Simple method for modeling the crystal size distribution (CSD) by solving a population balance equation in batch crystallization is presented. The kinetic parameters for nucleation and growth rates were estimated based on measurements of supersaturation using Mettler-Toledo RC1 reaction calorimeter and CSD was determined through image analysis.
|Number of pages||6|
|Journal||Inzynieria Chemiczna i Procesowa|
|Issue number||3 II|
|Publication status||Published - 2004|
ASJC Scopus subject areas
- Chemical Engineering(all)