Abstract
Model of fluidized-bed crystallizer with axial dispersion, based on the crystal flux vector in particle phase space, is introduced. Computer simulations are performed and results are compared with experiment of Toyokura [1] and plug flow model from [2]. Values of parameters of crystal size distribution calculated, especially mass fraction and the mode, are very close to experiment.
| Translated title of the contribution | Axial dispersion in fluidized-bed crystallizer |
|---|---|
| Original language | Polish |
| Pages (from-to) | 1513-1518 |
| Number of pages | 6 |
| Journal | Chemical and Process Engineering - Inzynieria Chemiczna i Procesowa |
| Volume | 22 |
| Issue number | 3 E |
| Publication status | Published - 2001 |
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
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