u = φ where 2 φ = 0. (1.1) (y εh) = Dt y ε h t ε φ h h x and



Similar documents
LECTURE 5: Fluid jets. We consider here the form and stability of fluid jets falling under the influence of gravity.

Differential Relations for Fluid Flow. Acceleration field of a fluid. The differential equation of mass conservation

Dimensional analysis is a method for reducing the number and complexity of experimental variables that affect a given physical phenomena.

Fluids and Solids: Fundamentals

du u U 0 U dy y b 0 b

Stability of Evaporating Polymer Films. For: Dr. Roger Bonnecaze Surface Phenomena (ChE 385M)

MODULE VII LARGE BODY WAVE DIFFRACTION

Chapter 28 Fluid Dynamics

LECTURE 6: Fluid Sheets

Lecture 24 - Surface tension, viscous flow, thermodynamics

Basic Principles in Microfluidics

Dimensional Analysis

Fluid Mechanics: Static s Kinematics Dynamics Fluid

Lecture 8 - Turbulence. Applied Computational Fluid Dynamics

Comparison of flow regime transitions with interfacial wave transitions

Physics of the Atmosphere I

1. Fluids Mechanics and Fluid Properties. 1.1 Objectives of this section. 1.2 Fluids

Basic Equations, Boundary Conditions and Dimensionless Parameters

11 Navier-Stokes equations and turbulence

Abaqus/CFD Sample Problems. Abaqus 6.10

XI / PHYSICS FLUIDS IN MOTION 11/PA

Modeling and Simulations of Cavitating and Bubbly Flows

Fundamentals of Fluid Mechanics

INTRODUCTION TO FLUID MECHANICS

Structural Axial, Shear and Bending Moments

CE 6303 MECHANICS OF FLUIDS L T P C QUESTION BANK PART - A

A Resource for Free-standing Mathematics Qualifications

Distinguished Professor George Washington University. Graw Hill

Lecture 3 Fluid Dynamics and Balance Equa6ons for Reac6ng Flows

Chapter 7. Potential flow theory. 7.1 Basic concepts Velocity potential

Nonlinear evolution of unstable fluid interface

Viscous flow in pipe

Navier-Stokes Equation Solved in Comsol 4.1. Copyright Bruce A. Finlayson, 2010 See also Introduction to Chemical Engineering Computing, Wiley (2006).

Lecture 3. Turbulent fluxes and TKE budgets (Garratt, Ch 2)

Viscous potential flow analysis of Kelvin-Helmholtz instability in a channel

circular motion & gravitation physics 111N

Problem #1 [Sound Waves and Jeans Length]

Chapter 5 Using Newton s Laws: Friction, Circular Motion, Drag Forces. Copyright 2009 Pearson Education, Inc.

Copyright 2011 Casa Software Ltd. Centre of Mass

1 The basic equations of fluid dynamics

AP PHYSICS C Mechanics - SUMMER ASSIGNMENT FOR

Unit 4 Practice Test: Rotational Motion

Basics of vehicle aerodynamics

Lecture 5 Hemodynamics. Description of fluid flow. The equation of continuity

Practice Problems on Boundary Layers. Answer(s): D = 107 N D = 152 N. C. Wassgren, Purdue University Page 1 of 17 Last Updated: 2010 Nov 22

Exergy Analysis of a Water Heat Storage Tank

Contents. Microfluidics - Jens Ducrée Physics: Navier-Stokes Equation 1

A LAMINAR FLOW ELEMENT WITH A LINEAR PRESSURE DROP VERSUS VOLUMETRIC FLOW ASME Fluids Engineering Division Summer Meeting

Chapter 6 Work and Energy

Math 0980 Chapter Objectives. Chapter 1: Introduction to Algebra: The Integers.

1.Name the four types of motion that a fluid element can experience. YOUR ANSWER: Translation, linear deformation, rotation, angular deformation.

Dimensional Analysis

For Water to Move a driving force is needed

Statics of Structural Supports

Physics 41 HW Set 1 Chapter 15

Lecture L22-2D Rigid Body Dynamics: Work and Energy

Backwater Rise and Drag Characteristics of Bridge Piers under Subcritical

Chapter 3 Falling Objects and Projectile Motion

MICROWAVE ELECTRONICS. Prof. L. C. R. J. L. J. Chu Bahiana Briggs

Stress and deformation of offshore piles under structural and wave loading

Ch 2 Properties of Fluids - II. Ideal Fluids. Real Fluids. Viscosity (1) Viscosity (3) Viscosity (2)

CHAPTER: 6 FLOW OF WATER THROUGH SOILS

Forces on the Rocket. Rocket Dynamics. Equation of Motion: F = Ma

Fundamentals of THERMAL-FLUID SCIENCES

Lecture 16 - Free Surface Flows. Applied Computational Fluid Dynamics

CEE 370 Fall Laboratory #3 Open Channel Flow

The Influence of Aerodynamics on the Design of High-Performance Road Vehicles

How To Understand General Relativity

Experiment 3 Pipe Friction

So if ω 0 increases 3-fold, the stopping angle increases 3 2 = 9-fold.

1) The time for one cycle of a periodic process is called the A) wavelength. B) period. C) frequency. D) amplitude.

Gauss Formulation of the gravitational forces

Presentation of problem T1 (9 points): The Maribo Meteorite

State Newton's second law of motion for a particle, defining carefully each term used.

Head Loss in Pipe Flow ME 123: Mechanical Engineering Laboratory II: Fluids

Fluid Dynamics Basics

NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES

Lecture 17. Last time we saw that the rotational analog of Newton s 2nd Law is

LECTURE 2: Stress Conditions at a Fluid-fluid Interface

STRESS AND DEFORMATION ANALYSIS OF LINEAR ELASTIC BARS IN TENSION

A Comparison of Analytical and Finite Element Solutions for Laminar Flow Conditions Near Gaussian Constrictions

Open Channel Flow. M. Siavashi. School of Mechanical Engineering Iran University of Science and Technology

Chapter 5 MASS, BERNOULLI AND ENERGY EQUATIONS

AgoraLink Agora for Life Science Technologies Linköpings Universitet Kurs i Fysiologisk mätteknik Biofluidflöden

Cubes and Cube Roots

TEACHER S CLUB EXAMS GRADE 11. PHYSICAL SCIENCES: PHYSICS Paper 1

L r = L m /L p. L r = L p /L m

Physics 9e/Cutnell. correlated to the. College Board AP Physics 1 Course Objectives

39th International Physics Olympiad - Hanoi - Vietnam Theoretical Problem No. 3

PHYSICS 111 HOMEWORK SOLUTION #10. April 8, 2013

Displacement (x) Velocity (v) Acceleration (a) x = f(t) differentiate v = dx Acceleration Velocity (v) Displacement x

p atmospheric Statics : Pressure Hydrostatic Pressure: linear change in pressure with depth Measure depth, h, from free surface Pressure Head p gh

PHYS 101-4M, Fall 2005 Exam #3. MULTIPLE CHOICE. Choose the one alternative that best completes the statement or answers the question.

APPLIED MATHEMATICS ADVANCED LEVEL

6 J - vector electric current density (A/m2 )

01 The Nature of Fluids

Fluid structure interaction of a vibrating circular plate in a bounded fluid volume: simulation and experiment

Transcription:

Kelvin-Helmholtz and Rayleigh-Taylor Instabilities Consider two fluid regions, y > 0 and y < 0. In y > 0 let the fluid have uniform velocity u = (U, 0, 0 and constant density ρ =, whereas in y < 0 let ρ = ρ 2 and u = (U 2, 0, 0. Gravity is assumed to act in the negative y-direction, g = (0, g, 0. This configuration could represent wind blowing over a lake, or a model of separated flow over a step. We will assume the flow is inviscid. It can therefore suffer the tangential velocity discontinuity at y = 0. The vortex sheet associated with this discontinuity would diffuse outwards if µ 0, but we will neglect this spreading and assume that the interface has the shape y = εh(x, t. As there is no vorticity elsewhere in the flow initially, we expect the flow to be irrotational, i.e. Then we write u = φ where 2 φ = 0. (. φ = U x + εφ in y > 0, φ = U 2 x + εφ 2 in y < 0. (.2 We want φ 0 as y and φ 2 0 as y. The kinematic boundary condition takes the form on the interface or neglecting terms of O(ε 2, 0 = D φ (y εh = Dt y ε h t ε φ h x x. (.3 φ y = h t + U h x and φ 2 y = h t + U 2 h x. (.4 To leading order we can evaluate (.4 on y = 0 rather than y = εh. The other condition to apply is that the pressure must be continuous across the interface or if we ignore surface tension for the moment p = p 2 on y = εh. The time-dependent Bernoulli condition is from (0.4 ( φ p + ρ t + 2 φ 2 + gy = constant, so that to leading order on the interface y = εh, ( ( φ t + U φ x + gh φ2 = ρ 2 t + U φ 2 2 x + gh. (.5 Once more, we can evaluate (.5 on y = 0 rather than y = εh. As neither x or t appears in the coefficients of the problem, we can seek a solution proportional to e ikx+st. Here k > 0 is a real wave-number, and s is possibly complex. If we can find a value of k for which the corresponding s has a positive real part (Re(s > 0, then the interface y = 0 is unstable. We write h = h 0 e ikx+st, φ = Φ (ye ikx+st, φ 2 = Φ 2 (ye ikx+st.

Then Φ (y satisfies the ODE and boundary conditions Φ k 2 Φ = 0, Φ 0 as y Φ (0 = h 0 (s + iku (.6 from which it follows that Φ (y = h 0 k (s + iku e ky and similarly Φ 2 (y = h 0 k (s + iku 2e ky. (.7 The pressure constraint (.4 requires that or combining (.8 and (.7, [(s + iku Φ (0 + gh 0 ] = ρ 2 [(s + iku 2 Φ 2 (0 + gh 0 ] (.8 [ gk (s + iku 2] = ρ 2 [ gk + (s + iku2 2]. (.9 This is a quadratic equation for s(k, which is in general known as the dispersion relation. Solving this equation we obtain s = ik ρ [ U + ρ 2 U 2 k 2 ρ 2 (U U 2 2 ± + ρ 2 ( + ρ 2 2 + kg ρ ] /2 ρ 2. (.0 + ρ 2 For instability, s must have a positive real part. It is clear that this will occur if and only if the quantity in square brackets is positive, that is if Instability if: k 2 ρ 2 (U U 2 2 > kg(ρ 2 2 ρ 2. (. Instability of a vortex sheet: If U U 2, we see from (. that instability always occurs for large enough k, i.e. for short wavelengths. The smaller the wavelength the larger the growth rate. This is known as the Kelvin-Helmholtz instability. Water waves: For example, consider air moving over a stationary lake, so that U 2 = 0, ρ 2. Instability occurs if k > g U 2 ρ 2 (.2 Heavy fluid over light fluid: If > ρ 2 we see that every value of k leads to instability (recall k > 0. This is known as the Rayleigh-Taylor instability. Wave frequencies: If U = U 2 = 0 and < ρ 2 then the interface can support surface waves of frequency ω (s = iω where ω = ( /2 ρ2 gk. (.3 ρ 2 + The phase velocity c = ω/k for small water waves ( = 0 is therefore c = (g/k /2. 2

Three dimensional disturbances: So far we have only considered 2-D perturbations. If instead we allow the surface to take the form y = εh 0 e ikx+ilz+st where κ = (k 2 + l 2 /2, (.4 then the analysis is very similar, with for example Φ e κy. The instability condition (. remains the same with the k on the RHS replaced by κ. As κ k, we can infer from this that if a mode with a particular (k, l is unstable so is the mode with (k, 0, and indeed the growth rate is larger for the 2-D disturbance. We will meet this idea later an example of Squires theorem. If a configuration is unstable, we have shown that the largest growth rates have large k, and are formally infinite. In practice, some physical effect we have neglected will become important. Two processes we might expect to limit the size of the wave-number and growth-rates are viscosity and surface tension. The curvature of the surface (.4 is The effect of Surface Tension K = n = [( εikh 0,, εilh 0 e ikx+ilz+st ] = εκ 2 h 0 e ikx+ilz+st. (.5 The normal stress condition p = p 2 is now replaced by p = p 2 + γk. Making this modification, the dispersion relation (.0 takes the form s = ik ρ [ U + ρ 2 U 2 k 2 ρ 2 (U U 2 2 ± + ρ 2 ( + ρ 2 2 + κg( ρ 2 κ 3 ] /2 γ. (.6 + ρ 2 The cubic term γκ 3 will clearly dominate the large wave-numbers irrespective of the other parameters, so as we might expect, surface tension strongly resists high-curvature perturbations. Likewise, if κ, the linear gravitational term will be largest, so that the long wavelengths will be unstable if > ρ 2. If ρ 2 >, however, it is possible for the flow to be stable for all k and l. Once more we can show that the most unstable case has l = 0 so we can replace κ by k. The term in brackets is negative for all k > 0, giving stability, if (U U 2 2 < 2( + ρ 2 ρ 2 [γg(ρ 2 ] /2. (.7 As U U 2 increases, the first wave to go unstable has k 2 = g(ρ 2 /γ We can now calculate the wind speed necessary to drive waves on the surface of a lake. If we put g = 9.8, U 2 = 0, ρ 2 = 000 =.25 and γ = 0.074 appropriate for air above water, we find U = 6.6m/s. At this critical wind-speed, the wavelength of the waves is 2π/k =.7cm. 3

Fluids in a rigid cylinder We have seen that a vortex sheet can be stabilised by the combined action of gravity and surface tension. Is it possible for the gravitational instability of a heavy fluid being held over a light fluid to be nullified? Let us consider a vertical, rigid cylinder of radius a. We shall use cylindrical polar coordinates (r, θ, z, Once more z > 0 contains a fluid of density and z < 0 has density ρ 2. We perturb the interface z = 0 to z = εh(r, θ. Then the velocity is u = φ with 2 φ = 0, or u = ( φ r, φ r θ, φ z, r r ( r φ r The separable solutions to Laplace s equation in this geometry are + r 2 2 φ θ 2 + 2 φ z 2 = 0. (.8 φ = Ae ±kz J m (kre imθ+st (.9 where J m is a Bessel function. u(r = J m (kr is the solution to the problem u + r u + u (k 2 m2 = 0 with u(0 = (.20. r 2 The possible values of k are determined by the rigid wall at r = a, where the normal velocity, φ/ r = 0 or J m(ka = 0. This gives a set of possible values k = k mn, for m = 0,..., n =, 2... Note that m = 0 is an axisymmetric disturbance. The kinematic constraint is that φ/ z = h/ t on z = 0 which suggests we look at perturbations z = εh 0 J m (kre imθ+st = K = k 2 h. (.2 The pressure boundary condition on z = h is ( ( φ t + gh φ2 = ρ 2 t + gh Putting all this together, we obtain the dispersion relation + γk. (.22 s 2 = k[g( ρ 2 γk 2 ] + ρ 2 where J m(ka = 0. (.23 We see that we get stability provided the smallest admissable value of ka satisfies (ka 2 min > ga2 ( ρ 2 γ. (.24 It turns out that the smallest value of ka occurs when m =, and (ka min.8. This predicts that the largest pipe radius for which surface tension can support water above air is about 2cm. Does this agree with your physical intuition, or did you expect the fluid to fall out in an axisymmetric manner? The theory predicts that if the interface is unstable the air will rush in one side of the pipe (say near θ 0 and the fluid will fall out on the other (θ π. 4

Inviscid instability of a cylindrical jet When we turn on a tap a jet of water emerges, whose cylindrical surface quickly becomes kinked and then breaks up into drops. As we shall see, this is a capillary or surface tension instability. Gravity may be neglected during the evolution of the jet. Consider a liquid cylinder 0 < r < a moving with constant velocity (0, 0, U in the axial z-direction. The outside we consider to be dynamically negligible, so that the external pressure is constant on the surface. We envisage a surface perturbation of the form r = a( + εζ a ( + εe ikz+imθ. (.25 Here m must be an integer, but k can be any positive number. The curvature of this surface K = n takes the form (ignoring terms proportional to ε 2 n = (, εimζ, ikaεζ K = r + ε a (m2 + k 2 a 2 ζ = a + εζ a (m2 + k 2 a 2. (.26 Taking the velocity u = (0, 0, U + φ, the kinematic boundary condition on r = a is and the pressure condition is 0 = D φ (r a aεζ = Dt r The solutions to Laplace s equation take the form = εaζ(s + iku, (.27 ρsφ + 2ρ2Uikφ + γk = constant. (.28 φ = εai m (krζ where u = I m (kr satisfies u + u r (k 2 + m2 r 2 u = 0. (.29 I m is called a modified Bessel function (compare (.20. It behaves like r m near r = 0 and increases monotonically, behaving like e kr as r. Combining (.29, (.28 and (.27, we find that (s + iku 2 = γ ρa 3 ( m2 k 2 a 2 ( kai m (ka I m (ka. (.30 The last factor involving Bessel functions is always positive, so doesn t affect the stability. We see the RHS is negative if m or if ka, However, the long, axisymmetric waves with m = 0 and 0 < ka < are unstable. The jet is unstable to all axial wavelengths larger than its circumference (2πa. Calculation shows that the greatest value of s occurs at ka 0.7. This was shown by Lord Rayleigh in 879. Try it in your kitchen! The theory predicts a wavelength of about 4.5 jet diameters. 5