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MECH 3300 Assignment # 1

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<strong>MECH</strong> <strong>3300</strong><br />

<strong>Assignment</strong> # 1<br />

Due: January 24 th , 2011, 9:30<br />

1. Show that the following expression ( ∙ ∇) produces the following differential form<br />

for the convective acceleration:<br />

<br />

+ <br />

+ <br />

<br />

2. When a valve is opened, fluid flows in the expansion duct (see figure) according to<br />

the approximation:<br />

= 1 − <br />

tanh<br />

2 <br />

Find:<br />

a) Find an expression for the acceleration<br />

of the flow;<br />

b) the fluid acceleration at (x, t) = (L, L/U);<br />

c) the time for which the fluid acceleration<br />

at x = L is zero;<br />

d) Why does the fluid acceleration<br />

becomes negative after the time found in c).<br />

3. A piston compresses gas in a cylinder by moving at constant speed V. Let the gas<br />

density and length at t = 0 be ρ 0 and L 0 , respectively. Let the gas velocity vary<br />

linearly from u = V at the piston face to u = 0 at x = L. If the gas density varies only<br />

with time, find an expression for ρ(t).<br />

4. For a laminar flow between parallel plates, the flow is 2D (v ≠ 0) if the walls are<br />

porous. A special case solution is:<br />

= ( − )(h − ) where A and B are constant.<br />

Find a) a general formula for velocity v if v = 0 at y = 0. b) What is the value of the<br />

constant B if v = v w at y = +h<br />

1


5. A frictionless, incompressible steady flow field is given by<br />

= 2 − <br />

in arbitrary units. Let the density be ρ 0 = constant and neglect gravity. Find an<br />

expression for the pressure gradient in the x direction.<br />

6. Consider a steady, 2D, incompressible flow of a newtonian fluid in which the velocity<br />

field is known: u = -2xy, v = y 2 -x 2 , w = 0.<br />

a) Does this flow satisfy conservation of mass;<br />

b) Find the pressure field, p(x,y) if the pressure at the point (x = 0, y = 0) is<br />

equal to p a .<br />

7. From the Navier-Stokes equations for incompressible flow in polar coordinates, find<br />

the most general case of purely circulating motion v θ (r), v r = v z = 0, for flow with no<br />

slip between two fixed concentric cylinders as in the figure.<br />

2

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