Review of WAG field experience JR Christensen, EH Stenby, A Skauge SPE Reservoir Evaluation & Engineering 4 (02), 97-106, 2001 | 1092 | 2001 |
Ten years with the CPA (Cubic-Plus-Association) equation of state. Part 1. Pure compounds and self-associating systems GM Kontogeorgis, ML Michelsen, GK Folas, S Derawi, N Von Solms, ... Industrial & engineering chemistry research 45 (14), 4855-4868, 2006 | 499 | 2006 |
Chilled ammonia process for CO2 capture V Darde, K Thomsen, WJM van Well, EH Stenby Energy procedia 1 (1), 1035-1042, 2009 | 412 | 2009 |
The friction theory (f-theory) for viscosity modeling SE Quiñones-Cisneros, CK Zéberg-Mikkelsen, EH Stenby Fluid Phase Equilibria 169 (2), 249-276, 2000 | 309 | 2000 |
Ten years with the CPA (Cubic-Plus-Association) equation of state. Part 2. Cross-associating and multicomponent systems GM Kontogeorgis, ML Michelsen, GK Folas, S Derawi, N Von Solms, ... Industrial & Engineering Chemistry Research 45 (14), 4869-4878, 2006 | 297 | 2006 |
Measurement and modeling of CO2 solubility in NaCl brine and CO2–saturated NaCl brine density W Yan, S Huang, EH Stenby International Journal of Greenhouse Gas Control 5 (6), 1460-1477, 2011 | 268 | 2011 |
Evaluation of activity coefficient models in prediction of alkane solid-liquid equilibria JAP Coutinho, SI Andersen, EH Stenby Fluid Phase Equilibria 103 (1), 23-39, 1995 | 211 | 1995 |
Modeling phase equilibria for acid gas mixtures using the CPA equation of state. Part II: Binary mixtures with CO2 I Tsivintzelis, GM Kontogeorgis, ML Michelsen, EH Stenby Fluid Phase Equilibria 306 (1), 38-56, 2011 | 203 | 2011 |
A Model for Estimating CO2 Solubility in Aqueous Alkanolamines J Gabrielsen, ML Michelsen, EH Stenby, GM Kontogeorgis Industrial & engineering chemistry research 44 (9), 3348-3354, 2005 | 197 | 2005 |
One parameter friction theory models for viscosity SE Quiñones-Cisneros, CK Zéberg-Mikkelsen, EH Stenby Fluid Phase Equilibria 178 (1-2), 1-16, 2001 | 174 | 2001 |
A dynamic two-phase pore-scale model of imbibition K Mogensen, EH Stenby Transport in Porous Media 32, 299-327, 1998 | 172 | 1998 |
Modeling phase equilibria for acid gas mixtures using the CPA equation of state. I. Mixtures with H2S I Tsivintzelis, GM Kontogeorgis, ML Michelsen, EH Stenby AIChE journal 56 (11), 2965-2982, 2010 | 153 | 2010 |
Prediction of mineral scale formation in geothermal and oilfield operations using the Extended UNIQUAC model: Part II. Carbonate-scaling minerals AV García, K Thomsen, EH Stenby Geothermics 35 (3), 239-284, 2006 | 153* | 2006 |
Application of the cubic-plus-association (CPA) equation of state to cross-associating systems GK Folas, J Gabrielsen, ML Michelsen, EH Stenby, GM Kontogeorgis Industrial & engineering chemistry research 44 (10), 3823-3833, 2005 | 151 | 2005 |
Prediction of high-pressure gas solubilities in aqueous mixtures of electrolytes K Aasberg-Petersen, E Stenby, A Fredenslund Industrial & engineering chemistry research 30 (9), 2180-2185, 1991 | 150 | 1991 |
Global approach for calculation of minimum miscibility pressure K Jessen, ML Michelsen, EH Stenby Fluid Phase Equilibria 153 (2), 251-263, 1998 | 144 | 1998 |
A linear gradient theory model for calculating interfacial tensions of mixtures YX Zuo, EH Stenby Journal of colloid and interface science 182 (1), 126-132, 1996 | 135 | 1996 |
Application of the cubic-plus-association (CPA) equation of state to complex mixtures with aromatic hydrocarbons GK Folas, GM Kontogeorgis, ML Michelsen, EH Stenby Industrial & engineering chemistry research 45 (4), 1527-1538, 2006 | 133 | 2006 |
Experimental validation of a rate-based model for CO2 capture using an AMP solution J Gabrielsen, HF Svendsen, ML Michelsen, EH Stenby, GM Kontogeorgis Chemical Engineering Science 62 (9), 2397-2413, 2007 | 131 | 2007 |
Extension of the cubic-plus-association equation of state to glycol− water cross-associating systems SO Derawi, GM Kontogeorgis, ML Michelsen, EH Stenby Industrial & engineering chemistry research 42 (7), 1470-1477, 2003 | 127 | 2003 |