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Further experimental and modeling efforts are required in a comparable time and space resolutions for the validation of CFD models for fluidized bed reactors.
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Sedimentation and fluidization: part I. Transactions of the Institution of Chemical Engineers 32, 35] empirical correlation, and Mazzei et al. [2006. A revised mono-dimensional particle bed model for fluidized beds.
The simplified non-isothermal model for fluidized bed reactors developed earlier (Parts I, II) is extended here to the case of exothermic consecutive reaction, A → B → C. It is shown that simple adiabatic operation is not possible when the second reaction, B →- C is relatively fast because the desired operating temperature corresponds to an unstable steady state.
A new mathematical model is being proposed in this paper that gives relatively better results compared to the prevailing models for bubbling fluidized bed reactors utilizing Geldart B particles.
This paper describes the complete production process for solar cells, highlights challenges relevant to systems engineering, and overviews work in three distinct areas: the application of real time optimization in silicon production, the development of scale-up models for a fluidized bed poly-silicon process and a new process concept for silicon wafer production.
Models in the literature for fluidized bed coal combustors are tabulated and examined with regard to their critical assumptions.
A predictive model of the radiation distribution for fluidized bed photocatalytic reactors was proposed and solved by means of the Monte Carlo approach coupled with the ray tracing technique.
The lumped model developed in the earlier paper, for fluidized bed steam-oxygen-char gasification is modified by taking into consideration the bubbling nature of the fluid flow.
The present work describes a comprehensive mathematical model for simulating fluidized bed polypropylene reactors.
This paper presents a predictive aggregation rate model for spray fluidized bed melt granulation.
An improved coupling method is proposed to ensure mass conservation in a previously developed DPM-CFD model (C.L. Wu et al., Three-dimensional discrete particle model for gas solid fluidized bed on unstructured mesh, Chemical Engineering Journal 152 (2009), 514 529).
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