A CFD and experimental study on cavitation in positive displacement pump : benefits and drawbacks of the "full" cavitation model

Iannetti, Aldo and Stickland, Matthew and Dempster, William (2015) A CFD and experimental study on cavitation in positive displacement pump : benefits and drawbacks of the "full" cavitation model. Engineering Applications of Computational Fluid Mechanics, 10 (1). pp. 57-71. ISSN 1994-2060 (https://doi.org/10.1080/19942060.2015.1110535)

[thumbnail of Iannetti_etal_EACFM_2015_a_CFD_and_experimental_study_cavitation_positive_displacement_pump_benefits]
Preview
 Text. Filename: Iannetti_etal_EACFM_2015_a_CFD_and_experimental_study_cavitation_positive_displacement_pump_benefits.pdf
Accepted Author Manuscript
License: Creative Commons Attribution 4.0 logo
Download (1MB)| Preview
[thumbnail of Iannetti-etal-EngAppsComputFluidMechs-2015-A-CFD-and-experimental-study-cavitation-positive-displacement-pump-benefits-and-drawbacks-full-cavitation-model]
Preview
 Text. Filename: Iannetti_etal_EngAppsComputFluidMechs_2015_A_CFD_and_experimental_study_cavitation_positive_displacement_pump_benefits_and_drawbacks_full_cavitation_model.pdf
Final Published Version
License: Creative Commons Attribution-NoDerivatives 4.0 logo
Download (2MB)| Preview

Abstract

To fill the lack of literature in the numerical study of Positive Displacement (PD) pumps in cavitating condition, a comprehensive and transient Computational Fluid Dynamics (CFD) model of a PD pump, simulating the cavitation arising during the suction stroke, was created. The “full” cavitation model was utilised to study its capability on PD pumps cavitation. A set of three plunger speeds were simulated. Using the highest plunger speed an assessment was made of the effect of 1.5, 3, 4.5 and 15 ppm of air mass fraction on pump performance and cavitation. An experimental test rig, replicating the CFD model, was designed and built in order to validate the numerical model and find its weaknesses. CFD modelled, in a consistent way, the fluid dynamics phenomena related to cavitation (chamber pressure approaching the vapour pressure, the vaporization/condensation and the pressure spike occurrence at the end of the suction stroke marking the end of cavitation). On the other hand the CFD pressure trends calculated appeared stretched along the time axis with respect to the experimental data and this highlighted issues in the multiphase and cavitation models: the vaporization/condensation rate calculated by CFD did not follow the real dynamics correctly because the non-condensable gas expansion was overestimated. This was seen when comparing the CFD/experiments where the simulated pressure drop gradient, at the beginning of the suction stroke and the pressure peaks as the valve closed, exhibited a delay in their occurrence. The simulation results were sensitive to the dissolved air mass fraction as the delay depended on the amount of air dissolved in the water. Although the influence of the air mass fraction was considered consistent, the 3 ppm CFD case was the closest to the experiment results whereas the analyst expected the 15 ppm case to be more accurate.

ORCID iDs

Iannetti, Aldo, Stickland, Matthew ORCID logoORCID: https://orcid.org/0000-0001-9817-695X and Dempster, William ORCID logoORCID: https://orcid.org/0000-0001-8918-3832;
CORE (COnnecting REpositories)