Abstract:The dependence of power consumption on baffle length, L, in vessels agitated by a dual Rushton turbine system was studied within the turbulent regime, and also in relation to the impeller spacing, DH. A dependence of varying strength could be observed. The presence of baffles in the agitated systems provided a stabilizing effect with regard to the dependence of the Newton number Ne on the Reynolds number Re. A sharp decrease in power consumption could be detected for baffle lengths L < 0.3 H, with H the liquid… Show more
“…Towards higher immersion depths, the increase of Ne over baffle length again leads to a stronger growing power consumption. Such results with sigmoidal behavior have been reported in literature for single Rushton turbines [34] as well as dual Rushton turbines [36]. The results of this study have been approximated for both types of baffles with a cubic equation:…”
“…Towards higher immersion depths, the increase of Ne over baffle length again leads to a stronger growing power consumption. Such results with sigmoidal behavior have been reported in literature for single Rushton turbines [34] as well as dual Rushton turbines [36]. The results of this study have been approximated for both types of baffles with a cubic equation:…”
“…It is used to describe the hydrodynamic behavior. The power number is reportedly not affected by spacing of the stirrers in unbaffled systems , .…”
Section: Theorymentioning
confidence: 95%
“…is defined by the dynamic viscosity h. It is used to describe the hydrodynamic behavior. The power number is reportedly not affected by spacing of the stirrers in unbaffled systems [30,31]. Gas-liquid reactors equipped with multiple impellers ensure a higher efficiency of gas utilization and a longer retention time [21].…”
Despite the fact that aerated stirred tank reactors are widely used in industry and often studied, their design and scale‐up still remains challenging. Especially the specific power input is a crucial and geometry‐dependent scale‐up parameter, usually calculated with the dimensionless power number Po. Within the scope of this study, the power number is measured for different stirrer types and configurations in a laboratory and an industrial‐scale aerated stirred tank reactor. Good agreements to literature are found for the unaerated case for the two‐stage stirrer configurations at different stirrer spacing for both scales. By literature only the aerated case in the laboratory scale can be predicted. Scale‐up of an aerated industrial‐scale reactor is challenging because of a specific influence of the aeration. In case of a three‐stage Rushton configuration, an asymmetrical distribution of the stirrers should be preferred to ensure a high power number as well as good power performance under aerated conditions.
“…For a triple Rushton turbine, the correlation between mixing time and baffle width was h 95~b -0. 33 . Both cases showed a dependency for the number of baffles as follows: h 95~nB -0.…”
Section: Theoretical Backgroundmentioning
confidence: 95%
“…The investigations aim to complete the power analyses that have already been carried out by the authors for slim reactors [1,31] [32] as well as for dual Rushton turbines [33]. This physically expected behavior is excellently predicted by the CFD simulations for the standard RCI.…”
Previous studies have shown the great potential, but also the great challenges, in handling slim reactors often used for polymerization reactions. Experiments and simulations were carried out in reactors with aspect-to-diameter ratios of up to 5, to test and to evaluate the mixing and dispersion efficiency for liquid-liquid systems of single-and multiple-stage impellers. Therefore, power consumption, mixing time and minimum dispersion speed were determined for five different stirrer types under turbulent conditions. It was found that the dimensionless mixing time is highly sensitive to the configuration of the impellers, with almost no dependency on the turbulent power number. Another focus was the analysis of the effect of the baffles. The influence of the baffle length in slim reactors on the mixing time and the macroscopic flow field was determined.
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