Mostrar el registro sencillo del ítem

dc.contributor.author
Ibarra, Álvaro
dc.contributor.author
Rodríguez, Elena
dc.contributor.author
Sedran, Ulises Anselmo
dc.contributor.author
Arandes, José M.
dc.contributor.author
Bilbao, Javier Ignacio
dc.date.available
2019-06-21T02:09:07Z
dc.date.issued
2016-02
dc.identifier.citation
Ibarra, Álvaro; Rodríguez, Elena; Sedran, Ulises Anselmo; Arandes, José M.; Bilbao, Javier Ignacio; Synergy in the Cracking of a Blend of Bio-oil and Vacuum Gasoil under Fluid Catalytic Cracking Conditions; American Chemical Society; Industrial & Engineering Chemical Research; 55; 7; 2-2016; 1872-1880
dc.identifier.issn
0888-5885
dc.identifier.uri
http://hdl.handle.net/11336/78621
dc.description.abstract
The catalytic cracking of a blend of raw bio-oil (20 wt %) from black poplar sawdust fast pyrolysis and vacuum gasoil (VGO, 80 wt %) has been studied. The runs have been performed in a riser simulator reactor (RSR) under fluid catalytic cracking (FCC) conditions; that is, 500-560 °C, catalyst to feed mass ratio of 6 g cat ( g feed) -1 on a dry basis, reaction times of 3-10 s and a equilibrated commercial FCC catalyst. The cofeeding effect has been quantified by comparing the yields of product lumps and individual components in the gaseous fraction and gasoline lump in the cracking of VGO, raw bio-oil, and their blend (20% bio-oil/80% VGO), at the same conversion values (60-70 wt %). The cofeeding has a favorable synergy because it promotes the formation of C 3 -C 4 and gasoline (C 5 -C 12 ) hydrocarbon lumps, attenuating the formation of CO 2 , CO, and also coke formation. In the cracking of the blend (80% VGO/20% bio-oil) at 70 wt % conversion, a deoxygenation degree of 95 wt % has been obtained, with a total liquid fuel yield of 52.8 wt % and a gasoline yield of 31.6 wt %, with a low oxygenate fraction (<4 wt %) containing carboxylic acids, aldehydes, ketones, and phenols.
dc.format
application/pdf
dc.language.iso
eng
dc.publisher
American Chemical Society
dc.rights
info:eu-repo/semantics/restrictedAccess
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.subject
Fluid Catalytic Cracking
dc.subject
Bio-Oil
dc.subject
Vacuum Gas Oil
dc.subject
Fcc Catalyst
dc.subject.classification
Otras Ingeniería Química
dc.subject.classification
Ingeniería Química
dc.subject.classification
INGENIERÍAS Y TECNOLOGÍAS
dc.title
Synergy in the Cracking of a Blend of Bio-oil and Vacuum Gasoil under Fluid Catalytic Cracking Conditions
dc.type
info:eu-repo/semantics/article
dc.type
info:ar-repo/semantics/artículo
dc.type
info:eu-repo/semantics/publishedVersion
dc.date.updated
2019-06-19T16:54:25Z
dc.journal.volume
55
dc.journal.number
7
dc.journal.pagination
1872-1880
dc.journal.pais
Estados Unidos
dc.journal.ciudad
Washington
dc.description.fil
Fil: Ibarra, Álvaro. Universidad del Pais Vasco - Euskal Herriko Unibertsitatea, Campus Bizkaia; España
dc.description.fil
Fil: Rodríguez, Elena. Universidad del Pais Vasco - Euskal Herriko Unibertsitatea, Campus Bizkaia; España
dc.description.fil
Fil: Sedran, Ulises Anselmo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera". Universidad Nacional del Litoral. Instituto de Investigaciones en Catálisis y Petroquímica "Ing. José Miguel Parera"; Argentina
dc.description.fil
Fil: Arandes, José M.. Universidad del Pais Vasco - Euskal Herriko Unibertsitatea, Campus Bizkaia; España
dc.description.fil
Fil: Bilbao, Javier Ignacio. Universidad del Pais Vasco - Euskal Herriko Unibertsitatea, Campus Bizkaia; España
dc.journal.title
Industrial & Engineering Chemical Research
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1021/acs.iecr.5b04502


Archivos asociados

Documento no disponible

Comunidades y colecciones

  • Articulos(INCAPE) [657]
    Articulos de INST.DE INVEST.EN CATALISIS Y PETROQUIMICA "ING. JOSE MIGUEL PARERA"

Mostrar el registro sencillo del ítem