Fluidized Bed Reactor For Gasification Of Sugarcane Bagasse: Distribution Of Syngas, Bio-tar And Char

dc.creatorFigueroa J.E.J.
dc.creatorArdila Y.C.
dc.creatorFilho R.M.
dc.creatorMaciel M.R.W.
dc.date2014
dc.date2015-06-25T17:55:26Z
dc.date2015-11-26T14:38:21Z
dc.date2015-06-25T17:55:26Z
dc.date2015-11-26T14:38:21Z
dc.date.accessioned2018-03-28T21:43:19Z
dc.date.available2018-03-28T21:43:19Z
dc.identifier
dc.identifierChemical Engineering Transactions. Italian Association Of Chemical Engineering - Aidic, v. 37, n. , p. 229 - 234, 2014.
dc.identifier19749791
dc.identifier10.3303/CET1437039
dc.identifierhttp://www.scopus.com/inward/record.url?eid=2-s2.0-84899429701&partnerID=40&md5=086dfcb26ce0298dbfc14a3bef7890d7
dc.identifierhttp://www.repositorio.unicamp.br/handle/REPOSIP/86831
dc.identifierhttp://repositorio.unicamp.br/jspui/handle/REPOSIP/86831
dc.identifier2-s2.0-84899429701
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1249538
dc.descriptionA 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.
dc.description37
dc.description
dc.description229
dc.description234
dc.descriptionAkay, G., Jordan, C.A., Gasification of fuel cane bagasse in a downdraft gasifier: Influence of lignocellulosic composition and fuel particle size on syngas composition and yield (2011) Energy & Fuels, 25, pp. 2274-2283
dc.descriptionDias, M.O.S., Junqueira, T.L., Cavalett, O., Cunha, M.P., Jesus, C.D.F., Mantelatto, P.E., Rossell, C.E.V., Bonomi, A., Cogeneration in integrated first and second generation ethanol from sugarcane (2013) Chemical Engineering Research and Design, 91, pp. 1411-1417
dc.descriptionDias, M.O.S., Junqueira, T.L., Cavalett, O., Pavanello, L.G., Cunha, M.P., Jesus, C.D.F., Maciel Filho, R., Bonomi, A., Biorefineries for the production of first and second generation ethanol and electricity from sugarcane (2013) Applied Energy, 109, pp. 72-78
dc.descriptionJaimes Figueroa, J.E., Ardila, Y.C., Hoss Lunelli, B., Maciel Filho, R., Wolf Maciel, M.R., Evaluation of pyrolysis and steam gasification processes of sugarcane bagasse in a fixed bed reactor (2013) Chemical Engineering Transactions, 32, pp. 925-930. , DOI: 10.3303/CET1332155
dc.descriptionPaudel, B., Feng, Z.-G., Prediction of minimum fluidization velocity for binary mixtures of biomass and inert particles (2013) Powder Technology, 237, pp. 134-140
dc.descriptionSluiter, A., Hames, B., Ruiz, R., Scarlata, C., Sluiter, J., Templeton, D., Crocker, D., (2008) Determination of structural carbohydrates and lignin in biomass, , Laboratory Analytical Procedure (LAP), NREL/TP-510-42618, revised July 2012
dc.descriptionWen, C.Y., Yu, Y.H., A generalized method for predicting the minimum fluidization velocity (1966) AIChE Journal, 12, pp. 610-612
dc.languageen
dc.publisherItalian Association of Chemical Engineering - AIDIC
dc.relationChemical Engineering Transactions
dc.rightsfechado
dc.sourceScopus
dc.titleFluidized Bed Reactor For Gasification Of Sugarcane Bagasse: Distribution Of Syngas, Bio-tar And Char
dc.typeActas de congresos


Este ítem pertenece a la siguiente institución