Sphere Using Skin Friction Boundary Conditions

Statistical studies of turbulent flows: self-similarity, intermittency, and structure visualization

meters, we can re-arrange this expression to give

Numerical Methods in Aerodynamics. Turbulence Modeling. Lecture 5: Turbulence modeling

Multiscale Computation of Isotropic Homogeneous Turbulent Flow

DNS STUDY OF TURBULENT HEAT TRANSFER IN A SPANWISE ROTATING SQUARE DUCT

What is Turbulence? Fabian Waleffe. Depts of Mathematics and Engineering Physics University of Wisconsin, Madison

Transition to turbulence in plane Poiseuille flow

TME225 Learning outcomes 2018: week 1

Turbulens Teori och modellering

Turbulence Modeling. Cuong Nguyen November 05, The incompressible Navier-Stokes equations in conservation form are u i x i

Fluid Mechanics. Chapter 9 Surface Resistance. Dr. Amer Khalil Ababneh

AA214B: NUMERICAL METHODS FOR COMPRESSIBLE FLOWS

COMPUTATIONAL SIMULATION OF THE FLOW PAST AN AIRFOIL FOR AN UNMANNED AERIAL VEHICLE

Probability density function (PDF) methods 1,2 belong to the broader family of statistical approaches

Manhar Dhanak Florida Atlantic University Graduate Student: Zaqie Reza

Turbulence Solutions

DIRECT NUMERICAL SIMULATION OF SPATIALLY DEVELOPING TURBULENT BOUNDARY LAYER FOR SKIN FRICTION DRAG REDUCTION BY WALL SURFACE-HEATING OR COOLING

CVS filtering to study turbulent mixing

Turbulence modelling. Sørensen, Niels N. Publication date: Link back to DTU Orbit

TURBULENT BOUNDARY LAYERS: CURRENT RESEARCH AND FUTURE DIRECTIONS

TURBULENCE IN FLUIDS AND SPACE PLASMAS. Amitava Bhattacharjee Princeton Plasma Physics Laboratory, Princeton University

Turbulent Boundary Layers & Turbulence Models. Lecture 09

Applied Mathematics and Mechanics (English Edition)

Implicit Large Eddy Simulation of Transitional Flow over a SD7003 Wing Using High-order Spectral Difference Method

Modelling of turbulent flows: RANS and LES

MULTIDIMENSIONAL TURBULENCE SPECTRA - STATISTICAL ANALYSIS OF TURBULENT VORTICES

DEVELOPMENT OF CFD MODEL FOR A SWIRL STABILIZED SPRAY COMBUSTOR

O. A Survey of Critical Experiments

General introduction to Hydrodynamic Instabilities

Numerical analysis of fluid flow and heat transfer in 2D sinusoidal wavy channel

Boundary layer flows The logarithmic law of the wall Mixing length model for turbulent viscosity

A NOVEL VLES MODEL FOR TURBULENT FLOW SIMULATIONS

CONVECTIVE HEAT TRANSFER

LOW SPEED STREAKS INSTABILITY OF TURBULENT BOUNDARY LAYER FLOWS WITH ADVERSE PRESSURE GRADIENT

Max Planck Institut für Plasmaphysik

6 VORTICITY DYNAMICS 41

Mestrado Integrado em Engenharia Mecânica Aerodynamics 1 st Semester 2012/13

Chapter 5 Phenomena of laminar-turbulent boundary layer transition (including free shear layers)

Engineering. Spring Department of Fluid Mechanics, Budapest University of Technology and Economics. Large-Eddy Simulation in Mechanical

Answers to Homework #9

Euler equation and Navier-Stokes equation

Large Eddy Simulation as a Powerful Engineering Tool for Predicting Complex Turbulent Flows and Related Phenomena

A Solution Method for the Reynolds-Averaged Navier-Stokes Equation

Direct Numerical Simulations of Transitional Flow in Turbomachinery

Donald Slinn, Murray D. Levine

Turbulence Laboratory

SECONDARY MOTION IN TURBULENT FLOWS OVER SUPERHYDROPHOBIC SURFACES

Transcription:

DNS Study on Small ength Scale in Turbulent Flow Yonghua Yan Jie Tang Chaoqun iu Technical Report 2014-11 http://www.uta.edu/math/preprint/

DNS Study on Small ength Scale in Turbulent Flow Yonghua Yan, Jie Tang, Chaoqun iu University of Texas at Arlington Abstract According to our observation of turbulence generation, all small length scales are generated by shear layer instability. The size of small vortices should be determined by the smallest stable shear layer, e.g. smallest shear layer like laminar sub-layer in the wall bounded flow. This paper provides a new estimation of the smallest length scale by using the shear layer stability analysis, 3/4 which is different from Kolmogorov micro scales, or 0(Re ) I. Introduction Classical turbulence theory about vortex chains was given by Richardson. He has a famous poem that Big whirls have little whirls, which feed on their velocity; And little whirls have lesser whirls, and so on to viscosity in the molecular sense. However, the vortex chain generated by large vortex breakdown is never observed. As shown by our DNS, turbulence has different size of vortices from the large to small. However, they are all generated by shear layer instability (K-H type) without exception and no vortex breakdown is observed. In fact, no one ever observed the eddy cascade by instrument or computation. The Richardson energy cascade and vortex breakdown was accepted by Kolmogorov and vortex breakdown as the foundation of Kolmogorov s hypotheses. The famous Kolmogorof scale is given by Russian Mathematician Kolmogorof in 1941. The scale is obtained by dimensional analysis. Assume the velocity and length related to the largest eddy are and U, ν is the viscosity, ε is the kinetic energy, the velocity and length related to the smallest eddy are V and η, we will have the energy relation: 2 3 2 ε U U V SijSij ( ) 2 / U ν ν which means all energy, transported from largest eddy to the smallest η Vη eddy, is dissipated. Note that Reη = 1, ν 3 2 3 3 2 2 4 U V U V 3 4 Re ( ) 2 3 2 4 η ν η ν ν η η U Vη Re = and Reη = 1 ν ν Finally, (1) η η ( ) = Re or = Re 4 3 3/4 1

η represents the ratio of the Kolmogorov micro scale over the macro scale, which is very small, e.g. if 8 η 6 Re = 10, the ratio could be = 10 which cannot be resolved by any modern computers for a 3-D DNS. Kolmogorov s hypothesis is based on dimensional analysis and seems to have no possibility to be incorrect. However, there are still some questions: 1) If the Kolmogorov micro scale is generated by large vortex breakdown, it needs 20 cycles to 6 break down for Re = 10. However, no one ever observed such 20 generations of vortex breakdown cycles, even a single one. 2) When the Reynolds number becomes very large the Kolmogorov s small scale becomes extremely small. However, no one observed the real Kolmogorov micro scales either by experiment or DNS. We believe the Kolmogorov s hypothesis and his micro-scale need to be revisited. II Shear ayer Instability and Turbulence Small Scales According to our DNS observation, all small vortices are generated by shear layer instability, the smallest scale should be the smallest stable shear layer. We have done some 1-D and axial-symmetric shear layer stability analysis and found that even we have the inflection points, the shear layer still could be stable if u the shear strength or is not large enough. z 0.4 0.3 0.2 0.1 0-2 -1 0 1 2-0.1 u1-0.2-0.3-0.4 u1 0.14 0.12 0.1 0.08 0.06 0.04 0.02 0-2 -1-0.02 0 1 u2 2-0.04-0.06-0.08-0.1-0.12-0.14 u2 0.14 0.12 0.1 0.08 0.06 0.04 0.02 0-1 -0.5-0.02 0 0.5 1-0.04 u1-u2-0.06-0.08-0.1-0.12-0.14 (a) Shear layer with inflection point (u1) (b) Rotational part (u2) (c) Shear part (u1-u2) Figure 1: Shear layer velocity decomposition We pick a typical 1-D shear layer described by following functions: U 1 = a tanh( by) As we know, the existence of inflation point makes the velocity profile to be unstable for inviscid fluid flow. However, Table 1. gives the results of c i (positive is unstable and negative is stable) for the satiability analysis for standard O-S equation at different values of b for the velocity profile U=a tanh(by) at Re=100 and a=1.43. It shows that although there is an inflation point, where the second derivative equals 0, for every curve, with relative small value for b the flow could be stable. Thus, the conclusion can be made that the stability is not only related to the inflation point of the velocity profile but also related to the slope of the curve ( the curve is steeper with larger b) for viscous flow. To make a flow be unstable, the existence of inflation point is just a necessary condition, and the velocity profile should be steep enough. The numerical study is carried out in an axis-symmetric coordinate. u1-u2 2

b 0.1 0.2 0.6 0.9 1.0 2.0 3.0 4.0 c i <0 <0 <0 <0 <0 0.1186 0.3965 0.5517 Table 1. Results of c i at different values of b for the velocity profile U=1.43 tanh(b*y) at Re=100, α=1.0 According to our observation, the size of the smallest stable shear layer should be considered as the smallest scale. For any wall bounded turbulent flow, there is always a laminar sub-layer which is the smallest stable shear layer: + + z ν τw z = 1 10, z =, δv =, uτ = (2) δ u ρ v τ On the other hand, Kolmogorov s smallest scale was derived by dimensional analysis but has not been confirmed by any experiment or computation yet when Reynolds number is large, which is the assumption given by Kolmogorov. The serious weakness of classical theory given by Richardson and Kolmogorof is that nobody ever observed. As a roughly estimate, we need 20 vortex breakdowns to get Kolmogorov scale, but we even cannot see a single one. As the experiment tools are so powerful and the visualization technology is so advanced nowadays, it is very hard to believe we still cannot detect the vortex breakdown process. The only conclusion we can believe is that the classical theory on turbulence generation may be incorrect and Kolmogorov s smallest scale may not exist. III A Counterexample to Kolmogorov Scale 3.1 Tip vortex relaminarization a contradiction to classical turbulence theory As reported by both experiment and large eddy simulation (Cai te al, 2008; Figures 2 and 3), the tip vortex was developed on a 3-D airfoil and becomes turbulent on the airfoil surface. According to the classical trubulence theory, the tip vortex should be more turbulent and has smaller length scales as leaving the airfoil surface and traveling to the free stream since the Reynolds number becomes larger. As Reynolds number becomes larger, the length scale will be smaller according to Kolmogorov s theory and many smaller vortices will be found by vortex breakdown according to Richardson s vortex cascade. Unfortunately, the observation by both experiment and ES shows the oposite. The flow is relaminarized and all small length scales disappear. This example strongly oposes classical turbulence theory and strongly supports our new theroy that is turbulence is not generated by vortex breakdown but by shear layer instability since strong shear layers disapper when the tip vortex left the airfoil surface. This is apparently an counterexample to Kolmogorov s miscroscale since we find the smallest scale 3 η 4 becomes 1 as the flow re-laminarized. According to Kolmogorov s miscroscale hypothesis, = Re, the Reynolds number should be 1, which is impossible according to the definition of Reynolds number. 3

Figure 2: Instantaneous field of axial vorticity: Iso-surface of vorticity component ω x =3 Figure 3. Contours of streamwise vorticity ω x in cross planes at different locations (Tip vortex left the wall surface at x=1.00) 3.2 Important conclusions Although Kolmogorov s micro scale is derived based on dimensional analysis, there is no evidence by experiment or DNS to confirm Kolmogorov s vortex breakdown and micro scale (for smallest vortex, Re=1.) According to our observation, all small scales are generated by shear layer instability, the smallest length scale should be the smallest stable shear layer. 4

It is hard to prove a theory correct, but a counterexample is good enough to overthrow a theory. The tipvortex is a counterexample to Kolmogorov s micro scale hypothesis. 3.3 Future work More detailed description of the DNS results and more deep analysis will be given in the final AIAA paper. Reference [1] Cai, J., Jiang,., iu, C., arge Eddy Simulation of Wing Tip Vortex in the Near Field, International Journal of CFD, Vol 22, Issue 5, pp289-330, June 2008. [2] Kolmogorov, Andrey Nikolaevich (1941). "The local structure of turbulence in incompressible viscous fluid for very large Reynolds numbers". Proceedings of the USSR Academy of Sciences 30: 299 303. (Russian), translated into English by Kolmogorov, Andrey Nikolaevich (July 8, 1991). "The local structure of turbulence in incompressible viscous fluid for very large Reynolds numbers". Proceedings of the Royal Society of ondon, Series A: Mathematical and Physical Sciences 434 (1991): 9 13. Bibcode 1991RSPSA.434...9K. doi:10.1098/rspa.1991.0075 [3] iu, C. and Yan, Y., DNS Study of Turbulence Structure in a Boundary layer, AIAA2014-1449, January 13-17, 2014, Maryland, USA 5