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658 <strong>Solution</strong>s Manual • Fluid Mechanics, Fifth Edition<br />
(c) Assume ρ = ρ o = ρ tire , for how would we know ρ exit if we didn’t use compressibleflow<br />
theory Then the incompressible Bernoulli relation predicts<br />
po<br />
169120 kg<br />
ρ o = = = 1.945<br />
3<br />
RT 287(303) m<br />
o<br />
V<br />
einc ,<br />
2∆p<br />
2(169120 −100000)<br />
≈ = ≈<br />
ρ<br />
1.945<br />
o<br />
m<br />
267 s<br />
Ans. (c)<br />
This is 8% lower than the “exact” estimate in part (a).<br />
9.43 Air flows isentropically through a duct with T o = 300°C. At two sections with<br />
identical areas of 25 cm 2 , the pressures are p 1 = 120 kPa and p 2 = 60 kPa. Determine (a) the<br />
mass flow; (b) the throat area, and (c) Ma 2 .<br />
<strong>Solution</strong>: If the areas are the same and the pressures different, than section (1)<br />
must be subsonic and section (2) supersonic. In other words, we need to find<br />
where<br />
p 1/po<br />
120<br />
= = 2.0 for the same A 1/A* = A 2/A*—search Table B.1 (isentropic)<br />
p/p 60<br />
2 o<br />
After laborious but straightforward iteration, Ma = 0.729, Ma ≈ 1.32 Ans. (c)<br />
1 2<br />
A/A* = 1.075 for both sections, A* = 25/1.075 = 23.3 cm Ans. (b)<br />
With critical area and stagnation conditions known, we may compute the mass flow:<br />
2 3.5<br />
p = 120[1 + 0.2(0.729) ] ≈ 171 kPa and T = 300 + 273 = 573 K<br />
o<br />
1/2 1/2<br />
m<br />
= 0.6847poA*/[RT o] = 0.6847(171000)(0.00233)/[287(573)]<br />
kg<br />
m ≈ 0.671 Ans. (a) s<br />
o<br />
2<br />
9.44 In Prob. 3.34 we knew nothing about compressible flow at the time so merely assumed<br />
exit conditions p 2 and T 2 and computed V 2 as an application of the continuity equation. Suppose