Three-dimensional (3-D) unsteady incompressible and non-cavitating flow in a radial flow pump during the rapid stopping period was numerically studied by CFD. The dynamic mesh (DM) method combined with non-conformal grid boundaries was applied to simulate the transient stopping process. In order to exclude the uncertainty of the unsteady inlet and outlet boundaries, a loop pumping system was established, which was composed of pipes, a reservoir with an air part on the top, and a driving pump. Simulations were performed based on the standard k-ɛ turbulence model and volume of fluid (VOF) model. Results showed that the air part in the reservoir approximated real conditions when using the VOF model. Pressure fluctuations were reduced and a sharp increase of pressure at the inlet of the pump was observed at the beginning of the stopping period. Specific transient characteristics, such as the flow-rate, head and efficiency, were analyzed during the deceleration period and compared with corresponding quasi-steady results. The deviation of the quasi-steady hypothesis in predicting the transient stopping process of radial flow pumps is thought to be caused by differences in the predicted vortex in the impeller. The transient curve showing the relationship between the instantaneous flow coefficient and total pressure rise coefficient was analyzed and compared with the quasi-steady curve. The two curves had a crossover point when the stall just occurs in the impeller during the transient process. Simulation results were also compared and validated using published data.
Skip Nav Destination
e-mail: liujintao86@hotmail.com
e-mail: andycas@zju.edu.cn
Article navigation
November 2011
Research Papers
Numerical Simulation of the Transient Flow in a Radial Flow Pump during Stopping Period
J. Liu,
J. Liu
Institute of Chemical Process Machinery, Department of Chemical and Biological Engineering, Engineering Research Center of High Pressure Process Equipment and Safety, Ministry of Education,
e-mail: liujintao86@hotmail.com
Zhejiang University
, Hangzhou, 310027, P. R. China
Search for other works by this author on:
Z. Li,
Z. Li
Institute of Chemical Process Machinery, Department of Chemical and Biological Engineering, Engineering Research Center of High Pressure Process Equipment and Safety, Ministry of Education,
e-mail: andycas@zju.edu.cn
Zhejiang University
, Hangzhou, 310027, P. R. China
Search for other works by this author on:
L. Wang,
L. Wang
Institute of Chemical Process Machinery, Department of Chemical and Biological Engineering, Engineering Research Center of High Pressure Process Equipment and Safety, Ministry of Education,
Zhejiang University
, Hangzhou, 310027, P. R. China
Search for other works by this author on:
L. Jiao
L. Jiao
Institute of Chemical Process Machinery, Department of Chemical and Biological Engineering, Engineering Research Center of High Pressure Process Equipment and Safety, Ministry of Education,
Zhejiang University
, Hangzhou, 310027, P. R. China
Search for other works by this author on:
J. Liu
Institute of Chemical Process Machinery, Department of Chemical and Biological Engineering, Engineering Research Center of High Pressure Process Equipment and Safety, Ministry of Education,
Zhejiang University
, Hangzhou, 310027, P. R. China
e-mail: liujintao86@hotmail.com
Z. Li
Institute of Chemical Process Machinery, Department of Chemical and Biological Engineering, Engineering Research Center of High Pressure Process Equipment and Safety, Ministry of Education,
Zhejiang University
, Hangzhou, 310027, P. R. China
e-mail: andycas@zju.edu.cn
L. Wang
Institute of Chemical Process Machinery, Department of Chemical and Biological Engineering, Engineering Research Center of High Pressure Process Equipment and Safety, Ministry of Education,
Zhejiang University
, Hangzhou, 310027, P. R. China
L. Jiao
Institute of Chemical Process Machinery, Department of Chemical and Biological Engineering, Engineering Research Center of High Pressure Process Equipment and Safety, Ministry of Education,
Zhejiang University
, Hangzhou, 310027, P. R. China
J. Fluids Eng. Nov 2011, 133(11): 111101 (7 pages)
Published Online: October 24, 2011
Article history
Received:
January 24, 2011
Revised:
September 15, 2011
Online:
October 24, 2011
Published:
October 24, 2011
Citation
Liu, J., Li, Z., Wang, L., and Jiao, L. (October 24, 2011). "Numerical Simulation of the Transient Flow in a Radial Flow Pump during Stopping Period." ASME. J. Fluids Eng. November 2011; 133(11): 111101. https://doi.org/10.1115/1.4005137
Download citation file:
Get Email Alerts
Related Articles
CFD Calculation of a Mixed Flow Pump Characteristic From Shutoff to Maximum Flow
J. Fluids Eng (September,2002)
Numerical Simulation of the Transient Flow in a Centrifugal Pump During Starting Period
J. Fluids Eng (August,2010)
Unsteady Hydrodynamic Forces due to Rotor-Stator Interaction on a Diffuser Pump With Identical Number of Vanes on the Impeller and Diffuser
J. Fluids Eng (July,2005)
Numerical Study of Pressure Fluctuations Caused by Impeller-Diffuser Interaction in a Diffuser Pump Stage
J. Fluids Eng (September,2001)
Related Proceedings Papers
Related Chapters
Dynamic Behavior of Pumping Systems
Pipeline Pumping and Compression Systems: A Practical Approach
Introduction
Mixed-flow Pumps: Modeling, Simulation, and Measurements
CFD Simulations of a Mixed-flow Pump Using Various Turbulence Models
Mixed-flow Pumps: Modeling, Simulation, and Measurements