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The geometry and size was found to influence the gas velocity pattern as well as the extraction efficiency.
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The surfactant-assisted flow improvement is dependent on gas liquid ratio, gas velocity and two-phase flow pattern.
In this way, the influence of the superficial gas velocity, liquid height and aeration pattern on the column flow structure was analysed.
A series of 2D simulations were conducted to study the effects of gas velocity and tube arrangement on the flow pattern.
In a fluidized bed, the granules show a fluidization pattern depending on the geometry of the gas inlet, the gas velocity, characteristics of the particles, the dryer design, etc. Computational Fluid Dynamics (CFD) allows to model this behaviour.
Some underestimation of the pressure gradient is observed for the highest values of the superficial gas velocity and operating pressure due to the droplets entrainment and the wavy pattern of the gas liquid interface that are not taken into account.
These measurements have been used to identify flow regime transitions, variations in flow patterns and local hydrodynamic structure as obtained with different gas distributors and varying gas velocity.
The 'Flow Pattern Parameter (FPP)' consists of particle kinetic energy, bed aspect ratio (H/D), pore size of air distributor, minimum fluidization velocity, and superficial gas velocity.
Fluidizing gas velocity (m s-1).
Particle velocity also increases linearly with the gas velocity.
Experimental observations show that the flow pattern is elongated bubble flow and no small dispersed bubbles exist in the liquid slug in conditions of 0.168 0.672 m s−1 superficial liquid velocity and 0.04 0.32 m s−1 superficial gas velocity.
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