For control purposes, a mathematical model of a tube-fin evaporator of a va
pour compression plant running with R22 is analyzed. The refrigerant behavi
or in an evaporating region is described by a homogeneous model. The balanc
e equations, together with the constitutive equations, determine a differen
tial system which makes explicit the mechanism of dynamic behavior. At firs
t, the numerical solution of the steady state is obtained, both in evaporat
ing and superheated regions. Moreover, the numerical analysis allows us to
evaluate the transition phase and to locate the interface. Subsequently, va
rious analytical aspects are discussed. For the nonlinear two-phase flow, t
he dependence of the solution on the boundary data is estimated by means of
a qualitative analysis. Then, a linearized model for the single-phase how
is deduced and solved explicitly. The analytical solution is compared with
the numerical results and the degree of superheating is estimated in terms
of the model parameters. (C) 1999 Elsevier Science Ltd. All rights reserved
.