Precise control of dissolved oxygen in bioreactors - a model-based geometric algorithm

被引:20
作者
Gomes, J
Menawat, AS
机构
[1] Indian Inst Technol, Dept Biochem Engn & Biotechnol, New Delhi 110016, India
[2] Adv Solut & Know How 1426, N Saline, MI 48176 USA
关键词
nonlinear control; dissolved oxygen; on-line; streptomyces; set-point tracking; spectinomycin;
D O I
10.1016/S0009-2509(99)00305-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this paper, we develop a Model-Based Geometric Control Algorithm (MGA) for controlling the dissolved oxygen concentration in fermentation processes. The algorithm is developed on a generic system description which encompasses a wide range of models commonly used to describe bioprocesses. Consequently, the algorithm we have derived will apply to any process whose model fits the generic description. The algorithm uses information contained in the shape (geometry) of the profile of the state variables as they evolve in time to adapt to process variations. There are two components in the algorithm, an estimator and a controller, whose functions complement each other. The estimator component of the algorithm predicts the states and the parameters of the system one time step ahead. Since the estimator is deadbeat, the algorithm converges in a finite number of steps. The control component of the algorithm uses the states predicted by the estimator and executes a control action so that predicted error falls below a desired level. Simulations for comparing the performance of the IMC, PI and MGA controllers are presented. The MGA was implemented on-line to control the dissolved oxygen in an aminoglycoside antibiotic production process by a Streptomyces and the results of its performance are also presented. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:67 / 78
页数:12
相关论文
共 55 条
[1]   STABLE ADAPTIVE OBSERVERS FOR NONLINEAR TIME-VARYING SYSTEMS [J].
BASTIN, G ;
GEVERS, MR .
IEEE TRANSACTIONS ON AUTOMATIC CONTROL, 1988, 33 (07) :650-658
[2]   ADAPTIVE ESTIMATION OF BIOREACTORS - MONITORING PLASMID INSTABILITY [J].
CHATTAWAY, T ;
STEPHANOPOULOS, G .
CHEMICAL ENGINEERING SCIENCE, 1989, 44 (01) :41-48
[3]   THE EFFECT OF DISSOLVED-OXYGEN AND AERATION RATE ON ANTIBIOTIC PRODUCTION OF STREPTOMYCES-FRADIAE [J].
CHEN, HC ;
WILDE, F .
BIOTECHNOLOGY AND BIOENGINEERING, 1991, 37 (06) :591-595
[4]  
Cohen G., 1953, Transactions of the ASME, P827, DOI DOI 10.1115/1.4015451
[5]   KINETICS OF BACTERIAL GROWTH - RELATIONSHIP BETWEEN POPULATION DENSITY AND SPECIFIC GROWTH RATE OF CONTINUOUS CULTURES [J].
CONTOIS, DE .
JOURNAL OF GENERAL MICROBIOLOGY, 1959, 21 (01) :40-50
[6]   COMPUTER-AIDED MATERIAL BALANCING FOR PREDICTION OF FERMENTATION PARAMETERS [J].
COONEY, CL ;
WANG, HY ;
WANG, DIC .
BIOTECHNOLOGY AND BIOENGINEERING, 1977, 19 (01) :55-67
[7]  
Dourado A., 1983, MODELLING CONTROL BI
[8]   Robust adaptive neural network control for a class of non-linear systems [J].
Ge, SS ;
Lee, TH .
PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART I-JOURNAL OF SYSTEMS AND CONTROL ENGINEERING, 1997, 211 (03) :171-181
[9]  
Gomes J, 1998, Adv Biochem Eng Biotechnol, V59, P1
[10]   ESTIMATION OF FERMENTATION PARAMETERS USING PARTIAL DATA [J].
GOMES, J ;
MENAWAT, AS .
BIOTECHNOLOGY PROGRESS, 1992, 8 (02) :118-125