2024-03-29T13:59:33Zhttp://digital.csic.es/dspace-oai/requestoai:digital.csic.es:10261/2119852020-12-09T15:59:52Zcom_10261_35com_10261_5com_10261_84col_10261_288col_10261_337
DIGITAL.CSIC
author
Abanades García, Juan Carlos
author
Alonso Carreño, Mónica
author
Rodríguez Gómez, Nuria
author
González García, Belén
author
Grasa Adiego, Gemma
author
Murillo Villuendas, Ramón
funder
Grupo Hunosa
funder
Fundación Endesa
orcid
Abanades García, Juan Carlos [0000-0003-1711-6993]
orcid
Alonso Carreño, Mónica [0000-0002-1955-9432]
orcid
Grasa Adiego, Gemma [0000-0002-4242-5846]
orcid
Murillo Villuendas, Ramón [0000-0002-0299-506X]
2020-05-22T11:41:59Z
2020-05-22T11:41:59Z
2009-02-09
Energy Procedia 1: 1147-1154 (2009)
http://hdl.handle.net/10261/211985
10.1016/j.egypro.2009.01.151
http://dx.doi.org/10.13039/501100007827
Post-combustion carbonate looping processes are based on the capture of CO2 from the flue gases of an existing power plant in a circulating fluidized bed (CFB) reactor of CaO (the carbonator) at around 650 ∘C. The calcination of CaCO3 in a new oxy-fired experimental results from a small test facility (30 kWt) operated in continuous mode using two interconnected CFB reactors as carbonator and calciner. Capture efficiencies between 70 and 97% have been obtained under realistic flue gas conditions in the carbonator reactor. The similarity between process conditions and those existing in CFBC power plants should allow a rapid scaling up of this technology.
openAccess
Capture
Carbonate looping
Carbonation
Calcination
Pilot testing
Capturing CO2 from combustion flue gases with a carbonation calcination loop. Experimental results and process development
comunicación de congreso
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URL
https://digital.csic.es/bitstream/10261/211985/1/Energy%20Procedia%201%20%282009%29%201147%e2%80%931154.pdf
File
MD5
dd48585e8d4854a4d3e3b1b24bd58a52
1064602
application/pdf
Energy Procedia 1 (2009) 1147–1154.pdf