4.7 Article

Hydrodynamics of cold-rig biomass gasifier using semi-dual fluidized-bed

Journal

POWDER TECHNOLOGY
Volume 234, Issue -, Pages 97-106

Publisher

ELSEVIER
DOI: 10.1016/j.powtec.2012.09.022

Keywords

Gasification; Semi-dual fluidized-bed (sDFB); Solid circulation rate; Internal mixing; Computational fluid dynamics (CFD); Eulerian-Eulerian model

Funding

  1. Ministry of Knowledge Economy, Korea

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This study reports a semi-dual fluidized-bed (sDFB) biomass gasifier, which is a novel design of dual fluidized-bed (DFB) with the internal mixing of solid particles between riser and gasifier to enhance the heat and mass transfer. A cold-rig experiment of sDFB (0.8 m width x 0.2 m depth x 3.85 m height) was performed to investigate fluid hydrodynamics and solid circulations. Pressures were sampled at 43 points along the sDFB gasifier. An external circulation rate of sand was measured for 60 s after 2 min of the operating time. In order to estimate the amount of direct back-mixing particles through the gasifier-riser interconnection area, an Eulerian-Eulerian two-dimensional computational fluid dynamics (CFD) model was developed for the cold-rig sDFB. This CFD model included the kinetic theory of granular flow and the k- dispersed turbulence model. The CFD simulation results were validated with the experiment data. About 17% back-mixing of particles through the gasifier-riser interconnection area were obtained from the CFD simulation. This indicates that the sDFB has a possibility of having higher heat and mass transfer than the conventional DFB. (C) 2012 Elsevier B.V. All rights reserved.

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