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http://hdl.handle.net/10261/107919
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Campo DC | Valor | Lengua/Idioma |
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dc.contributor.author | Alonso Carreño, Mónica | - |
dc.contributor.author | Diego de Paz, María Elena | - |
dc.contributor.author | Pérez, C. | - |
dc.contributor.author | Chamberlain, J.R. | - |
dc.contributor.author | Abanades García, Juan Carlos | - |
dc.date.accessioned | 2014-11-21T12:26:19Z | - |
dc.date.available | 2014-11-21T12:26:19Z | - |
dc.date.issued | 2014-10 | - |
dc.identifier.citation | International Journal of Greenhouse Gas Control 29: 142-152 (2014) | es_ES |
dc.identifier.issn | 1750-5836 | - |
dc.identifier.uri | http://hdl.handle.net/10261/107919 | - |
dc.description.abstract | This paper reports experimental results from a new 300 kWth calcium looping pilot plant designed to capture CO2 “in situ” during the combustion of biomass in a fluidized bed. This novel concept relies on the high reactivity of biomass as a fuel, which allows for effective combustion around 700 °C in air at atmospheric pressure. In these conditions, CaO particles fed into the fluidized bed combustor react with the CO2 generated during biomass combustion, allowing for an effective CO2 capture. A subsequent step of regeneration of CaCO3 in an oxy-fired calciner is also needed to release a concentrated stream of CO2. This regeneration step is assumed to be integrated in a large scale oxyfired power plant and/or a larger scale post-combustion calcium looping system. The combustor-carbonator is the key reactor in this novel concept, and this work presents experimental results from a 300 kWth pilot to test such a reactor. The pilot involves two 12 m height interconnected circulating fluidized bed reactors. Several series of experiments to investigate the combustor-carbonator reactor have been carried out achieving combustion efficiencies close to 100% and CO2 capture efficiencies between 70 and 95% in dynamic and stationary state conditions, using wood pellets as a fuel. Different superficial gas velocities, excess air ratios above stoichiometric requirements, and solid circulating rates between combustor-carbonator and combustor-calciner have been tested during the experiments. Closure of the carbon and oxygen balances during the combustion and carbonation trials has been successful. A simple reactor model for combustion and CO2 capture in the combustor-carbonator has been applied to aid in the interpretation of results, which should facilitate the future scaling up of this process concept. | es_ES |
dc.description.sponsorship | This work was partially funded under the MENOS CO2 project (CDTI, Spanish Ministry of Economy and Competitivity). M.E. Diego acknowledges the award of a fellowship Grant under the CSIC JAE Programme, co-funded by the European Social Fund. | es_ES |
dc.language.iso | eng | es_ES |
dc.publisher | Elsevier | es_ES |
dc.relation.isversionof | Postprint | es_ES |
dc.rights | openAccess | es_ES |
dc.subject | Biomass combustion | es_ES |
dc.subject | CO2 capture | es_ES |
dc.subject | Negative emissions | es_ES |
dc.subject | Calcium looping | es_ES |
dc.subject | BECCS | es_ES |
dc.title | Biomass combustion with in situ CO2 capture by CaO in a 300 kWth circulating fluidized bed facility | es_ES |
dc.type | artículo | es_ES |
dc.identifier.doi | 10.1016/j.ijggc.2014.08.002 | - |
dc.description.peerreviewed | Peer reviewed | es_ES |
dc.relation.publisherversion | http://dx.doi.org/10.1016/j.ijggc.2014.08.002 | es_ES |
dc.relation.csic | Sí | es_ES |
dc.type.coar | http://purl.org/coar/resource_type/c_6501 | es_ES |
item.fulltext | With Fulltext | - |
item.languageiso639-1 | en | - |
item.openairecristype | http://purl.org/coar/resource_type/c_18cf | - |
item.openairetype | artículo | - |
item.cerifentitytype | Publications | - |
item.grantfulltext | open | - |
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Biomass_combustion_Alonso.pdf | 3,17 MB | Adobe PDF | Visualizar/Abrir |
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