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Computational fluid dynamics modelling of biomass fast pyrolysis in fluidised bed reactors, focusing different kinetic schemes

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dc.contributor.author Panneerselvam, Ranganathan
dc.contributor.author Sai Gu
dc.date.accessioned 2017-03-30T06:31:42Z
dc.date.available 2017-03-30T06:31:42Z
dc.date.issued 2016-02-16
dc.identifier.citation Bioresource Technology, 213:333–341 en_US
dc.identifier.uri http://hdl.handle.net/123456789/2708
dc.description.abstract The present work concerns with CFD modelling of biomass fast pyrolysis in a fluidised bed reactor. Initially, a study was conducted to understand the hydrodynamics of the fluidised bed reactor by investigating the particle density and size, and gas velocity effect. With the basic understanding of hydrodynamics, the study was further extended to investigate the different kinetic schemes for biomass fast pyrolysis process. The Eulerian–Eulerian approach was used to model the complex multiphase flows in the reactor. The yield of the products from the simulation was compared with the experimental data. A good comparison was obtained between the literature results and CFD simulation. It is also found that CFD prediction with the advanced kinetic scheme is better when compared to other schemes. With the confidence obtained from the CFD models, a parametric study was carried out to study the effect of biomass particle type and size and temperature on the yield of the products. 2016 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY-NC-NDlicense en_US
dc.language.iso en en_US
dc.publisher Elsevier en_US
dc.subject Biomass en_US
dc.subject Fast pyrolysis en_US
dc.subject Fluidised bed en_US
dc.subject CFD en_US
dc.subject Multiphase flows en_US
dc.title Computational fluid dynamics modelling of biomass fast pyrolysis in fluidised bed reactors, focusing different kinetic schemes en_US
dc.type Article en_US


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