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- W2136361569 abstract "A laboratory continuous mixed suspension salting out crystallizer was designed and constructed to test the dynamic crystallization model proposed by Randolph and Larson. The model relates the crystal size distribution to nucleation and growth kinetics and operating conditions. The ammonium alum-ethanol-water system was selected because of its ease of operation and control.The results of this work were in agreement with the steady state model. Under the conditions of these experiments, it was found that the nucleation rate dNo/dt was related to the growth rate r by dNo/dt = k1r2. The crystallizer was also operated under unsteady state conditions which resulted from variations in the production rate. The theoretical model with experimentally determined parameters was simulated on an analog computer and solved for production rate changes. The results indicated that the model was in agreement with the dynamic data for production rate upsets." @default.
- W2136361569 created "2016-06-24" @default.
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- W2136361569 date "1965-07-01" @default.
- W2136361569 modified "2023-09-26" @default.
- W2136361569 title "Size distribution dynamics in a salting out crystallizer" @default.
- W2136361569 doi "https://doi.org/10.1002/aic.690110431" @default.
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