| 1 |
Investigation on vapor liquid equilibrium for strongly-zeotropic ternary mixture of 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) + trifluoromethane (R23) + tetrafluoromethane (R14)
Qin YB, Wang ZL, Zhang H, Wu YL
International Journal of Heat and Mass Transfer, 114, 1135, 2017 |
| 2 |
Application of the UMR-PRU model to multicomponent systems: Prediction of the phase behavior of synthetic natural gas and oil systems
Louli V, Boukouvalas C, Voutsas E, Magoulas K, Tassios D
Fluid Phase Equilibria, 261(1-2), 351, 2007 |
| 3 |
Stability analysis of molality-based virial expansion G(E)-models
Blagov S, Asprion N, Hasse H
Fluid Phase Equilibria, 227(2), 267, 2005 |
| 4 |
Phase-equilibrium calculations for non-aqueous and aqueous associating systems using continuous thermodynamics
Browarzik D
Fluid Phase Equilibria, 230(1-2), 143, 2005 |
| 5 |
Measurements and modeling of bubble points in binary carbon dioxide systems with tetrahydropyran and methylcyclohexane
Nasrifar K, Mooijer-van den Heuvel MM, Peters CJ, Ayatollahi S, Moshfeghian M
Fluid Phase Equilibria, 204(1), 1, 2003 |
| 6 |
A versatile liquid activity model for SRK, PR and a new cubic equation-of-state TST
Twu CH, Sim WD, Tassone V
Fluid Phase Equilibria, 194, 385, 2002 |
| 7 |
A modified PSRK model for the prediction of the vapor-liquid equilibria of asymmetric systems
Yang QY, Zhong CL
Fluid Phase Equilibria, 192(1-2), 103, 2001 |
| 8 |
Bench-scale application of supercritical fluid extraction for the removal of phenol from aqueous solution
Boukouvalas C, Louli V, Magoulas K
Separation Science and Technology, 36(10), 2279, 2001 |
| 9 |
Phase behaviour of water plus nonionic surfactant systems: experiments and modelling applying the Peng-Robinson equation of state with the Wong-Sandler mixing rules and the UNIQUAC g(E)-model
Rudolph ESJ, Langeveld JH, de Loos TW, Arons JD
Fluid Phase Equilibria, 173(1), 81, 2000 |
| 10 |
Isothermal vapor-liquid equilibrium data for the acetone plus methanol plus lithium nitrate system
Yan WD, Rose C, Zhu M, Gmehling J
Journal of Chemical and Engineering Data, 43(3), 482, 1998 |
