Reconsider the unsteady boundary layer flow around a circular
cylinder in terms of the boundary layer equations. Assuming that
the potential flow outside the boundary layer is steady and
unseparated, give all boundary conditions to be satisfied. Make
sure to write them in terms of boundary layer variables only. Solve
the pressure field inside the boundary layer.
For the same flow, consider the proposed solution (from
Stokes’ second problem)
where is the potential flow slip velocity immediately above
the boundary layer. The solution above satisfies the equation
Find out what the velocity must be. Also find the velocity
component inside the boundary layer. Note:
Define a suitable boundary layer thickness for the proposed
solution of the previous question. How does it vary with and
? Explain why the proposed solution is reasonable for very small
times. Hint: Ask yourself, what happens to the magnitude of
when ? Does the same happen to the magnitudes of
, , , . and ?
Argue that for larger times, the proposed solution is no longer good.
Base yourself here on results like those found
on the program web page
and links on that page like
Shankar’s thesis and
the Van Dommelen & Shen separation process
as well as what you know about the proposed solution, such as, say,
its boundary layer thickness.
According to potential flow theory, what would be the lift per
unit span of a flat-plate airfoil of chord 2 m moving at 30 m/s at
sea level at an angle of attack of 10 degrees? What would be the
viscous drag if you compute it as if the airfoil is a flat plate
aligned with the flow with that chord and the flow is laminar? Only
include the shear stress over the last 98% of the chord, since near
the leading edge the shear stress will be much different from an
aligned flat plate. What is the lift to drag ratio? Comment on the
value. Use kg/m and
m/s.
Assume that a flow enters a two dimensional duct of constant
area. If no boundary layers developed along the wall, the
centerline velocity of the flow would stay constant. Assuming that
a Blasius boundary layer develops along each wall, what is the
correct expression for the centerline velocity?
Continuing the previous question. Approximate the Blasius
velocity profile to be parabolic up to , and constant from
there on. At what point along the duct would you estimate that
developed flow starts based on that approximation? Sketch the
velocity profile at this point, as well as at the start of the duct
and at the point of the duct where the range
corresponds to of the duct height accurately in a single
graph. Remember the previous question while doing this!