Stagnation Point - Bernoulli Equation

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Discussion Overview

The discussion revolves around the concept of stagnation pressure in the context of a manometer and its relationship to fluid dynamics, specifically using the Bernoulli equation. Participants are exploring the conditions under which pressure at a certain point in a fluid system can be considered stagnation pressure, particularly when that point is below the actual stagnation point.

Discussion Character

  • Homework-related
  • Technical explanation
  • Conceptual clarification
  • Debate/contested

Main Points Raised

  • One participant questions why the pressure at point 1 in the manometer is considered stagnation pressure, given that it is below the stagnation point.
  • Another participant asserts that stagnation pressure is found where the air velocity is zero, which they argue occurs at the entrance to the manometer.
  • A different participant supports the idea that the entrance to the manometer represents a stagnation point, thus providing stagnation pressure at that location.
  • One participant expresses confusion over the instructor's explanation regarding the cancellation of height differences between point 1 and the stagnation point, seeking clarification on this aspect.
  • Another participant reiterates the instructor's explanation, suggesting that the height difference cancels out when calculating the pressure at the gauge fluid level in the manometer.
  • Further elaboration is provided on how the pressure at the water surface in the manometer relates to the stagnation pressure at point 1, emphasizing the cancellation of the height term in the calculations.

Areas of Agreement / Disagreement

Participants express differing views on the definition and application of stagnation pressure, particularly regarding its location and the implications of height differences in the manometer. There is no clear consensus on the interpretation of the instructor's explanation or the correctness of the solutions provided.

Contextual Notes

Participants note that the discussion involves assumptions about fluid velocity and pressure relationships, as well as the specific conditions under which stagnation pressure is defined. There are unresolved aspects regarding the instructor's explanation and the mathematical steps involved in the calculations.

LauraMorrison
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Homework Statement


Can anyone tell me why, in the figure attached, the pressure in the manometer at 1 is a stagnation pressure?
I understand that you get stagnation pressure at a stagnation point but point one is below the stagnation point, not on the stagnation point. Therefore how can it be a stagnation pressure?


Homework Equations



Ps = P1 + 1/2ρV12


The Attempt at a Solution

 

Attachments

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The stagnation pressure is the pressure within that section of pipe where the velocity of the air has been declerated to zero, and not at the point below it where the air is still moving.
 
At the very entrance to the "manometer", the velocity of the air is zero; otherwise, there would be a flow of air through the manometer. So the very entrance to the manometer is a stagnation point. The pressure at that location is the stagnation pressure given by your equation.
 
Yes, that is what I thought. The solutions to the question do not agree with this though. I have attached the part of the solution relating to the manometer as the overall question asks to calculate the speed V2. I don't know if this changes anything?

I also emailed my lecturer about this, however his explanation is fairly unsatisfactory as I still don't understand how the height between 1 and the stagnation point cancels. He said:

"The fact that the lower branch of the tube is directed into the flow signifies that stagnation pressure acts there. The change in height between point 1 and the tube entry is canceled out in when calculating the pressure acting at the level of the gauge fluid (water) in the manometer. That is you could take BE between point 1 and tube entry, then relate pressure at tube entry to gauge fluid level, which gives the same result."
 

Attachments

LauraMorrison said:
Yes, that is what I thought. The solutions to the question do not agree with this though. I have attached the part of the solution relating to the manometer as the overall question asks to calculate the speed V2. I don't know if this changes anything?

I also emailed my lecturer about this, however his explanation is fairly unsatisfactory as I still don't understand how the height between 1 and the stagnation point cancels. He said:

"The fact that the lower branch of the tube is directed into the flow signifies that stagnation pressure acts there. The change in height between point 1 and the tube entry is canceled out in when calculating the pressure acting at the level of the gauge fluid (water) in the manometer. That is you could take BE between point 1 and tube entry, then relate pressure at tube entry to gauge fluid level, which gives the same result."

The final result in the solution relating to the manometer looks OK to me. The cancellation explanation given to you by your instructor also seems correct to me. Suppose z represents the distance between point 1 and the stagnation location of the manometer. Since the free stream velocity is constant between point 1 and the location of the manometer inlet (except, of course, immediately at the stagnation point), the pressure in the free stream at the elevation of the manometer inlet is p1airgz. So the exact stagnation pressure at the manometer inlet is

p1airgz+(1/2)ρairv12.

Now, let's go inside the manometer. Let's ask what the pressure is within the manometer at the elevation of point 1. This is at the top surface of the water. The top surface of the water is located at the elevation of the manometer inlet minus the distance z. So the pressure at the surface of the water is

p1airgz+(1/2)ρairv12airgz = p1+(1/2)ρairv12

Note that, as your instructor indicated, the term ρairgz has canceled out, and the pressure at the top of the water surface is just equal to the stagnation pressure at point 1.
 
Thank you very much, great help.
 

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