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Título: | Mn-based oxygen carriers prepared by impregnation for Chemical Looping Combustion with diverse fuels |
Autor: | Costa, T. R. CSIC; Gayán Sanz, Pilar CSIC ORCID ; Abad Secades, Alberto CSIC ORCID ; García Labiano, Francisco CSIC ORCID ; Diego Poza, Luis F. de CSIC ORCID ; Melo, Dulce M. A.; Adánez Elorza, Juan CSIC ORCID | Palabras clave: | CO2 capture Chemical looping combustion Oxygen carrier Manganese oxide |
Fecha de publicación: | 2-jun-2018 | Editor: | Elsevier | Citación: | Fuel Processing Technology 178: 236-250 (2018) | Resumen: | Chemical Looping Combustion (CLC) is considered one of the low cost alternatives for CO2 capture for fossil fuels combustion and to reach negative emissions through biomass CLC. The cornerstone of the CLC process is the oxygen carrier performance that represents the main additional cost with respect to the conventional combustion. Manganese-based oxygen carriers are subjected to a growing interest because they are low cost, not toxic and environmentally friendly. In this work five impregnated oxygen carriers, with manganese oxide Mn3O4 or Mg6MnO8 as their active phase and three commercial supports based on zirconia and synthetic calcium aluminate, were prepared. Their behaviour for CLC was examined by TGA, batch fluidized bed reactor, TPR, SEM-EDX and XRD. After a preliminary screening two carriers (Mn-ZrM and Mn-ZrSG) were subjected to multiple redox cycles by TGA and batch fluidized bed reactor. Both showed high solids conversion by TGA under the tested conditions, appropriated resistance to fracture, rate indexes relatively high, although Mn-ZrM showed agglomeration and deactivation during batch fluidized bed tests. Reactivity in batch fluidized bed reactor of the Mn-ZrSG oxygen carrier with methane increases with temperature although suffered from significant deactivation. This was different to the results found during multiple redox cycles by TGA. There was not a clear reason for this decrease in the reactivity that likely could be due to the uncomplete oxidation in the batch fluidized bed reactor, although further investigations are needed. On the other hand, it presented high and constant reactivity with CO and H2 in all the range of temperatures tested, being suitable for iG-CLC processes of coal or biomass and syngas combustion. Agglomeration problems were not found and the attrition losses were small. Calculated lifetime was around 11,000 h, much higher than any other Mn-based material developed or tested for CLC. | Descripción: | 13 Figures, 4 Tables.-- © 2018. 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 editor: | http://dx.doi.org/10.1016/j.fuproc.2018.05.019 | URI: | http://hdl.handle.net/10261/183982 | DOI: | 10.1016/j.fuproc.2018.05.019 | ISSN: | 0378-3820 |
Aparece en las colecciones: | (ICB) Artículos |
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Fuel Proc Technol 178 (2018) 236–250.pdf | Artículo principal | 1,58 MB | Adobe PDF | Visualizar/Abrir |
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