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Die Fokker‐Planck‐Gleichung zur Beschreibung von axialen Transport‐ und Mischvorgängen in Rohrreaktoren
Authors:Prof. Karl Sommer  Eva Schlosser  Prof. Dr.‐Ing. Heinz Dauth
Affiliation:1. Technische Universit?t München, Lehrstuhl für Verfahrenstechnik disperser Systeme, Maximus‐von‐Imhof‐Forum 2, 85354 Freising, Deutschland;2. Fachhochschule Ansbach, Fachbereich IBT, Residenzstra?e 8, 91522 Ansbach, Deutschland
Abstract:One way to explain the mechanism of powder mixing is the Fokker‐Planck equation. The equation comprises two decisive parameters, the transport coefficient U that depends on the active transport of the mixing device and the dispersion coefficient D which describes the mobility of the single particles. The idea is to calculate the dispersion and transport coefficient by using the powder characteristics. To verify this assumption, measurements with different components and different rotation speeds were made.
Keywords:Kalkstein  Kontinuierliche Prozesse  Konvektions‐Diffusions‐Modell  Mischen  Continuous processes  Convection diffusion model  Limestone  Mixing
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