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In the proposed model, the bed is divided into several sequential sections.
In the proposed model, the bed is divided into several sections consisting of bubble and emulsion phases.
In the proposed model, the bed is divided into several sequential sections where flow of the gas is considered to be plug flow through the bubbles and perfectly mixed through the emulsion phase.
Also, the well-established design model, the Bed depth service time (BDST) model was used to analyze the experimental data.
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Before modeling the bed occupancy, we examined whether the series was stationary.
In this model, the amalgamated beds and beds with lingulid brachiopods, heavy minerals and P-clasts result from the superposition of several sea-level rise episodes of VHF cycles, occurring within the retrogradation phase of a HF cycle.
The physical model of the bed main body is established, as depicted in Figure 10.
A detailed model for the bed can be written from the basic mass balance equations.
Open image in new window Figure 10 Physical model of the bed main body Open image in new window Figure 11 Force routines and bed main structure.
A model of the bed is shown to predict observed energy consumption.
The choice of the turbulence model and the bed load coefficient in the Meyer-Peter & Müller formula are of great importance.
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