





There are 4 types of differences between a single-phase fluid and one with two or more coexisting phases:
(1) There are chemical changes that occur when chemical reactions change the relative numbers of molecules of each phase. These can also include special surface reactions at the phase interfaces. Then it is often necessary to treat the phases and species individually as well as consider their interactions.
(2) There are thermal differences, which occur when the different phases have different temperatures and because velocity equilibration can be much faster than temperature equilibration.
(3) There are dynamic differences, which occur when it is necessary to describe each phase by its own separate velocity field.
(4) Finally, there are spatial separations, which means that the granularity of the different phases is large enough that it must be taken into consideration.
Many important multiphase flow problems involve the flow of “obstacles,” such as drops, bubbles, or solid particles, in a background gas or liquid flow. A number of levels of complexity have been postulated to treat these types of problems:
(i) In single-fluid models, the different phases are considered a single fluid whose properties are composites of those of the various phases present. All phases of the flow are assumed to be closely coupled and thus move with the same velocity. Flows containing very small droplets or particles can often be treated this way, but such a model improperly describes rain for which the relative motion between air and water droplets is important.
(ii) In two-fluid models, it is assumed that the different phases move at very nearly the same mean velocity. However, the small velocity difference may be significant in differential compression or expansion or to describe settling of heavier particles over an extended period.
(iii) In multifluid models, each volume of fluid is characterized by a distribution of particle or droplet sizes and characteristics. Solving these equations is difficult and expensive because separate momentum equations are needed for each phase or particle size.
Liquid droplets in a background gas describe a wide range of problems from rain to atomization of liquid fuel. Types and levels of models used to study these problems include locally homogeneous flow models, which are similar to the single-fluid models, separated flow models, which are multifluid models, and drop life history models, which describe the detailed behavior of individual droplets.
In locally homogeneous flow models, the gas and liquid phases are assumed to be in dynamic and thermodynamic equilibrium, so that the phases have the same velocity and temperature. This limiting case only accurately represents a spray consisting of very small drops.
In separated flow models, the effects of finite rates of transport between the phases are considered. This is really a very broad category of models, ranging from those in which particulates are treated as Lagrangian particles in a continuum background to the case of full multiphase, multifluid continuum models such as those based on the types of equations shown above.
The third type of model, drop-life history models, focuses on individual droplets and attempts to calculate their dynamic behavior self-consistently with changes in their environments.