Abstract
The liquid–liquid flow behaviour and mass transfer rates for a rotor–stator spinning disc reactor are reported. The measured mass transfer rate is at least 25 times higher compared to packed column. This makes that the rotor–stator spinning disc reactor is a promising multiphase reactor.
Original language | English |
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Pages (from-to) | 267-243 |
Number of pages | 7 |
Journal | Chemical Engineering Journal |
Volume | 185-186 |
DOIs | |
Publication status | Published - 2012 |