Some issues related to the modeling of interfacial areas in gas-liquid flows I. The conceptual issues

Two-phase flow modeling has been under constant development for the past forty years. valid for two-phase flows where the phases are strongly coupled to the two-fluid model valid for two-phase flows where the phases are a priori weakly coupled. However the latter model has been used extensively in computer codes because of its potential in handling many different physical situations. The two-fluid model is based on the balance equations for mass, momentum and energy, averaged in a certain sense and expressed for each phase and for the interface between the phases. The difficulty in using the two-fluid model stems from the closure relations needed to arrive at a complete set of partial differential equations describing the flow. These closure relations should supply the information lost during the averaging of the balance equations and should specify in particular the interactions of mass, momentum and energy between the phases. Another requirement for the interaction terms is that they should satisfy the interfacial balance equations. Some of these terms such as the added mass term or the lift force term do not depend on the interfacial area but some others do, such as the mass transfer term, the drag term or the heat flux term. It is then necessary to model the interfacial area in order to evaluate the corresponding fluxes. Another benefit resulting from the modeling of the interfacial area would be to replace the usual static flow pattern maps which specify the flow configuration by a dynamic follow-up of the flow pattern. All these reasons explain why so much effort has been put during the past twenty years on the modeling and measurement of the interfacial area in two-phase flows. This article contains two parts. The first one deals with the conceptual issues and has the following objectives: 1. to give precise definitions of the interfacial area concentrations; 2. to explain the origin of the interfacial area concentration transport equation suggested by M. Ishii in 1975; 3. to explain some paradoxical behaviors encountered when calculating the interfacial area concentration transport velocity. (C) 2001 Academie des sciences/Editions scientifiques et medicales Elsevier SAS.