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A population balance approach considering heat and mass transfer—Experiments and CFD simulations

✍ Scribed by Eckhard Krepper; Matthias Beyer; Dirk Lucas; Martin Schmidtke


Book ID
113826010
Publisher
Elsevier Science
Year
2011
Tongue
English
Weight
906 KB
Volume
241
Category
Article
ISSN
0029-5493

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## Abstract The pressure drop and mass transfer efficiency for two‐phase flow in a structured packed column were simulated using a commercial CFD package, CFX version 10. The distillation of the methanol/isopropanol system was carried out in a 0.073 m diameter column, with an element composed of a