..perhaps the hardest place to use Bernoulli’s equation (so don’t)

Slides:



Advertisements
Similar presentations
Human Movement in a Fluid Medium
Advertisements

Instructor: André Bakker
Convection.
External Convection: Laminar Flat Plate
CHAPTER 5 Principles of Convection
Boundary Layer Flow Describes the transport phenomena near the surface for the case of fluid flowing past a solid object.
Pharos University ME 352 Fluid Mechanics II
VIII. Viscous Flow and Head Loss. Contents 1. Introduction 2. Laminar and Turbulent Flows 3. Friction and Head Losses 4. Head Loss in Laminar Flows 5.
Flow over immersed bodies. Boundary layer. Analysis of inviscid flow.
External Flows.
MECH 221 FLUID MECHANICS (Fall 06/07) Tutorial 9
Anoop Samant Yanyan Zhang Saptarshi Basu Andres Chaparro
Flow Over Immersed Bodies
15. Physics of Sediment Transport William Wilcock (based in part on lectures by Jeff Parsons) OCEAN/ESS
0.1m 10 m 1 km Roughness Layer Surface Layer Planetary Boundary Layer Troposphere Stratosphere height The Atmospheric (or Planetary) Boundary Layer is.
CHE/ME 109 Heat Transfer in Electronics
Lecture 7 Exact solutions
Introduction to Convection: Flow and Thermal Considerations
Key Boundary Layer Equations Normal transition from Laminar to Turbulent x Boundary layer thickness (m) at distance x down plate = Shear stress on plate.
ES 202 Fluid and Thermal Systems Lecture 26: Friction Drag on a Flat Plate (2/11/2003)
Fluid Dynamics: Boundary Layers
Paul Drosinis UBC Phys 420. Introduction Short history on fluid dynamics Why bother studying fluid flow? Difference between Newtonian and Non-Newtonian.
External Flow: The Flat Plate in Parallel Flow
Convection Prepared by: Nimesh Gajjar. CONVECTIVE HEAT TRANSFER Convection heat transfer involves fluid motion heat conduction The fluid motion enhances.
Lesson 12 Laminar Flow - Slot Flow
Introduction to Convection: Flow and Thermal Considerations
Drag Lecture 6 Chapter 3.
ERT 209 HEAT & MASS TRANSFER Sem 2/ Prepared by; Miss Mismisuraya Meor Ahmad School of Bioprocess Engineering University Malaysia Perlis 17 February.
Dr. Kamel Mohamed Guedri Umm Al-Qura University, Room H1091
Boundary Layer Laminar Flow Re ‹ 2000 Turbulent Flow Re › 4000.
Introduction to Fluid Mechanics
Boundary Layer Velocity Profile z ū Viscous sublayer Buffer zone Logarithmic turbulent zone Ekman Layer, or Outer region (velocity defect layer)
Mass Transfer Coefficient
Chapter 6 Introduction to Forced Convection:
Aerodynamic Forces Lift and Drag.
2004Fluid Mechanics II Prof. António Sarmento - DEM/IST u Contents: –1/7 velocity law; –Equations for the turbulent boundary layer with zero pressure gradient.
A model of a river boat is to be tested at 1:13.5 scale. The boat is designed to travel at 9mph in fresh water at 10 o C. (1)Estimate the distance from.
Introduction to Fluid Mechanics
 ~ 0 [u(x,y)/Ue] (1 – u(x,y)/Ue)dy
15. Physics of Sediment Transport William Wilcock (based in part on lectures by Jeff Parsons) OCEAN/ESS 410.
External Flows An internal flow is surrounded by solid boundaries that can restrict the development of its boundary layer, for example, a pipe flow. An.
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
Reynolds Analogy It can be shown that, under specific conditions (no external pressure gradient and Prandtle number equals to one), the momentum and heat.
Compressible Frictional Flow Past Wings P M V Subbarao Professor Mechanical Engineering Department I I T Delhi A Small and Significant Region of Curse.
CE 1501 Flow Over Immersed Bodies Reading: Munson, et al., Chapter 9.
Elementary Mechanics of Fluids
MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 8: BOUNDARY LAYER FLOWS
INTRODUCTION TO CONVECTION
Chapter 7 EXTERNAL FORCED CONVECTION
PHAROS UNIVERSITY ME 253 FLUID MECHANICS II
U/U = sin(  /2);  = y/  Given U and viscosity table 9.2 Sketch  (x),  *(x),  w (x) LAMINARLAMINAR T A B L E 9.2.

Boundary Layer on a Flat Plate: Blasius Solution H z from Kundu’s book Assuming displacement of streamlines is negligible →u = U = constant everywhere,
External Flow: The Flat Plate in Parallel Flow
APPLICATION TO EXTERNAL FLOW
BOUNDARY LAYERS Zone of flow immediately in vicinity of boundary Motion of fluid is retarded by frictional resistance Boundary layer extends away from.
External Flow: The Flat Plate in Parallel Flow Chapter 7 Section 7.1 through 7.3.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 6 Introduction to convection.
External flow: drag and Lift
Chapter 12-2 The Effect of Turbulence on Momentum Transfer
Chapter 6: Introduction to Convection
Ship Hydrodynamics - Resistance
Date of download: 10/26/2017 Copyright © ASME. All rights reserved.
Subject Name: AERODYNAMICS - I
External Flows An internal flow is surrounded by solid boundaries that can restrict the development of its boundary layer, for example, a pipe flow. An.
Fundamentals of Convection
9th Lecture : Turbulence (II)
Heat Transfer Coefficient
Section 8, Lecture 1, Supplemental Effect of Pressure Gradients on Boundary layer • Not in Anderson.
Fundamentals of TRANSPORT MECHANISMs
Presentation transcript:

..perhaps the hardest place to use Bernoulli’s equation (so don’t) Boundary layer ..perhaps the hardest place to use Bernoulli’s equation (so don’t)

Drag on a surface – 2 types Pressure stress / form drag Shear stress / skin friction drag A boundary layer forms due to skin friction

Boundary layer – velocity profile Far from the surface, the fluid velocity is unaffected. In a thin region near the surface, the velocity is reduced Which is the “most correct” velocity profile? …this is a good approximation near the “front” of the plate

Boundary layer growth The free stream velocity is u0, but next to the plate, the flow is reduced by drag Farther along the plate, the affect of the drag is felt by more of the stream, and because of this The boundary layer grows

Boundary layer transition At a certain point, viscous forces become to small relative to inertial forces to damp fluctuations The flow transitions to turbulence Important parameters: Viscosity μ, density ρ Distance, x Velocity UO Reynolds number combines these into one number

First focus on “laminar” boundary layer A practical “outer edge” of the boundary layer is where u = uo x 99% Across the boundary layer there is a velocity gradient du/dy that we will use to determine τ

Let’s look at the growth of the boundary layer quantitatively.

The velocity profiles grow along the surface What determines the growth rate and flow profile?

Blasius δ(x) Resistance of fluid to change in velocity due to viscous forces depends on…? Velocity, UO Viscosity, μ Density, ρ Position, x The Reynolds number Blasius (1908) derived:

B L thickness & fluid properties

Blasius, cont’d: Surface shear stress a δ(x) Shear stress

Boundary layer transition At a certain point, viscous forces become to small relative to inertial forces to damp fluctuations The flow transitions to turbulence Important parameters: Viscosity μ, density ρ Distance, x Velocity UO Reynolds number combines these into one number

How does BL transition?

Next focus on “turbulent” boundary layer A practical “outer edge” of the boundary layer is (still) where u = uo x 99% Across the boundary layer there is a velocity gradient as well as variations in the velocity that determine τ

Turbulence: average & fluctuating velocity The velocity profile concerns the mean velocity. The fluctuating part contributes to the internal stress for high Re flow.

Three zones in the turbulent BL

Viscous sub-layer The velocity in the viscous sub-layer is linear

Log law of the wall

Majority of the boundary layer 105 < Re < 107

Shear stress, thickness of turbulent boundary layer (somewhat empirical)

Laminar, Turbulence, Induced Turbulence Turbulent Induced δ cf FS Cf

Example 9.8 from text Assume that a boundary layer over a smooth, flat plate is laminar at first and then becomes turbulent at a critical Reynolds number of 5 x 105. If we have a plate 3 m long x 1 m wide, and if air at 20°C and atmospheric pressure flows past this plate with a velocity of 30 m/s what will be the average resistance coefficient Cf for the plate? Also, what will be the total shearing resistance of one side of the plate and what will be the resistance due to the turbulent part and the laminar part of the boundary layer? What is the answer to the same questions if the boundary layer is “tripped” by some sufficiently large roughness element that the boundary layer is turbulent from the beginning?

Example