Abstract
In Taylor-Couette flow the total energy dissipation rate and therefore the drag can be determined by measuring the torque on the system. We do so for Reynolds numbers between and after having injected (i) small bubbles () up to a volume concentration of and (ii) buoyant particles () of comparable volume concentration. In case (i) we observe a crossover from little drag reduction at smaller Re to strong drag reduction up to 20% at . In case (ii) we observe at most little drag reduction throughout. Several theoretical models for bubbly drag reduction are discussed in view of our findings.
- Received 21 September 2004
DOI:https://doi.org/10.1103/PhysRevLett.94.044501
©2005 American Physical Society