| 1 |
PVT, saturated liquid density and vapor-pressure measurements of main components of the biofuels at high temperatures and high pressures: Methyl palmitate
Rasulov SM, Abdulagatov IM
Fuel, 218, 282, 2018 |
| 2 |
Measurements of bubble point pressure and saturated liquid density for ((R1234yf+R290))
Zhong Q, Li HY, Dong XQ, Zhang HY, Zhao YX, Guo H, Shen J, Gong MQ
Journal of Chemical Thermodynamics, 118, 77, 2018 |
| 3 |
Accurately modeling benzene and alkylbenzenes using a group contribution based SAFT approach
Das G, dos Ramos MC, McCabe C
Fluid Phase Equilibria, 362, 242, 2014 |
| 4 |
Upward extrapolation of saturated liquid densities
Lai NA, Wendland M, Fischer J
Fluid Phase Equilibria, 280(1-2), 30, 2009 |
| 5 |
Measurements of saturated-liquid densities for isobutane at T = (280 to 407) K
Miyamoto H, Koshi T, Uematsu M
Journal of Chemical Thermodynamics, 40(8), 1222, 2008 |
| 6 |
Saturated liquid densities of propane at T = (280 to 365) K
Miyamoto H, Uematsu M
Journal of Chemical Thermodynamics, 39(2), 225, 2007 |
| 7 |
Measurements of vapour pressures and saturated-liquid densities for n-butane at T = (280 to 424) K
Miyamoto H, Uematsu M
Journal of Chemical Thermodynamics, 39(5), 827, 2007 |
| 8 |
Surface tension of 1,1,1,2,2,3,3,4,4-nonafluorohexane and 1,1,2,2-tetraflu-oroethyl-2,2,2-trifluoroethyl ether
Tanaka K, Higashi Y
KAGAKU KOGAKU RONBUNSHU, 33(1), 1, 2007 |
| 9 |
A new cubic equation of state for reservoir fluids
Esmaeilzadeh F, Roshanfekr M
Fluid Phase Equilibria, 239(1), 83, 2006 |
| 10 |
Empirical correction to the Peng-Robinson equation of state for the saturated region
Lin H, Duan YY
Fluid Phase Equilibria, 233(2), 194, 2005 |
