Crystal size distribution in precipitates
โ Scribed by Prof. W. J. Dunning
- Publisher
- John Wiley and Sons
- Year
- 1973
- Tongue
- English
- Weight
- 546 KB
- Volume
- 8
- Category
- Article
- ISSN
- 0232-1300
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โฆ Synopsis
Abstract
After a short introduction on the principles of nucleation and growth โ here especially considering defect crystals โ particle size distribution in precipitates is discussed. At first batch crystallization is referred to briefly. The situation in stirred continuous tank crystallizers is investigated in detail. Size distribution is considered in dependence on steady state flow rates of the reacting solutions, residence time of crystals in the tank, resulting in an exponential equation for the number of crystals per unit volume: \documentclass{article}\pagestyle{empty}\begin{document}$ n\left(r \right) = \frac{{\dot n_0 }}{{f\left(s \right)}}e^ - \frac{{vr}}{{V \cdot f\left(s \right)}} $\end{document}. With two and more tanks in series size distribution additionally becomes dependent on the difference of the supersaturations, of the occurrence of nucleation, and of the residence time of crystals in the various tanks. Equations for the size distribution are given for special conditions with two and more tanks in series.
๐ SIMILAR VOLUMES
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
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