Abstract
Stirred tank reactor yields are successfully described by the following model. The impeller is considered to act as a local micro‐mixer that perfectly mixes the recirculating stream down to the molecular level. All other portions of the vessel act as a large volume macro‐mixer, throughout which the impeller discharge stream remains completely segregated. Changes in overall conversion due to variations in mean residence time, impeller size, and rev./min. as predicted by this micro‐ and macro‐mixer model agree with Worrell's data for a relatively slow, second‐order, irreversible reaction.
Original language | English |
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Pages (from-to) | 723-727 |
Number of pages | 5 |
Journal | AIChE Journal |
Volume | 11 |
Issue number | 4 |
DOIs | |
State | Published - 1 Jan 1965 |
Externally published | Yes |
ASJC Scopus subject areas
- Biotechnology
- Environmental Engineering
- General Chemical Engineering