In order to investigate the ammonia + water + lithium bromide absorption
refrigeration cycle process and to simulate it accurately, a vapor-liquid
equilibrium calculation model was proposed to obtain thermodynamic
characteristic data of the ternary mixtures. The calculation of parameters
of liquid phase is based on Wilson?s equation and NRTL equation. The vapor
phase, assumed to consist of ammonia and water only, is described by The
Redlich-Kwong Equation of State. The data of the equilibrium vapor pressure
and the ammonia concentration in liquid phase calculated by this model was
compared with the experimental data, the difference is between 0.5% to 9.6%
within the temperature range from303 K to 425 K. The COP obtained by the
simulation matches with that obtained by experiment and the absolute
deviation is less than 0.02. Therefore, this calculation model can be used
for simulation to extend the temperature range and pressure range of the
system, so as to determine the design parameters of the absorption
refrigeration system. The simulation results indicates that under different
working conditions, the optimal generator temperature and concentration of
adding lithium bromide can be selected, to which the theoretical
explanations were given in this paper.