Ternary liquid–liquid equilibrium
(LLE) data were measured
and correlated for the water + acetonitrile + (butan-1-ol or 2-methylpropan-1-ol)
systems at (303.2, 323.2, and 343.2) K and 1 atm. A double-walled
glass cell with the direct analytical method was used to measure the
liquid–liquid equilibrium data. The phase equilibrium samples
were analyzed and quantified using gas chromatography. The nonrandom
two-liquid activity coefficient model was used to fit the experimental
tie-lines using nonlinear least-squares regression of the data. Relative
selectivity values for solvent separation efficiency were calculated
from the tie-line data. The plait point for each temperature was estimated
with the graphical Coolidge method.