Erdem Simsek
Ruhr University Bochum
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Featured researches published by Erdem Simsek.
Journal of Pressure Vessel Technology-transactions of The Asme | 2006
Harald Kruggel-Emden; S. Wirtz; Erdem Simsek; Viktor Scherer
The discrete element method can be used for modeling moving granular media in which heat and mass transport takes place. In this paper the concept of discrete element modeling with special emphasis on applicable force laws is introduced and the necessary equations for heat transport within particle assemblies are derived. Possible flow regimes in moving granular media are discussed. The developed discrete element model is applied to a new staged reforming process for biomass and waste utilization which employs a solid heat carrier. Results are presented for the flow regime and heat transport in substantial vessels of the process.
Journal of Pressure Vessel Technology-transactions of The Asme | 2007
Harald Kruggel-Emden; Erdem Simsek; S. Wirtz; Viktor Scherer
Based on LEAT’s discrete element codes, granular flow and mixing on conveying equipment are studied in two and three dimensions. Discrete element simulations, which are briefly introduced, provide detailed information on particle positions and velocities over time. This information is used to derive quantities characterizing the dynamic process of mixing. The main focus of the study presented is the mixing process of inhomogeneous particle ensembles on different grate types. For this purpose, the introduced mixing parameters are used to compare the mixing in a 3D situation with the corresponding 2D approximation on identical grates and to compare different grate designs in two dimensions.
Particulate Science and Technology | 2008
Erdem Simsek; S. Wirtz; Viktor Scherer; Harald Kruggel-Emden; Rafal Grochowski; Peter Walzel
The mixing of thin granular layers transported on the surface of an oscillating trough is experimentally and numerically examined. The particle dispersion was experimentally quantified by an image processing system recording the growth of the mixing layer thickness of two differently colored but otherwise identical sand particle streams along the longitudinal position within the transporting channel. Granular flow and dispersion on the vibrating conveyor were studied numerically based on a three-dimensional discrete element code. Both experiments and simulations were used to derive quantities characterizing the transversal dispersion. The mixing was found to be directly proportional to the vertical acceleration of the conveyor and inversely proportional to the mass flow of the transported material. Keeping the above-mentioned parameters constant, the dispersion increases with increasing mean particle diameter. When performing the experiments with materials of different mean particle diameters and tuning the mass flow to achieve the same level of dimensionless bed height, the magnitude of the dispersion coefficient remains constant, as was also confirmed by the numerical simulation.
ASME 2006 Pressure Vessels and Piping/ICPVT-11 Conference | 2006
Harald Kruggel-Emden; Erdem Simsek; S. Wirtz; Viktor Scherer
Based on LEAT’s discrete element codes, granular flow and mixing on conveying equipment is studied in two and three dimensions. Discrete element simulations, which are briefly introduced, provide detailed information on particle positions and velocities over time. This information is used to derive quantities characterizing the dynamic process of mixing. The main focus of the study presented is the mixing process of inhomogeneous particle ensembles on different grate types. For this purpose the introduced mixing parameters are used to compare the mixing in a 3D situation with the corresponding 2D approximation on identical grates and to compare different grate designs in two dimensions.Copyright
Powder Technology | 2007
Harald Kruggel-Emden; Erdem Simsek; S. Rickelt; S. Wirtz; Viktor Scherer
Powder Technology | 2009
Erdem Simsek; B. Brosch; S. Wirtz; Viktor Scherer; F. Krüll
Chemical Engineering Science | 2010
T. Bluhm-Drenhaus; Erdem Simsek; S. Wirtz; Viktor Scherer
Powder Technology | 2011
Florian Sudbrock; Erdem Simsek; S. Rickelt; S. Wirtz; Viktor Scherer
Powder Technology | 2010
Florian Sudbrock; Erdem Simsek; S. Wirtz; Viktor Scherer
Powder Technology | 2012
Erdem Simsek; Florian Sudbrock; S. Wirtz; Viktor Scherer