Navier-Stokes Equations homework assignment - MIT, Exercises of Aeronautical Engineering

Homework assignment on Navier-Stokes Equations

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16.100 Homework Assignment # 6
Due: Monday, October 31 9am
Reading Assignment
Anderson, 3rd edition: Chapter 15, Sections 1-4, 7
Chapter 16, pages 745-751, 781-786
Problem 1
y
0
U
Consider an initially stationary, long flat plate. At time t
=
0, the plate is set in motion at
velocity U. As time evolves, the air above the plate will begin to move as the viscous effects
diffuse the momentum away from the plate. We will define the height of the boundary layer of
non-negligible momentum,
0
)(t
δ
, as the y-location at which the velocity is only 1% of the wall
velocity. Assume the flow is incompressible.
a) Apply the conservation of mass in differential form (i.e. not integral form) to show that
the vertical velocity, v, is zero everywhere in the flow for all time.
b) Next, show that the conservation of x-momentum can be reduced to the following form:
2
2
y
u
t
u
=
ν
(1)
c) Show that the following x-velocity is a solution to Equation (1) and that it satisfies the
initial and boundary conditions:
()
()
=
η
ξξ
π
η
νη
η
0
0
2
2
4
1
deerf
ty
erf
U
u
Note that
()
η
erf is known as the error function and its values are available in Matlab and
Excel using the erf function.
d) Plot the velocity distribution as a function of
η
. Determine the boundary layer thickness
as a function of time. For air at standard day conditions, at what time does the boundary
layer thickness reach 1 inch above the plate? What time for 1 foot above the plate?
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16.100 Homework Assignment # 6

Due: Monday, October 31 9am

Reading Assignment

Anderson, 3

rd edition: Chapter 15, Sections 1-4, 7

Chapter 16, pages 745-751, 781-

Problem 1

y

U 0

Consider an initially stationary, long flat plate. At time t = 0 , the plate is set in motion at

velocity U. As time evolves, the air above the plate will begin to move as the viscous effects

diffuse the momentum away from the plate. We will define the height of the boundary layer of

non-negligible momentum,

0

δ ( t ), as the y-location at which the velocity is only 1% of the wall

velocity. Assume the flow is incompressible.

a) Apply the conservation of mass in differential form (i.e. not integral form) to show that

the vertical velocity, v , is zero everywhere in the flow for all time.

b) Next, show that the conservation of x-momentum can be reduced to the following form:

2

2

y

u

t

u

c) Show that the following x-velocity is a solution to Equation (1) and that it satisfies the

initial and boundary conditions:

( )

( ) ∫

− ≡

= −

η ξ ξ π

η

η ν

η

0

0

2 2

4

1

erf e d

y t

erf U

u

Note that erf ( )η is known as the error function and its values are available in Matlab and

Excel using the erf function.

d) Plot the velocity distribution as a function of η. Determine the boundary layer thickness

as a function of time. For air at standard day conditions, at what time does the boundary

layer thickness reach 1 inch above the plate? What time for 1 foot above the plate?

e) Determine the skin friction coefficient c (^) f as a function of time where

c

u

y

f

wall

U wall

y

=

ρ

1

2 0

2

0

c (^) f 0

2

Plot as a function of U t. As time proceeds, is the plate easier or harder to keep

moving at the same velocity? Notice that at t = 0 , the skin friction has some rather large

values. Obviously, in a real situation, the friction does not reach these values. What basic part in the specification of the problem is the cause for this? Hint: it is not the

infinite length of the plate.

Problem 2

Consider the flow between two concentric cylinders as shown below:

R 0

R 1

The inner cylinder has radius R 0 and rotates at an angular velocity of ω 0. The outer cylinder has

radius R 1 and rotates at an angular velocity of ω 1. Assume the fluid between the cylinders has a

density ρ and dynamic viscosity of μ. Also, assume that the resulting flow is steady and

parallel such that the radial velocity, ur , is equal to zero.

a) Using the continuity equation, show that the circumferential velocity, u (^) θ, is independent of

b) Using the circumferential momentum equation, and applying boundary conditions, determine

the circumferential velocity.

c) Without solving directly for the static pressure, use the radial momentum equation to show

that the static pressure must increase with increasing radius.