The formulation of a model for the evolution of the flow of a solid-liquid
mixture (coal-water) in a horizontal pipeline with partial phase separation
is the aim of this work. Problems of instabilities due to complex eigenval
ues, observed in previous models, seem to be completely solved in the prese
nt model, in which we give the genesis of the different terms written in th
e equations, coming from the natural definition of mass and momentum balanc
e, and the consequent proof of well-posedness of the obtained PDE system wi
th boundary-Cauchy data.
The model describes a three-layer flow. Most of the material is carried by
the upper layer, while the bottom layer consists of an immobile sediment. T
he intermediate layer grows to a maximum thickness and has the role of regu
lating the mass exchange between the extreme layers.
In the last section, we present some simulations for a particular choice of
flow regime, and boundary-Cauchy data, that were suggested by experimental
results provided by Snamprogetti (Fano, Italy). (C) 2001 Elsevier Science
Ltd. All rights reserved.