Nonlinear modelling of a synchronized chemostat with impulsive state feedback control

Mathematical and Computer Modelling

Volumn 52, Issue 1-2, 2010, Pages 227-240

  Sun, Kaibiao ^a   Tian, Yuan ^b   Chen, Lansun ^a   Kasperski, Andrzej ^c  

^a DALIAN UNIVERSITY OF TECHNOLOGY   (China)

^b DALIAN UNIVERSITY   (China)

^c UNIVERSITY OF ZIELONA GÓRA   (Poland)

Author keywords

Continuous culture; Feedback control; Nonlinear biomass yield; Optimization; State impulsive

Indexed keywords

ACTIVE AREA; ADVERSE EFFECT; BIOMASS CONCENTRATIONS; BIOMASS YIELD; BIOPROCESS OPTIMIZATION; BIOPROCESSES; BIOREACTOR CONTROL; BIOREACTOR DYNAMICS; CONTINUOUS CULTURE; DISSOLVED OXYGEN CONTENTS; DYNAMIC PROPERTY; EXISTENCE AND STABILITY; NON-LINEAR MODELLING; OPERATING CONDITION; OPERATIONS AND CONTROL; PERIODIC SOLUTION; SUBSTRATE CONCENTRATIONS; SUBSTRATE INHIBITION;

BIOCONVERSION; BIOMASS; BIOREACTORS; CONTROL SYSTEM STABILITY; DISSOLUTION; DISSOLVED OXYGEN; FEEDBACK; FEEDBACK CONTROL; MATHEMATICAL MODELS; NONLINEAR FEEDBACK; OPTIMIZATION;

STATE FEEDBACK;

EID: 77953321802     PISSN: 08957177     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.mcm.2010.02.012     Document Type: Article

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