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The technique is demonstrated by obtaining one- and two-dimensional images of bubbles rising in a model fluidized bed reactor.
Banholzer et al. [4], used a medical x-ray CT scanner to conduct a feasibility study on a model fluidized bed (43-mm ID and 150-mm long) under a range of experimental conditions.
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In this paper, the relationship between mass transfer coefficient, catalyst recycle rate and the internal structure, operating conditions are investigated in a φ300mm cold model fluidized bed.
Particles were dropped onto target specimens made of the same materials as were used in Part I as tube materials for cold model fluidized bed wear tests.
This paper presents results of an ongoing investigation into modelling fluidized dense-phase pneumatic conveying of powders.
Two approaches to modelling fluidized bed reactors were evaluated and compared in this work: a phenomenological 1D approach based on empirical closures and a more fundamental 2D approach based on computational fluid dynamics (CFD).
In the process developed model, a fast fluidized bed model and a bubbling fluidized bed model are used to respectively represent the oxidation reactor and the reduction reactor, while fluidized bed hydrodynamics and oxygen carrier redox reaction kinetics are considered to grasp the unique characteristics of CLAS process.
A Chebyshev super spectral viscosity method and operator splitting are used to solve a hyperbolic system of conservation laws with a source term modeling a fluidized bed.
A model a gas fluidized bed is considered which leads to a hyperbolic system of conservation laws with a source term.
The aim of this study is to develop a model of a fluidized bed granulator by combining the gas and particle dynamics with a simple model of particle wetting.
In this paper, a model of the fluidized bed polymerization reactor for linear low density polyethylene (LLDPE) production is developed using the Aspen Custom Modeler (ACM) to predict the polymer characteristics and flow behavior.
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