NIST TRC ThermoML Dataset

Isobaric vapor-liquid equilibria for the binary and ternary mixtures of 2-propanol, water, and 1,3-propanediol at P = 101.3 kPa: Effect of the 1,3-propanediol addition Lin, Y.F.; Tu, C.H.; Fluid Phase Equilibria 2014, 368, 104-111

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Boiling point at pressure
Methodology: Ebulliometric method (Recirculating still)
Phase(s): Gas' Liquid
Substances:
1. 2-propanol C3H8O (KFZMGEQAYNKOFK-UHFFFAOYSA-N) - Commercial source
2. 1,3-propanediol C3H8O2 (YPFDHNVEDLHUCE-UHFFFAOYSA-N) - Commercial source

Data

P = 101.3 kPa
x (mol mol^-1)	T_bp (K)
0	487.55
0.458	373.88
0.501	371.84
0.567	369.17
0.635	366.66
0.692	364.51
0.755	362.3
0.811	360.52
0.878	358.55
0.935	357.01
0.968	356.17
0.027	445.58
1	355.46
0.054	425.51
0.118	402.32
0.192	391.08
0.231	387.35
0.268	384.16
0.328	380.35
0.388	377.21

33179; propan-2-ol + propan-1,3-diol; 00082:00552