Published: CABEQ 30 (4) (2016) 411–418
Paper type: Original Scientific Paper
C. Marangoni, E. J. Zierhut, I. G. B. Parisotto, R. A. F. Machado and A. Bolzan
Abstract
A control strategy with distributed corrective action for distillation has been proposed
and consists of a conventional dual temperature control combined with an additional
column tray. In this work, we evaluated the influence of the location of this internal
loop as part of the new proposal, compared to a conventional system. Tests were
carried out in a 13-column tray distillation equipment and feed temperature was disturbed. Two different column trays from the stripping section were used (11 and 12) for internal decentralized temperature control, each one separately, plus the dual control of top and bottom temperatures. The results demonstrated that this proposed control approach with distributed corrective action is faster than the conventional one, regardless of the column tray in use. It was also determined that the internal loop close to the feed (disturbance) is more interesting as a way to minimize transients.
This work is licensed under a Creative Commons Attribution 4.0 International License
Keywords
distillation, dynamics, distributed, dual control