Online optimal experimental re-design in robotic parallel fed-batch cultivation facilities

dc.contributor.authorCruz Bournazou, Mariano Nicolas
dc.contributor.authorBarz, Tilman
dc.contributor.authorNickel, D. B.
dc.contributor.authorLopez Cárdenas, Diana Carolina
dc.contributor.authorGlauche, Florian
dc.contributor.authorKnepper, Andreas
dc.contributor.authorNeubauer, Peter
dc.date.accessioned2022-05-11T09:08:20Z
dc.date.available2022-05-11T09:08:20Z
dc.date.issued2016-10-03
dc.description.abstractWe present an integrated framework for the online optimal experimental re-design applied to parallel nonlinear dynamic processes that aims to precisely estimate the parameter set of macro kinetic growth models with minimal experimental effort. This provides a systematic solution for rapid validation of a specific model to new strains, mutants, or products. In biosciences, this is especially important as model identification is a long and laborious process which is continuing to limit the use of mathematical modeling in this field. The strength of this approach is demonstrated by fitting a macro-kinetic differential equation model for Escherichia coli fed-batch processes after 6 h of cultivation. The system includes two fully-automated liquid handling robots; one containing eight mini-bioreactors and another used for automated at-line analyses, which allows for the immediate use of the available data in the modeling environment. As a result, the experiment can be continually re-designed while the cultivations are running using the information generated by periodical parameter estimations. The advantages of an online re-computation of the optimal experiment are proven by a 50-fold lower average coefficient of variation on the parameter estimates compared to the sequential method (4.83% instead of 235.86%). The success obtained in such a complex system is a further step towards a more efficient computer aided bioprocess development. Biotechnol. Bioeng. 2017;114: 610–619. © 2016 Wiley Periodicals, Inc.en
dc.description.sponsorshipBMBF, 02PJ1150, Verbundprojekt: Plattformtechnologien für automatisierte Bioprozessentwicklung (AutoBio); Teilprojekt: Automatisierte Bioprozessentwicklung am Beispiel von neuen Nukleosidphosphorylasenen
dc.identifier.eissn1097-0290
dc.identifier.issn0006-3592
dc.identifier.urihttps://depositonce.tu-berlin.de/handle/11303/16866
dc.identifier.urihttp://dx.doi.org/10.14279/depositonce-15644
dc.language.isoenen
dc.rights.urihttp://rightsstatements.org/vocab/InC/1.0/en
dc.subject.ddc570 Biowissenschaften; Biologiede
dc.subject.otherE. collien
dc.subject.otherfed-batch processen
dc.subject.otheronline Optimal Experimental re-designen
dc.subject.othermacro-kinetic growth modelen
dc.subject.otherHigh Throughput Bioprocess Developmenten
dc.subject.otherparallel mini bioreactorsen
dc.subject.otherParameter Estimationen
dc.titleOnline optimal experimental re-design in robotic parallel fed-batch cultivation facilitiesen
dc.typeArticleen
dc.type.versionacceptedVersionen
dcterms.bibliographicCitation.doi10.1002/bit.26192en
dcterms.bibliographicCitation.issue3en
dcterms.bibliographicCitation.journaltitleBiotechnology & bioengineeringen
dcterms.bibliographicCitation.originalpublishernameWileyen
dcterms.bibliographicCitation.originalpublisherplaceNew York, NYen
dcterms.bibliographicCitation.pageend619en
dcterms.bibliographicCitation.pagestart610en
dcterms.bibliographicCitation.volume114en
tub.accessrights.dnbfreeen
tub.affiliationFak. 3 Prozesswissenschaften::Inst. Biotechnologie::FG Bioverfahrenstechnikde
tub.affiliation.facultyFak. 3 Prozesswissenschaftende
tub.affiliation.groupFG Bioverfahrenstechnikde
tub.affiliation.instituteInst. Biotechnologiede
tub.publisher.universityorinstitutionTechnische Universität Berlinen

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