3.4 Specification of a laminar boundary layer profile as an inflow condition is often used in incompressible flow simulations. Let us consider the Blasius profile, which is a similarity solution for the steady laminar boundary layer on a flat plate. Fig. 3.25 Flat-plate laminar boundary layer 1. Assume two-dimensional, steady flow with no imposed pressure gradient as shown in Fig. 3.25. Show that the Navier-Stokes equations inside the bound- ary layer can be reduced to ди ди u +v. =V- əx Əy 8²u dy2¹ Әр U Əy = 0, and ди Əx + Əv dy

Elements Of Electromagnetics
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2)
3.4 Specification of a laminar boundary layer profile as an inflow condition is often
used in incompressible flow simulations. Let us consider the Blasius profile, which
is a similarity solution for the steady laminar boundary layer on a flat plate.
u(x, y)
Fig. 3.25 Flat-plate laminar
boundary layer
1. Assume two-dimensional, steady flow with no imposed pressure gradient as
shown in Fig. 3.25. Show that the Navier-Stokes equations inside the bound-
ary layer can be reduced to
ди ди
8²u
U +v =V
Əx Əy მy2
U
ap
მ
= 0, and
ди
Əx
Əv
dy
Transcribed Image Text:2) 3.4 Specification of a laminar boundary layer profile as an inflow condition is often used in incompressible flow simulations. Let us consider the Blasius profile, which is a similarity solution for the steady laminar boundary layer on a flat plate. u(x, y) Fig. 3.25 Flat-plate laminar boundary layer 1. Assume two-dimensional, steady flow with no imposed pressure gradient as shown in Fig. 3.25. Show that the Navier-Stokes equations inside the bound- ary layer can be reduced to ди ди 8²u U +v =V Əx Əy მy2 U ap მ = 0, and ди Əx Əv dy
მ
2. Consider the streamfunction (with u =
transform from (x, y) to (x, n), where
n =
√ux/Ux
Using the above and a streamfunction in the form = √xUf(n), show that
the governing equations can be reduced to
ff" +2f"" = 0
with boundary conditions of f(0) = f'(0) = 0 and lim, f(n) = 1. This
equation is referred to as the Blasius equation and its solution is known as the
Blasius profile.
and v=
3. Solve the Blasius equation numerically. Note that this is a boundary-value prob-
lem.
y
== Rex.
u
Plot as a function of 1,√e a as a function of n, C, as a function of Re, C as a function
U₂
U₂
of Re,
as a function of Re,, as a function of Re,, where, Re
X
du
is the skin friction coefficient, T = μ|
dy y=0
coefficient of the plate,
is the momentum thickness.
-L(₁-7)
y=01 U₂
=
and a coordinate
UL.
number, Re, =is Reynolds number based on plate length, L is the plate length, C,
=
V
Ux
is local wall shear stress, Cp
=
dy is the displacement thickness, 0 =
is local Reynolds
Tdx
PUL
-L-(1-7)
U₂
Jx=0
Tw
ŽPUZ
is the drag
dy
Transcribed Image Text:მ 2. Consider the streamfunction (with u = transform from (x, y) to (x, n), where n = √ux/Ux Using the above and a streamfunction in the form = √xUf(n), show that the governing equations can be reduced to ff" +2f"" = 0 with boundary conditions of f(0) = f'(0) = 0 and lim, f(n) = 1. This equation is referred to as the Blasius equation and its solution is known as the Blasius profile. and v= 3. Solve the Blasius equation numerically. Note that this is a boundary-value prob- lem. y == Rex. u Plot as a function of 1,√e a as a function of n, C, as a function of Re, C as a function U₂ U₂ of Re, as a function of Re,, as a function of Re,, where, Re X du is the skin friction coefficient, T = μ| dy y=0 coefficient of the plate, is the momentum thickness. -L(₁-7) y=01 U₂ = and a coordinate UL. number, Re, =is Reynolds number based on plate length, L is the plate length, C, = V Ux is local wall shear stress, Cp = dy is the displacement thickness, 0 = is local Reynolds Tdx PUL -L-(1-7) U₂ Jx=0 Tw ŽPUZ is the drag dy
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