Por favor, use este identificador para citar o enlazar a este item: http://hdl.handle.net/10261/223423
COMPARTIR / EXPORTAR:
logo share SHARE logo core CORE BASE
Visualizar otros formatos: MARC | Dublin Core | RDF | ORE | MODS | METS | DIDL | DATACITE

Invitar a revisión por pares abierta
Título

A pyrolysis process coupled to a catalytic cracking stage: A potential waste-to-energy solution for mattress foam waste

AutorVeses Roda, Alberto CSIC ORCID ; Sanahuja-Parejo, Olga CSIC ORCID; Martínez Berges, Isabel; Callén Romero, M. Soledad ; López Sebastián, José Manuel CSIC ORCID ; García Martínez, Tomás CSIC ORCID ; Murillo Villuendas, Ramón CSIC ORCID
Palabras claveMattress foam
Pyrolysis
Syngas
Refuse-derived fuel
Waste
Fecha de publicación29-oct-2020
EditorElsevier
CitaciónWaste Management 120: 415-423 (2021)
ResumenPyrolysis coupled to either thermal or catalytic cracking of mattress foam waste was performed in a laboratory-scale facility consisting of a fixed-bed reactor joined to a tubular cracking reactor. The results showed a great potential for the production of syngas specially at high cracking temperatures. Particularly, fixing 800 °C in the cracking reactor, a CO and CH4 rich gas with a remarkable amount of H2 was obtained. The addition of catalysts (dolomite, olivine or HiFUEL®) significantly decreased undesirable tar formation, (below 10 wt%), simultaneously increasing the gas yield and keeping CO and CH4 as the main components in the stream, becoming a preferable route that the non-catalytic process. Accordingly, this stream could be used preferably for further applications in energy generation because its heating value ranged between 15.7 MJ/Nm3 and 19.6 MJ/Nm3. In particular, the gas obtained by the use of dolomite could be advantageous for the production of organic compounds such as dimethyl ether (DME) as well as its use an engine or boiler to generate electricity in small facilities. In addition, the solid fraction obtained after de process could be used as a medium quality refused derived fuel (LHV ~ 12 MJ/kg) in order to support the internal energy requirements of the process.
Descripción3 figures, 5 tables.-- Supplementary information available.-- © 2020. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/
Versión del editorhttp://dx.doi.org/10.1016/j.wasman.2020.09.052
URIhttp://hdl.handle.net/10261/223423
DOI10.1016/j.wasman.2020.09.052
ISSN0956-053X
Aparece en las colecciones: (ICB) Artículos




Ficheros en este ítem:
Fichero Descripción Tamaño Formato
WM-20-1139_R2.pdfArtículo principal557,91 kBAdobe PDFVista previa
Visualizar/Abrir
1-s2.0-S0956053X20305717-mmc1.docxInformación suplementaria215,47 kBMicrosoft Word XMLVisualizar/Abrir
Mostrar el registro completo

CORE Recommender

SCOPUSTM   
Citations

9
checked on 20-mar-2024

WEB OF SCIENCETM
Citations

8
checked on 20-feb-2024

Page view(s)

231
checked on 01-may-2024

Download(s)

175
checked on 01-may-2024

Google ScholarTM

Check

Altmetric

Altmetric


Este item está licenciado bajo una Licencia Creative Commons Creative Commons