A thermodynamic database has been developed for the
LiCl-NaCl-KCl-MgCl2-CaCl2- MnCl2-FeCl2-FeCl3-CoCl2-NiCl2-AlCl3
system. All binary subsystems as well as all higher order (mostly ternary)
subsystems for which experimental data were available have been considered. In
particular, a complete critical evaluation of all available phase diagram and
thermodynamic data has been performed for the condensed phases (liquid, LiAlCl4(s),
NaAlCl4(s), KAlCl4(s), LiCl-NaCl-KCl solid solution) and
gaseous species (LiAlCl4(g), Li2Al2Cl8(g),
NaAlCl4(g), Na2Al2Cl8(g), KAlCl4(g),
K2Al2Cl8(g)) of the LiCl-NaCl-KCl-AlCl3
system, and optimized model parameters have been found. For the first time, the
entire composition range (0 £
£ 1) was considered. The binary systems ACl-AlCl3
(where A = Li, Na and K) show strong negative deviations from ideality at the
equimolar composition (due to short-range ordering in the liquid phase) and the
binary mixtures exhibit a region of liquid-liquid immiscibility at high AlCl3
content. The existence in such melts of the AlCl4- and Al2Cl7-
species was observed in particular by Raman spectroscopy. The liquid was
modeled using the Modified Quasichemical Model which takes into account
cation-cation short-range order. In order to introduce two
different compositions of maximum short-range-ordering near the AAlCl4
and AAl2Cl7 compositions (where A is an alkali), pure
liquid aluminum chloride was modeled as a mixture of AlCl3 and Al2Cl6
(with two paired aluminum cations). Particular
attention was paid to the LiCl-NaCl-AlCl3, LiCl-KCl-AlCl3
and NaCl-KCl-AlCl3 systems. The model predicts the existence of a
reciprocal liquid-liquid miscibility gap in the basic region of the
LiCl-NaCl-AlCl3 and LiCl-KCl-AlCl3 systems.