A model is presented which relates the crystal size distribution (CSD) from a mixed-suspension, mixed-product-removal (MSMPR) crystallizer to the distribution of growth rates. This model is based on the assumption that individual contact nuclei have some inherent growth rate which remains constant,
Modeling of growth rate dispersion of citric acid monohydrate in continuous crystallizers
β Scribed by K. A. Berglund; M. A. Larson
- Publisher
- American Institute of Chemical Engineers
- Year
- 1984
- Tongue
- English
- Weight
- 623 KB
- Volume
- 30
- Category
- Article
- ISSN
- 0001-1541
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The influence of growth rate dispersion on the product-size distribution of batch cooling crystallization is investigated by computer simulations. The model accounts for primary and magma density-dependent secondary nucleation, and growth rate dispersion of the constant crystal growth type. The mode
Empirical size-dependent growth rate models are studied for their effect on the population density distributions from a continuous, mixed suspension, mixed product removal (CMSMPR) crystallizer. The growth rate models and/or their corresponding population density distributions are examined for conti