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The particle and liquid loading were varied in order to determine the effect of phase hold up on bed homogeneity.
We achieved a dispersed phase hold up inside the active extraction part up to 50%, and a specific surface of over 3000 m2/m3.
Correlations have been developed, using nonlinear regression, for the prediction of drop diameter, dispersed phase hold up, terminal rise velocity and jetting velocity.
It has been observed that the drop diameter, dispersed phase hold up, terminal rise velocity and jetting velocity increase with an increase in nozzle diameter.
Also, dispersed phase hold up increases with dispersed phase velocity whereas terminal rise velocity and drop diameter show a marginal dependency.
The influence of operating parameters, such as phase hold up, phase mixing, aspect ratio and superficial gas velocity, on an aerobic biodegradation in a bioreactor of 0.16 m i.d. and 2.7 m in height, was analysed.
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A second phase, held in in Croton last week, netted 29 more weapons in six hours, at a cost of $1,225.
Further the average rate passes through a maximum as the dispersed phase hold-up is increased.
Effects at low dispersed phase hold-up were observed to be very strong and are thus important, but were not taken into account in further analysis of the effect of dispersed phase hold-up on mass transfer.
Effects of phase hold-ups and particle mixing are addressed, as well as liquid and gas superficial velocities.
Empirical correlations have been developed for fractional dispersed phase hold-up and dispersed side mass transfer coefficients.
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