Applying Bernoulli's to this geometry.

AI Thread Summary
The discussion focuses on applying Bernoulli's principle to a half-spherical vessel with an orifice. Participants analyze the velocity at the orifice, questioning the assumption that pressure at both the top and bottom is equal, which is crucial for applying Torricelli's Law. There is confusion regarding the height variable 'z' and its relation to the vessel's geometry, particularly whether it should be defined as the radius 'R' or an arbitrary height. The assumption that the velocity at the fluid surface is zero is debated, with some suggesting it should be finite. Overall, the conversation highlights the complexities in interpreting fluid dynamics in this specific geometry.
pyroknife
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I have attached the geometry of interest with some parts of the solution. The geometry is a vessel that is half of a sphere with an orifice at the bottom.

The first expression that they have written, the "A*(2*g*z)^0.5=..." is from conservation of flow rate. 2*g*z is the velocity at the inlet of the orifice.

I don't understand how they got that velocity since there should be a pressure drop from z to the orifice opening.
Basically it just seems like they did Potential energy (@ z) = Kinetic Energy at orifice opening.
So that gives g*z=0.5*v^2=>v=(2*g*z)^0.5

but isn't there a pressure gain as well of density*gravity*z?
The only way they could have gotten that velocity is if the pressure at both locations are the same.
 

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This problem is an application of Torricelli's Law, which is a particular form of the more general Bernoulli equation:

http://en.wikipedia.org/wiki/Torricelli's_law

The pressure at the open top of the sphere and at the bottom where the outlet is are approximately equal to each other and to the ambient atmospheric pressure.
 
SteamKing said:
This problem is an application of Torricelli's Law, which is a particular form of the more general Bernoulli equation:

http://en.wikipedia.org/wiki/Torricelli's_law

The pressure at the open top of the sphere and at the bottom where the outlet is are approximately equal to each other and to the ambient atmospheric pressure.

Thanks for the reply. What you stated above I agree with, but isn't that different from what the drawing shows? it looks like at height z is at a location that is not exposed to the ambient pressure and same with at z=0 (orifice opening)? That's what has me confused.

If Z is indeed at the top, wouldn't Z=R?

Thus the expression should be 2*g*R, instead of 2*g*z.

It looks like z is some arbitary height, at z=R (P=Patm), but at other points below R, it should be Patm+(density*gravity*(R-z)) from the hydrostatic pressure relation.
 
I'm wondering why the velocity on the surface v1 = 0. Seems to me that v1 is finite (= -dz/dt). Maybe it's deliberately ignored. But if not, (v1^2)/2 = (v2^2)/2 - gz > 0.
 
pyroknife said:
Thanks for the reply. What you stated above I agree with, but isn't that different from what the drawing shows? it looks like at height z is at a location that is not exposed to the ambient pressure and same with at z=0 (orifice opening)? That's what has me confused.

If Z is indeed at the top, wouldn't Z=R?

Thus the expression should be 2*g*R, instead of 2*g*z.

It looks like z is some arbitary height, at z=R (P=Patm), but at other points below R, it should be Patm+(density*gravity*(R-z)) from the hydrostatic pressure relation.

I think z is the instantaneous level of the fluid.
 
rude man said:
I'm wondering why the velocity on the surface v1 = 0. Seems to me that v1 is finite (= -dz/dt). Maybe it's deliberately ignored. But if not, (v1^2)/2 = (v2^2)/2 - gz > 0.

In all the classes I've taken, we assume the velocity at the free space is Zero.
 
rude man said:
I think z is the instantaneous level of the fluid.
Sorry, what does that mean?
 
rude man said:
I'm wondering why the velocity on the surface v1 = 0. Seems to me that v1 is finite (= -dz/dt). Maybe it's deliberately ignored. But if not, (v1^2)/2 = (v2^2)/2 - gz > 0.
Hi rude man,

The cross sectional area at the top of a huge tank like this is usually assumed to be much larger than the cross sectional area of the oriface, so the kinetic energy at the top is usually neglected in Bernoulli.

chet
 
pyroknife said:
Sorry, what does that mean?

It means the fluid surface is at z.
 
  • #10
Chestermiller said:
Hi rude man,

The cross sectional area at the top of a huge tank like this is usually assumed to be much larger than the cross sectional area of the oriface, so the kinetic energy at the top is usually neglected in Bernoulli.

chet

Hi Chet,
I defer to the majority ...

PS congrats for making Sci Advisor! Richly deserved!
 
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  • #11
rude man said:
It means the fluid surface is at z.

Hmmmm I see, that would explain velocity=0 there and P=Patm. What about at z=0. Would you make an assumption that's the bottom surface (lack of a better term)?
 
  • #12
pyroknife said:
Hmmmm I see, that would explain velocity=0 there and P=Patm. What about at z=0. Would you make an assumption that's the bottom surface (lack of a better term)?

Yes.
Look at the given equation r^2 + (R - z)^2 = R^2
so if z=0, r=0 as the figure corroborates.
It also states dz/dt < 0 which again implies z=0 at the bottom.

The figure should have indicated z as going + from the bottom to the surface instead of an ambiguous two-way arrow.
 
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