External Flow and Boundary Layer Concepts

Similar documents
BOUNDARY LAYER FLOWS HINCHEY

τ du In his lecture we shall look at how the forces due to momentum changes on the fluid and viscous forces compare and what changes take place.

Principles of Convection

Friction Factors and Drag Coefficients

M E 320 Professor John M. Cimbala Lecture 38

DAY 19: Boundary Layer

Empirical Co - Relations approach for solving problems of convection 10:06:43

Lecture-4. Flow Past Immersed Bodies

Lecture 7 Boundary Layer

Chapter 8: Flow in Pipes

Day 24: Flow around objects

Fluid: Air and water are fluids that exert forces on the human body.

FACULTY OF CHEMICAL & ENERGY ENGINEERING FLUID MECHANICS LABORATORY TITLE OF EXPERIMENT: MINOR LOSSES IN PIPE (E4)

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

Chapter 10 Flow in Conduits

SENTHIL SELIYAN ELANGO ID: UB3016SC17508 AIU HYDRAULICS (FLUID DYNAMICS)

Outlines. simple relations of fluid dynamics Boundary layer analysis. Important for basic understanding of convection heat transfer

Chapter 3 Lecture 8. Drag polar 3. Topics. Chapter-3

Basic Fluid Mechanics

UNIT II Real fluids. FMM / KRG / MECH / NPRCET Page 78. Laminar and turbulent flow

Lecture 30 Review of Fluid Flow and Heat Transfer

1. Introduction, tensors, kinematics

Boundary-Layer Theory


Introduction to Turbulence AEEM Why study turbulent flows?

Problem 4.3. Problem 4.4

Fluid Mechanics. Professor Brian Launder Room GB/C031. Flow Management : An introduction

Chapter 8: Flow in Pipes

FLUID MECHANICS. Chapter 9 Flow over Immersed Bodies

SG Turbulence models for CFD

Given the water behaves as shown above, which direction will the cylinder rotate?

R09. d water surface. Prove that the depth of pressure is equal to p +.

Fluid Mechanics Prof. T.I. Eldho Department of Civil Engineering Indian Institute of Technology, Bombay. Lecture - 17 Laminar and Turbulent flows

Convection. forced convection when the flow is caused by external means, such as by a fan, a pump, or atmospheric winds.

Tutorial 10. Boundary layer theory

External Flows. Dye streak. turbulent. laminar transition

Laminar Flow. Chapter ZERO PRESSURE GRADIENT

Turbulence - Theory and Modelling GROUP-STUDIES:

PART 1B EXPERIMENTAL ENGINEERING. SUBJECT: FLUID MECHANICS & HEAT TRANSFER LOCATION: HYDRAULICS LAB (Gnd Floor Inglis Bldg) BOUNDARY LAYERS AND DRAG

Department of Mechanical Engineering

Signature: (Note that unsigned exams will be given a score of zero.)

Signature: (Note that unsigned exams will be given a score of zero.)

UNIT 4 FORCES ON IMMERSED BODIES. Lecture-01

Applied Fluid Mechanics

FLOW IN CONDUITS. Shear stress distribution across a pipe section. Chapter 10

CEE 3310 External Flows (Boundary Layers & Drag, Nov. 14, Re 0.5 x x 1/2. Re 1/2

Unit operations of chemical engineering

Theory and Fundamental of Fluid Mechanics

CEE 3310 External Flows (Boundary Layers & Drag, Nov. 12, Re 0.5 x x 1/2. Re 1/2

CLASS SCHEDULE 2013 FALL

Turbulent Boundary Layers & Turbulence Models. Lecture 09

Chemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2017

Turbulence Laboratory

An-Najah National University Civil Engineering Department. Fluid Mechanics. Chapter 1. General Introduction

Fluids II (Fluids in motion)

Visualization of flow pattern over or around immersed objects in open channel flow.

Forced Convection: Inside Pipe HANNA ILYANI ZULHAIMI

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

Only if handing in. Name: Student No.: Page 2 of 7

PIPE FLOWS: LECTURE /04/2017. Yesterday, for the example problem Δp = f(v, ρ, μ, L, D) We came up with the non dimensional relation

Vortex Induced Vibrations

Chapter 3 NATURAL CONVECTION

7.6 Example von Kármán s Laminar Boundary Layer Problem

FE Fluids Review March 23, 2012 Steve Burian (Civil & Environmental Engineering)

Fluid Mechanics Prof. T. I. Eldho Department of Civil Engineering Indian Institute of Technology, Bombay

2, where dp is the constant, R is the radius of

Prof. Scalo Prof. Vlachos Prof. Ardekani Prof. Dabiri 08:30 09:20 A.M 10:30 11:20 A.M. 1:30 2:20 P.M. 3:30 4:20 P.M.

FLUID MECHANICS PROF. DR. METİN GÜNER COMPILER

Fluids. Fluids in Motion or Fluid Dynamics

HVAC Clinic. Duct Design

External Forced Convection. Copyright The McGraw-Hill Companies, Inc. Permission required for reproduction or display.

Recap: Static Fluids

4.2 Concepts of the Boundary Layer Theory

Part A: 1 pts each, 10 pts total, no partial credit.

CEE 3310 External Flows (Boundary Layers & Drag), /2 f = 0.664

APPLIED FLUID DYNAMICS HANDBOOK

7.11 Turbulent Boundary Layer Growth Rate

The Reynolds experiment

Chapter 1: Basic Concepts

Physical Properties of Fluids

There are no simple turbulent flows

MEC-E2001 Ship Hydrodynamics. Prof. Z. Zong Room 213a, K3, Puumiehenkuja 5A, Espoo

Review for Exam Hyunse Yoon, Ph.D. Adjunct Assistant Professor Department of Mechanical Engineering, University of Iowa

SCHOOL OF CHEMICAL ENGINEERING FACULTY OF ENGINEERING AND TECHNOLOGY SRM UNIVERSITY COURSE PLAN

Module 2: External Flows Lecture 6: Exact Solution of Boundary Layer Equation. The Lecture Contains: Blasius Solution. Numerical Approach

Review for Exam Hyunse Yoon, Ph.D. Assistant Research Scientist IIHR-Hydroscience & Engineering University of Iowa

Mechanical Engineering Science for Medical Engineers Level: 4 Credit value: 8 GLH: 62 TQT: 80

Introduction to Aerospace Engineering

Momentum (Newton s 2nd Law of Motion)

FLUID MECHANICS. Lecture 7 Exact solutions

Simulating Drag Crisis for a Sphere Using Skin Friction Boundary Conditions

WALL ROUGHNESS EFFECTS ON SHOCK BOUNDARY LAYER INTERACTION FLOWS

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

Viscous Flow in Ducts

centrifugal acceleration, whose magnitude is r cos, is zero at the poles and maximum at the equator. This distribution of the centrifugal acceleration

The most common methods to identify velocity of flow are pathlines, streaklines and streamlines.

EXPERIMENT II - FRICTION LOSS ALONG PIPE AND LOSSES AT PIPE FITTINGS

EXAMPLES (SEDIMENT TRANSPORT) AUTUMN 2018

Fluid dynamics - viscosity and. turbulent flow

Given a stream function for a cylinder in a uniform flow with circulation: a) Sketch the flow pattern in terms of streamlines.

Transcription:

1

2 Lecture (8) on Fayoum University External Flow and Boundary Layer Concepts By Dr. Emad M. Saad Mechanical Engineering Dept. Faculty of Engineering Fayoum University Faculty of Engineering Mechanical Engineering Dept. 2015-2016

3 Characteristics of External Flow

4 Characteristics of External Flow

5 Characteristics of External Flow

6 Characteristics of External Flow

7 Characteristics of External Flow

8 Lift and Drag Concepts

9 Boundary-layer

10 Boundary-layer

11 Boundary-layer Concept Upstream the velocity profile is uniform, (free stream flow) a long way downstream we have the velocity profile as shown in figure. This is the known as fully developed flow. But how do we get to that state? This region, where there is a velocity profile in the flow due to the shear stress at the wall, we call the boundary layer or is the layer of fluid in the immediate vicinity of a bounding surface where the effects of viscosity are significant. The stages of the formation of the boundary layer are shown in the figure below:

12 Boundary-layer Concept

13 Boundary-layer Concept We define the thickness of this boundary layer as the distance from the wall to the point where the velocity is 99% of the "free stream" velocity, the velocity in the middle of the pipe or river. Boundary layer thickness, δ = distance from wall to point where u = 0.99 u main stream The value of δ will increase with distance from the point where the fluid first starts to pass over the boundary - the flat plate in our example. It increases to a maximum in fully developed flow. Correspondingly, the drag force D on the fluid due to shear stress to at the wall increases from zero at the start of the plate to a maximum in the fully developed flow region where it remains constant. We can calculate the magnitude of the drag force by using the momentum equation. Our interest in the boundary layer is that its presence greatly affects the flow through or round an object. So here we will examine some of the phenomena associated with the boundary layer and discuss why these occur.

14 Boundary-layer Types 1. Laminar Boundary Layer Flow The laminar boundary is a very smooth flow, while the turbulent boundary layer contains swirls or "eddies." The laminar flow creates less skin friction drag than the turbulent flow, but is less stable. Boundary layer flow over a wing surface begins as a smooth laminar flow. As the flow continues back from the leading edge, the laminar boundary layer increases in thickness. 2. Turbulent Boundary Layer Flow At some distance back from the leading edge, the smooth laminar flow breaks down and transitions to a turbulent flow. From a drag standpoint, it is advisable to have the transition from laminar to turbulent flow as far aft on the wing as possible, or have a large amount of the wing surface within the laminar portion of the boundary layer. The low energy laminar flow, however, tends to break down more suddenly than the turbulent layer.

15 Boundary-layer Types

Surface Roughness Effect on Boundary-layer 16 In turbulent flow if the height of the roughness of a pipe is greater than the thickness of the laminar sub-layer then this increases the amount of turbulence and energy losses in the flow. If the height of roughness is less than the thickness of the laminar sub-layer the pipe is said to be smooth and it has little effect on the boundary layer. In laminar flow the height of roughness has very little effect

Boundary layers in Pipes 17 Fully developed laminar parabolic velocity profile

Boundary layers in Pipes 18 Fully developed turbulent velocity profile

Boundary layers in Pipes 19 Once the boundary layer has reached the center of the pipe the flow is said to be fully developed. (Note that at this point the whole of the fluid is now affected by the boundary friction) The length of pipe before fully developed flow is achieved is different for the two types of flow. The length is known as the entry length. Laminar flow entry length 120 diameter i.e. Le = 120 D Turbulent flow entry length 60 diameter i.e. Le = 60 D

20 Boundary-layer Control

21