1 |
Modelling of phase equilibria of glycol ethers mixtures using an association model Garrido NM, Folas GK, Kontogeorgis GM Fluid Phase Equilibria, 273(1-2), 11, 2008 |
2 |
High-pressure vapor-liquid equilibria of systems containing ethylene glycol, water and methane - Experimental measurements and modeling Folas GK, Berg OJ, Solbraa E, Fredheim AO, Kontogeorgis GM, Michelsen ML, Stenby EH Fluid Phase Equilibria, 251(1), 52, 2007 |
3 |
Data and prediction of water content of high pressure nitrogen, methane and natural gas Folas GK, Froyna EW, Lovland J, Kontogeorgis GM, Solbraa E Fluid Phase Equilibria, 252(1-2), 162, 2007 |
4 |
Re: A.H. Mohammadi and D. Richon on "Data and prediction of water content of high pressure nitrogen, methane and natural gas" [Fluid Phase Equililbria 252 (2007) 162-174] Folas GK, Froyna EW, Lovland J, Kontogeorgis GM, Solbraa E Fluid Phase Equilibria, 255(1), 98, 2007 |
5 |
Modelling of associating mixtures for applications in the oil & gas and chemical industries Kontogeorgis GM, Folas GK, Muro-Sune N, von Solms N, Michelsen ML, Stenby EH Fluid Phase Equilibria, 261(1-2), 205, 2007 |
6 |
Calculation of the interfacial tension of the methane-water system with the linear gradient theory Schmidt KAG, Folas GK, Kvamme B Fluid Phase Equilibria, 261(1-2), 230, 2007 |
7 |
Vapor-liquid, liquid-liquid and vapor-liquid-liquid equilibrium of binary and multicomponent systems with MEG modeling with the CPA EoS and an EoS/G(E) model Folas GK, Kontogeorgis GM, Michelsen ML, Stenby EH Fluid Phase Equilibria, 249(1-2), 67, 2006 |
8 |
Application of the cubic-plus-association equation of state to mixtures with polar chemicals and high pressures Folas GK, Kontogeorgis GM, Michelsen ML, Stenby EH Industrial & Engineering Chemistry Research, 45(4), 1516, 2006 |
9 |
Application of the cubic-plus-association (CPA) equation of state to complex mixtures with aromatic hydrocarbons Folas GK, Kontogeorgis GM, Michelsen ML, Stenby EH Industrial & Engineering Chemistry Research, 45(4), 1527, 2006 |
10 |
Ten years with the CPA (Cubic-Plus-Association) equation of state. Part 1. Pure compounds and self-associating systems Kontogeorgis GM, Michelsen ML, Folas GK, Derawi S, von Solms N, Stenby EH Industrial & Engineering Chemistry Research, 45(14), 4855, 2006 |