The combustion of model soot (i.e. Printex U) by NO2 and O2 in the presence of water was investigated in a fixed bed micro reactor under isothermal conditions. A wide range of experimental conditions (e.g. 250–350 °C, 0–5 vol% O2, 0–500 ppmv NO2, 0–5 vol% H2O) were considered in order to investigate the role of NO2, O2 and H2O in the combustion process. It was found that the oxidation of soot is initiated by NO2 at temperatures where oxygen is unreactive. In addition, a synergistic effect between NO2 and O2 on soot combustion was observed in the presence of the NO2-O2 mixture. Both the direct reaction between soot and NO2 and also the contribution of gaseous oxygen on the combustion process appeared to rise with the increasing temperature and in the presence of water. Finally, the kinetic analysis of the experimental results showed a non-negligible dependence of the kinetic parameters on carbon conversion and in particular the poor accuracy of the shrinking-core model at low conversion degree.

Oxidation of model soot by NO2 and O2 in the presence of water vapor

Matarrese, R.;Castoldi, L.;Lietti, L.
2017-01-01

Abstract

The combustion of model soot (i.e. Printex U) by NO2 and O2 in the presence of water was investigated in a fixed bed micro reactor under isothermal conditions. A wide range of experimental conditions (e.g. 250–350 °C, 0–5 vol% O2, 0–500 ppmv NO2, 0–5 vol% H2O) were considered in order to investigate the role of NO2, O2 and H2O in the combustion process. It was found that the oxidation of soot is initiated by NO2 at temperatures where oxygen is unreactive. In addition, a synergistic effect between NO2 and O2 on soot combustion was observed in the presence of the NO2-O2 mixture. Both the direct reaction between soot and NO2 and also the contribution of gaseous oxygen on the combustion process appeared to rise with the increasing temperature and in the presence of water. Finally, the kinetic analysis of the experimental results showed a non-negligible dependence of the kinetic parameters on carbon conversion and in particular the poor accuracy of the shrinking-core model at low conversion degree.
2017
Diesel aftertreatment; DPF; NO2; Oxidation kinetics; Printex U; Soot oxidation mechanism; Chemistry (all); Chemical Engineering (all); Industrial and Manufacturing Engineering; Applied Mathematics
File in questo prodotto:
File Dimensione Formato  
Matarrese et al_CES 2017.pdf

Accesso riservato

: Post-Print (DRAFT o Author’s Accepted Manuscript-AAM)
Dimensione 924.94 kB
Formato Adobe PDF
924.94 kB Adobe PDF   Visualizza/Apri
11311-1037606 Castoldi.pdf

accesso aperto

: Post-Print (DRAFT o Author’s Accepted Manuscript-AAM)
Dimensione 1.24 MB
Formato Adobe PDF
1.24 MB Adobe PDF Visualizza/Apri

I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.

Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11311/1037606
Citazioni
  • ???jsp.display-item.citation.pmc??? ND
  • Scopus 33
  • ???jsp.display-item.citation.isi??? 24
social impact