Head Loss and Pressure Rise During Gradual Expansion

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Discussion Overview

The discussion revolves around the concepts of head loss and pressure rise during the gradual expansion of fluid flow in pipes, specifically focusing on the implications of velocity changes and empirical factors in fluid mechanics. Participants are exploring theoretical aspects and practical applications related to these phenomena.

Discussion Character

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

Main Points Raised

  • One participant seeks clarification on the meaning of the equation a1=a2=1.06, questioning its relevance to the problem.
  • Another participant asks about the definition of the kinetic energy correction factor, α, as mentioned in the textbook.
  • There is confusion regarding the use of the velocity of the narrow section (7 m/s) for calculating irreversible head loss, while the velocity in the expansion section is noted to be 3.11 m/s.
  • Some participants express uncertainty about why the velocity of the narrow section is preferred over that of the wide section when head losses occur during the transition.
  • A participant mentions an empirical factor (0.07) related to diverging sections and discusses its applicability to laminar viscous flow, suggesting that it captures the pressure drop effect based on the narrow cross-section velocity.
  • Clarification is sought on what constitutes a diverging section in this context, with a later response defining it as the section of pipe transitioning from a smaller to a larger diameter.
  • Participants inquire about the meaning of "straightens out" in relation to the flow streamlines after passing through the diverging fitting.
  • It is explained that the term refers to the establishment of a new velocity profile in the wider section of the pipe after the diverging fitting.

Areas of Agreement / Disagreement

Participants express varying levels of understanding and confusion regarding the application of velocities in head loss calculations, the definition of diverging sections, and the interpretation of empirical factors. No consensus is reached on the correct approach to these issues.

Contextual Notes

Participants highlight the dependence on definitions and the potential limitations of empirical factors in different flow regimes. The discussion remains open-ended with unresolved questions regarding the application of theoretical concepts to practical scenarios.

mech-eng
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Homework Statement


head loss and gradual expansion.png
,
irreversible head loss.png


There is an Head Loss question, two pipes join and expanding parts 30 degrees from the horizantal.

Homework Equations




The Attempt at a Solution



Before attemting a solution I try to understand what a1=a2=1.06 is?

Would you like to give some information about it?

Thank you.

Source: Fluid Mechanics, Fundamentals and Applications by Çengel/Cimbala
 
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What does your book say about the definition of ##\alpha##?
 
I understand it was in a earlier chapter and it is kinetic energy correction factor but why is the velocity of narrow part, namely 7 m/s, is used while calculating irreversible head loss in the expansion section because the velocity is 3.11 m/s in that section?

Thank you.
 
Is there anyone who can explain why the V1, the velocity of narrow section is used instead of the velocity V2, the velocity of wide section. And we should note that the head losses happen in the wide section or when passing to it.

Thank you.
 
mech-eng said:
I understand it was in a earlier chapter and it is kinetic energy correction factor but why is the velocity of narrow part, namely 7 m/s, is used while calculating irreversible head loss in the expansion section because the velocity is 3.11 m/s in that section?

Thank you.
The 0.07 is an empirical factor, presumably developed for a diverging section of very long extent. I know that, for a laminar viscous flow, in such a situation, only the flow near the narrow cross section determines the pressure drop for the diverging section. This is not a laminar viscous flow but apparently the same kind of situation prevails. So the use of the loss coefficient K would seem to capture this effect, and only includes the velocity at the narrow cross section. It neglects the fact that the diverging section straightens out after the larger cross section.

Chet
 
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Chestermiller said:
The 0.07 is an empirical factor, presumably developed for a diverging section of very long extent. I know that, for a laminar viscous flow, in such a situation, only the flow near the narrow cross section determines the pressure drop for the diverging section. This is not a laminar viscous flow but apparently the same kind of situation prevails. So the use of the loss coefficient K would seem to capture this effect, and only includes the velocity at the narrow cross section. It neglects the fact that the diverging section straightens out after the larger cross section.

Chet

But what does a divergin section refer to for this context? Is it narrow section?

Thank you.
 
mech-eng said:
But what does a divergin section refer to for this context? Is it narrow section?

Thank you.
The diverging section is the part of the pipe between the small cross section and the large cross section, going from small to large.
 
Chestermiller said:
It neglects the fact that the diverging section straightens out after the larger cross section.
Chet

What does "diverging section straightens out after ..." refer to? I cannot fix the meaning of "straightens out". Would you please explain it another way?

Thank you.
 
mech-eng said:
What does "diverging section straightens out after ..." refer to? I cannot fix the meaning of "straightens out". Would you please explain it another way?

Thank you.
You've got two straight pipes, with diameters D1 < D2, connected by a diverging conical fitting. The flow in pipe with diameter D1 is turbulent with straight streamlines, as is the flow in the pipe with diameter D2 after the fitting, like so:

images?q=tbn:ANd9GcTYTVfH71YSyY6y_n9Qzgr7tB9BG-fVoarQdYR-7sG_wXTndMH0.png

The phrase 'straightens out' refers to what happens to the streamlines in the fluid after they pass downstream of the diverging fitting and a new velocity profile is established in the pipe with diameter D2.

By convention, the minor loss KL in the diverging fitting is based on the flow velocity V1 in the pipe with diameter D1 as it enters the fitting, rather than the velocity V2 as it exits.
 

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