1 |
Solubility of CO2 in 15, 30, 45 and 60 mass% MEA from 40 to 120 degrees C and model representation using the extended UNIQUAC framework (vol 64, pg 6393, 2011) Aronu UE, Gondal S, Hessen ET, Haug-Warberg T, Hartono A, Hoff KA, Svendsen HF Chemical Engineering Science, 78, 246, 2012 |
2 |
Density, viscosity, and N2O solubility of aqueous amino acid salt and amine amino acid salt solutions Aronu UE, Hartono A, Svendsen HF Journal of Chemical Thermodynamics, 45(1), 90, 2012 |
3 |
CO2 capture solvent selection by combined absorption-desorption analysis Aronu UE, Hoff KA, Svendsen HF Chemical Engineering Research & Design, 89(8A), 1197, 2011 |
4 |
Vapor-liquid equilibrium in amino acid salt system: Experiments and modeling Aronu UE, Hessen ET, Haug-Warberg T, Hoff KA, Svendsen HF Chemical Engineering Science, 66(10), 2191, 2011 |
5 |
Vapor-liquid equilibrium in aqueous amine amino acid salt solution: 3-(methylamino)propylamine/sarcosine Aronu UE, Hoff KA, Svendsen HF Chemical Engineering Science, 66(17), 3859, 2011 |
6 |
Kinetics of carbon dioxide absorption into aqueous amine amino acid salt: 3-(methylamino)propylamine/sarcosine solution Aronu UE, Hartono A, Svendsen HF Chemical Engineering Science, 66(23), 6109, 2011 |
7 |
Kinetics of Carbon Dioxide Absorption into Aqueous Amino Acid Salt: Potassium Salt of Sarcosine Solution Aronu UE, Hartono A, Hoff KA, Svendsen HF Industrial & Engineering Chemistry Research, 50(18), 10465, 2011 |