Catalytic
naphtha reforming is a key process both in refineries
and in the production of aromatic compounds. However, the characteristics
of dual-production modes render the process model difficult to adapt
to changing production needs. Because catalytic naphtha reforming
has a complicated reaction mechanism along with multiple operation
variables and objectives, its optimization is challenging. We herein
report the modeling and optimization steps employed to resolve these
issues. A detailed continuous catalytic regenerative (CCR) reforming
process model was established, integrating the reaction kinetic model,
reactor model, heater model, compressor model, and separator model.
On the basis of the CCR model, multiobjective optimizations were performed,
and a hierarchical structure of stochastic algorithm was proposed,
thus reducing computation costs during model calculations. Three multiobjective
optimization problems were solved using the proposed algorithm, with
these cases being based on refinery production, the production of
aromatic compounds, and energy conservation. Optimization results
were consistent with the industrial process and identified improvements
through tuning the key operational parameters, such as inlet temperature,
pressure, and hydrogen-to-oil molar ratio. Optimal operating points
were also listed for different requirements of the reforming process.