Boundary Layer Analyses

Slides:



Advertisements
Similar presentations
Aerodynamic Characteristics of Airfoils and wings
Advertisements

Boundary layer with pressure gradient in flow direction.
Lakshmi Sankar Module 3.3 Panel Methods Lakshmi Sankar
2004Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST von Kárman Equation for flat plates (dp e /dx≠0) u For laminar or turbulent flows: in the.
DESIGN OF AIRFOILS FOR WIND TURBINE BLADES Presented by Parezanovic Vladimir Faculty of Mechanical Engineering Belgrade University.
1 FLOW SEPARATION Aerodynamics Bridge-Pier Design Combustion Chambers Human Blood Flow Building Design Etc. (Form Drag, Pressure Distribution, Forces and.
External Convection: Laminar Flat Plate
MAE 5130: VISCOUS FLOWS Introduction to Boundary Layers
Pharos University ME 352 Fluid Mechanics II
External Flows.
AE 3903/4903 Airfoil Design Lecture 1. OVERVIEW Introductory Remarks Your first analysis tool – Panel Method.
Anoop Samant Yanyan Zhang Saptarshi Basu Andres Chaparro
Flow Over Immersed Bodies
Lecture 7 Exact solutions
Introduction to Convection: Flow and Thermal Considerations
Quanitification of BL Effects in Engineering Utilitites… P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Engineering Parameters.
Fluid Dynamics: Boundary Layers
AE 1350 Lecture Notes #7 We have looked at.. Continuity Momentum Equation Bernoulli’s Equation Applications of Bernoulli’s Equation –Pitot’s Tube –Venturi.
Lecture #17 Boundary Layer Measurements  Boundary layer Thickness  * Displacement Thickness  Momentum Thickness.
Introduction to Convection: Flow and Thermal Considerations
Boundary layer concept
Pharos University ME 253 Fluid Mechanics II
Boundary Layer Laminar Flow Re ‹ 2000 Turbulent Flow Re › 4000.
Introduction to Fluid Mechanics
LESSON LD04 Aerodynamics
Wind Engineering Module 3.1 Lakshmi Sankar Recap In module 1.1, we looked at the course objectives, deliverables, and the t-square web site. In module.
Mass Transfer Coefficient
2D Airfoil Aerodynamics
Chapter 6 Introduction to Forced Convection:
2004Fluid Mechanics II Prof. António Sarmento - DEM/IST u Contents: –1/7 velocity law; –Equations for the turbulent boundary layer with zero pressure gradient.
Introduction to Fluid Mechanics
 ~ 0 [u(x,y)/Ue] (1 – u(x,y)/Ue)dy
Chapter 7 External Convection
Note – throughout figures the boundary layer thickness is greatly exaggerated! CHAPTER 9: EXTERNAL INCOMPRESSIBLE VISCOUS FLOWS Can’t have fully developed.
Von Karman Integral Method (BSL) PRANDTL BOUNDARY LAYER EQUATIONS for steady flow are Continuity N-S (approx) 12  If we solve these, we can get V x, (and.
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.
CE 1501 Flow Over Immersed Bodies Reading: Munson, et al., Chapter 9.
Chapter 7 EXTERNAL FORCED CONVECTION
PHAROS UNIVERSITY ME 253 FLUID MECHANICS II
Wind Energy Program School of Aerospace Engineering Georgia Institute of Technology Computational Studies of Horizontal Axis Wind Turbines PRINCIPAL INVESTIGATOR:
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 over immersed bodies If a body is immersed in a flow, we call it an external flow. Some important external flows include airplanes, motor.
CONVECTIVE HEAT TRANSFER Mohammad Goharkhah Department of Mechanical Engineering, Sahand Unversity of Technology, Tabriz, Iran.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 6 Introduction to convection.
External flow: drag and Lift
Date of download: 9/19/2016 Copyright © ASME. All rights reserved. From: A Reduced-Order Model of the Mean Properties of a Turbulent Wall Boundary Layer.
LESSON LD04 Aerodynamics
Review of Airfoil Aerodynamics
MAE 3241: AERODYNAMICS AND FLIGHT MECHANICS
“SINIR TABAKA TEORİSİ” İstanbul Teknik Üniversitesi
Ship Hydrodynamics - Resistance
Date of download: 10/26/2017 Copyright © ASME. All rights reserved.
Control of Boundary Layer Structure for Low Re Blades
Momentum Integral Equation
Fluid Mechanics & Hydraulics
convective heat transfer
Panel Methods.
APISAT 2010 Sep. 13~15, 2010, Xi’An, China
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.
Transition of the laminar boundary layer on a flat plate into a fully turbulent boundary layer (not to scale). Trip Wires:
Heat Transfer Coefficient
LESSON LD04 Aerodynamics
Turbulent Boundary Layer
Steady-State Aerodynamics Codes for HAWTs
LESSON LD04 Aerodynamics
Section 8, Lecture 1, Supplemental Effect of Pressure Gradients on Boundary layer • Not in Anderson.
3rd Lecture : Integral Equations
Presentation transcript:

Boundary Layer Analyses Module 3.4: Wind Engineering L. Sankar School of Aerospace Engineering

Outline Thwaites Method for Computing Laminar Boundary Layers Michel’s Transition Criterion Head’s method for Turbulent Flow Squire-Young Formula for Drag Prediction See http://www.ae.gatech.edu/~lsankar/AE2020 for background material.

Thwaites’ method I This is an empirical method based on the observation that most laminar boundary layers obey the following relationship. Ref: Thawites, B., Incompressible Aerodynamics, Clarendon Press, Oxford, 1960: Thwaites recommends A = 0.45 and B = 6 as the best empirical fit.

Thwaites’ Method II The above equation may be analytically integrated yielding For blunt bodies such as airfoils, the edge velocity ue is zero at x=0, the stagnation point. For sharp nosed geometries such as a flat plate, the momentum thickness q is zero at the leading edge. Thus, the term in the square bracket always vanishes. The integral may be evaluated, at least numerically, when ue is known.

Thwaites’ method III After q is found, the following relations are used to compute the shape factor H.

Thwaites’ method IV After q is found, we can also find skin friction coefficient from the following empirical curve fits:

MATLAB Code from PABLO %--------Laminar boundary layer lsep = 0; trans=0; endofsurf=0; theta(1) = sqrt(0.075/(Re*dueds(1))); i = 1; while lsep ==0 & trans ==0 & endofsurf ==0 lambda = theta(i).^2*dueds(i)*Re; % test for laminar separation if lambda < -0.09 lsep = 1; itrans = i; break; end; H(i) = fH(lambda); L = fL(lambda); cf(i) = 2*L./(Re*theta(i)); if i>1, cf(i) = cf(i)./ue(i); end; i = i+1; % test for end of surface if i> n endofsurf = 1; itrans = n; break; end; K = 0.45/Re; xm = (s(i)+s(i-1))/2; dx = (s(i)-s(i-1)); coeff = sqrt(3/5); f1 = ppval(spues,xm-coeff*dx/2); f1 = f1^5; f2 = ppval(spues,xm); f2 = f2^5; f3 = ppval(spues,xm+coeff*dx/2); f3 = f3^5; dth2ue6 = K*dx/18*(5*f1+8*f2+5*f3); theta(i) = sqrt((theta(i-1).^2*ue(i-1).^6 + dth2ue6)./ue(i).^6); % test for transition rex = Re*s(i)*ue(i); ret = Re*theta(i)*ue(i); retmax = 1.174*(rex^0.46+22400*rex^(-0.54)); if ret>retmax trans = 1; itrans = i;

Reationship between l and H function H = fH(lambda); if lambda < 0 if lambda==-0.14 lambda=-0.139; end; H = 2.088 + 0.0731./(lambda+0.14); elseif lambda >= 0 H = 2.61 - 3.75*lambda + 5.24*lambda.^2;

Skin Friction function L = fL(lambda); if lambda < 0 end; L = 0.22 + 1.402*lambda +(0.018*lambda)./(lambda+0.107); elseif lambda >= 0 L = 0.22 + 1.57*lambda - 1.8*lambda.^2; We invoke (or call this function) at each i-location as follows: H(i) = fH(lambda); L = fL(lambda); cf(i) = 2*L./(Re*theta(i));

Transition prediction A number of methods are available for predicting transition. Examples: Eppler’s method Michel’s method Wind turbine designers and laminar airfoil designers tend to use Eppler’s method Aircraft designers tend to use Michel’s method.

Michel’s Method for Transition Prediction % test for transition rex = Re*s(i)*ue(i); ret = Re*theta(i)*ue(i); retmax = 1.174*(rex^0.46+22400*rex^(-0.54)); if ret>retmax trans = 1; itrans = i; end;

Turbulent Flow A number of CFD methods, and integral boundary layer methods exist. The most popular of these is Head’s method. This method is used in a number of computer codes, including PABLO.

Head’s Method Von Karman Momentum Integral Equation: A new shape parameter H1: Evolution of H1 along the boundary layer: These two ODEs are solved by marching from transition location to trailing edge.

Empirical Closure Relations Ludwig-Tillman relationship: Turbulent separation occurs when H1 = 3.3

Coding Closure Relations in Head’s Method function y=H1ofH(H); if H <1.1 y = 16; else if H <= 1.6 y = 3.3 + 0.8234*(H-1.1).^(-1.287); y = 3.3 + 1.5501*(H-0.6778).^(-3.064); end; function H=HofH1(H1); if H1 <= 3.32 H = 3; elseif H1 < 5.3 H = 0.6778 + 1.1536*(H1-3.3).^(-0.326); else H = 1.1 + 0.86*(H1-3.3).^(-0.777); end function cf = cfturb(rtheta,H); cf = 0.246*(10.^(-0.678*H))*rtheta.^(-0.268);

Drag Prediction Squire-Young Formula