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Bioprocess control from a multivariate process trajectory.
Linköping University, Department of Physics, Chemistry and Biology, Biotechnology. Linköping University, The Institute of Technology. Novozymes Biopharma AB, Lund, Sweden.
Linköping University, The Institute of Technology. Linköping University, Department of Physics, Chemistry and Biology, Biotechnology.ORCID iD: 0000-0001-9711-794X
2004 (English)In: Bioprocess and biosystems engineering (Print), ISSN 1615-7591, E-ISSN 1615-7605, Vol. 26, no 6, p. 401-411Article in journal (Refereed) Published
Abstract [en]

A multivariate bioprocess control approach, capable of tracking a pre-set process trajectory correlated to the biomass or product concentration in the bioprocess is described. The trajectory was either a latent variable derived from multivariate statistical process monitoring (MSPC) based on partial least squares (PLS) modeling, or the absolute value of the process variable. In the control algorithm the substrate feed pump rate was calculated from on-line analyzer data. The only parameters needed were the substrate feed concentration and the substrate yield of the growth-limiting substrate. On-line near-infrared spectroscopy data were used to demonstrate the performance of the control algorithm on an Escherichia coli fed-batch cultivation for tryptophan production. The controller showed good ability to track a defined biomass trajectory during varying process dynamics. The robustness of the control was high, despite significant external disturbances on the cultivation and control parameters.

Place, publisher, year, edition, pages
2004. Vol. 26, no 6, p. 401-411
National Category
Natural Sciences
Identifiers
URN: urn:nbn:se:liu:diva-40927DOI: 10.1007/s00449-003-0327-zLocal ID: 54656OAI: oai:DiVA.org:liu-40927DiVA, id: diva2:261776
Available from: 2009-10-10 Created: 2009-10-10 Last updated: 2023-11-02
In thesis
1. Multivariate monitoring, modelling and control for stabilization of bioprocesses
Open this publication in new window or tab >>Multivariate monitoring, modelling and control for stabilization of bioprocesses
2002 (English)Doctoral thesis, comprehensive summary (Other academic)
Abstract [en]

The obstacles to overcome low reproducibility and stability of bioprocesses are numerous. Underlying biochemical processes are inherently non-linear, complex and subject to shifting initial conditions. Problems with high variability are also associated to production strains and scale-up of a bioprocess to largescale bioreactors. Reliable on-line monitoring of key process variables is still a challenging task and hinders the closed-loop control of these key process variables. In this thesis, methods for stabilization of bioprocesses by means of multivariate on-line monitoring, modelling and control are studied.

The foundation was laid with the development of integrated multivariate bioprocess monitoring, modelling and control within a real-time knowledge-based expert system. Thereby, a large number of signals from different advanced on-line analyzers ranging from mass spectroscopy via on-line HPLC to nearinfrared spectroscopy and electronic noses, could be used in combination with a variety of multivariate modelling and control tools for a flexible development of methods for stabilization of bioreactor processes. Subsequently, it could be shown how problems related to the initial conditions of a bioprocess can be solved by a multivariate assessment of the preculture quality. Furthermore, it was demonstrated how qualitative and quantitative key process variables can be made available and applied for process supervision; here, multivariate statistical process modelling and neural network sensor fusion from on-line monitoring of bioprocesses with advanced on-line analyzers were used. Finally, a closed-loop control method was presented, showing how feedback control of a multivariate key process variable trajectory can improve adherence to the specifications of the bioprocess. As model systems, aerobic fed-batch cultivations using recombinant Escherichia coli and anaerobic yoghurt batch fermentations have been used. The results provide general methods for multivariate stabilization of bioprocesses in precultivation steps, laboratory-scale and production-scale. They show that multivariate monitoring, modelling and control can provide a functional and versatile framework for reduced batch-tobatch variation and stabilization of bioprocesses with possible implications on product quality and process economics.

Place, publisher, year, edition, pages
Linköping: Linköping University, 2002. p. 57
Series
Linköping Studies in Science and Technology. Dissertations, ISSN 0345-7524 ; 788
National Category
Control Engineering
Identifiers
urn:nbn:se:liu:diva-179550 (URN)9173734721 (ISBN)
Public defence
2002-12-12, hörsal Key 1, K-huset, Linköpings universitet, Linköping, 13:30
Opponent
Available from: 2021-09-24 Created: 2021-09-24 Last updated: 2023-03-07Bibliographically approved

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Mandenius, Carl-Fredrik

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