Flow through piping (a highly viscous additive)

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SUMMARY

The discussion centers on the impact of changing the suction and discharge line sizes in a piping system transferring a highly viscous additive using a mono screw/lobe pump. The original suction line is 4 inches, and the discharge line is 3 inches, with proposed changes to 6 inches and 5 inches, respectively. It is established that while lobe pumps are positive displacement and primarily depend on pump speed for flow rate, altering pipe sizes can influence flow under certain conditions, such as long piping lengths or very high viscosity. However, the consensus is that any changes in flow rate due to these adjustments will be negligible under normal operating conditions.

PREREQUISITES
  • Understanding of positive displacement pumps, specifically mono screw and lobe pumps.
  • Knowledge of fluid dynamics, particularly regarding flow rates and pressure drops.
  • Familiarity with piping systems and their impact on fluid transfer.
  • Awareness of viscosity effects on flow in industrial applications.
NEXT STEPS
  • Research the operational principles of mono screw and lobe pumps.
  • Learn about calculating pressure drops in piping systems for viscous fluids.
  • Investigate the effects of pipe diameter changes on flow rates in positive displacement systems.
  • Explore best practices for optimizing piping layouts for high-viscosity additives.
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Engineers, process designers, and technicians involved in fluid transfer systems, particularly those working with highly viscous materials and positive displacement pumps.

Mudabbir
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Dear Members

Good day to all.
We recently installed a piping system to transfer a highly viscous additive from an ISO tank to another holding tank by using a mono screw/lobe pump.
My question to you all is,the discharge size of the iso tank is 3 inches, will my flow be effected if i change the suction line from 4in to 6in and discharge line from 3in to 5in
 
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"Lobe pumps" are, I believe, positive displacement, right? The flowrate depends only on the pump speed, not the piping sizes.

edit: within reason. if you reduce the pipe size too much you could overpressurize the pump casing
 
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If the piping is long enough and/or the viscosity is really high then you might see a small increase in flow rate because of a decrease in frictional pressure drop from the increase in diameter and reduction in velocity. But with normal assumptions I would expect to see a negligible change in flow rate.
 
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