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The development of a heterogeneous model describing the behavior of the fluidized bed reactor in polymer production is presented.
The tools and methods for evaluating or simulating the behavior of the fluidized bed heat exchanger (HEX) and the dense particle flow within it are explained along with criteria for the selection of storage powders.
The behavior of the fluidized catalytic cracking process is playing a main part on the overall benefits of refinery units and improving in process or control of fluidized catalytic cracking plants will result in exciting benefits economically.
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A two-phase bubbling bed model is employed to describe quantitatively the behavior of the catalytic fluidized bed.
The lack of accurate, instantaneous, and simultaneous techniques for measurement along the bed cross section prevents a precise description of the dynamic flow behavior in the fluidized bed.
Observations of the fluidized bed behavior following the addition of the dispersed glycerol are also discussed.
In this paper we investigate the behavior of a fluidized bed of silica nanoparticles under the influence of externally applied vibrations and an electrostatic field.
A two-phase model is proposed for describing the behavior of a fluidized bed reactor used for polyethylene production.
The behavior of a fluidized bed is modeled using a "two-fluid" theory, which involves conservation of mass, momentum, energy and species equations for the two interpenetrating continua.
The results effectively support the reliability of collision behavior research between fluidized solid particles and tube walls by vibration signals analysis, which lays the foundation of reasonable design and further application of the fluidized bed evaporator.
The internal dimensions of the fluidized bed are (0.42times 0.38~hbox {m}).
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com