Screw Pump Sizing: Calculations for Inverted Pumps

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SUMMARY

This discussion focuses on the calculations necessary for sizing an inverted screw pump, which utilizes fins attached to the inside of a rotating pipe instead of a traditional screw. The user is moving between 150 to 400 lbs of dry powder per minute and seeks formulas to determine the diameter, fin height, spiral pattern, and speed of the pump. Participants recommend using equations from standard screw pumps, emphasizing that the principles remain consistent regardless of the configuration. Additionally, they suggest exploring Polymer Processing literature and the rheological behavior of granular materials for further insights.

PREREQUISITES
  • Understanding of screw pump design principles
  • Familiarity with rheological behavior of granular materials
  • Knowledge of Polymer Processing literature
  • Basic engineering mathematics for pump sizing calculations
NEXT STEPS
  • Research equations for standard screw pumps
  • Explore Polymer Processing literature, focusing on authors like Bernhardt and Tadmor
  • Investigate the deformational behavior of granular materials
  • Learn about kinetic friction effects in screw pump design
USEFUL FOR

Engineers, process designers, and researchers involved in the design and optimization of screw pumps, particularly those working with granular materials and polymer processing applications.

hmvyoral
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Does anyone know where i can get the calculations for sizing an inverted screw pump. Inverted being that there is no screw but the fins art attached to the inside of a pipe and the pipe is rotating. I am moving any where from 150 to 400 lbs of dry powder per minute, depending on the amount of powder being produced. I don't have the exact length yet, hence why i just need the formulas. The idea is to find the diameter, fin height, spiral patern, and speed. If anyone knows where i can get the calculations i would apreciate the help.
 
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hmvyoral said:
Does anyone know where i can get the calculations for sizing an inverted screw pump. Inverted being that there is no screw but the fins art attached to the inside of a pipe and the pipe is rotating. I am moving any where from 150 to 400 lbs of dry powder per minute, depending on the amount of powder being produced. I don't have the exact length yet, hence why i just need the formulas. The idea is to find the diameter, fin height, spiral patern, and speed. If anyone knows where i can get the calculations i would apreciate the help.

Use the equations for a regular screw pump. It doesn't matter whether the screw is rotating and the casing is stationary or the casing is rotating and the screw is stationary.
 
Chestermiller said:
Use the equations for a regular screw pump. It doesn't matter whether the screw is rotating and the casing is stationary or the casing is rotating and the screw is stationary.

I would like to use the equations for a screw pump, but i am unable to find any online. I had figured that everything would be the same because all i did was eliminiate the screw shaft and put the fins on the wall of the casing. If you know where i can get some calculations i would apreiciated it.
 
Try looking in the Polymer Processing literature in the area of extrusion. They use screw pumps (extruders) to compact and melt granular and powdery solids as part of producing a polymer melt. Look under the names of Bernhardt, Tadmor, Tadmor and Klein, and Osswald. In order to design a screw pump for a granular material, you need to have some idea of the rheological behavior of the granular material on a scale somewhat larger than the particle size. I'm not sure how much work has been done in this area, since I haven't followed it. But consider looking under the subject of Deformational Behavior of Granular Materials. In a screw pump, kinetic friction on the granular bed is also important. I hope this is helpful.
 
Thank you, I will start looking into that. I will let you know if i find anything.
 

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