Fixed Bed Reactor for Catalytic Hydrocarbon Oxidation
Application ID: 257
Tubular reactors are generally modelled with the assumption that the concentration and temperature gradients only occur in the axial direction. The only transport mechanism operating in this direction is the overall flow itself, which is considered to be of plug-flow.
In this example a more general approach is taken, an approach that accounts for variations of the concentrations and temperature in the radial direction. Furthermore, mixing in the axial direction is accounted for through effective diffusivities and conductivities, which is due to turbulence and the presence of packing.
The example models the partial oxidation of o-xylene in air to phthalic anhydrid (PA) in a multitube fixed-bed reactor. The reaction is exothermic and it requires good cooling to occur at optimal rates, therefore a cooling flux at the outer boundary is included as a function of the temperature.
This application was built using the following:COMSOL Multiphysics®
The combination of COMSOL® products required to model your application depends on the physics interfaces that define it. Particular physics interfaces may be common to several products (see the Specification Chart for more details). To determine the right combination of products for your project, you should evaluate all of your needs in light of each product\'s capabilities, consultation with the COMSOL Sales and Support teams, and the use of an evaluation license.