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Micromixing in a Rotor-Stator Spinning Disc Reactor
Arturo N Manzano Martínez1, Kevin M P van Eeten1, Jaap C Schouten1
1Laboratory of Chemical Reactor Engineering, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, P.O. Box 513, 5600 MB Eindhoven, The Netherlands.
Summary
This study quantifies micromixing times in a rotor-stator spinning disc reactor. Faster speeds significantly reduce mixing times, enabling enhanced process intensification beyond conventional equipment.
Area of Science:
- Chemical Engineering
- Fluid Dynamics
- Reaction Engineering
Background:
- Micromixing is crucial for controlling reaction outcomes in many chemical processes.
- Traditional reactors face limitations in achieving extremely short micromixing times.
- Rotor-stator spinning disc reactors offer potential for enhanced mixing.
Purpose of the Study:
- To determine micromixing times in a rotor-stator spinning disc reactor.
- To investigate the effect of rotational speed on mixing efficiency.
- To compare performance with theoretical models and conventional equipment.
Main Methods:
- Utilized the Villermaux-Dushman reaction scheme to assess mixing.
- Measured segregation indices at various disc rotational speeds.
- Calculated micromixing times using the engulfment model with self-engulfment.
- Correlated results with energy dissipation rates.
Main Results:
- Segregation index decreased as disc speed increased.
- Micromixing times ranged from 1.13 × 10-4 to 8.76 × 10-3 seconds.
- Results align with the theoretical dependence on energy dissipation rate (ε-0.5).
Conclusions:
- Rotor-stator spinning disc reactors achieve shorter micromixing times than traditional equipment.
- High energy dissipation rates in these reactors enable further reduction in mixing times.
- This technology facilitates process intensification for fast reactions.

