Deutsch
 
Hilfe Datenschutzhinweis Impressum
  DetailsucheBrowse

Datensatz

DATENSATZ AKTIONENEXPORT

Freigegeben

Konferenzbeitrag

A theoretical analysis of oscillations and dynamic instabilities in continuous fluidized bed spray granulation

MPG-Autoren
/persons/resource/persons86440

Radichkov,  R.
Process Synthesis and Process Dynamics, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;

/persons/resource/persons86359

Kienle,  A.
Process Synthesis and Process Dynamics, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;
Otto-von-Guericke-Universität Magdeburg, External Organizations;

/persons/resource/persons86412

Müller,  T.
Process Synthesis and Process Dynamics, Max Planck Institute for Dynamics of Complex Technical Systems, Max Planck Society;
Otto-von-Guericke-Universität Magdeburg, External Organizations;

Externe Ressourcen
Es sind keine externen Ressourcen hinterlegt
Volltexte (beschränkter Zugriff)
Für Ihren IP-Bereich sind aktuell keine Volltexte freigegeben.
Volltexte (frei zugänglich)
Es sind keine frei zugänglichen Volltexte in PuRe verfügbar
Ergänzendes Material (frei zugänglich)
Es sind keine frei zugänglichen Ergänzenden Materialien verfügbar
Zitation

Radichkov, R., Kienle, A., Heinrich, S., Müller, T., Peglow, M., & Mörl, L. (2005). A theoretical analysis of oscillations and dynamic instabilities in continuous fluidized bed spray granulation. In Proceedings of the 3rd Nordic Drying Conference.


Zitierlink: https://hdl.handle.net/11858/00-001M-0000-0013-9C15-9
Zusammenfassung
The main goal of this work is the theoretical prediction and qualitative analysis of the nonlinear behavior of fluidized bed granulation with external classification. First a new population balance model including a mass balance of the fluidized bed unit has been developed. Using methods from nonlinear systems analysis, such as a numerical bifurcation and stability analysis, unstable regions in the parameter space have been predicted. Due to the simplicity of the model the presented results are only qualitative. Future research will concentrate more on a quantitative investigation of the nonlinear process behavior with more detailed models and experimental validation.