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This document summarizes a study that modeled and optimized a catalytic naphtha reformer. It developed a detailed kinetic model involving 35 components and 36 reactions. The model was parameterized using industrial plant data. Initial optimization identified a constant reactor inlet temperature configuration for optimal operation over the catalyst lifetime. The analysis was extended to study time-optimal control profiles and constant octane cases. The model can be used to determine optimal operating conditi

Author
ahmadgolrokh
Language
EN

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