Some questions on pressure drops and head loss in pipe flow

Click For Summary

Discussion Overview

The discussion revolves around the concept of pressure drops and head loss in pipe flow, specifically addressing the conditions under which pressure drop is considered constant, the implications of incompressible fluids, and the relationship between fluid velocity and pressure gradient. Participants explore theoretical and practical aspects of fluid mechanics related to these topics.

Discussion Character

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

Main Points Raised

  • Some participants question why pressure drop is considered constant through a pipe and seek clarification on the conditions that lead to dP/dx being constant.
  • Others inquire about how an incompressible fluid can "know" about differing conditions in various parts of the pipe, particularly when the average fluid velocity is the same throughout.
  • There are requests for explanations regarding the derivation of specific formulas related to pressure drop and fluid velocity.
  • Some participants assert that if fluid velocity is constant, then other flow characteristics, including the axial pressure gradient, must also be constant.
  • Concerns are raised about the applicability of pressure drop definitions in scenarios involving gases or varying temperatures, suggesting that these conditions complicate the relationship between pressure drop and other parameters.
  • One participant discusses practical implications of pipe sizing and pressure maintenance in relation to flow rates and pipe resistance.

Areas of Agreement / Disagreement

Participants express differing views on the constancy of pressure drop and the implications of fluid incompressibility. There is no consensus on the relationship between fluid velocity and pressure drop, and the discussion remains unresolved with multiple competing perspectives presented.

Contextual Notes

Participants reference specific equations and concepts from fluid mechanics, but there are indications of missing assumptions and unresolved mathematical steps regarding the pressure drop and its dependence on fluid properties.

Who May Find This Useful

This discussion may be of interest to students and professionals in fluid mechanics, engineering, and related fields who are exploring the principles of fluid flow, pressure dynamics, and practical applications in pipe design.

mech-eng
Messages
825
Reaction score
13
pressure drop.png


I would like to ask you that why pressure drop is constant through pipe? How can we know that dP/dx=constant?

Thank you.
 
Engineering news on Phys.org
If it's an incompressible fluid, how does the fluid know that the conditions in one part of the pipe are different from another part of the pipe? The average fluid velocity is the same everywhere.
 
Chestermiller said:
If it's an incompressible fluid, how does the fluid know that the conditions in one part of the pipe are different from another part of the pipe?

I cannot work out your answer. Both sentences. What do you want to mean by "If it's an incompressible fluid, how does the fluid know that the conditions in one part of the pipe are different from another part of the pipe? What condition? I am asking about how the formula 8.19 appeared or is derived?

Chestermiller said:
The average fluid velocity is the same everywhere.

What is the relation between the pressure drop and average fluid velocity you have mentioned?

Thank you.
 
If the fluid velocity is constant throughout the pipe, then everything else about the flow must also be constant, including the axial pressure gradient. What other possibility is there?
 
Chestermiller said:
If the fluid velocity is constant throughout the pipe, then everything else about the flow must also be constant, including the axial pressure gradient. What other possibility is there?

I do not know what other possibility is but I want to study it. Under what topics of fluid mechanics, can I find this situation. And would you like to explain with what equation or from where do we know that if fluid velocity is constant then all other things should be constant. This means that all other things only the function of velocity as well.

So, I will study more but I need guidance.

Thank you.
 
What is your existing background in fluid mechanics? Have you ever taken a course in the subject?
 
boneh3ad said:
What is your existing background in fluid mechanics? Have you ever taken a course in the subject?

Yes I have taken a course, I try to make a refresh these days. But as you see, I stick in some parts of the topics. But I try to understand those part by asking.

Thank you.
 
Last edited:
mech-eng said:
I do not know what other possibility is but I want to study it. Under what topics of fluid mechanics, can I find this situation. And would you like to explain with what equation or from where do we know that if fluid velocity is constant then all other things should be constant. This means that all other things only the function of velocity as well.

So, I will study more but I need guidance.

Thank you.
Try reading the first few chapters of Transport Phenomena by Bird, Stewart, and Lightfoot.
 
The equation posted is the definition of pressure loss over the length at a given velocity.. (Initial pressure-final pressure)/length...
 
  • #10
Rx7man said:
The equation posted is the definition of pressure loss over the length at a given velocity.. (Initial pressure-final pressure)/length...
What if the substance is a gas (axially varying velocity) or if the temperature is varying axially (axially varying viscosity). The the pressure gradient is not constant for these situations. Do you still maintain that this is the definition of the the pressure loss?
 
  • #11
I'd say so... the formula given doesn't account for any variation of other parameters...
If you wanted a formula to include different flow rates, viscosities, pressures, compressability, etc it would get complicated really quickly..

As presented, at a given pressure, flow, and viscosity, you can find the pressure drop per unit length.
 
  • #12
Rx7man said:
I'd say so... the formula given doesn't account for any variation of other parameters...
If you wanted a formula to include different flow rates, viscosities, pressures, compressability, etc it would get complicated really quickly..

As presented, at a given pressure, flow, and viscosity, you can find the pressure drop per unit length.
I agree. But it's certainly not a definition.
 
  • Like
Likes   Reactions: Rx7man
  • #13
deleted post
 
Last edited:
  • #14
why pressure drop is constant through pipe? How can we know that dP/dx=constant?
.......
if a pressure gauge located at one end of a pipe reads 100psi then that
does not say that a pressure gauge located anywhere else along the pipe
will read 100psi.

any fluid traveling through a pipe will meet pipe resistance from the walls of the pipe.

the formula is used to determine the size of pipe that you need to use in order to
lessen the amount of pressure drop between inlet and outlet of the pipe.

an example of using a larger pipe for instance
will allow for a lesser pressure drop at the outlet side
of the pipe.
you want to use a water pump to deliver 5000 gpm
across a distance of 1 mile and still have 43 psi water pressure.
so if your using a water pump that has a 5000 gpm output @ 100psi
but your 1 mile long pipe only has a 1 square inch inside cross section
then the resistance to fluid flow would be so great that the pressure drop
that occurs between the inlet and outlet sides of the pipe would call
for a design change of pipe size in order to attain the 5000 gpm flow rate
at the desired 43 psi water pressure.

as long as you have a large enough pipe diameter and the water will
not need to be elevated then you can retain most if not all of the pressure
over the 1 mile pipe run but larger pipes cost a lot more money than smaller pipes
or water pumps with a higher pressure and gpm output.

in fact if there is enough of a downgrade where the pipe is installed then you will end up
with a higher pressure than the original 100 psi due to the force of gravity pulling the entire
contents of water in the pipe downwards.

to carry that a little further even if the 1 mile long pipe is level you can retain the 100 psi
pressure and the 5000 gpm flow rate if a large enough pipe is used due to the force of
gravity acting on the water in the pipe.
 
Last edited:
  • #15
Chestermiller said:
If it's an incompressible fluid, how does the fluid know that the conditions in one part of the pipe are different from another part of the pipe? The average fluid velocity is the same everywhere.

This post is very hard to understand. What is the relation between being imcompressible fluid and fluid know the conditions in parts of the pipe? What's if average fluid velocity is the same everywhere?

Thank you.
 

Similar threads

  • · Replies 38 ·
2
Replies
38
Views
4K
  • · Replies 11 ·
Replies
11
Views
4K
  • · Replies 31 ·
2
Replies
31
Views
5K
Replies
1
Views
4K
  • · Replies 47 ·
2
Replies
47
Views
11K
Replies
0
Views
2K
  • · Replies 8 ·
Replies
8
Views
4K
Replies
8
Views
2K
  • · Replies 2 ·
Replies
2
Views
4K
  • · Replies 5 ·
Replies
5
Views
2K