1 |
Vapor - liquid equilibrium of the carbon dioxide/methane mixture at three isotherms Petropoulou E, Voutsas E, Westman SF, Austegard A, Stang HGJ, Lovseth SW Fluid Phase Equilibria, 462, 44, 2018 |
2 |
Thermodynamics of the carbon dioxide plus argon (CO2 + Ar) system: An improved reference mixture model and measurements of vapor-liquid, vapor-solid, liquid-solid and vapor-liquid-solid phase equilibrium data at the temperatures 213-299 K and pressures up to 16 MPa Lovseth SW, Austegard A, Westman SF, Stang HGJ, Herrig S, Neumann T, Span R Fluid Phase Equilibria, 466, 48, 2018 |
3 |
Vapor-liquid equilibrium data for the carbon dioxide and carbon monoxide (CO2 + CO) system at the temperatures 253, 273, 283 and 298 K and pressures up to 13 MPa Westman SF, Austegard A, Stang HGJ, Lovseth SW Fluid Phase Equilibria, 473, 37, 2018 |
4 |
CO2 transport: Data and models - A review Munkejord ST, Hammer M, Lovseth SW Applied Energy, 169, 499, 2016 |
5 |
Vapor liquid equilibrium data for the carbon dioxide and nitrogen (CO2 + N-2) system at the temperatures 223, 270, 298 and 303 K and pressures up to 18 MPa Westman SF, Stang HGJ, Lovseth SW, Austegard A, Snustad I, Storset SO, Ertesvag IS Fluid Phase Equilibria, 409, 207, 2016 |
6 |
Vapor-liquid equilibrium data for the carbon dioxide and oxygen (CO2 + O-2) system at the temperatures 218, 233, 253, 273, 288 and 298 K and pressures up to 14 MPa Westman SF, Stang HGJ, Lovseth SW, Austegard A, Snustad I, Ertesvag IS Fluid Phase Equilibria, 421, 67, 2016 |
7 |
Formulating the optimization problem when using sequential quadratic programming applied to a simple LNG process Wahl PE, Lovseth SW Computers & Chemical Engineering, 82, 1, 2015 |
8 |
Annotated bibliography-Use of optimization in LNG process design and operation Austbo B, Lovseth SW, Gundersen T Computers & Chemical Engineering, 71, 391, 2014 |
9 |
Optimization of a simple LNG process using sequential quadratic programming Wahl PE, Lovseth SW, Molnvik MJ Computers & Chemical Engineering, 56, 27, 2013 |