 |
Journal articles
Scale-up and Modeling of Fixed-Bed Reactors for Catalytic Phenol Oxidation over Adsorptive Active Carbon
Abstract : The wet air oxidation of phenol over a commercial active carbon catalyst has been studied in laboratory-scale and pilot-plant fixed-bed reactors at mild temperatures and oxygen partial pressures of 120−160 °C and 0.05−0.2 MPa, respectively. The performances of the fixed-bed reactors have been assessed and compared to each other for both up- and downflow operation mode. Depending on the flow mode and reactor scale, distinct phenol destruction rates have been observed in the experiments. A series of batch experiments are carried out to obtain phenol removal kinetics, which are subsequently implemented in the modeling of the pilot-plant fixed-bed reactor. A one-dimensional, nonisothermal piston dispersion model is developed to describe in detail the interplay of reaction kinetics, gas−liquid hydrodynamics, and heat and mass transfer in both flow directions. The model predicts reasonably well the experimental data, thus allowing for a thorough explanation of the observed pilot-plant reactor performance.
https://hal-normandie-univ.archives-ouvertes.fr/hal-02409980
Contributor : Isabelle Polaert <>
Submitted on : Friday, December 13, 2019 - 4:08:42 PM
Last modification on : Thursday, February 6, 2020 - 9:18:02 AM
Contributor : Isabelle Polaert <>
Submitted on : Friday, December 13, 2019 - 4:08:42 PM
Last modification on : Thursday, February 6, 2020 - 9:18:02 AM
Links full text
