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Erling H. Stenby
Erling H. Stenby
Professor of Applied Thermodynamics, Technical University of Denmark
Verified email at kemi.dtu.dk - Homepage
Title
Cited by
Cited by
Year
Review of WAG field experience
JR Christensen, EH Stenby, A Skauge
SPE Reservoir Evaluation & Engineering 4 (02), 97-106, 2001
10682001
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
4822006
Chilled ammonia process for CO2 capture
V Darde, K Thomsen, WJM van Well, EH Stenby
Energy procedia 1 (1), 1035-1042, 2009
3992009
The friction theory (f-theory) for viscosity modeling
SE Quiñones-Cisneros, CK Zéberg-Mikkelsen, EH Stenby
Fluid Phase Equilibria 169 (2), 249-276, 2000
3062000
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
2902006
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
2492011
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
2082011
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
2041995
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
2012005
One parameter friction theory models for viscosity
SE Quiñones-Cisneros, CK Zéberg-Mikkelsen, EH Stenby
Fluid Phase Equilibria 178 (1-2), 1-16, 2001
1692001
A dynamic two-phase pore-scale model of imbibition
K Mogensen, EH Stenby
Transport in Porous Media 32, 299-327, 1998
1691998
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
154*2006
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
1492010
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
1482005
Global approach for calculation of minimum miscibility pressure
K Jessen, ML Michelsen, EH Stenby
Fluid Phase Equilibria 153 (2), 251-263, 1998
1461998
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
1362006
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
1341996
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
1322007
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
1301991
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
1262003
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