2011
DOI: 10.1016/j.ces.2011.01.028
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Kinetic model of NOx ozonation and its experimental verification

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Cited by 46 publications
(26 citation statements)
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“…Therefore, to fully understand the ozonation process studies in the batch reactor were conducted. Based on the obtained experimental data the kinetic model for the ozonation process of NO x was proposed, and the reaction rate constants were determined and experimentally verified (Skalska et al 2011b).…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…Therefore, to fully understand the ozonation process studies in the batch reactor were conducted. Based on the obtained experimental data the kinetic model for the ozonation process of NO x was proposed, and the reaction rate constants were determined and experimentally verified (Skalska et al 2011b).…”
Section: Resultsmentioning
confidence: 99%
“…As a result the residence time was in the range from 10 to 30 seconds. An overview of the experimental setup was described in previous articles (Skalska et al 2010b(Skalska et al , 2011a(Skalska et al , 2011b.…”
Section: Methodsmentioning
confidence: 99%
“…In fact, NO 2 solubility is low (0.3÷0.5 g/l for p NO2 = 0.1 MPa), which is only one order higher than the solubility of NO [10]. The absorbed NO 2 reacts with water producing nitrous and nitric acid [18]:…”
Section: Mechanism Of No Oxidation By Ozonementioning
confidence: 99%
“…The basic reaction scheme of NOx oxidation by ozone in gaseous phase is as follows (Skalska et al, 2011) The products of NOx oxidation in gaseous phase are determined by the molar ratio O3/NO in the temperature range of 20−100 °C. For O3/NO ≈ 1 the main nitrogenous component of flue gas after ozonation remains NO2, because the reaction (1) is fast (Skalska et al, 2011) and the product of reaction (2) N2O3 is unstable.…”
Section: The Mechanisms Of Chemical Reactions Of Nox and So2 With Ozonementioning
confidence: 99%
“…The basic reaction scheme of NOx oxidation by ozone in gaseous phase is as follows (Skalska et al, 2011) The products of NOx oxidation in gaseous phase are determined by the molar ratio O3/NO in the temperature range of 20−100 °C. For O3/NO ≈ 1 the main nitrogenous component of flue gas after ozonation remains NO2, because the reaction (1) is fast (Skalska et al, 2011) and the product of reaction (2) N2O3 is unstable. However, the role of N2O3 in the absorber cannot be overestimated, because N2O3 is well-soluble, while NO and NO2 are only weakly-soluble (Sander, 1999 (9) However, the efficiency NOx capture in this way (8, 9) from flue gas is limited to about 60% due to the reactions of disproportionation of nitrous acid with release of NO (Joshi et al, 1985) (11) Further increasing the molar ratio O3/NO > 1 results in oxidation of NO2 to NO3 in reaction (3), which combined with NO2 gives a very well-soluble dinitrogen pentoxide (N2O5) (Wang et al, 2015).…”
Section: The Mechanisms Of Chemical Reactions Of Nox and So2 With Ozonementioning
confidence: 99%