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https://doi.org/10.1016/s0032-5910(01)00382-5
Copy DOIJournal: Powder Technology | Publication Date: Oct 18, 2001 |
Citations: 12 |
In this paper, a model was constructed in order to simulate the behaviour of slow growing crystals in high viscosity systems in a tower crystallizer. This type of crystallizer, ideally, is an application of the plug–flow concept. Plug–flow conditions are an advantage when a narrow crystal size distribution is the goal desired. The model was based on the following assumptions: steady state operation, no nucleation or growth rate dispersion, no breakage, size-dependent growth and settling of crystals. A simulation example for sucrose is presented although the model applies to other similar systems.
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