In
this work, the solubility of nisoldipine in ethyl acetate, toluene, 1-butanol, 1-propanol,
ethanol, acetonitrile, water, 2-propanol, cyclohexane, and two binary
solvents mixtures (2-propanol/ethanol + water) at the temperature
ranging from 278.15 to 318.15 K, solvent effect in a monosolvent system,
and model correlation are studied. The solubility of nisoldipine is
positively correlated with temperature. At a certain temperature,
the subsequence of solubility of nisoldipine was of the order ethyl
acetate (2.782 × 10–2, 298.15 K) > acetonitrile
(1.687 × 10–2, 298.15 K) > 1-butanol (1.105
× 10–2, 298.15 K) > 2-propanol (9.350 ×
10–3, 298.15 K) > 1-propanol (7.804 × 10–3, 298.15 K) > ethanol (6.483 × 10–3, 298.15 K) > toluene (3.092 × 10–3, 298.15
K) > cyclohexane (1.114 × 10–4, 298.15 K)
>
water (1.154 × 10–5, 298.15 K). To study the
effect of solvation interaction on solubility, the solute–solvent
and solvent–solvent interactions were studied. Hydrogen-bonding
acceptor (HBA) interaction of the solvent with the solute and nonspecific
dipolarity/polarizability interactions are in favor of the increase
of solubility of nisoldipine. In addition, the solubility increases
with an increasing composition of 2-propanol or ethanol and decreases
with an increase of water. Four thermodynamic models (modified Apelblat
model, λh model, Jouyban–Acree model,
and Apelblat–Jouyban–Acree model) were used to correlate
the relationships between the solubility of nisoldipine and temperature.
The correlation results obtained from all systems show that the largest
values of relative average deviation (RAD) and root-mean-square deviation
(RMSD) are 1.35% and 1.13 × 10–4, respectively.
Moreover, statistical analysis was used to evaluate the appropriateness
of the models; in a word, these four models can describe the solubility
behavior of nisoldipine very well.