In the present work, the results of a complete dynamical analysis of open- and closed-loop continuous bioreactor for cultures of substrate inhibited aerobic microorganisms were presented. In the closed loop system the dissolved oxygen concentration was controlled at a pre-set value by means of a proportionalintegral feedback control scheme manipulating the inlet substrate concentration. A mathematical model was developed coupling the mass balance equation for the substrates (carbon-source and oxygen) and the controller. Solutions of both open- and closed-loop systems were assessed by means of parametric continuation technique and bifurcational analysis tools. The dynamics behavior was studied by changing the main operating parameters - dilution rate and gas-liquid mass transfer rate - and the controller parameters - gain and set-point - in a wide intervals. We have found that the regimes strongly depend on the operating conditions. In particular, the open-loop unstable steady state may be stabilized in closedloop system, provided the proper choice of both the gain and the reset time for the selected set-point value of oxygen concentration. Copyright �� 2013, AIDIC Servizi S.r.l.
Non-linear analysis of feedback controlled aerobic cultures / Olivieri, Giuseppe; M. E., Russo; E., Mancusi; Marzocchella, Antonio; Maffettone, PIER LUCA; Salatino, Piero. - STAMPA. - 32:(2013), pp. 811-816. (Intervento presentato al convegno ICheaP-11, 11th International Conference on Chemical and Process Engineering tenutosi a Milan (IT) nel 3 - 5 June 2013) [10.3303/CET1332136].
Non-linear analysis of feedback controlled aerobic cultures
OLIVIERI, GIUSEPPE;MARZOCCHELLA, ANTONIO;MAFFETTONE, PIER LUCA;SALATINO, PIERO
2013
Abstract
In the present work, the results of a complete dynamical analysis of open- and closed-loop continuous bioreactor for cultures of substrate inhibited aerobic microorganisms were presented. In the closed loop system the dissolved oxygen concentration was controlled at a pre-set value by means of a proportionalintegral feedback control scheme manipulating the inlet substrate concentration. A mathematical model was developed coupling the mass balance equation for the substrates (carbon-source and oxygen) and the controller. Solutions of both open- and closed-loop systems were assessed by means of parametric continuation technique and bifurcational analysis tools. The dynamics behavior was studied by changing the main operating parameters - dilution rate and gas-liquid mass transfer rate - and the controller parameters - gain and set-point - in a wide intervals. We have found that the regimes strongly depend on the operating conditions. In particular, the open-loop unstable steady state may be stabilized in closedloop system, provided the proper choice of both the gain and the reset time for the selected set-point value of oxygen concentration. Copyright �� 2013, AIDIC Servizi S.r.l.I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.