Applying Bernoulli's to this geometry.

Click For Summary

Discussion Overview

The discussion revolves around the application of Bernoulli's principle and Torricelli's Law to a specific geometry involving a half-spherical vessel with an orifice at the bottom. Participants explore the implications of pressure and velocity at different heights within the vessel, considering both theoretical and practical aspects of fluid dynamics.

Discussion Character

  • Exploratory
  • Technical explanation
  • Debate/contested
  • Mathematical reasoning

Main Points Raised

  • One participant questions the derivation of velocity at the orifice, suggesting that a pressure drop should be considered, which may not align with the assumption of equal pressures at the top and bottom of the vessel.
  • Another participant asserts that the pressures at the top and bottom are approximately equal to atmospheric pressure, referencing Torricelli's Law.
  • Concerns are raised about the representation of height z in the geometry, with suggestions that z may not be exposed to ambient pressure and that it should be defined relative to the radius R of the sphere.
  • Some participants discuss the assumption that the velocity at the fluid surface is zero, while others propose that it could be finite and question the implications of this assumption on the energy equations.
  • There is a clarification that z represents the instantaneous level of the fluid, which is relevant for understanding the dynamics at different heights.
  • One participant mentions that the cross-sectional area at the top of the tank is typically much larger than that of the orifice, leading to the neglect of kinetic energy at the top in Bernoulli's equation.
  • Another participant emphasizes the need for clarity in the representation of z in the diagram, suggesting it should indicate a positive direction from the bottom to the surface.

Areas of Agreement / Disagreement

Participants express differing views on the assumptions regarding pressure and velocity at various points in the vessel. There is no consensus on the interpretation of height z or the implications of neglecting certain kinetic energies, indicating ongoing debate and exploration of the topic.

Contextual Notes

Participants highlight potential ambiguities in the diagram and assumptions about pressure and velocity, which may affect the application of Bernoulli's principle. The discussion remains open-ended with unresolved questions regarding the assumptions made in the analysis.

pyroknife
Messages
611
Reaction score
4
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.
 

Attachments

  • Untitled.jpg
    Untitled.jpg
    19.6 KB · Views: 418
Physics news on Phys.org
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!
 
Last edited:
  • #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.
 

Similar threads

Replies
1
Views
2K
Replies
31
Views
4K
  • · Replies 1 ·
Replies
1
Views
4K
  • · Replies 45 ·
2
Replies
45
Views
7K
  • · Replies 7 ·
Replies
7
Views
2K
  • · Replies 1 ·
Replies
1
Views
3K
Replies
2
Views
1K
Replies
15
Views
3K
  • · Replies 1 ·
Replies
1
Views
3K
  • · Replies 5 ·
Replies
5
Views
4K