Thomas H. van den BergStefan LutherDaniel P. LathropDetlef Lohse
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 Re=7 x 10(4) and Re=10(6) after having injected (i) small bubbles (R=1 mm) up to a volume concentration of alpha=5% and (ii) buoyant particles (rhop/rhol=0.14) 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 Re=10(6). 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.
Arnout FrankenSagy EphratiPaolo CifaniBernard J. Geurts
Pim A. BulleeRuben A. VerschoofDennis BakhuisSander G. HuismanChao SunRob G. H. LammertinkDetlef Lohse
Yuichi MuraiHiroshi OiwaYasushi Takeda
Detlef LohseThomas H. van den BergDennis P. M. van GilsDaniel P. Lathrop
Rodrigo EzetaDennis BakhuisSander G. HuismanChao SunDetlef Lohse