Cyrus
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SW VandeCarr said:Thanks for the link. My intent was to ignore mass flows completely since I had no way to model them. Why was I able to get the "right" answer? Two posters got 120 Pa, but these had to involve mass flows. Are they correct? Those that got 60 Pa assumed stagnation along the entire wall front which is how I set up the problem.
My main concern is that you have a slug of mass with an initial momentum, mv, and then you said it comes to a dead stop. Well, where did the rest of the momentum go?
If you use one of the drag coefficients in the link I gave you, then the pressure is simply:
P=\frac{F}{A}=\frac{1}{2}\rho V^2 C_D
How simpler does it get? Based on the bluff body values in that link, you're looking at a C_D \~= 1.1-1.3. Keep in mind, this is an averaged pressure over the entire face, with edges that can have turbulence. (Which is probably more realistic than your "infinite" wall anyways)Note: The only difference between the formula above and what you will get with Bernoulli is a factor of C_D. So, because C_D=1.1-1.3 the value you got earlier is off by 10-30%. (The first value was an under prediction).
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