Head loss in a circuit of pump and pipes

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Discussion Overview

The discussion revolves around the discrepancies observed between predicted and actual head loss in a circuit involving a pump and pipes, particularly as the flow rate increases. Participants explore potential factors contributing to this difference, including assumptions about pipe friction, flow resistance, and the effects of flow rate on pressure drop.

Discussion Character

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

Main Points Raised

  • Some participants suggest that overly conservative assumptions about pipe friction and fitting loss may explain the discrepancies, but this does not account for the increasing trend of differences as flow rate increases.
  • There is a proposal that pressure drop should be proportional to flow rate, with the expectation that errors would grow with increasing flow.
  • Others argue that pressure drop is proportional to the square of the flow rate, questioning whether this holds true for low flow speeds without turbulence.
  • A participant raises concerns about the average velocity used in calculating Darcy losses, suggesting that the velocity measured by a rotameter may be an overestimate due to energy losses in the circuit.
  • Questions are posed regarding the relationship between flow rate, velocity drop, and the implications for comparing Darcy losses to experimental losses.

Areas of Agreement / Disagreement

Participants express multiple competing views regarding the relationship between flow rate and pressure drop, with no consensus reached on the underlying causes of the observed discrepancies. The discussion remains unresolved, with ongoing questions about the accuracy of measurements and assumptions.

Contextual Notes

Limitations include the lack of specific experimental details, assumptions about flow conditions, and the potential for measurement errors. The discussion also highlights the complexity of fluid dynamics and the need for precise calculations in varying flow conditions.

physea
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Hello! In an experiment (I don't have the details) the predicted head loss in a circuit of pump and pipes was higher as the flow rate increased, than the actual head loss (pressure differential). Can you tell me please what could result in that? What systematically acting factor created an increase in the difference of head loss between predicted and measured?
 
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You made an overly conservative assumption about the pipe friction and fitting loss, probably...or an error somewhere.
 
russ_watters said:
You made an overly conservative assumption about the pipe friction and fitting loss, probably...or an error somewhere.

OK but this won't explain the increasing trend of the experimental/theoretical as flow rate increases? It would be a constant difference!
 
physea said:
OK but this won't explain the increasing trend of the experimental/theoretical as flow rate increases? It would be a constant difference!
I would have expected the pressure drop to be proportional to the flow rate. After all, with no flow, there would be no pressure difference. A (correctly) calculated head loss would show this too so the error would also grow as flow increases. The electrical analogue to this would be a wrongly marked resistor and a consequential change in measured V/I slope.
 
sophiecentaur said:
I would have expected the pressure drop to be proportional to the flow rate. After all, with no flow, there would be no pressure difference. A (correctly) calculated head loss would show this too so the error would also grow as flow increases. The electrical analogue to this would be a wrongly marked resistor and a consequential change in measured V/I slope.

Why it would grow as flow increases?
 
physea said:
Why it would grow as flow increases?
As far as I can see from what you wrote, you have a measured resistance to flow and you are comparing this with a calculated resistance. If that's what is happening then there will be a steady ratio between pressure drop and flow. You have to acknowledge that, with no flow, there will be no pressure drop (calculated or measured) so how can there be a constant difference?
(Unless I am reading your OP wrongly.)
 
physea said:
OK but this won't explain the increasing trend of the experimental/theoretical as flow rate increases? It would be a constant difference!
It should neither be constant nor even linear: it should be a square function.
Why it would grow as flow increases?
I don't understand why you would think this. Does your car need the same power at any speed?
 
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sophiecentaur said:
I would have expected the pressure drop to be proportional to the flow rate.
Pressure drop is proportional to the square of the flow rate.
 
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russ_watters said:
Pressure drop is proportional to the square of the flow rate.
Oh. Is that right for low flow speeds, without turbulence? Is there not a linear region?
 
  • #10
physea said:
Hello! In an experiment (I don't have the details) the predicted head loss in a circuit of pump and pipes was higher as the flow rate increased, than the actual head loss (pressure differential). Can you tell me please what could result in that? What systematically acting factor created an increase in the difference of head loss between predicted and measured?
Let's see the actual calculation and schematic of the system.
 
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  • #11
sophiecentaur said:
Oh. Is that right for low flow speeds, without turbulence? Is there not a linear region?
Laminar is linear because there is slipping along the wall, like pushing a block across the floor. Look up the Darcy-Weisbach equation.
 
  • #12
russ_watters said:
Laminar is linear because there is slipping along the wall, like pushing a block across the floor. Look up the Darcy-Weisbach equation.
OK. Not Totally Wrong but only right for low flow volume. It's a square law for the OP then, which gives even more departure from constant difference.
 
  • #13
I was thinking that there is a problem with the Uavg used to calculate Darcy losses.

A rotameter is used to measure flow rate at the beginning of the circuit. The liquid runs through the circuit that has bends, constrictions and other fittings. Would the U obtained from the rotameter be the Uavg? I expect it to be an overestimate.

1) Why would the velocity drop across the circuit? due to energy losses?
2) Why would that create an increasing trend of Darcy vs Experimental losses? Do higher rotameter values create higher Uavg?
 
  • #14
physea said:
I was thinking that there is a problem with the Uavg used to calculate Darcy losses.

A rotameter is used to measure flow rate at the beginning of the circuit. The liquid runs through the circuit that has bends, constrictions and other fittings. Would the U obtained from the rotameter be the Uavg? I expect it to be an overestimate.

1) Why would the velocity drop across the circuit? due to energy losses?
2) Why would that create an increasing trend of Darcy vs Experimental losses? Do higher rotameter values create higher Uavg?

1) Does the velocity actually drop? Have you some values or a graph?
2) Have you taken on board my Electrical Equivalent? Most people have done some EE at School and it's more of a common language than fluid dynamics.
 
  • #15
Please see my post #10. If you don't provide the information I requested, then it is my determination that you are just wasting all of our time. In that case, I will have to close this thread. You have a few hours to respond.
 
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