Aqueous calcium chloride solution
(CaCl2–H2O) and magnesium chloride solution
(MgCl2–H2O) are regarded as potential
working fluids of absorption
heat transformers (AHTs) because of their characteristics of low corrosiveness.
The vapor pressure of a working fluid is an important property for
applications in absorption systems. However, current experimental
data are mostly limited to temperature and concentration ranges, which
are suitable for dehumidification systems, whose temperature requirement
is always lower than 323.15 K. Thus, more accurate data of vapor pressures
are anticipated. In this paper, the equilibrium vapor pressures of
aqueous CaCl2 and MgCl2 solution were measured
with the static method in the temperature range from 323.15 to 373.15
K. The mass fraction of CaCl2 varied from 0.1 to 0.5, and
the mass fraction of MgCl2 varied from 0.05 to 0.3. The
measured data were correlated with a common-used e–NRTL model,
whose average absolute relative deviations (AARD) for CaCl2–H2O and MgCl2–H2O
were 2.27 and 1.61%, respectively. The data were then correlated with
a modified Antoine equation, and the AARD were reduced to 0.51 and
0.50%, respectively. The thermodynamic performance of CaCl2–H2O and MgCl2–H2O
for the AHT were also estimated for a typical cycle. The results demonstrate
that compared with the common-used LiBr–H2O, both
CaCl2–H2O and MgCl2–H2O deliver lower circulation ratios with a coefficient of performance
difference less than 2%, so their application prospects are illustrated.