Javascript must be enabled to continue!
Effect of outlet impeller diameter on performance prediction of centrifugal pump under single-phase and cavitation flow conditions
View through CrossRef
Abstract
In this current study, the transient numerical calculations using CFD code are carried out under different outlet impeller diameters for the flow field within a centrifugal pump under single-phase and cavitation conditions. Both qualitative and quantitative analyses are carried out on all of these results in order to better understand the flow structure within a centrifugal pump. Also, the investigations using different outlet impeller diameters configurations relating to the static pressure, velocity magnitude, vapour volume fraction variations, as well as pressure fluctuations in both time and frequency domain at the impeller and volute of the pump are analysed. Velocity and static pressure variations of the pump under different outlet impeller diameters range (200, 210 and 220 mm) are investigated. Reliable model is developed and validated, at various pump operating conditions, to analyse the characteristics of pressure fluctuations in both time and frequency domain. Cavitation occurrence, under different outlet impeller diameters and flow rates, are detected and correlated, using a CFD model (volume fraction distributions). Based on the developed model’s findings, at the set operating conditions ranges, the distribution and impact (cavitation and head-wises) of both the pressure and velocity are analysed. The average pressure fluctuation in the volute for do = 210 mm is higher than for do = 200 mm by about 6.74%, also the maximum pressure fluctuation for do = 220 mm is higher than for do = 210 mm by around 7.4%. Furthermore, the maximum pressure fluctuation in the impeller for do = 210 mm is higher than for do = 200 mm by 12.48%, also for do = 220 mm is higher than for do = 210 mm by 10.8%. The developed CFD models are proved valuable tools in identifying and optimizing the pump performance and characterization. The head for when do = 220 mm is higher than for when do = 200 mm under both single-phase and cavitation conditions by around 14.13% and 14.69%. The maximum pressure fluctuation for do = 200 mm is lower than for do = 210 mm by 41.58%. Furthermore, the maximum pressure fluctuation at the impeller for do = 220 mm is higher than the two models. There is a small clearance between the impeller and the volute for this model, leading to the pressure fluctuation amplitudes being higher than the other above models.
Title: Effect of outlet impeller diameter on performance prediction of centrifugal pump under single-phase and cavitation flow conditions
Description:
Abstract
In this current study, the transient numerical calculations using CFD code are carried out under different outlet impeller diameters for the flow field within a centrifugal pump under single-phase and cavitation conditions.
Both qualitative and quantitative analyses are carried out on all of these results in order to better understand the flow structure within a centrifugal pump.
Also, the investigations using different outlet impeller diameters configurations relating to the static pressure, velocity magnitude, vapour volume fraction variations, as well as pressure fluctuations in both time and frequency domain at the impeller and volute of the pump are analysed.
Velocity and static pressure variations of the pump under different outlet impeller diameters range (200, 210 and 220 mm) are investigated.
Reliable model is developed and validated, at various pump operating conditions, to analyse the characteristics of pressure fluctuations in both time and frequency domain.
Cavitation occurrence, under different outlet impeller diameters and flow rates, are detected and correlated, using a CFD model (volume fraction distributions).
Based on the developed model’s findings, at the set operating conditions ranges, the distribution and impact (cavitation and head-wises) of both the pressure and velocity are analysed.
The average pressure fluctuation in the volute for do = 210 mm is higher than for do = 200 mm by about 6.
74%, also the maximum pressure fluctuation for do = 220 mm is higher than for do = 210 mm by around 7.
4%.
Furthermore, the maximum pressure fluctuation in the impeller for do = 210 mm is higher than for do = 200 mm by 12.
48%, also for do = 220 mm is higher than for do = 210 mm by 10.
8%.
The developed CFD models are proved valuable tools in identifying and optimizing the pump performance and characterization.
The head for when do = 220 mm is higher than for when do = 200 mm under both single-phase and cavitation conditions by around 14.
13% and 14.
69%.
The maximum pressure fluctuation for do = 200 mm is lower than for do = 210 mm by 41.
58%.
Furthermore, the maximum pressure fluctuation at the impeller for do = 220 mm is higher than the two models.
There is a small clearance between the impeller and the volute for this model, leading to the pressure fluctuation amplitudes being higher than the other above models.
Related Results
Study on cavitation flow and high-speed vortex interference mechanism of high-speed inducer centrifugal pump based on full flow channel
Study on cavitation flow and high-speed vortex interference mechanism of high-speed inducer centrifugal pump based on full flow channel
Abstract
High-speed centrifugal pumps are crucial in aerospace and petrochemical industries due to their high speed and head. To enhance cavitation performance, the inducer...
PRELIMINARY DESIGN OF RDE FEEDWATER PUMP IMPELLER
PRELIMINARY DESIGN OF RDE FEEDWATER PUMP IMPELLER
Nowadays, pumps are being widely used in the thermal power generation including nuclear power plants. Reaktor Daya Eksperimental (RDE) is a proposed nuclear reactor concept for the...
Analysis of the axial force distribution characteristics of multistage pumps and its correlation with hydraulic property
Analysis of the axial force distribution characteristics of multistage pumps and its correlation with hydraulic property
As the centrifugal pump is running, the fluid usually flows into the impeller along pump shaft, and the fluid flows out radially by the force of the impeller. The force is mutual, ...
Effect of Curvilinear Element Blade for Open-Type Centrifugal Impeller on Stator Performance
Effect of Curvilinear Element Blade for Open-Type Centrifugal Impeller on Stator Performance
Abstract
The effect of a curvilinear element blade for an open-type centrifugal impeller on stator performance was investigated by experiment using an actual single ...
Prediction of Cavitation Evolution and Cavitation Erosion on Centrifugal Pump Blades by the DCM-RNG Method
Prediction of Cavitation Evolution and Cavitation Erosion on Centrifugal Pump Blades by the DCM-RNG Method
Cavitation can reduce the efficiency and service life of the centrifugal pumps, and a long-term operation under cavitation conditions will cause cavitation damage on the surface of...
Research progress in hydrofoil cavitation prediction and suppression methods
Research progress in hydrofoil cavitation prediction and suppression methods
To reduce the adverse damage caused by cavitation phenomena to the hydraulic machinery, such as surface erosion of the equipment, increased mechanical vibration, and decreased serv...
Effect of Vaned Diffuser on a Small Centrifugal Impeller Performance
Effect of Vaned Diffuser on a Small Centrifugal Impeller Performance
A small transonic centrifugal compressor with 3D vaned diffuser has been developed for a turbine engine by Nanjing University of Aeronautics and Astronautics. The centrifugal impel...
NUMERICAL CALCULATIONS OF THE IMPELLER OF A CENTRIFUGAL PUMP USED IN THE OIL AND GAS INDUSTRY
NUMERICAL CALCULATIONS OF THE IMPELLER OF A CENTRIFUGAL PUMP USED IN THE OIL AND GAS INDUSTRY
Pumps are used to transport liquid products within technological installations inside and outside
any petrochemical industry enterprise. Pumps are also used in drilling oil and gas...

