Abstract
In this study we present a measuring method and extensive experimental data on the gas phase RTD in a mechanically agitated gas-liquid reactor with standard dimensions over a wide range of superficial gas velocities, agitation rates and agitator sizes. The results are modelled successfully, using the weighed moments method, by a simple RTD model of one mixer in series with a plug flow zone. All results are correlated in one relation, which can be used for scale-up.
Original language | Undefined |
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Pages (from-to) | 3339-3346 |
Number of pages | 8 |
Journal | Chemical engineering science |
Volume | 47 |
Issue number | 13 |
DOIs | |
Publication status | Published - 1992 |
Keywords
- METIS-105844
- IR-10801