NIST TRC ThermoML Dataset

Vapor-liquid equilibria for the quaternary reactive system ethyl acetate + ethanol + water + acetic acid and some of the constituent binary systems at 101.3 kPa Calvar, N.; Domínguez, A.; Tojo, J.; Fluid Phase Equilibria 2005, 235, 215-222

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Boiling point at pressure
Methodology: EBULLIO:UFactor:8
Phase(s): Liquid
Substances:
1. acetic acid C2H4O2 (QTBSBXVTEAMEQO-UHFFFAOYSA-N) - Commercial source
2. water H2O (XLYOFNOQVPJJNP-UHFFFAOYSA-N) - Commercial source

Data

P = 101.325 kPa
x (mol mol^-1)	T_bp (K)
0.0901	386.54
0.5337	377.47
0.5698	377.18
0.6046	376.7
0.6546	376.28
0.6808	375.98
0.7057	375.68
0.7332	375.45
0.7789	375.0
0.8287	374.62
0.8555	374.45
0.1414	384.47
0.8963	374.11
0.9140	373.99
0.9391	373.84
0.9653	373.66
0.9902	373.31
0.1934	382.96
0.2593	381.86
0.3241	380.39
0.3627	379.83
0.4454	378.65
0.4702	378.35
0.5071	377.84

282; acetic acid + water; 00004:00051