Solving a Water Pressure Problem: Gauge Pressure at B

AI Thread Summary
The discussion revolves around calculating gauge pressure at point B in a water system using Bernoulli's equation. The user initially questions why there isn't a coefficient of two in the equation due to the pipe splitting. Responses clarify that the Bernoulli equation applies to a single parcel of water and that side branches do not affect the energy conservation principle. The user also realizes an error in the area calculation of the pipes, confirming that the shape of the ducts does not impact the outcome as long as the cross-sectional areas are correctly accounted for. The conversation concludes with a clarification on the distinction between pressure and height in the context of Bernoulli's equation.
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Hi,

I am working on this water pressure problem,

jfk.Figure.P13.34.jpg


given:

v_A = 2.0 \frac{m}{s}
gauge pressure_A = 50 kPa
the view is from above, no height changes

find: gauge pressure @ B

so,

A_Av_A=2(A_Bv_B)
1.5*10^{-2}m^2(2.0\frac{m}{s})=2(5*10^{-3}m^2v_B)
v_B=9.0\frac{m}{s}

Bernoulli's equation (w/o the \rho gh components bc height is constant):

p_A+\frac{1}{2}\rho _Av_A^2=p_B+\frac{1}{2}\rho _Bv_B^2

My question is, how come the right side of the equation is not 2(p_B+\frac{1}{2}\rho _Bv_B^2)? Shouldn't there be a coefficient of two, because the pipe splits in half?

Thanks
 
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1st: I think you made a mistake in the calculation of vB

2nd: No there is no factor of 2. why should there be one? Bernoulli equation is just the energy conservation for some parcel of water as if follows its path along the tubes. Side branches have no effect.
 
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dauto said:
Side branches have no effect.

Thanks

And what mistake do you think I made for v_B? It worked out giving me the right answer :o.
 
I got 3/s from the middle equation. May be the middle equation is wrong and the final result is correct. Hard to tell since you never specified the shape of the ducts (circular cross section I assume, but is it?).
 
dauto said:
I got 3/s from the middle equation. May be the middle equation is wrong and the final result is correct. Hard to tell since you never specified the shape of the ducts (circular cross section I assume, but is it?).

Oh you're right, sorry. Yeah they are circular pipes but I just wrote down the area incorrectly. I wrote down the pipes' radii for their area when I shouldn't wrote their radii^2*pi. Thanks for the help!
 
As long as the pipe cross sections are similar figures, the shape doesn't matter (assuming no turbulence) as it's only the ratio of the areas that counts.
The factor of two, because of two pipes, has been 'used' in the calculation of the output velocity.
Pressure and velocity are intensive variables so the number of pipes doesn't matter, once you've calculated the velocity.
 
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in bernoulli's equation P+ρ g h =constant , are P and ρ g h different ? aren't they the same? thanks.
 
In general, they are different.
In particular, h depends on the arbitrary definition of zero height. You can choose whatever you like, as only height differences have a physical relevance.
 
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