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<dc:dc xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:invenio="http://invenio-software.org/elements/1.0" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><dc:identifier>doi:10.1016/j.fuproc.2015.09.014</dc:identifier><dc:language>eng</dc:language><dc:creator>Manyá Cervelló, Juan José</dc:creator><dc:creator>García-Ceballos, F.</dc:creator><dc:creator>Azuara Medel, Manuel</dc:creator><dc:creator>Latorre Sierra, María Nieves</dc:creator><dc:creator>Royo Pascual, Carlos Jesús</dc:creator><dc:title>Pyrolysis and char reactivity of a poor-quality refuse-derived fuel (RDF) from municipal solid waste</dc:title><dc:identifier>ART-2015-92300</dc:identifier><dc:description>The present study focuses on analyzing the pyrolysis and combustion behaviors of a refuse-derived fuel (RDF), which is generated in a MSW treatment plant located in Zaragoza (Spain). Pyrolysis experiments were carried out in a TGA apparatus and a fixed-bed reactor at different peak temperatures (400 and 600 °C) and heating rates (5 and 40 °C min- 1). The reactivity towards oxygen of produced chars was also measured in the same TGA device at a heating rate of 10 °C min- 1 and a final temperature of 800 °C. Pyrolysis results were significantly affected by peak temperature and heating rate. The found effect of peak temperature on char and fixed-carbon yields as well as on measured properties (H:C and O:C ratios, BET surface area and average pore diameter) was in agreement with previous studies. However, the effect of heating rate, especially on the release rate of volatiles, could be explained by a change in the pyrolysis reaction scheme. The RDF-derived chars obtained at the highest heating rate showed a higher reactivity in air. In addition, an increase in peak temperature also led to a higher reactivity. This result can indicate that the carbon present in the RDF-derived char is dispersed within an ash matrix containing a high number of active sites, the distribution of which could be improved when heating rate (and, to a lesser extent, peak temperature) is increased. The addition of 10 wt.% RDF to two-phase olive mill waste prior to slow pyrolysis led to an apparent increase in the carbonization efficiency as well as to an enhancement of the resultant char''s reactivity in air.</dc:description><dc:date>2015</dc:date><dc:source>http://zaguan.unizar.es/record/47432</dc:source><dc:doi>10.1016/j.fuproc.2015.09.014</dc:doi><dc:identifier>http://zaguan.unizar.es/record/47432</dc:identifier><dc:identifier>oai:zaguan.unizar.es:47432</dc:identifier><dc:relation>info:eu-repo/grantAgreement/ES/MINECO/ENE2013-47880-C3-1-R</dc:relation><dc:identifier.citation>FUEL PROCESSING TECHNOLOGY 140 (2015), 276-284</dc:identifier.citation><dc:rights>All rights reserved</dc:rights><dc:rights>http://www.europeana.eu/rights/rr-f/</dc:rights><dc:rights>info:eu-repo/semantics/openAccess</dc:rights></dc:dc>

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