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The liquid solid mass transfer does not limit the overall reaction rate when a 20 ppi foam is used.
Results from the study shows that a great degree of mass transfer does occur in the region in the vicinity of the nozzle tip.
Apparently, the rate of mass transfer does not only depend on hydrodynamics but also on possible interaction between solute, solvent and sorbent.
It is also shown that for the air-water system breaking up the gas bubbles to increase the mass transfer does not have a large effect, due to rapid recoalescence of the bubbles.
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This implies that time-averaged hydrodynamics and mass transfer do not vary significantly regardless of changes in the frequency and amplitude of the slip velocity, because the effect is cancelled within the time oscillation period.
Macropore-diffusion affects activity and selectivity if pellets with dia > 2 mm are used; intracystalline mass-transfer does not seem to be important with respect to catalyst-activity and selectivity at temperatures below 600 K.
Most importantly, we show that, in a context of high mass resolution, the transfer does not significantly disturb isotopic ratios over large scanned fields provided external coils are properly adjusted to compensate ambient magnetic fields.
Intra-particle mass transfer thus does not appear to be a limiting step.
Increasing the aeration rate might improve the hydrodynamic conditions in the bioreactor and accelerate the mass transfer of DO, but it also detached the biofilm from the surface of bio-carrier, which reduced the consumption of DO, and accordingly, decreased the DO gradient in the bioreactor.
Furthermore, activation loss and mass transfer loss did not occur after 200 cycles.
A mass transfer correction did not improve the fit (data not shown).
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