T–x–y diagram
y–x diagram
Close-up near the azeotrope
Relative volatility α12
Excess properties
Activity coefficients
ΔHmix versus temperature
Excess heat capacity CpE
Design with NRTL equilibrium
Ideal-solution design (original design)
Parameters and data sources
NRTL (Aspen/DDB): a12 = −0.8009, b12 = 246.18 K, a21 = 3.4578, b21 = −586.0809 K, α = 0.3. Aspen Plus databank values regressed from the Dortmund Data Bank, tabulated in Beneke et al., Understanding Distillation Using Column Profile Maps (Wiley, 2013), Appendix B.
This study's fit: aij = 0, b12 = −37.54 K, b21 = 640.64 K (weighted least squares on the Kamihama et al. data). Van Laar: A12 = 1.700, A21 = 0.953 (same fit). Course example: values marked as illustrative in the course handout code.
Vapour pressure: report version = ethanol from the NIST WebBook (Ambrose & Sprake 1970), water from the IAPWS-IF97 saturation line; repo version = common tabulated mmHg / °C Antoine constants (valid for ethanol up to 80 °C).
Experimental data: N. Kamihama et al., J. Chem. Eng. Data 57 (2012) 339–344, via NIST TRC ThermoML; ΔHmix minimum at 25 °C: Larkin (1975), Ott et al. (1986).