The model reaction studied in a laboratory scale FBR was the oxidative dehydrogenation of ethane on a VOx/Al2O3 catalyst. A network was derived from experimental data consisting of several parallel and consecutive reactions (Klose et al. 2004). There are several errors that could not be completely eliminated during the experiments (in particular uncertainties in the measured flow rates and compositions at the reactor outlet). The simplified reactor model applied to analyse the primary data suffers from incorrect representation of back mixing and temperature gradients. Various rivalling kinetic models such as simple Power-Law equations (Hamel 2002) and more complicated Langmuir-Hinshelwood & Hougen-Watson equations (Klose et al. 2004) were alternatively analysed in a comparative manner. Conventional non-linear least square technique was used for parameter estimation. Due to the errors in experimental data it was difficult to estimate a high number of parameters in the kinetic models considered. For this reason, statistical techniques such as sensitivity and cross-correlation coefficient analysis as well as the determination of confidence intervals were applied to verify the reliability of the parameters. This approach also allows determining the number of parameters that could be identified in a reliable manner.
References: Box, G. E. P., Lucas, H. L., Biometrika, 46 (1959), 77. Hafley, W. L., Lewis, J. S., Ind. & Eng. Chem., 55 (1963), 37. Hamel, C., Master Thesis, Otto-von-Guericke University Magdeburg, 2002. Klose, F., Joshi, M., Hamel, C., Seidel-Morgenstern, A., App. Cat. A, 260 (2004), 101. Mezaki, R., Kittrell, J. R., Ind. & Eng. Chem., 59 (1967), 63. Verenich, S., Laari, A., Kallas, A., Ind. & Eng. Chem. Res., 42 (2003), 5091.
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