
This paper investigates the multi‐phase behaviour of droplets injected into a nozzle at two separate wall locations. The physical features of the droplets (rate of mass, density and radius) at each injector location are identical. This system can be described by a two‐phase Eulerian—Eulerian approach that yields classical systems of equations: three for the gaseous phase and three for the dispersed droplet phase. An underlying assumption in the two phase model is that no interaction occurs between droplets. The numerical solution of the model (using the MacCormack scheme) indicates however that the opposite jets do interact to form one jet. This inconsistency is overcome in the current paper by associating the droplets from a given injection location with a separate phase and subsequently solving equations describing a multiphase system (here, three‐phase system). Comparison of numerical predications between the two‐phase and the multiphase model shows significantly different results. In particular the multiphase model shows no jet interaction.
nozzle, droplets, Heat and mass transfer, heat flow, MacCormack scheme, Multiphase and multicomponent flows, jet interaction, Finite difference methods applied to problems in fluid mechanics, two-phase Eulerian-Eulerian approach
nozzle, droplets, Heat and mass transfer, heat flow, MacCormack scheme, Multiphase and multicomponent flows, jet interaction, Finite difference methods applied to problems in fluid mechanics, two-phase Eulerian-Eulerian approach
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