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In this paper a numerical simulation study of dynamic behavior of a fluidized bed with liquid injection is presented.
A two-phase model is proposed for describing the behavior of a fluidized bed reactor used for polyethylene production.
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.
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.
It reduces to the conventional two-fluid model (TFM) if local equilibrium or homogeneity is assumed within each grid, and reverts to the energy-minimization multi-scale (EMMS) model if it is used to describe global behavior of a fluidized bed.
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Vahidi and Shahrokhi [9] studied the dynamic behavior and control of a fluidized bed reactor for polyethylene production.
It is important to understand the flow hydrodynamics behavior of a circulating fluidized bed (CFB) reactor for efficient operation.
In the present study, nonlinear hydrodynamic behavior of a circulating fluidized bed with a riser 0.10 m in inner diameter and 10 m in height was characterized in terms of the Hurst exponent and V statistic obtained by the R/S analysis, as well as Mann–Whitney statistic determined by short-term predictability analysis.
High speed photographs were studied to describe bubbling behavior in a fluidized bed over a range of pressures.
An innovative method using a micro-three-dimensional acceleration sensor and a micro-three-dimensional gyroscope to trace the motion behavior of a large object in the dense zone of a fluidized bed is proposed here.
Then several PTSs, served as object spies delivering in situ information they detect, are utilized to study the motion behavior of spherical and non-spherical objects on the inclined air distributor of a fluidized bed.
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