On the basis of non-isothermal experiments
in an integral pilot-scale reactor, the heterogeneously catalyzed
gas phase oxidation of propylene to acrolein was investigated at industrial
relevant process conditions. From an extensive experimental data set
both reaction scheme and reaction rates were derived. Beside the main
components propylene, oxygen, acrolein, and water, the proposed reaction
network includes a variety of side products. The reaction rates were
modeled by a semi-mechanistical approach given by Mars and van Krevelen.
On the basis of a two-dimensional, pseudohomogeneous reactor model,
the kinetic parameters were estimated successfully by introducing
a systematic procedure for a stepwise determination using different
regions with different characteristics to estimate the pre-exponential
factors and activation energies individually, i.e., separate from
each other. The model is able to predict the data included in the
parameter estimation and independent data measured at different process
conditions as well. Furthermore, it provides reliable results for
an industrial plant.