Published: CABEQ 19 (3) (2005) 243–253
Paper type: Original Scientific Paper
J. G. Segovia-Hernández, S. Hernández, A. Jiménez and R. Femat
Abstract
Because of its significant energy savings, the Petlyuk column provides an interesting
alternative to the use of conventional distillation systems. Its dynamic and operational
characteristics, however, require a proper understanding to promote its practical
use. In this work, a proportional-integral controller with dynamic estimation of unknown
disturbances is implemented for the control of a Petlyuk column for the separation of ternary mixtures. The proposed controller comprises three feedback terms: proportional, integral and quadratic actions. The last term provides a dynamic estimation of uncertainties and improves the closed-loop performance. Comparison with the classical PI control law was carried out to analyze the performance of the proposed controller in face to unknown feed disturbances and set point changes. The results show that the closed-loop response of the Petlyuk column is significantly improved with the proposed controller.
This work is licensed under a Creative Commons Attribution 4.0 International License
Keywords
distillation, Thermally coupled distillation, distillation control, disturbance rejection