On-line state estimation and adaptive optimization using state equations for continuous production of bioethanol

Abstract On-line optimization of bioprocesses is a difficult task due to the absence of accurate mathematical models and complex non-linear dynamic behaviour. In the present investigation, state equations were used to develop an algorithm to estimate unmeasurable state variables and time-varying parameters which were then used for adaptive, dynamic optimization of a continuous bioreactor. The manipulated variable was adjusted based on the steepest-descent technique to continuously drive the process to the optimal operating conditions in a reasonable time period. The estimation algorithm is shown to predict the unmeasured state variables to within ± 5% during dynamic fluctuations caused by both sudden changes in dilution rate and gradual changes in nutrient feed supply. The control algorithm is shown to quickly and smoothly adjust the manipulated variable to keep the bioreactor operating at its highest productivity as compared to steady state conditions even during inverse-response dynamic conditions.

[1]  Rolf Isermann,et al.  Adaptive on-line steady-state optimization of slow dynamic processes , 1978, Autom..

[2]  Gordon A. Hill,et al.  Optimum CFST bioreactor design: Experimental study using batch growth parameters for saccharomyces cerevisiae producing ethanol , 1992 .

[3]  Jean-Marc Engasser Bioreactor engineering: the design and optimization of reactors with living cells , 1988 .

[4]  G. T. Tsao,et al.  Annual Reports on Fermentation Processes , 1981 .

[5]  G. Guidoboni Continuous fermentation systems for alcohol production , 1984 .

[6]  G Stephanopoulos,et al.  Studies on on‐line bioreactor identification. IV. Utilization of pH measurements for product estimation , 1984, Biotechnology and bioengineering.

[7]  William A. Weigand,et al.  Computer Applications to Fermentation Processes , 1978 .

[8]  H C Lim,et al.  Experimental and simulation studies of multivariable adaptive optimization of continuous bioreactors using bilevel forgetting factors , 1989, Biotechnology and bioengineering.

[9]  I. Dunn,et al.  Adaptive on-line optimal control of bioreactors: application to anaerobic degradation , 1992 .

[10]  G B Semomes,et al.  Experimental multivariable adaptive optimization of the steady‐state cellular productivity of a continuous baker's yeast culture , 1989, Biotechnology and bioengineering.

[11]  Gilbert Shama,et al.  Developments in bioreactors for fuel ethanol production , 1988 .

[12]  S. Rohani,et al.  Absorption of radiation by substances at “high” concentrations: A new equation and process monitoring applications , 1993 .

[13]  H C Lim,et al.  Experimental adaptive on‐line optimization of cellular productivity of a continuous bakers' yeast culture , 1985, Biotechnology and bioengineering.

[14]  G A Hill,et al.  Effects of high product and substrate inhibitions on the kinetics and biomass and product yields during ethanol batch fermentation , 1992, Biotechnology and bioengineering.

[15]  Thomas F. Edgar,et al.  Process Dynamics and Control , 1989 .

[16]  K B Konstantinov,et al.  On‐line monitoring of hybridoma cell growth using a laser turbidity sensor , 1992, Biotechnology and bioengineering.

[17]  Sohrab Rohani,et al.  On-line monitoring of a wide range of biomass concentrations based on a new equation using a spectrophotometer: process control applications , 1994 .

[18]  H C Lim,et al.  Fast inferential adaptive optimization of a continuous yeast culture based on carbon dioxide evolution rate , 1990, Biotechnology and bioengineering.

[19]  Denis Dochain,et al.  Online Estimation of Microbial Specific Growth-rates - An Illustrative Case-study , 1988 .

[20]  Denis Dochain,et al.  On-line estimation of microbial specific growth rates , 1986, Autom..

[21]  R. Thatipamala,et al.  Spectrophotometric method for high biomass concentration measurements , 1991, Biotechnology and bioengineering.

[22]  G Stephanopoulos,et al.  Studies on on‐line bioreactor identification. II. Numerical and experimental results , 1984, Biotechnology and bioengineering.

[23]  Michael J. Rolf,et al.  ADAPTIVE ON-LINE OPTIMIZATION FOR CONTINUOUS BIOREACTORS , 1984 .

[24]  G. A. Hill,et al.  A modified ghose model for batch cultures of Saccharomyces cerevisiae at high ethanol concentrations , 1990 .