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NO reduction capacity of four major solid fuels in reburning conditions – Experiments and modeling

Authors :
Jean-Michel Commandre
Sylvain Salvador
Philippe Dagaut
Julien Cances
Centre de recherche d'Albi en génie des procédés des solides divisés, de l'énergie et de l'environnement (RAPSODEE)
Centre National de la Recherche Scientifique (CNRS)-IMT École nationale supérieure des Mines d'Albi-Carmaux (IMT Mines Albi)
Institut Mines-Télécom [Paris] (IMT)-Institut Mines-Télécom [Paris] (IMT)
Institut de Combustion, Aérothermique, Réactivité et Environnement (ICARE)
Université d'Orléans (UO)-Centre National de la Recherche Scientifique (CNRS)-Institut des Sciences de l'Ingénierie et des Systèmes (INSIS)
IMT École nationale supérieure des Mines d'Albi-Carmaux (IMT Mines Albi)
Institut Mines-Télécom [Paris] (IMT)
Laboratoire de combustion et systèmes reactifs (LCSR)
Centre National de la Recherche Scientifique (CNRS)-Université d'Orléans (UO)
Source :
Fuel, Fuel, Elsevier, 2008, 87 (3), pp.274-289. ⟨10.1016/j.fuel.2007.05.011⟩, Fuel, Elsevier, 2008, 87 (3), p.274-289. ⟨10.1016/j.fuel.2007.05.011⟩
Publication Year :
2008
Publisher :
HAL CCSD, 2008.

Abstract

International audience; The combustion of solid fuels in the rotary kiln and in the calciner of a cement plant generates fuel and thermal NO. This NO can be reduced inside the reducing zone of the calciner. This occurs in two different ways: homogeneous reduction by hydrocarbons and heterogeneous reduction by char. The purpose of this paper is to identify the relative contribution of volatile matters or char on the NO reduction process, which largely depends on the nature of the solid fuel used for reburning.Experiments were undertaken in an Entrained Flow Reactor (EFR), at three temperatures: 800, 900 and 1000 °C. Four major fuels used in the cement production process were studied: a lignite, a coal, an anthracite and a petcoke. Specific experiments were undertaken to determine (i) their devolatilisation kinetics and the gas species released. A wide range of species influencing the NO chemistry was carefully analyzed. Then, (ii) the char oxidation and (iii) the char NO reduction kinetics were characterized. Finally, (iv), the “global” NO reduction capability of each fuel was quantified through experiments during which all phenomena could occur together. This corresponds to the situation of an industrial reactor in reducing conditions. Anthracite and petcoke reduce only very small quantities of NO whereas lignite and coal reduce, respectively, 90% and 80% of the initially present 880 ppm of NO (at 1000 °C after 2 s).The four types of experiments described above were then modeled using a single particle thermo-chemical model that includes heterogeneous reactions and detailed chemistry in the gas phase. This model reveals that both NO reduction on char and NO reduction by volatiles mechanisms contribute significantly to the global NO reduction. After short residence times (several tenth of a second), gas phase reactions reduce NO efficiently; after long residence times (several seconds) the char reduces larger quantities of NO.

Details

Language :
English
ISSN :
00162361 and 18737153
Database :
OpenAIRE
Journal :
Fuel, Fuel, Elsevier, 2008, 87 (3), pp.274-289. ⟨10.1016/j.fuel.2007.05.011⟩, Fuel, Elsevier, 2008, 87 (3), p.274-289. ⟨10.1016/j.fuel.2007.05.011⟩
Accession number :
edsair.doi.dedup.....efdcb76866690afcf4e1a81d63bfc849
Full Text :
https://doi.org/10.1016/j.fuel.2007.05.011⟩