| 1 |
Experimental-Modeling Study of Phase Equilibria, Densities, and Viscosities for the Propanenitrile-Decane Mixture at Low Pressure
Correa ML, Cardona LF, Velasquez JA, Forero LA
Journal of Chemical and Engineering Data, 66(2), 1089, 2021 |
| 2 |
Critical Properties of Metal-Containing Ionic Liquids
Valderrama JO, Forero LA, Rojas RE
Industrial & Engineering Chemistry Research, 58(17), 7332, 2019 |
| 3 |
Correlation and Prediction of Thermal Conductivity Using the Redlich-Kwong Cubic Equation of State and the Geometric Similitude Concept for Pure Substances and Mixtures
Cardona LF, Forero LA, Velasquez JA
Industrial & Engineering Chemistry Research, 58(51), 23417, 2019 |
| 4 |
A generalized cubic equation of state for non-polar and polar substances
Forero LA, Velasquez JA
Fluid Phase Equilibria, 418, 74, 2016 |
| 5 |
A simple and generalized model to represent the vapor-liquid equilibria and the liquid-molar-volume of alcohol-alkane binary mixtures
Forero LA, Velasquez JA
Fluid Phase Equilibria, 430, 112, 2016 |
| 6 |
Extension of a Group Contribution Method To Estimate the Critical Properties of Ionic Liquids of High Molecular Mass
Valderrama JO, Forero LA, Rojas RE
Industrial & Engineering Chemistry Research, 54(13), 3480, 2015 |
| 7 |
A modified Patel-Teja cubic equation of state. Part II: Parameters for polar substances and its mixtures
Forero LA, Velasquez JA
Fluid Phase Equilibria, 364, 75, 2014 |
| 8 |
A modified Patel-Teja cubic equation of state: Part I - Generalized model for gases and hydrocarbons
Forero LA, Velasquez JA
Fluid Phase Equilibria, 342, 8, 2013 |
| 9 |
An analytical expression for the vapor pressure of ionic liquids based on an equation of state
Valderrama JO, Forero LA
Fluid Phase Equilibria, 317, 77, 2012 |
| 10 |
The Patel-Teja and the Peng-Robinson EoSs performance when Soave alpha function is replaced by an exponential function
Forero LA, Velasquez JA
Fluid Phase Equilibria, 332, 55, 2012 |
