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The bed material was quartz sand (300 g, particle size 0.3 to 0.385 mm) with static height of 29 mm.
Several other factors influence the profiles, including the overall gas holdup, the volumetric overall gas liquid mass transfer coefficient, and the static height of liquid in the column.
A distance-independent diameter growth model and a static height model for Eucalyptus grandis in Zimbabwe were developed from spacing experiments designed as Nelder wheels and randomised complete blocks (RCB).
In this study, the lift coefficient, the lift drag ratio and the static height stability are chosen as the objective functions to obtain the optimal wing profiles of a WIG craft.
The radioactive particle tracking (RPT) technique is employed to explore the impact of the particle shape factor on the biomass distribution and velocity profiles when it is fluidized in a 152 mm diameter bed with a 228 mm static height.
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The combustion experiments were performed at 1 atm and 1223 K, in a fluidized bed (i.d. 120 mm) of sand (average diam. 325 μm) with static heights of 0.10 0.21 m.
The results show that the maximum spouting pressure drop increases with static bed height, entrainment zone height, draft tube diameter and fluidizing gas velocity.
Effects of spouting and fluidizing gas velocity, static bed height, entrainment zone height and draft tube diameter on the maximum spouting pressure drop, minimum stable spouting velocity and solids circulation rate were investigated.
If the static bed height is no more than 300 mm then the bed height has minimal effect on the fluidization characteristics.
f H is a static form height function.
The average pressure increased linearly with the static bed height.
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