2012
DOI: 10.1021/jp307789r
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Kinetic Analysis of O2- and NO2-Based Oxidation of Synthetic Soot

Abstract: This study demonstrates the application of two different methods to evaluate the kinetics of O 2 -and NO 2 -based oxidation of carbonaceous matter. The influence of reactor setup and experiment execution on the accuracy and interpretation of the kinetic parameters is also discussed. The fundamental difference between the two methods lies in how rate changes during the progress of oxidation are interpreted: by changes in the fraction of atoms available for reaction (traditional approach) or by changes in the ac… Show more

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Cited by 15 publications
(10 citation statements)
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“…Calculated adsorption energies and structural parameters for the binding of NO to the defected Mn-doped CeO 2 (111) surface. , which has superior oxidation activity (Wang-Hansen et al, 2013). Consequently, the activity of the catalyst surface is enhanced because active oxygen is formed for oxidation reactions.…”
Section: Co-adsorption Of No and O 2 On Defective Mn-doped Ceo 2 (111mentioning
confidence: 99%
“…Calculated adsorption energies and structural parameters for the binding of NO to the defected Mn-doped CeO 2 (111) surface. , which has superior oxidation activity (Wang-Hansen et al, 2013). Consequently, the activity of the catalyst surface is enhanced because active oxygen is formed for oxidation reactions.…”
Section: Co-adsorption Of No and O 2 On Defective Mn-doped Ceo 2 (111mentioning
confidence: 99%
“…Oxidation of organic carbonaceous residues to CO and CO 2 by HNO 3 /NO x is well known in mass spectrometry research of NO 2 and HNO 3 27,28. Soot oxidation research and the automobile industry make use of carbon oxidation under high NO x conditions [29][30][31][32]. For instance, high NO x levels and enhanced temperatures in the vehicle exhaust are used to facilitate regeneration of diesel particulate filters and to burn off carbonaceous deposits to CO 2 .…”
mentioning
confidence: 99%
“…Plots of the average, axial and radial temperature profiles for different configurations are shown in Figure . Axially, a temperature gradient of ∼32 °C is established over a single, 2‐cm long catalyst, which can result in roughly 70 % error in the estimated reaction rate constant for a typical oxidation reaction of soot with oxygen, based on the kinetic parameters extracted from the literature . Therefore, an inert monolith of the same length as the catalyst is inserted upstream the catalyst, which provides a higher radial heat transfer, resulting in a more uniform radial temperature profile at the inlet of the catalyst.…”
Section: Resultsmentioning
confidence: 99%