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These parameters were measured as a function of the inlet temperature of the spouting gas (Tgi), the feed mass flow rate of the concentrated extract relative to mass flow rate of the spouting gas (Ws/Wg), the ratio between the feed flow rate of spouting gas relative to feed flow rate at a minimum spouting condition (Q/Qms) and the static bed height (H0).
The process variables studied were the ratio between the feed flow rate of the coating suspension to the spouting gas flow rate (Ws/Wg), the mass of capsules loaded to the equipment (M0), and the ratio between the spouting gas flow rate to the gas flow rate at minimum spouting condition (Q/Qms).
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The characteristic curve and minimum spouting conditions for a simulated conical bed, with glass particles of 6 mm diameter are compared with the experimental results showing deviations of 12.1% for the pressure drop and 5.6% for the minimum spouting velocity.
Initially, the discussion will concentrate on experimental studies emphasizing variation of minimum spouting and spout-fluidizing velocity, operating pressure, mixing and jet penetration length.
The results show that the minimum spouting velocity increases with cone angle, particle diameter and static bed height.
Minimum spouting velocity values obtained from full and half bed experiments resulted in a maximum 15% difference.
Proper design of such beds requires the prediction of various hydrodynamic characteristics, such as the minimum spouting velocity and maximum spoutable height.
The respective minimum spouting velocities are compared with experimental values and with values obtained through empirical correlations reported in the literature.
The voidage profiles above minimum spouting are found to follow a similarity relationship and an explicit equation for the circulation rate is developed using that relationship and the calculated voidage at the top of the spout.
The minimum spouting velocity increases with entrainment zone height, while it decreases with static bed height, draft tube diameter and fluidizing gas velocity.
The DEM simulation results indicate that the minimum spouting velocity (Ums) is almost the same for both wet and dry system, which agrees well with the prediction by a simplified formula.
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CEO of Professional Science Editing for Scientists @ prosciediting.com