Vapor-liquid equilibrium pressures have been measured as a function of
overall composition for binary mixtures of NH3 and CHF2CF3 at constan
t temperatures of -19.00, 3.23, 35.00, and 49.90 degrees C. The coexis
tence curves for vapor-liquid equilibrium at each temperature were reg
ressed from these measurements using a modified form of the Peng-Robin
son equation of state to calculate molar volumes and the fugacities of
each component in the two phases. The coexistence curves at 35.00 and
49.90 degrees C exhibit both a maximum and a minimum in pressure, est
ablishing the existence of double azeotropes at these two temperatures
. The double azeotropes are unusual in that they exist at temperatures
for which the vapor pressures of the two components are notably diffe
rent. Double azeotropy is attributed to the weak association of NH3 in
the liquid phase, leading to the maximum-pressure azeotrope at high N
H3 concentrations, and to similar vapor pressures for unassociated NH3
and CHF2CF3 in nearly ideal (Raoult's law) dilute NH3 solutions, whic
h leads to the minimum-pressure azeotrope.