“…Herein 𝐸 𝑘𝑖𝑛 is the turbulent kinetic energy and 𝐸 𝜎 is the surface energy, with the density of the continuous phase 𝜌 𝑑 , the mean relative velocity 𝑢 ̅, the drop diameter 𝑑 In addition to these design improvements the application of the measurement technology has been extended to other multiphase flows and apparats, from extraction columns to mixer-settlers [29,30], reaction pumps [31], bubble columns [24,25,27,32], crystallization processes [28], evaporation [33] and spray regimes in distillation and absorption columns [34,35], where for the latter minor adaptions were necessary [36].…”