DocumentCode :
3290901
Title :
Lyapunov-based continuous-stirred tank bioreactor control to maximize biomass production using the haldane and monod specific growth models
Author :
Kapadia, A. ; Nath, N. ; Burg, T.C. ; Dawson, D.M.
Author_Institution :
Dept. of Electr. & Comput. Eng., Clemson Univ., Clemson, SC, USA
fYear :
2010
fDate :
June 30 2010-July 2 2010
Firstpage :
6734
Lastpage :
6739
Abstract :
A novel robust controller is proposed for a continuous-stirred tank bioreactor that controls the culture dilution rate into the bioreactor in order to maximize a cost function representing the biomass yield. To that end, an optimal desired biomass concentration trajectory is designed based on a numerical extremum-seeking algorithm to maximize the biomass yield. A nonlinear robust controller is designed to ensure the biomass concentration tracks the desired trajectory while providing stable operation. Lyapunov-based stability analyses are used to prove semi-global tracking.
Keywords :
Lyapunov methods; bioreactors; cost optimal control; nonlinear control systems; process control; renewable materials; robust control; stability; tanks (containers); Haldane growth model; Lyapunov based stability; Monod specific growth model; biomass concentration trajectory; biomass production maximization; continuous stirred tank bioreactor; cost function; dilution rate; nonlinear robust controller; numerical extremum seeking algorithm; semiglobal tracking; Adaptive control; Biological processes; Biological system modeling; Biomass; Bioreactors; Continuous production; Linear feedback control systems; Neural networks; Programmable control; Robust control;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
American Control Conference (ACC), 2010
Conference_Location :
Baltimore, MD
ISSN :
0743-1619
Print_ISBN :
978-1-4244-7426-4
Type :
conf
DOI :
10.1109/ACC.2010.5531387
Filename :
5531387
Link To Document :
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