This paper illustrates the impact of seal configuration on the through-flow leakage in centrifugal pumps with shrouded impellers. The flow model is based on the Petrov-Galerkin finite element method, and the computational domain permits the primary/secondary flow interaction at both ends of the clearance gap. The model is applied to a hydraulic pump with two different seal configurations for the purpose of comparison. The computed results show a strong dependency of the leakage flow percentage and swirl-velocity retention on the overall shape of the shroud-to-housing passage including, in particular, the seal geometry. The results are generally consistent with documented observations and measurements in similar pump stages. From a rotordynamic standpoint, the current computational model conceptually provides the centered-rotor “zeroth-order” flow field for existing perturbation models of fluid/rotor interaction. The flow model is applied to two different secondary passage configurations of a centrifugal pump, and the results used in interpreting existing rotordynamic data concerning the same passage configurations.
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December 1993
Research Papers
Flow Field in the Secondary, Seal-Containing Passages of Centrifugal Pumps
E. A. Baskharone,
E. A. Baskharone
Department of Mechanical Engineering, Texas A&M University, College Station, Texas 77843
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S. J. Hensel
S. J. Hensel
Department of Mechanical Engineering, Texas A&M University, College Station, Texas 77843
Search for other works by this author on:
E. A. Baskharone
Department of Mechanical Engineering, Texas A&M University, College Station, Texas 77843
S. J. Hensel
Department of Mechanical Engineering, Texas A&M University, College Station, Texas 77843
J. Fluids Eng. Dec 1993, 115(4): 702-709 (8 pages)
Published Online: December 1, 1993
Article history
Received:
August 10, 1992
Revised:
December 30, 1992
Online:
May 23, 2008
Citation
Baskharone, E. A., and Hensel, S. J. (December 1, 1993). "Flow Field in the Secondary, Seal-Containing Passages of Centrifugal Pumps." ASME. J. Fluids Eng. December 1993; 115(4): 702–709. https://doi.org/10.1115/1.2910202
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