화학공학소재연구정보센터
검색결과 : 14건
No. Article
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