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Boundary Layer I HW #2 Instructor: M
Boundary Layer I
HW #2 Instructor: M. Behbahani-Nejad.
1. A certain flow given by u = y5, v = -x2, w = 0 has a temperature field given by T = y + t2x. Calculate the local time-rate of change of T at (1, 2), and also the material derivative of T at (1, 2) at any time t. From this last result, what conclusions can you draw?
2. The trajectories of the fluid particles in a particular flow are specified by
x = x0et, y = x0 + (y0 – x0)e-2t
(a) Sketch a few trajectories in the x - y plane for different values of x0 and y0
(b) Obtain the Lagrangian velocities by differentiating the x and y function above w.r.t time.
(c) By elimination (x0, y0) between the trajectory equations above and the velocity components, obtain expressions for u and v in terms of (x, y, t); this constitude the Eulerian velocity components for this flow.
3. A compressible fluid is caused to flow through a tube of constant diameter in such a way that the velocity along the axis is given by
u = u1 + u2/2 + u2 – u1/2 tanh x
Where u1 and u2 are the velocities when x is minus or plus infinity, respectively. The density does not change with time at any point. The density at x = - ¥ is r = r1. Obtain an equation for the distribution of density along the tube.
4. Computation algorithms for Navier-Stokes equations are often expressed in column-vector notation. For Cartesian coordinates, the divergence form of the Navier-Stokes equations can be written as:
¶U/¶t + ¶E/¶x + ¶F/¶y + ¶G/¶z = 0
Where U, E, F and G are 5-element column vectors. Show that
U =
|
r |
|
ru |
|
rv |
|
rw |
|
Et |
E =
|
ru |
|
P + ru2 - txx |
|
ruv - txy |
|
ruw - txz |
|
(Et + P)u - utxx - vtxy - wtwz + qx |
and give the corresponding forms for F and G.
Expert Solution
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