2 research outputs found
Thermodynamic Functions for Solubility of 1‑Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
Solubility
of 1-hydroxybenzotriazole in 16 neat solvents including methanol,
ethanol, <i>n</i>-propanol, isopropanol, acetone, butanone,
isoamyl alcohol, <i>n</i>-hexanol, <i>n</i>-heptanol,
isooctyl alcohol, <i>N</i>,<i>N</i>-dimethylformamide
(DMF), dimethyl sulfoxide (DMSO), ethyl acetate, acetonitrile, 1,4-dioxane,
and toluene was measured using the method of isothermal saturation
over a temperature range from (278.15 to 313.15) K under atmospheric
pressure (101.1 kPa). The mole fraction solubility of 1-hydroxybenzotriazole
in the selected solvents increased with an increase of temperature.
They followed the order from high to low in studied neat solvents:
DMF > DMSO > ethanol > <i>n</i>-propanol > isopropanol
> methanol > butanone > acetone >1,4-dioxane > <i>n</i>-heptanol > <i>n</i>-hexanol > isoamyl
alcohol > isooctyl alcohol > ethyl acetate > acetonitrile
> toluene. The obtained solubility data of 1-hydroxybenzotriazole
in the studied solvents were correlated with the <i>λh</i> equation, modified Apelblat equation, and NRTL and Wilson models.
The largest value of root-mean-square deviation was 7.65 × 10<sup>–4</sup>, and relative average deviation, 4.21%. The values
of root-mean-square deviation obtained with the modified Apelblat
equation were smaller than those with the other equations for a given
solvent. By and large, the four thermodynamic models all provided
acceptable results for 1-hydroxybenzotriazole in the studied solvents.
Moreover, the apparent dissolution enthalpy and the mixing enthalpy,
mixing Gibbs energy, mixing entropy, reduced excess enthalpy, and
activity coefficient at infinitesimal concentration were derived.
The obtained solubility and thermodynamic studies could provide the
fundamental data for optimizing the reaction and purification procedure
of 1-hydroxybenzotriazole
Solubility Measurement and Thermodynamic Modeling of 4‑Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
The
solubility of 4-nitrophthalimide in different solvents are
of great importance for the design of its purification process via
crystallization. The work reported new solubility data for 4-nitrophthalimide
in 12 pure solvents of methanol, ethanol, isopropanol, cyclohexanone,
acetone, acetonitrile, ethyl acetate, 2-butanone, chloroform, 1,4-dioxane
benzyl alcohol and <i>N</i>,<i>N</i>-dimethylformamide.
They were determined by a high-performance liquid chromatography at <i>T</i> = (273.15 to 323.15) K under pressure of 0.1 MPa. The
4-nitrophthalimide solubility in the selected solvents increased with
the temperature increase. At a given temperature, the solubility of
4-nitrophthalimide is largest in <i>N</i>,<i>N</i>-dimethylformamide and lowest in chloroform. The solubility data
in the these solvents ranked as <i>N</i>,<i>N</i>-dimethylformamide > cyclohexanone > (1,4-dioxane, acetone,
2-butanone,
benzyl alcohol) > ethyl acetate > acetonitrile > methanol
> ethanol
> isopropanol > chloroform. The experimental solubility data
were
correlated by modified Apelblat equation, <i>λh</i> equation, Wilson model, and NRTL model. The obtained values of root-mean-square
deviation and relative average deviation are all less than 16.17 Ă—
10<sup>–4</sup> and 1.58%, respectively. The modified Apelblat
equation achieved the best correlating results in totally