Achour, LilaSpecklin, MathieuAsuaje, MiguelKouidri, SmaineBelaidi, Idir2024-10-022024-10-022024978-303166608-72195-4356https://link.springer.com/chapter/10.1007/978-3-031-66609-4_46https://doi.org/10.1007/978-3-031-66609-4_46https://dspace.univ-boumerdes.dz/handle/123456789/14305Computational Fluid Dynamics is commonly employed to assess the effect of oil-water emulsions on pump performance, usually using two-phase models. However, these models often neglect the emulsion’s non-Newtonian behavior, despite its known experimental significance in enhancing pump performance. This study attempts to evaluate both single-phase non-Newtonian and two-phase approaches to model emulsion flow within centrifugal pumps. The non-Newtonian single-phase and several two-phase models are evaluated by comparing the predicted pump heads with experimental data of a multistage pump from the literature. The findings show that the non-Newtonian single-phase model generally provides better agreement with experimental measurements, particularly for emulsions with low dispersed phase fractions. Nevertheless, for emulsions with a high dispersed phase fraction (≈ 50%), the difference between the two approaches is insignificant. Thus, due to the lack of a universal multiphase model for emulsion simulation, the non-Newtonian single-phase model can serve as a viable alternative, overcoming the limitations of two-phase approaches in simulating complex multiphase fluid systems.enCFDEmulsionNon-NewtonianPumpTwo-phase modelsBook chapter