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Powder technology, 2018-01, Vol.323, p.238-249
2018

Details

Autor(en) / Beteiligte
Titel
Discrete particle simulation of food grain drying in a fluidised bed
Ist Teil von
  • Powder technology, 2018-01, Vol.323, p.238-249
Ort / Verlag
Lausanne: Elsevier B.V
Erscheinungsjahr
2018
Link zum Volltext
Quelle
Access via ScienceDirect (Elsevier)
Beschreibungen/Notizen
  • Drying is a common practice for post-harvest processing of food grains. Fluidised beds are often adopted for this purpose. It is of importance to understand the fluidised bed drying process for improving its energy efficiency. This work establishes a numerical drying model based on the combined approach of computational fluid dynamics and discrete element method for describing heat and mass transfer in the gas-solid flow system. Water evaporation is modelled in resemblance to a chemical reaction, thereby requiring fewer model parameters. The model is first described in detail. Then it is tested by comparing model predictions with those experimental data of corn kernel from the literature. General drying characteristics including grain and air moisture contents are reproduced qualitatively. The predicted drying rate curves are quantitatively comparable with those of experimental data. Finally, the effects of inlet air velocity and temperature are examined. The model predictions confirm that the drying rate increases with both the inlet air velocity and temperature. However, the drying product quality, here represented by the standard deviation of grain moisture distribution, increases with increasing air velocity or decreasing air temperature. This grain scale model would be useful to the design and control of the drying process. [Display omitted] •A CFD-DEM based model is developed for drying food particles in a fluidised bed.•A high air velocity or a high air temperature can reduce the drying period.•A high air velocity or low air temperature improves the drying product quality.

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