Chapter 3 Ideal Fluid Flow

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

1 The basic equations of fluid dynamics

- momentum conservation equation ρ = ρf. These are equivalent to four scalar equations with four unknowns: - pressure p - velocity components

Fundamentals of Fluid Mechanics

CBE 6333, R. Levicky 1 Differential Balance Equations

Basic Equations, Boundary Conditions and Dimensionless Parameters

4 Microscopic dynamics

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

When the fluid velocity is zero, called the hydrostatic condition, the pressure variation is due only to the weight of the fluid.

Fluids and Solids: Fundamentals

Lecture 4 Classification of Flows. Applied Computational Fluid Dynamics

FLUID MECHANICS IM0235 DIFFERENTIAL EQUATIONS - CB _1

NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES

INTRODUCTION TO FLUID MECHANICS

Distinguished Professor George Washington University. Graw Hill

The Navier Stokes Equations

11 Navier-Stokes equations and turbulence

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

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

Introduction to COMSOL. The Navier-Stokes Equations

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

CBE 6333, R. Levicky 1 Review of Fluid Mechanics Terminology

LECTURE 2: Stress Conditions at a Fluid-fluid Interface

Dimensional Analysis

Chapter 7. Fundamental Theorems: Vorticity and Circulation

Physics of the Atmosphere I

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

High Speed Aerodynamics Prof. K. P. Sinhamahapatra Department of Aerospace Engineering Indian Institute of Technology, Kharagpur

Dimensionless form of equations

Pre-requisites

Fluid Mechanics Prof. S. K. Som Department of Mechanical Engineering Indian Institute of Technology, Kharagpur

Physics 1A Lecture 10C

Stokes flow. Chapter 7

CONSERVATION LAWS. See Figures 2 and 1.

Center of Gravity. We touched on this briefly in chapter 7! x 2

Chapter 10 Rotational Motion. Copyright 2009 Pearson Education, Inc.

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

Differential Balance Equations (DBE)

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

Lecture 3 Fluid Dynamics and Balance Equa6ons for Reac6ng Flows

Lecture 16. Newton s Second Law for Rotation. Moment of Inertia. Angular momentum. Cutnell+Johnson: 9.4, 9.6

INTRODUCTORY LECTURES ON FLUID DYNAMICS. Roger K. Smith

du u U 0 U dy y b 0 b

Laminar Flow and Heat Transfer of Herschel-Bulkley Fluids in a Rectangular Duct; Finite-Element Analysis

MODULE VII LARGE BODY WAVE DIFFRACTION

How To Know If A Solution Of The Navier-Stokes Equations Is Smooth

Modeling Mechanical Systems

Chapter 2. Derivation of the Equations of Open Channel Flow. 2.1 General Considerations

KINEMATICS OF PARTICLES RELATIVE MOTION WITH RESPECT TO TRANSLATING AXES

Kyu-Jung Kim Mechanical Engineering Department, California State Polytechnic University, Pomona, U.S.A.

Lecture 6 - Boundary Conditions. Applied Computational Fluid Dynamics

Viscous flow through pipes of various cross-sections

An Introduction to Partial Differential Equations

Lecture 11 Boundary Layers and Separation. Applied Computational Fluid Dynamics

EXAMPLE: Water Flow in a Pipe

Viscous flow in pipe

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

Let s first see how precession works in quantitative detail. The system is illustrated below: ...

LECTURE 6: Fluid Sheets

Practice Problems on the Navier-Stokes Equations

Scalars, Vectors and Tensors

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

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

Viscosity and the Navier-Stokes equations

2.016 Hydrodynamics Reading # Hydrodynamics Prof. A.H. Techet

BACHELOR OF SCIENCE DEGREE

Chapter 28 Fluid Dynamics

Lecturer, Department of Engineering, Lecturer, Department of Mathematics,

SIZE OF A MOLECULE FROM A VISCOSITY MEASUREMENT

Basic Principles in Microfluidics

FLUID MECHANICS FOR CIVIL ENGINEERS

Midterm Solutions. mvr = ω f (I wheel + I bullet ) = ω f 2 MR2 + mr 2 ) ω f = v R. 1 + M 2m

Hydrodynamics of stellar explosions

A new approach for regularization of inverse problems in image processing

A CODE VERIFICATION EXERCISE FOR THE UNSTRUCTURED FINITE-VOLUME CFD SOLVER ISIS-CFD

PEDAGOGY: THE BUBBLE ANALOGY AND THE DIFFERENCE BETWEEN GRAVITATIONAL FORCES AND ROCKET THRUST IN SPATIAL FLOW THEORIES OF GRAVITY *

A fundamental study of the flow past a circular cylinder using Abaqus/CFD

Distance Learning Program

8.2 Elastic Strain Energy

Model of a flow in intersecting microchannels. Denis Semyonov

11. Rotation Translational Motion: Rotational Motion:

3 The boundary layer equations

SOLID MECHANICS TUTORIAL MECHANISMS KINEMATICS - VELOCITY AND ACCELERATION DIAGRAMS

Parabolic Equations. Chapter 5. Contents Well-Posed Initial-Boundary Value Problem Time Irreversibility of the Heat Equation

The Basics of FEA Procedure

Elasticity Theory Basics

Chapter 4. Dimensionless expressions. 4.1 Dimensional analysis

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

Perfect Fluidity in Cold Atomic Gases?

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

Mathematical Modeling and Engineering Problem Solving

VISCOSITY OF A LIQUID. To determine the viscosity of a lubricating oil. Time permitting, the temperature variation of viscosity can also be studied.

Salem Community College Course Syllabus. Course Title: Physics I. Course Code: PHY 101. Lecture Hours: 2 Laboratory Hours: 4 Credits: 4

Dynamics of Rotational Motion

4.3 Results Drained Conditions Undrained Conditions References Data Files Undrained Analysis of

Chapter 5 MASS, BERNOULLI AND ENERGY EQUATIONS

Quasi-static evolution and congested transport

FLUID DYNAMICS. Intrinsic properties of fluids. Fluids behavior under various conditions

An Introduction to Hydrocode Modeling. Gareth S. Collins

Isaac Newton s ( ) Laws of Motion

Transcription:

2.20 - Marine Hydrodynamics, Spring 2005 Lecture 7 2.20 - Marine Hydrodynamics Lecture 7 Chapter 3 Ideal Fluid Flow The structure of Lecture 7 has as follows: In paragraph 3.0 we introduce the concept of inviscid fluid and formulate the governing equations and boundary conditions for an ideal fluid flow. In paragraph 3.1 we introduce the concept of circulation and state Kelvin s theorem (a conservation law for angular momentum). In paragraph 3.2 we introduce the concept of vorticity. Inviscid Fluid ν = 0 Ideal Fluid Flow + Dρ Incompressible Flow ( 1.1) =0 or v = 0 Dt 1

3.0 Governing Equations and Boundary Conditions for Ideal Flow Inviscid Fluid, Ideal Flow Recall Reynolds number is a qualitative measure of the importance of viscous forces compared to inertia forces, UL inertia forces R e = = ν viscous forces For many marine hydrodynamics problems studied in 13.021 the characteristic lengths and velocities are L 1m and U 1m/s respectively. The kinematic viscosity in water is ν water =10 6 m 2 /s leading thus to typical Reynolds numbers with respect to U and L in the order of UL R e = 10 6 >>> 1 ν 1 viscous forces 0 inertia forces R e This means that viscous effects are << compared to inertial effects - or confined within very small regions. In other words, for many marine hydrodynamics problems, viscous effects can be neglected for the bulk of the flow. Neglecting viscous effects is equivalent to setting the kinematic viscosity ν = 0, but ν = 0 inviscid fluid Therefore, for the typical marine hydrodynamics problems we assume incompressible flow + inviscid fluid ideal fluid flow which turns out to be a good approximation for many problems. 2

Governing Equations for Ideal Fluid Flow Continuity Equation: v nˆ= u n no flux + free (to) slip ˆ= U }{{ n } given v = 0 Momentum (Navier-Stokes Euler) equations: v 1 + v v = p gĵ t ρ By neglecting the viscous stress term (ν 2 v) the Navier-Stokes equations reduce to the Euler equations. (Careful not to confuse this with the Euler equation in 1.6). The N-S equations are second order PDE s with respect to space (2 nd order in 2 ), thus: (a) require 2 kinematic boundary conditions, and (b) produce smooth solutions in the velocity field. The Euler equations are first order PDE s, thus: (a) require 1 kinematic bound ary condition, and (b) may allow discontinuities in the velocity field. Boundary Conditions for Euler equations (Ideal Flow): KBC: Note: No slip condition v tˆ = U tˆ does not apply. The no slip condition is required to ensure that the velocity gradients are finite and therefore the viscous stresses ˆτ ij are finite. But since ν = 0 the viscous stresses are identically zero (ˆτ ij μ = ρν =0) and the velocity gradients can be infinite. Or else the velocity field need not be continuous. 3

y u(0) u(dy) u Viscousflow τ w μ y < < U Inviscidflow τ 0 u w y DBC: p =... Pressure given on the boundary Similarly to the argument for the KBC, viscous stresses ˆτ ij cannot be specified on any boundary since ν = 0. Summary of consequences neglecting viscous effects this far: Neglecting viscous effects is equivalent to setting the kinematic viscosity equal to zero: ν = 0 Setting ν = 0 inviscid fluid Setting ν = 0 the viscous term in the Navier-Stokes equations drops out and we obtain the Euler equations. The Euler equations are 1st order PDE s in space, thus (a) require only one boundary condition for the velocity and (b) may allow for velocity jumps. Setting ν = 0 all the viscous stresses ˆτ ij μ = ρν are identically 0. This may allow for infinite velocity gradients. This affects (a) the KBC, allowing free slip, and (b) the DBC, where no viscous stresses can be specified on any boundary. 4

3.1 Circulation Kelvin s Theorem 3.1.1 Γ Instantaneous circulation around any arbitrary closed contour C. C dx v v Γ= }{{} v dx C tangential velocity The circulation Γ is an Eulerian idea and is instantaneous, a snapshot. 5

3.1.2 Kelvin s Theorem (KT) : For ideal fluid under conservative body forces, dγ = 0 following any material contour C, dt i.e., Γ remains constant under for Ideal Fluid under Conservative Forces (IFCF). This is a statement of conservation of angular momentum. (Mathematical Proof: cf JNN pp 103) Kinematics of a small deformable body: (a) Uniform translation Linear momentum (b) Rigid body rotation Angular momentum (c) Pure strain No linear or angular momentum involved (no change in volume (d) Volume dilatation For Ideal Fluid under Conservative body Forces: (a) Linear momentum Can change (b) Angular momentum By K.T., cannot change (c) Pure strain Can change (d) Volume dilatation Not allowed (incompressible fluid) Kelvin s Theorem is a statement of conservation of angular momentum under IFCF. 6

Example 1: Angular momentum of point mass. v 1 v 2 r 1 θ m 1 m 2 r2 Angular momentum of point mass: L = r (m v) = mvr = mr 2 θ Conservation of angular momentum: L = L 1 2 m 1 =m 2 m1 v 1 r 1 = m 2 v 2 r 2 = v 1 r 1 = v 2 r 2 or r 1 2 θ 1 = r 2 2 θ 2 Conservation of angular momentum does not imply constant angular velocity: Angular Momentum angular velocity ω 7

Example 2: Conservation of circulation around a shrinking circular material volume V m. υ r 1 1 υ 2 r 2 V m V m 2π 2π Γ 1 = dθr 1 v 1 = dθr 2 v 2 =Γ 2 0 0 Example 3: Conservation of circulation around a shrinking arbitrary material volume V m,c m. Γ 1 = v 1 d x = v 2 d x = Γ 2 C 1 C 2 8

3.2 Vorticity 3.2.1 Definition of Vorticity ( ) ( ) ( ) w v w u v u ω = v = î ĵ + kˆ y z x z x y Relationship of vorticity to circulation - Apply Stokes Theorem: Γ= v d x = ( v) nds ˆ = ω nds ˆ Flux of vorticity out of S C any S covering C any S covering C 3.2.2 What is Vorticity? For example, special case: 2D flow - w = 0; =0; ω y = ω x = 0 and z ω z = v u x y (a) Translation: u = constant, v = constant time t + Δt uiˆ + υ ˆj uiˆ + υ ˆj time t uiˆ + υ ˆj uiˆ + υ ˆj v x u =0, =0 ω z = 0 no vorticity y 9

(b) Pure Strain (no volume change): Area t+ Δt Area t No volume change Area t =Area t+ Δt u v u v = ; u = -v; =0; =0 ω z =0 x y y x 10

(c) Angular deformation δ x = u dy Δt y r υ = u dyi ˆ + y υ dy ˆ j y time t + Δt time t dy δ y = ( υ dx)δt x r dx υ = 0 r υ = u dx i ˆ + υ dx ĵ x x u v ω = 0 only if = δx = δy( for dx = dy) y x 11

(d) Pure rotation with angular velocity Ω time t + Δt Ω Δt υ r = Ωdyî time t dy Ω Δt Ω r υ = 0 dx r υ =Ωdx ĵ v x i.e. vorticity 2(angular velocity). u =Ω; = Ω; ω z =2Ω y 3.2.3 Irrotational Flow A flow is irrotational if the vorticity is zero everywhere or if the circulation is zero along any arbitrary closed contour: ω 0 everywhere Γ 0 for any C Further on, if at t = t o, the flow is irrotational, i.e., Γ 0 for all C, then Kelvin s theorem states that under IFCF, Γ 0 for all C for all time t: (Special case of Kelvin s theorem) once irrotational, always irrotational 12