Non-linear Analysis of Feedback Controlled Aerobic Cultures

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 pro...

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Main Authors: G. Olivieri, M.E. Russo, E. Mancusi, A. Marzocchella, P.L. Maffettone, P. Salatino
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2013-06-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/6530
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spelling doaj-aed3694df44445ecb146f7d00cfb49ff2021-02-22T20:59:21ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162013-06-013210.3303/CET1332136Non-linear Analysis of Feedback Controlled Aerobic CulturesG. OlivieriM.E. RussoE. MancusiA. MarzocchellaP.L. MaffettoneP. SalatinoIn 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 proportional-integral 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 closed-loop system, provided the proper choice of both the gain and the reset time for the selected set-point value of oxygen concentration.https://www.cetjournal.it/index.php/cet/article/view/6530
collection DOAJ
language English
format Article
sources DOAJ
author G. Olivieri
M.E. Russo
E. Mancusi
A. Marzocchella
P.L. Maffettone
P. Salatino
spellingShingle G. Olivieri
M.E. Russo
E. Mancusi
A. Marzocchella
P.L. Maffettone
P. Salatino
Non-linear Analysis of Feedback Controlled Aerobic Cultures
Chemical Engineering Transactions
author_facet G. Olivieri
M.E. Russo
E. Mancusi
A. Marzocchella
P.L. Maffettone
P. Salatino
author_sort G. Olivieri
title Non-linear Analysis of Feedback Controlled Aerobic Cultures
title_short Non-linear Analysis of Feedback Controlled Aerobic Cultures
title_full Non-linear Analysis of Feedback Controlled Aerobic Cultures
title_fullStr Non-linear Analysis of Feedback Controlled Aerobic Cultures
title_full_unstemmed Non-linear Analysis of Feedback Controlled Aerobic Cultures
title_sort non-linear analysis of feedback controlled aerobic cultures
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2013-06-01
description 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 proportional-integral 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 closed-loop system, provided the proper choice of both the gain and the reset time for the selected set-point value of oxygen concentration.
url https://www.cetjournal.it/index.php/cet/article/view/6530
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AT amarzocchella nonlinearanalysisoffeedbackcontrolledaerobiccultures
AT plmaffettone nonlinearanalysisoffeedbackcontrolledaerobiccultures
AT psalatino nonlinearanalysisoffeedbackcontrolledaerobiccultures
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