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Investigation of Flow Rate and Viscous Dissipation in a Single Screw Pump-Extruder

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Published/Copyright: March 1, 2022
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Abstract

The focus of this investigation was to determine the effect of barrel rotation and screw rotation on the flow rate and viscous dissipation inside the screw pump-extruder. The screw pump-extruder was built to allow for barrel rotation and screw rotation independently. A Newtonian fluid, Polypropylene glycol, was chosen as the working fluid. The experimental results can be summarized by noting that the pumping capacity of the device was independent of which element was rotated at constant angular velocity and that barrel rotation generated higher temperature rise than screw rotation for the two screws evaluated. Also this analysis suggested that a large amount of viscous dissipation inside this extruder arises from the clearance flow. A new analytical model was proposed to evaluate the viscous dissipation for screw rotation. Calculations using this new mathematical model provided good agreement with the experimental data for both barrel and screw rotation.


* Mail address: G. A. Campell, Chem. Ing. Dept., Clarkson University, Potsdam, N.Y., 13699, USA


Acknowledgments

We would like to thank Dow Chemical, Becton Dickinson, Eastman Chemical, XALOY and American Leiztritz, 3M, and American National Can for funding part of this research. This work was also supported in part by Center for Advanced Materials Processing at Clarkson University, a center of advanced technology supported by the New York State Science and Technology Foundation.

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Received: 2001-11-09
Accepted: 2001-11-14
Published Online: 2022-03-01
Published in Print: 2022-03-01

© 2001 Walter de Gruyter GmbH, Berlin/Boston, Germany

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