Equation of state for solid carbon dioxide based on the Gibbs free energy A Jäger, R Span Journal of Chemical & Engineering Data 57 (2), 590-597, 2012 | 97 | 2012 |
TREND. Thermodynamic Reference and Engineering Data 4.0 R Span, T Eckermann, S Herrig, S Hielscher, A Jäger, M Thol Ruhr-Universitaet Bochum, Bochum, Germany, 2015 | 94 | 2015 |
Calculation of phase equilibria for multi-component mixtures using highly accurate Helmholtz energy equations of state J Gernert, A Jäger, R Span Fluid Phase Equilibria 375, 209-218, 2014 | 90 | 2014 |
A benchmark open-source implementation of COSMO-SAC IH Bell, E Mickoleit, CM Hsieh, ST Lin, J Vrabec, C Breitkopf, A Jäger Journal of chemical theory and computation 16 (4), 2635-2646, 2020 | 82 | 2020 |
Phase equilibria with hydrate formation in H2O+ CO2 mixtures modeled with reference equations of state A Jäger, V Vinš, J Gernert, R Span, J Hrubý Fluid Phase Equilibria 338, 100-113, 2013 | 54 | 2013 |
Helmholtz energy transformations of common cubic equations of state for use with pure fluids and mixtures IH Bell, A Jäger Journal of Research of the National Institute of Standards and Technology …, 2016 | 47 | 2016 |
Calculation of critical points from Helmholtz-energy-explicit mixture models IH Bell, A Jäger Fluid Phase Equilibria 433, 159-173, 2017 | 29 | 2017 |
Model for gas hydrates applied to CCS systems part I. Parameter study of the van der Waals and Platteeuw model V Vinš, A Jäger, R Span, J Hrubý Fluid Phase Equilibria 427, 268-281, 2016 | 28 | 2016 |
Accurate thermodynamic-property models for CO2-rich mixtures R Span, J Gernert, A Jäger Energy Procedia 37, 2914-2922, 2013 | 28 | 2013 |
Model for gas hydrates applied to CCS systems part III. Results and implementation in TREND 2.0 A Jäger, V Vinš, R Span, J Hrubý Fluid Phase Equilibria 429, 55-66, 2016 | 27 | 2016 |
Model for gas hydrates applied to CCS systems part II. Fitting of parameters for models of hydrates of pure gases V Vinš, A Jäger, J Hrubý, R Span Fluid Phase Equilibria 435, 104-117, 2017 | 24 | 2017 |
A theoretically based departure function for multi-fluid mixture models A Jäger, IH Bell, C Breitkopf Fluid Phase Equilibria 469, 56-69, 2018 | 19 | 2018 |
A new approach to model mixed hydrates S Hielscher, V Vinš, A Jäger, J Hrubý, C Breitkopf, R Span Fluid Phase Equilibria 459, 170-185, 2018 | 17 | 2018 |
A combination of multi-fluid mixture models with COSMO-SAC A Jäger, E Mickoleit, C Breitkopf Fluid Phase Equilibria 476, 147-156, 2018 | 16 | 2018 |
Influence of equations of state and mixture models on the design of a refrigeration process E Mickoleit, C Breitkopf, A Jäger International Journal of Refrigeration 121, 193-205, 2021 | 13 | 2021 |
Modification of a model for mixed hydrates to represent double cage occupancy S Hielscher, B Semrau, A Jäger, V Vinš, C Breitkopf, J Hrubý, R Span Fluid Phase Equilibria 490, 48-60, 2019 | 13 | 2019 |
Complex phase equilibria of gas hydrates and other solid and fluid phases modeled with highly accurate equations of state A Jäger | 13 | 2016 |
Algorithm to identify vapor–liquid–liquid equilibria of binary mixtures from vapor–liquid equilibria IH Bell, UK Deiters, A Jager Industrial & Engineering Chemistry Research 61 (6), 2592-2599, 2022 | 10 | 2022 |
Systematic analysis of additives on the performance parameters of sCO2 cycles and their individual effects on the cycle characteristics S Rath, E Mickoleit, U Gampe, C Breitkopf, A Jäger Energy 252, 123957, 2022 | 9 | 2022 |
Phase equilibria of carbon dioxide and methane gas-hydrates predicted with the modified analytical SLV equation of state V Vinš, A Jäger, J Hrubý, R Span EPJ Web of Conferences 25, 01098, 2012 | 8 | 2012 |