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 |
|---|---|
| Pages (from-to) | 723-727 |
| Number of pages | 5 |
| Journal | AICHE Journal |
| Volume | 11 |
| Issue number | 4 |
| DOIs | |
| State | Published - Jul 1965 |
| Externally published | Yes |