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Modeling of growth rate dispersion of citric acid monohydrate in continuous crystallizers
Iowa State University.
1984 (English)In: AIChE Journal, ISSN 0001-1541, E-ISSN 1547-5905, Vol. 30, no 2, p. 280-287Article in journal (Refereed) Published
Abstract [en]

A mathematical model for prediction of the crystal size distribution from a continuous crystallizer is presented. The kinetic data used for the model were obtained from batch contact nucleation experiments with citric acid monohydrate. In these experiments, the distribution of growth rates as well as the initial size distribution were estimated. Results from the model indicate that the excess number of crystals usually present at small sizes in continuous crystallizers is due to growth rate dispersion (where crystals of the same size may have different growth rates) and not size dependent growth.

Place, publisher, year, edition, pages
1984. Vol. 30, no 2, p. 280-287
National Category
Bioprocess Technology
Research subject
Biochemical Process Engineering
Identifiers
URN: urn:nbn:se:ltu:diva-4822DOI: 10.1002/aic.690300217Local ID: 2d06a8c0-3efe-11de-bf5b-000ea68e967bOAI: oai:DiVA.org:ltu-4822DiVA, id: diva2:977696
Note
Upprättat; 1984; 20090512 (ysko)Available from: 2016-09-29 Created: 2016-09-29 Last updated: 2017-11-24Bibliographically approved

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Berglund, Kris

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