Elias Trautner
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Elias Trautner has a total of 15 co-authors. Here are the top co-authors by number of shared publications:
- Markus Klein
Department of Aerospace Engineering, University of the Bundeswehr Munich, Neubiberg, Germany
11 shared publications - Josef Hasslberger
Department of Aerospace Engineering, University of the Bundeswehr Munich, Neubiberg, Germany
9 shared publications - Paolo Cifani
Scuola Normale Superiore , Pisa
3 shared publications - Theresa Trummler
Institute of Applied Mathematics and Scientific Computing, University of the Bundeswehr Munich, Werner-Heisenberg-Weg 39, 85577 Neubiberg, Germany
3 shared publications - Alexander Begemann
Institute of Applied Mathematics and Scientific Computing, University of the Bundeswehr Munich, Werner-Heisenberg-Weg 39, 85577 Neubiberg, Germany
2 shared publications - Andreas Iberl2 shared publications
Latest Publications
- Open Access
- 31 March 2026
- Published by Elsevier in International Journal of Multiphase Flow
- Vol. 200
Simulation of particle deposition in bubbly flows using an Eulerian–Lagrangian framework
- 31 March 2026
- Published by Elsevier in International Journal of Multiphase Flow
- Vol. 200
Open AccessSimulation of particle deposition in bubbly flows using an Eulerian–Lagrangian framework
- Open Access
- 1 December 2025
- Published by Springer Nature in Flow, Turbulence and Combustion
- Vol. 116 (1) , 8
LES of Liquid Jet Breakup Using an Eulerian-Lagrangian Approach Extended by a Primary Atomization Model
The present article is concerned with the modeling of primary atomization in Eulerian-Lagrangian Large Eddy Simulation of liquid jet breakup. Recent numerical studies have demonstrated that spray atomization does not strictly follow a large-to-small breakup cascade. Instead, numerous small droplets can directly be generated by the core jet. As these cannot be resolved in Large Eddy Simulations using interface capturing methods for primary atomization, modeling their formation by releasing small Lagrangian particles from the core jet might improve the predictive capabilities of such simulations. This study discusses a corresponding model proposed in the literature and demonstrates its application for a Large Eddy Simulation of a complex Diesel-like spray. The results indicate a promising performance, but also highlight the need for further investigation.
- 1 December 2025
- Published by Springer Nature in Flow, Turbulence and Combustion
- Vol. 116 (1) , 8
Open AccessLES of Liquid Jet Breakup Using an Eulerian-Lagrangian Approach Extended by a Primary Atomization Model
The present article is concerned with the modeling of primary atomization in Eulerian-Lagrangian Large Eddy Simulation of liquid jet breakup. Recent numerical studies have demonstrated that spray atomization does not strictly follow a large-to-small breakup cascade. Instead, numerous small droplets can directly be generated by the core jet. As these cannot be resolved in Large Eddy Simulations using interface capturing methods for primary atomization, modeling their formation by releasing small Lagrangian particles from the core jet might improve the predictive capabilities of such simulations. This study discusses a corresponding model proposed in the literature and demonstrates its application for a Large Eddy Simulation of a complex Diesel-like spray. The results indicate a promising performance, but also highlight the need for further investigation.
- Open Access
- 12 April 2025
- Published by Elsevier in International Journal of Multiphase Flow
- Vol. 189
A-posteriori assessment of mixed models for Large Eddy Simulation of polydisperse multiphase flows
- 12 April 2025
- Published by Elsevier in International Journal of Multiphase Flow
- Vol. 189
Open AccessA-posteriori assessment of mixed models for Large Eddy Simulation of polydisperse multiphase flows
- Open Access
- 23 December 2024
- Published by Springer Nature in Flow, Turbulence and Combustion
- Vol. 115 (1) , 243-273
Towards LES of Liquid Jet Atomization Using an Eulerian-Lagrangian Multiscale Approach
This study is concerned with Large Eddy Simulation of liquid jet atomization using a two-way coupled Eulerian-Lagrangian multiscale approach. The proposed framework combines Volume-of-Fluid interface capturing with Lagrangian Particle Tracking. The former is used to compute the core jet and large liquid elements in the near-nozzle region, whereas the latter is used to track the large number of small droplets in the dilute downstream region of the spray. The convective and surface tension sub-grid scale terms arising in the context of two-phase flow LES are closed using suitable models, and secondary atomization is considered by employing a modified version of the Taylor Analogy Breakup model. The introduced framework is used to simulate an oil-in-air atomization as well as the Diesel-like Spray A test case of the Engine Combustion Network. Compared to previous studies based on Eulerian-Lagrangian methods, the present work stands out for the high-fidelity numerical approach, the complex test cases and the detailed comparison of the results to experimental data, which indicates a promising performance.
- 23 December 2024
- Published by Springer Nature in Flow, Turbulence and Combustion
- Vol. 115 (1) , 243-273
Open AccessTowards LES of Liquid Jet Atomization Using an Eulerian-Lagrangian Multiscale Approach
This study is concerned with Large Eddy Simulation of liquid jet atomization using a two-way coupled Eulerian-Lagrangian multiscale approach. The proposed framework combines Volume-of-Fluid interface capturing with Lagrangian Particle Tracking. The former is used to compute the core jet and large liquid elements in the near-nozzle region, whereas the latter is used to track the large number of small droplets in the dilute downstream region of the spray. The convective and surface tension sub-grid scale terms arising in the context of two-phase flow LES are closed using suitable models, and secondary atomization is considered by employing a modified version of the Taylor Analogy Breakup model. The introduced framework is used to simulate an oil-in-air atomization as well as the Diesel-like Spray A test case of the Engine Combustion Network. Compared to previous studies based on Eulerian-Lagrangian methods, the present work stands out for the high-fidelity numerical approach, the complex test cases and the detailed comparison of the results to experimental data, which indicates a promising performance.
- Open Access
- 5 March 2024
- Published by Wiley in International Journal for Numerical Methods in Fluids
- Vol. 96 (6) , 1057-1077
Enforcing accurate volume conservation in VOF‐based long‐term simulations of turbulent bubble‐laden flows on coarse grids
- 5 March 2024
- Published by Wiley in International Journal for Numerical Methods in Fluids
- Vol. 96 (6) , 1057-1077
Open AccessEnforcing accurate volume conservation in VOF‐based long‐term simulations of turbulent bubble‐laden flows on coarse grids
- 16 November 2023
- Published by Springer Nature
- p. 344-349
Assessment of the Effect of the Surface Tension Contribution on the Emulsification in Linearly Forced Turbulence
- 16 November 2023
- Published by Springer Nature
- p. 344-349
Assessment of the Effect of the Surface Tension Contribution on the Emulsification in Linearly Forced Turbulence
- 16 November 2023
- Published by Springer Nature
- p. 279-284
Volume Conservation Methods for VOF-Based Long-Term Simulations of Turbulent Bubble-Laden Flows on Coarse Grids
- 16 November 2023
- Published by Springer Nature
- p. 279-284
Volume Conservation Methods for VOF-Based Long-Term Simulations of Turbulent Bubble-Laden Flows on Coarse Grids
- Open Access
Effect of the Density Ratio on Emulsions and Their Segregation: A Direct Numerical Simulation Study
Using direct numerical simulation (DNS) in combination with the volume of fluid method (VoF), we investigate the influence of the density ratio between the carrier and dispersed phase on emulsions, where the baseline simulation approximately corresponds to the ratio of water-in-gasoline emulsions. For this purpose, homogeneous isotropic turbulence (HIT) is generated using a linear forcing method, enhanced by a proportional–integral–derivative (PID) controller, ensuring a constant turbulent kinetic energy (TKE) for two-phase flows, where the TKE balance equation contains an additional term due to surface tension. Then, the forcing is stopped, and gravitational acceleration is activated. The proposed computational setup represents a unique and well-controlled configuration to study emulsification and segregation. We consider four different density ratios, which are applied in industrial processes, to investigate the influence of the density ratio on the statistically steady state of the emulsions, and their segregation under decaying turbulence and constant gravitational acceleration. At the statistically steady state, we hold the turbulence constant and study the effects of the density ratio , on the interface area, the Sauter mean diameter (SMD), and the statistical droplet size distribution. We find that all are affected by the density ratio, and we observe a relation between the SMD and . Furthermore, we assume a dependence of the critical Weber number on the density ratio. In the second part of our work, we study the segregation process. To this end, we consider the change in the center of mass of the disperse phase and the energy release, to analyze the dependence of segregation on the density difference . We show that segregation scales with the density difference and the droplet size, and a segregation time scale has been suggested that collapses the height of the center of mass for different density ratios.Open AccessEffect of the Density Ratio on Emulsions and Their Segregation: A Direct Numerical Simulation Study
Using direct numerical simulation (DNS) in combination with the volume of fluid method (VoF), we investigate the influence of the density ratio between the carrier and dispersed phase on emulsions, where the baseline simulation approximately corresponds to the ratio of water-in-gasoline emulsions. For this purpose, homogeneous isotropic turbulence (HIT) is generated using a linear forcing method, enhanced by a proportional–integral–derivative (PID) controller, ensuring a constant turbulent kinetic energy (TKE) for two-phase flows, where the TKE balance equation contains an additional term due to surface tension. Then, the forcing is stopped, and gravitational acceleration is activated. The proposed computational setup represents a unique and well-controlled configuration to study emulsification and segregation. We consider four different density ratios, which are applied in industrial processes, to investigate the influence of the density ratio on the statistically steady state of the emulsions, and their segregation under decaying turbulence and constant gravitational acceleration. At the statistically steady state, we hold the turbulence constant and study the effects of the density ratio , on the interface area, the Sauter mean diameter (SMD), and the statistical droplet size distribution. We find that all are affected by the density ratio, and we observe a relation between the SMD and . Furthermore, we assume a dependence of the critical Weber number on the density ratio. In the second part of our work, we study the segregation process. To this end, we consider the change in the center of mass of the disperse phase and the energy release, to analyze the dependence of segregation on the density difference . We show that segregation scales with the density difference and the droplet size, and a segregation time scale has been suggested that collapses the height of the center of mass for different density ratios. - Open Access
- 1 November 2022
- Published by AIP Publishing in Physics of Fluids
- Vol. 34 (11) , 113324
Numerical investigation of the segregation of turbulent emulsions
We study the segregation of emulsions in decaying turbulence using direct numerical simulations in combination with the volume of fluid method. To this end, we generate emulsions in forced homogeneous isotropic turbulence and then turn the forcing off and activate the gravitational acceleration. This allows us to study the segregation process in decaying turbulence and under gravity. We consider non-iso-density emulsions, where the dispersed phase is the lighter one. The segregation process is driven by both the minimization of the potential energy achieved by the sinking of the heavier phase as well as the minimization of the surface energy achieved by coalescence. To study these two processes and their impacts on the segregation progress in detail, we consider different buoyancy forces and surface tension coefficients in our investigation, resulting in five different configurations. The surface tension coefficient also alters the droplet size distribution of the emulsion. Using the three-dimensional simulation results and the monitored data, we analyze the driving mechanisms and their impact on the segregation progress in detail. We propose a dimensionless number that reflects the energy release dominating the segregation. Moreover, we evaluate the time required for the rise of the lighter phase and study correlations with the varied parameters: gravitational acceleration and surface tension coefficient.
- 1 November 2022
- Published by AIP Publishing in Physics of Fluids
- Vol. 34 (11) , 113324
Open AccessNumerical investigation of the segregation of turbulent emulsions
We study the segregation of emulsions in decaying turbulence using direct numerical simulations in combination with the volume of fluid method. To this end, we generate emulsions in forced homogeneous isotropic turbulence and then turn the forcing off and activate the gravitational acceleration. This allows us to study the segregation process in decaying turbulence and under gravity. We consider non-iso-density emulsions, where the dispersed phase is the lighter one. The segregation process is driven by both the minimization of the potential energy achieved by the sinking of the heavier phase as well as the minimization of the surface energy achieved by coalescence. To study these two processes and their impacts on the segregation progress in detail, we consider different buoyancy forces and surface tension coefficients in our investigation, resulting in five different configurations. The surface tension coefficient also alters the droplet size distribution of the emulsion. Using the three-dimensional simulation results and the monitored data, we analyze the driving mechanisms and their impact on the segregation progress in detail. We propose a dimensionless number that reflects the energy release dominating the segregation. Moreover, we evaluate the time required for the rise of the lighter phase and study correlations with the varied parameters: gravitational acceleration and surface tension coefficient.