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Journal ArticleDOI

Residence time distribution of solids in multistage fluidisation

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TLDR
In this paper, the residence time distribution of the solids in multistage fluidisation, wherein downcomers for transferring solids from stage to stage are provided to the horizontal perforated plates, is experimentally investigated covering a wide range in process variables using flat, baffle and spiral plates developed in the study.
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This article is published in Chemical Engineering Science.The article was published on 1982-01-01. It has received 15 citations till now. The article focuses on the topics: Residence time distribution & Baffle.

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Citations
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Journal ArticleDOI

Production of hydrogen and carbon nanotubes from methane decomposition in a two-stage fluidized bed reactor

TL;DR: In this article, a two-stage fluidized bed reactor with Ni/Cu/Al 2 O 3 catalyst was used to decompose methane with high activity in the high temperature condition and then the carbon produced will diffuse effectively to form carbon nanotubes in both low and high temperature regions.
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Stochastic models for transport in a fluidized bed

TL;DR: It turns out that discretization of the reactor into a moderate number of segments already gives excellent numerical approximations to the continuous model, and in the diffusion limit a partial differential equation for the particle density p(t,x) is obtained.
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Hydrodynamic and solids residence time distribution in a binary bubbling fluidized bed: 3D computational study coupled with the structure-based drag model

TL;DR: In this paper, the simulation of bubbling fluidized beds (BFB) residence time distribution (RTD) based on the structure-based drag model is conducted for the single and binary gas-solid phases systems, a comparison of computed results with experimental data proves that their model is applicable to both systems with better accuracy.
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Residence Time Distribution of Solids in a Fluidized Bed

TL;DR: In this paper, a single-stage fluidized bed provided with an internal, using uniformly sized particles and a binary solid mixture, varying gas flow rate, solids rate, bed height, dilution and the bed geometry has been determined.
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CFD simulation of solids residence time distribution in a multi-compartment fluidized bed

TL;DR: In this paper, a numerical investigation of the solids residence time distribution and the fluidized structure of a multi-compartment fluidized bed, in which the flow pattern is proved to be close to plug flow by using computational fluid dynamics (CFD) simulations.
References
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A model for residence time distribution in multistage systems with cross-flow between active and dead regions

TL;DR: In this paper, a three-parameter mathematical model for expressing the residence time distribution in multistage systems is proposed, in which a fraction of the feed short-circuits each stage consists of an active backmix region and a dead region with cross-flow of the material between the two regions.
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Pressure drop of the fluid and the flow patterns of the phases in multistage fluidisation

TL;DR: In this paper, the authors discussed the theoretical models, experimental data and the range of applicability along with the correlations to predict the characteristics of the bed and discussed the correlations with respect to the theoretical model and experimental data.
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An experimental investigation of the residence time distribution of solids in multistage fluidisation

TL;DR: In this paper, the cross-flow model was matched with the experimental data taken subsequently on the residence time distribution of solids in a multistage fluidised bed, and conditions for smooth fluidisation were suggested.
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