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The technical arrangement of the sample introduction system has been designed based on the fluidized bed concept.
The formation mechanisms of porous SiC layer are also discussed based on the fluidized bed-chemical vapor deposition principle.
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The mathematical model that we used in this study is composed of the continuity, momentum, energy, and species transfer equations to simulate the flow pattern and heat and mass transfer processes in the pharmaceutical drying processes based on the bubbling fluidized beds.
The technical design and operating conditions of the novel sample introduction system based on the fluidized-bed concept has been optimized.
The model is based on the description of the fluidized bed as a multistage crystallizer, in order to take into account the segregation and particles mixing within the bed.
A modified model considering the influence of spatial sensitivity of the electrodes is proposed to predict the particle charge density in the fluidized bed, based on the measured induced electrostatic current and pressure drop signals.
A predicting correlation for the minimum fluidization velocity in a supercritical water fluidized bed was obtained based on the experimental results of a fixed bed and the fluidized bed pressure drop.
The model presented is based on the Kunii Levenspiel theory for circulating fluidized bed and on the recent findings on the properties of CaO as a CO2 sorbent, while taking into account the effects of coal ash and sulfur species.
Recently, many novel reactor concepts based on membrane fluidized bed reactors have been proposed.
The method is based on the single micro-interactions occurring within the fluidized bed such as inter-particle collisions, droplet spread on the particle surface, aging of the deposited droplets and particle coalescence.
It was designed based on the principle of the atmospheric bubbling fluidized bed (Armesto et al. 2002).
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