Simulation of biomass char gasification in a downdraft reactor for syngas production

A steady state, one‐dimensional computational fluid dynamics model of wood char gasification in a downdraft reactor is presented. The model is not only based on reaction kinetics and fluid flow in the porous char bed but also on equations of heat and mass conservation. An original OpenFOAM solver is...

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Published inAIChE journal Vol. 62; no. 4; pp. 1079 - 1091
Main Authors Ephraim, Augustina, Pozzobon, Victor, Louisnard, Olivier, Minh, Doan Pham, Nzihou, Ange, Sharrock, Patrick
Format Journal Article
LanguageEnglish
Published New York Blackwell Publishing Ltd 01.04.2016
American Institute of Chemical Engineers
Wiley
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Summary:A steady state, one‐dimensional computational fluid dynamics model of wood char gasification in a downdraft reactor is presented. The model is not only based on reaction kinetics and fluid flow in the porous char bed but also on equations of heat and mass conservation. An original OpenFOAM solver is used to simulate the model and the results are found to be in good agreement with published experimental data. Next, a sensitivity analysis is performed to study the influence of reactor inlet temperature and gas composition on char conversion, bed temperature profile and syngas composition. In addition, the evolution of the complex reaction mechanisms involved in mixed atmosphere gasification is investigated, and the most suitable operating parameters for controlling syngas composition are evaluated. Our simulation results provide essential knowledge for optimizing the design and operation of downdraft gasifiers to produce syngas that meets the requirements of various biofuel applications. © 2015 American Institute of Chemical Engineers AIChE J, 62: 1079–1091, 2016
Bibliography:Suez Environment and the French "Investments for the future" Program - No. ANR-10-LABX-22-01
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ArticleID:AIC15111
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SourceType-Scholarly Journals-1
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content type line 23
ISSN:0001-1541
1547-5905
DOI:10.1002/aic.15111