Please use this identifier to cite or link to this item: http://repositorio.unicamp.br/jspui/handle/REPOSIP/86831
Type: Artigo de evento
Title: Fluidized Bed Reactor For Gasification Of Sugarcane Bagasse: Distribution Of Syngas, Bio-tar And Char
Author: Figueroa J.E.J.
Ardila Y.C.
Filho R.M.
Maciel M.R.W.
Abstract: A fluidized bed reactor to gasify sugarcane bagasse was designed and built in order to produce syngas. A study of the effect of two variables-ER ratio (defined as the ratio between the air flow introduced into the gasifier and the air stoichiometric flow required for complete combustion of the bagasse) and reaction temperature-on the product distribution (syngas, bio-tar and char) and syngas composition have been analyzed. The ER ratio has a positive effect on gas production, increasing production when a higher ER is used. The char yield decreased at higher temperatures and yield of bio-tar remained almost invariant regardless the value of ER. The amount of bio-tar in the syngas was very small, but it was found that the bio-tar was almost water (> 95 wt% of water). The highest ER promoted the production of larger quantities of hydrogen and carbon monoxide, while reducing the amount of carbon dioxide. Copyright © 2014,AIDIC Servizi S.r.l.
Editor: Italian Association of Chemical Engineering - AIDIC
Rights: fechado
Identifier DOI: 10.3303/CET1437039
Address: http://www.scopus.com/inward/record.url?eid=2-s2.0-84899429701&partnerID=40&md5=086dfcb26ce0298dbfc14a3bef7890d7
Date Issue: 2014
Appears in Collections:Unicamp - Artigos e Outros Documentos

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