1996
DOI: 10.1016/0009-2509(96)00100-5
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Mixing and reaction in a tubular jet reactor: A comparison of experiments with a model based on a prescribed PDF

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Cited by 17 publications
(6 citation statements)
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“…These investigations had been motivated by two following problems: the stabilization of the flame front and the saturation of air co-flow with the molecules of substances transferred by the internal jet. Investigations of jet mixers with emphasis on the jet mixer as a chemical reactor are presented in Guiraud et al (1991), Kruis and Falk (1996) and Baldyga and Bourne (1999). Unlike the papers mentioned above we investigate fully developed turbulent flows of the jet mixer both in the r-mode and in the j-mode.…”
Section: Introductionmentioning
confidence: 99%
“…These investigations had been motivated by two following problems: the stabilization of the flame front and the saturation of air co-flow with the molecules of substances transferred by the internal jet. Investigations of jet mixers with emphasis on the jet mixer as a chemical reactor are presented in Guiraud et al (1991), Kruis and Falk (1996) and Baldyga and Bourne (1999). Unlike the papers mentioned above we investigate fully developed turbulent flows of the jet mixer both in the r-mode and in the j-mode.…”
Section: Introductionmentioning
confidence: 99%
“…For example, it is often claimed that the β-PDF is suitable for the approximation of mixture fraction PDFs in mixing processes. In this case, the mixture fraction PDF would indeed be well characterized by its first two moments P( f ) ≈ P (2) ( f ;f , f 2 ). However, our results indicated that this is not always the case -we shall elaborate on this point below.…”
Section: Presumed Joint Probability Distributionmentioning
confidence: 97%
“…The factor ν i is computed as the difference of the stoichiometric coefficients of species i at the reactant ν i and product side ν i , respectively. Equation (2) shows that reaction rates depend in a non-linear fashion on temperature T and concentrations, making it a difficult task to determine mean reaction rates, since they cannot be computed from mean values of temperature and concentrations. In general mean values of an arbitrary variable or function g (e.g.…”
Section: Introductionmentioning
confidence: 99%
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