1 |
NMR spectroscopic method for studying homogenous liquid phase reaction kinetics in systems used in reactive gas absorption and application to monoethanolamine-water-carbon dioxide Behrens R, Dyga M, Sieder G, von Harbou E, Hasse H Chemical Engineering Journal, 374, 1127, 2019 |
2 |
Prediction of CO2 and H2S solubility and enthalpy of absorption in reacting N-methyldiethanolamine/water systems with ePC-SAFT Wangler A, Sieder G, Ingram T, Heilig M, Held C Fluid Phase Equilibria, 461, 15, 2018 |
3 |
Modeling the solubility of CO2 in aqueous methyl diethanolamine solutions with an electrolyte model based on COSMO-RS Gerlach T, Ingram T, Sieder G, Smirnova I Fluid Phase Equilibria, 461, 39, 2018 |
4 |
Monoalkylcarbonate Formation in Methyldiethanolamine-H2O-CO2 Behrens R, von Harbou E, Thiel WR, Bottinger W, Ingram T, Sieder G, Hasse H Industrial & Engineering Chemistry Research, 56(31), 9006, 2017 |
5 |
Predicting CO2 solubility in aqueous N-methyldiethanolamine solutions with ePC-SAFT Uyan M, Sieder G, Ingram T, Held C Fluid Phase Equilibria, 393, 91, 2015 |
6 |
Removal of carbon dioxide from flue gases with aqueous MEA solution containing ethanol von Harbou I, Hoch S, Mangalapally HP, Notz R, Sieder G, Garcia H, Spuhl O, Hasse H Chemical Engineering and Processing, 75, 81, 2014 |
7 |
CO2 Capture Technology - from Research to Large Scale Industrial Operation Tonnies I, Garcia H, Mangalapally HP, Hoch S, Notz R, Sieder G, Eck B, Hasse H Chemie Ingenieur Technik, 83(7), 1005, 2011 |
8 |
An extension of the Peng-Robinson equation of state for the correlation and prediction of high-pressure phase equilibrium in systems containing supercritical carbon dioxide and a salt Sieder G, Maurer G Fluid Phase Equilibria, 225(1-2), 85, 2004 |
9 |
Experimental investigation of the influence of the single salts sodium chloride and sodium acetate on the high-pressure phase equilibrium of the system carbon dioxide plus water plus acetic acid Sieder G, Maurer G Journal of Chemical and Engineering Data, 49(5), 1303, 2004 |
10 |
High-pressure phase equilibrium of the ternary system carbon dioxide plus water plus acetic acid at temperatures from 313 to 353 K Bamberger A, Sieder G, Maurer G Journal of Supercritical Fluids, 32(1-3), 15, 2004 |