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Monitoring and control of a class of distributed parameter bioreactors with application of the substrate consumption rate

Wybrane pełne teksty z tego czasopisma
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
This paper deals with the idea of estimation of the substrate consumption rate at each point of the tube of the classical distributed parameter bioreactor and with its application to the monitoring and control of this system. It is shown how to approximate the profile of this parameter on the basis of the orthogonal collocation method and of the recursive least-squares procedure with adjustable forgetting factor. Then, it is suggested how to apply this profile for monitoring of the bioreactor work (calculation of the current mass flux of the substrate being reacted in the reactor tube and of the total mass of the substrate converted in the bioreactor during its activity). Finally, the linearizing adaptive control law is derived on the basis of the substrate consumption rate estimated at the outlet of the bioreactor. This controller allows the outlet substrate concentration to be kept at its desired value by manipulating the velocity of the flowing medium. The idea presented in this paper has been validated by means of the computer simulation and the results, proving its very good properties, complete the paper.
Rocznik
Strony
5--22
Opis fizyczny
Bibliogr. 30 poz., rys., wzory
Twórcy
autor
  • Institute of Automatic Control, Technical University of Silesia ul. Akademicka 16, 44-100 Gliwice, Poland
autor
  • Institute of Automatic Control, Technical University of Silesia ul. Akademicka 16, 44-100 Gliwice, Poland
autor
  • Laboratoire d’Analyse et d’Architecture des Systemes Centre National de la Recherche Scientifique (LAAS/CNRS) 7, avenue du Colonel Roche, 31077 Toulouse Cedex 4, France
autor
  • Department of Computer Science and Applied Mathematics University of Kuopio P.O. Box 1627, 70211 Kuopio, Finland
Bibliografia
  • [1] D.I. Angelbeck and A.B. Shah Alam: Simulation studies on optimization of the activated sludge process. JWPCF, 1 (1978), 31-39.
  • [2] J.P. Babary, T. Damak and N. Tali-Maamar: On simulation of distributed parameter bioreactors. Proc. 13th IMACS’91 World Congress on Computation and Applied Mathematics, Trinity College, Dublin, Ireland, (1991).
  • [3] J.P. Babary, S. Julien, M.T. Nihtilä, J. Czeczot and M. Metzger: New boundary conditions and adaptive control of fixed-bed bioreactors. Chem. Engng. and Processing, 38, (1999), 35-44.
  • [4] J.P. Babary, M.T. Nihtilä and D. Dochain: Modelling and control algorithms for denitrification of drinking water. Proc 2nd IMACS Multiconference, Computational Engineering in Systems Applications. Symposium on Modeling, Analysis and Control, Nabeul-Hammamet (Tunisie), 1 (1998), 35-39
  • [5] J.P. Babary, N. Tali-Maamar and D. Dochain: Modelling and control of distributed parameter bioreactors. Proc. Modelling and Control of Biotechnological, Ecological and Biomedical Systems, Varna, Bulgaria, (1990), 21-27.
  • [6] C. Benthack, B. Srinivasan and D. Bonvin: Optimal operation modes for a fixed-bed bioreactor used in wastewater treatment. Proc. IFAC World Congress, San Francisco, (1996).
  • [7] G. Bastin and D. Dochain: On-line estimation and adaptive control of bioreactors. Elsevier, Amsterdam, 1990.
  • [8] W.L. Carpenter: Temperature relationship in aerobic treatment and disposal of pulp and paper wastes. JWPCF, 42 (1968), 733-742.
  • [9] M.B. Carver and H.W. Hinds: The method of lines and advective equation. Simulation, 31 (1978), 59-69.
  • [10] D. Contois: Kinetics of bacterial growth relationship between population density and specific growth rate of continuous cultures. J. Gen. Microb. 21 (1959), 40-50.
  • [11] J. Czeczot: Modelling and simulation of distributed parameter bioreactor including the influence of temperature on dynamic properties. Proc. ESM’94, A. Guash and R. Huber, (Eds), Simulation Councils Inc., Barcelona, Spain, (1994), 714-717.
  • [12] J. Czeczot: Substrate Consumption Rate - New Concept of Measuring and Monitoring in the Activated Sludge Process. Proc. 6th IFAC Int. Conf. on Computer Applications in Biotechnology, A. Munack and K. Schugerl, (Eds), Pergamon Elsevier, Garmisch-Partenkirchen, Germany, (1995), 205-208.
  • [13] J. Czeczot: On application of the substrate consumption rate to the monitoring and control of the biological processes of the water purification. Ph.D. Thesis, Silesian University of Technology, Gliwice, (1997), (in Polish).
  • [14] J. Czeczot: Monitoring of the distributed parameter chemical reactor basing on the estimation of the reaction rate. Proc. 9th Int. Symp. System Modelling Control, P.S. Szczepaniak, (Ed), Zakopane, Poland, (1998).
  • [15] J. Czeczot, J.P. Babary and M.T. Nihtilä: Adaptive control of a distributed parameter bioreactor based on the substrate consumption rate estimation. Proc. Int. Workshop on Decision and Control on Waste Bioprocessing, Narbonne, France, (1998), 23-27.
  • [16] J. Czeczot, M. Metzger, J.P. Babary and M.T. Nihtilä: Filtering in adaptive control of distributed parameter bioreactors in the presence of noisy measurements. Simulation Practice and Theory, 8(1-2), (2000), 39-56.
  • [17] J. Czeczot, M. Metzger, M.T. Nihtilä and J.P. Babary: Substrate consumption rate in adaptive control of a distributed parameter bioreactor for noisy measurements. Proc. 1st Conf. on Modelling and Simulation in Biology, Medicine and Biomedical Engineering, Noisy-le-Grand, France, (1999), 74-78.
  • [18] T. Damak, J.P. Babary and M. Nihtilä: Observer design and sensor location in distributed parameter bioreactors. Proc. DYCORD’92, Pergamon, Oxford, (1992), 315-320.
  • [19] D. Dochain, J.P. Babary and N. Tali-Maamar: Modelling and adaptive control of nonlinear distributed parameter bioreactors via orthogonal collocation. Automatica, 28(5), (1992), 873-883.
  • [20] D. Dochain, N. Tali-Maamar and J.P. Babary: On modelling, monitoring and control of fixed bed bioreactors. Computers Chem. Engng., 21(11), (1997), 1255-1266.
  • [21] A. Isidori: Nonlinear control systems. Springer, Berlin, 1989.
  • [22] M. Metzger: Influence of the temperature on the dynamical properties of the activated sludge wastewater process. Proc. 1st IAWQ Int. Specialized Conf. on Microorganisms in Activated Sludge and Biofilm Processes, Paris, (1993), 463-466.
  • [23] M. Metzger: Modelling and simulation of time-delay element via advective equation. Proc. ESM’94, A. Guash and R. Huber, (Eds), Simulation Councils Inc., Barcelona, Spain, (1994), 714-717,
  • [24] M. Metzger: Modelling, simulation and control of continuous processes. Edition of Jacek Skalmierski Computer Studio, Gliwice, Poland, (2000).
  • [25] R. Pujol, M. Hamon, X. Kandel and H. Lemmel: Biofilters: Flexible, reliable biological reactors. Proc. IAWQ Int. Specialised Conf. on Biofilm Reactors, Paris, (1993), 69-76.
  • [26] W.E. Schiesser: The numerical methods of lines. Academic Press, San Diego, 1991.
  • [27] K. Shimizu: A tutorial review on bioprocesses systems engineering. Computers Chem. Engng., 20(6-7), (1996), 915-941.
  • [28] N. Tali-Maamar, T. Damak, J.P. Babary And M. Nihtilä: Application of a collocation method for simulation of distributed parameter bioreactors. Mathematics and Computers in Simulation, 35, (1993), 303-319.
  • [29] J. Villadsen and M.L. Michelsen: Solution of differential equation models by polynomial approximation. Prentice-Hall, Englewood Cliffs, New York, 1978.
  • [30] W. Waldraff, D. Dochain, S. Bourrel and A. Magnus: On the use of observability measures for sensor location in tubular reactor. J. Proc. Cont., 8(5- 6), (1998), 497-505.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BSW9-0005-1054
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