Modeling and Control Design for Distillation Columns Based on the Equilibrium Theory

نویسندگان

چکیده

Distillation columns represent the most widely used separation equipment in petrochemical industry. It is usually difficult to apply traditional mechanism modeling method online optimization and control because of its complex structure, common simplified models produce obvious errors. Therefore, we analyze mass transfer process gas-liquid fluid on each column tray based theory equilibrium establish a nonlinear dynamic model distillation process. The proposed can accurately characterize characteristics process, structure largely compared with model. provides new approach for model-based methods columns, especially cases that require efficient models. Two case studies benzene-toluene systems show has high concentration observation accuracy. Finally, generic scheme designed this Simulation results strategy performs better than PID scheme.

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ژورنال

عنوان ژورنال: Processes

سال: 2023

ISSN: ['2227-9717']

DOI: https://doi.org/10.3390/pr11020607