Is Pump Flow Rate in a Closed Loop Constant?

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SUMMARY

The flow rate in a closed loop with a pump is not constant due to several factors, including frictional losses and elevation changes. Frictional losses increase with the length and restrictions of the piping system, leading to pressure loss at any given flow rate. Additionally, if the pressure drops below the saturation pressure of the fluid, phase changes can occur, causing the liquid to flash or boil. There are two main types of pumps: positive displacement pumps, which deliver a constant flow regardless of pressure, and rotodynamic (centrifugal) pumps, which adjust flow based on pressure differences.

PREREQUISITES
  • Understanding of fluid dynamics principles
  • Knowledge of pump types: positive displacement and rotodynamic (centrifugal) pumps
  • Familiarity with pressure head and frictional losses in piping systems
  • Basic concepts of phase changes in fluids
NEXT STEPS
  • Research the impact of frictional losses in piping systems
  • Learn about the design considerations for preventing phase changes in fluid systems
  • Study the differences between positive displacement and centrifugal pumps
  • Explore methods for calculating pressure loss in closed loop systems
USEFUL FOR

Engineers, fluid dynamics specialists, and anyone involved in the design and optimization of closed loop pumping systems will benefit from this discussion.

KingNothing
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Is the overall flow rate through a closed loop with a pump constant? I've always though that if a pump can do a specific amount of work, it doesn't matter if the 'loop' of tubing goes up and down, or what types of turns it takes. I've thought this because if the tubing goes down then up (or vice versa) the force needed to push it upwards would be the same amount of force exerted when it goes downwards.

Can anyone confirm this? If I'm wrong, why?
 
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Not exactly. If a closed loop goes up and down the pressure head cancels as you point out, but that is just one consideration. Here are two others:

- There are 'frictional' losses in a piping system. These frictional losses don't cancel out like pressure head. The longer the pipe, and the more restrictions in it, the more pressure loss there will be for any given flow rate.
- There is also a problem with elevation changes in a pipe system. If the pressure in the piping system drops below the 'saturation pressure' of the fluid, the liquid will begin to flash or boil.

So given any piping circuit, there will be a pressure loss which increases with flow rate, and when designed the piping system must also not change phase without care being taken to accommodate that phase change.

One other point to note is that there are fundamentally different types of pumps which can be broken down into two catagories, positive displacement and what is sometimes called a rotodynamic pump (ie: a centrifugal or similar). A positive displacement pump puts out a given quantity of liquid regardless of pressure, as long as it has the power of course. A rotodynamic pump or centrifugal pump puts out a flow rate which is dependent on the difference in pressure between the inlet and outlet. So for any given closed loop system, you can change a restriction in the system to give you more or less pressure restriction, and the constant displacement pump won't change flow, but the centrifugal pump will.
 

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