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-decane C10H22 (DIOQZVSQGTUSAI-UHFFFAOYSA-N) - Commercial source

Data

P = 101 kPa
x (mol mol^-1)	V^E (m³ mol^-1)
0.5803	5.52e-07
0.5901	5.5e-07
0.6003	5.47e-07

30628; 1-nitropropane + decane; 00206:00288