NIST TRC ThermoML Dataset

Solution thermodynamics near the liquid-liquid critical point Losada-Pérez, P.; Blesic, M.; Pérez-Sánchez, G.; Cerdeiriña, C.; Troncoso, J.; Romaní, L.; Szydlowski, J.; Rebelo, L.; Fluid Phase Equilibria 2007, 258, 7-15

Journal: Fluid Phase Equilibria
Sample Quantity(ies): Excess molar volume
Methodology: Calculated with densities of this investigation
Phase(s): Liquid
Substances:
1. 1-nitropropane C3H7NO2 (JSZOAYXJRCEYSX-UHFFFAOYSA-N) - Commercial source
2. n-tridecane C13H28 (IIYFAKIEWZDVMP-UHFFFAOYSA-N) - Commercial source

Data

P = 101 kPa
x (mol mol^-1)	V^E (m³ mol^-1)
0.6792	7.36e-07
0.6902	7.53e-07
0.7001	7.73e-07

30630; 1-nitropropane + tridecane; 00206:00710