PVT data from refractive index measurements for the ethane + nitrogen system from 270 to 350 K and pressures to 28 MPa
References (29)
- et al.
An optical method for the determination of the (pressure, density, temperature) relation. Measurements of ethylene in the temperature range from 283.15 to 373.15 K at pressures up to 30 MPa
J. Chem. Thermodyn.
(1989) - et al.
Pressure, volume, temperature relations of ethane
J. Chem. Thermodyn.
(1973) - et al.
Measurement and correlation of the (pressure, density, temperature) relation of nitrogen in the temperature range from 273.15 to 323.15 K at pressures up to 8 MPa
J. Chem. Thermodyn.
(1988) - et al.
P, V, T data from Burnett and refractive index measurements for the nitrogen—hydrogen system from 270 to 353 K pressures to 30 MPa
Fluid Phase Equilibria
(1991) - et al.
An interaction model for third virial coefficients which provides simplified equations for mixtures
Fluid Phase Equilibria
(1987) - et al.
Isotherms of nitrogen between 0°C and 150°C and at pressures from 20 to 80 atm.
Physica
(1934) - et al.
Isotherms and thermodynamical functions of ethane at temperatures between 0°C and 150°C and pressures up to 200 atm.
Physica
(1954) - et al.
Ein neues Gerät zur kontinuierlichen Druckmessung—Das Druckmessinterferometer. Technisches Messen
(1982) - et al.
Ein Verfahren zur genauen Bestimmung der Dichte von Gasen aus optischen Messungen VDI-Forschungsheft 619
(1983) - et al.
Precise determination of the compressibility factor of methane, nitrogen, and their mixtures from refractive index measurements
Int. J. Thermophys.
(1986)
Direct determination of the second refractivity virial coefficient of methane, nitrogen and five of their mixtures
Int. J. Thermophys.
Genaue Bestimmung der Dichte von Gasen aus Messungen des Brechungsindex. VDI-Forschungsheft 649
The density dependence of the refractivity of gases
Proc. R. Soc. London
Mixture rules for the Mie (n, 6) intermolecular pair potential and the Dymond—Alder pair potential
J. Chem. Phys.
Cited by (16)
Density Modeling of High-Pressure Mixtures using Cubic and Non-Cubic EoS and an Excess Volume Method
2021, Fluid Phase EquilibriaAn improved Helmholtz energy model for non-polar fluids and their mixtures. Part 2: Application to mixtures of non-polar fluids
2013, Fluid Phase EquilibriaCitation Excerpt :For the (nitrogen + ethane), surprisingly high deviations, reaching 0.76% at p = 3.0 MPa, were shown for the low-pressure Jaeschke and Humphreys [34] data on the isotherm of T = 270 K with mole fraction of nitrogen of 0.2485. Also, the Achtermann et al. [61] data reached a deviation of −0.576% at p = 25 MPa on the 310 K isotherm with mole fraction of nitrogen of 0.4996; and the Reamer et al. [63] reached a deviation of −0.589% on the 277.59 K isotherm at p = 62 MPa and mole fraction of nitrogen of 0.5244. For the (nitrogen + carbon dioxide) system, a deviation of 0.891% was reached by the Seitz et al. [55] data on the 373.15 K isotherm at p = 19.94 MPa and mole fraction of nitrogen of 0.80, and another deviation of 0.947% was reached by the Seitz et al. [55] data at T = 323.15 K, p = 19.94 MPa and mole fraction of nitrogen of 0.40.