Mechanistic models for multiphase flow calculations can improve our ability
to predict pressure drop and holdup in pipes, especially in situations tha
t cannot easily be modelled in a I;laboratory and for which reliable empiri
cal correlations are not available. In this paper, a new mechanistic model,
applicable to all pipe geometries and fluid properties, is presented. New
empirical correlations are proposed for liquid/wall and liquid/gas interfac
ial friction in stratified flow, for the liquid fraction entrained and the
interfacial friction in annular-mist flow, and for the distribution coeffic
ient used in the determination of holdup in intermittent flow.