Tassilo von Aretin
Dr.-Ing. Tassilo von Aretin
Lehrstuhl I für Technische Chemie
Technische Universität München
Lichtenbergstr. 4
D-85747 Garching
Germany
Email: tassilo.aretin(at)ch.tum.de
Werdegang
| geboren am | 07.02.1987 in Eggenfelden |
| 2006 | Abitur am Gymnasium Vilshofen |
| Okt. 2006 – Sep. 2011 | Studium des Chemieingenieurwesens an der Technischen Universität München |
| Jan. 2012 - Jun. 2015 | Promotion am Lehrstuhl I für Technische Chemie an der Technischen Universität München |
| Seit Aug. 2015 | BASF SE in Ludwigshafen am Rhein |
Forschungsprojekt
Kinetic Modeling of Olefins Cracking
Both ethene and propene offer a wide range of applications for the production of polymers. These hydrocarbons are mainly produced by steam cracking of naphtha or catalytic cracking of crude oil into petroleum fractions. Since the demand for propene is growing faster than for ethene, the production of low olefins on demand offers economic advantages. In this context the catalytic cracking of higher olefins on acid zeolites allows a process design with high propene yield. To obtain further mechanistic insight into the reactions occurring during catalytic cracking of olefins, a kinetic model of the reaction is developed. Due to the large number of reaction possibilities the single event kinetic modeling approach is used to link catalyst design and product distribution in catalytic cracking.
Veröffentlichungen
von Aretin, T., Hinrichsen, O.
Single-Event Kinetic Model for Cracking and Isomerization of 1‑Hexene on ZSM‑5
Industrial & Engineering Chemistry Research (2014), 53, 19460-19470.
von Aretin, T., Schallmoser, S., Standl, S., Tonigold, M., Lercher, J.A., Hinrichsen, O.
Single-Event Kinetic Model for 1-Pentene Cracking on ZSM-5
Industrial & Engineering Chemistry Research 54 (2015), 11792-11803.
von Aretin., T., Standl, S., Tonigold, M., Hinrichsen, O.
Optimization of the product spectrum for 1-pentene cracking on ZSM-5 using single-event methodology. Part 1. Two-zone reactor
Chemical Engineering Journal 309 (2017), 886-897.
von Aretin, T., Standl, S., Tonigold, M., Hinrichsen, O.
Optimization of the product spectrum for 1-pentene cracking on ZSM-5 using single-event methodology. Part 2. Recycle reactor
Chemical Engineering Journal 309 (2017), 873-885.
Konferenzbeiträge
Vorträge:
von Aretin, T., Hinrichsen, O.
Single-Event Kinetic Model for Cracking and Isomerization of 1-Hexene on ZSM-5
AIChE Annual Meeting (2014), Atlanta, USA
von Aretin, T., Standl, S., Hinrichsen, O.
Reactor Optimization for Maximized Propene Yields in Olefines Cracking on ZSM-5 using Single-Event Methodology
9th International Conference on Chemical Kinetics (2015), Gent, Belgien.
von Aretin, T., Standl, S., Schallmoser, S., Lercher, J.A., Hinrichsen, O.
Single-Event Kinetic Model for 1-Pentene Cracking on ZSM-5
European Symposium on Chemical Reaction Engineering (2015), Fürstenfeldbruck.
Poster:
von Aretin, T., Hinrichsen, O.
Kinetic Modeling of Olefin Cracking
46. Jahrestreffen Deutscher Katalytiker (2013), Weimar
von Aretin, T., Hinrichsen, O.
Kinetic Modeling of Olefins Cracking
Colloquium on Chemical Reaction Engineering (2013), Mailand, Italien
von Aretin, T., Hinrichsen, O.
Kinetic Modeling of Hexene Cracking
47. Jahrestreffen Deutscher Katalytiker (2014), Weimar
von Aretin, T., Hinrichsen, O.
Kinetic Modeling of 1-Pentene Cracking on ZSM-5
48. Jahrestreffen Deutscher Katalytiker (2015), Weimar.