Cross-section perimeter is a suitable parameter to describe the effects of different baffle geometries in shaken microtiter plates

BackgroundBiotechnological screening processes are performed since more than 8 decades in small scale shaken bioreactors like shake flasks or microtiter plates. One of the major issues of such reactors is the sufficient oxygen supply of suspended microorganisms. Oxygen transfer into the bulk liquid can in general be increased by introducing suitable baffles at the reactor wall. However, a comprehensive and systematic characterization of baffled shaken bioreactors has never been carried out so far. Baffles often differ in number, size and shape. The exact geometry of baffles in glass lab ware like shake flasks is very difficult to reproduce from piece to piece due to the hard to control flow behavior of molten glass during manufacturing. Thus, reproducibility of the maximum oxygen transfer capacity in such baffled shake flasks is hardly given.ResultsAs a first step to systematically elucidate the general effect of different baffle geometries on shaken bioreactor performance, the maximum oxygen transfer capacity (OTRmax) in baffled 48-well microtiter plates as shaken model reactor was characterized. This type of bioreactor made of plastic material was chosen, as the exact geometry of the baffles can be fabricated by highly reproducible laser cutting. As a result, thirty different geometries were investigated regarding their maximum oxygen transfer capacity (OTRmax) and liquid distribution during shaking. The relative perimeter of the cross-section area as new fundamental geometric key parameter is introduced. An empirical correlation for the OTRmax as function of the relative perimeter, shaking frequency and filling volume is derived. For the first time, this correlation allows a systematic description of the maximum oxygen transfer capacity in baffled microtiter plates.ConclusionsCalculated and experimentally determined OTRmax values agree within ± 30% accuracy. Furthermore, undesired out-of-phase operating conditions can be identified by using the relative perimeter as key parameter. Finally, an optimum well geometry characterized by an increased perimeter of 10% compared to the unbaffled round geometry is identified. This study may also assist to comprehensively describe and optimize the baffles of shake flasks in future.

[1]  E. Galindo,et al.  Interaction of cultural conditions and end-product distribution in Bacillus subtilis grown in shake flasks , 1989, Applied Microbiology and Biotechnology.

[2]  Per Christian Hansen,et al.  Analysis of Discrete Ill-Posed Problems by Means of the L-Curve , 1992, SIAM Rev..

[3]  Frank Kensy,et al.  Oxygen transfer phenomena in 48-well microtiter plates: determination by optical monitoring of sulfite oxidation and verification by real-time measurement during microbial growth. , 2005, Biotechnology and bioengineering.

[4]  E. G. Bailey,et al.  Effect of Oxygen-Supply Rates on Growth of Escherichia coli , 1965, Applied microbiology.

[5]  J Büchs,et al.  Out-of-phase operating conditions, a hitherto unknown phenomenon in shaking bioreactors. , 2001, Biochemical engineering journal.

[6]  J. Büchs,et al.  Characterization of gas-liquid mass transfer phenomena in microtiter plates. , 2003, Biotechnology and bioengineering.

[7]  Pedro Fernandes,et al.  Microlitre/millilitre shaken bioreactors in fermentative and biotransformation processes – a review , 2006 .

[8]  J Büchs,et al.  Optical method for the determination of the oxygen-transfer capacity of small bioreactors based on sulfite oxidation. , 2001, Biotechnology and bioengineering.

[9]  A. Schumpe,et al.  Estimation of gas solubilities in salt solutions at temperatures from 273 K to 363 K , 1996 .

[10]  H. J. Henzler,et al.  Suitability of the shaking flask for oxygen supply to microbiological cultures , 1991 .

[11]  Dianne P. O'Leary,et al.  The Use of the L-Curve in the Regularization of Discrete Ill-Posed Problems , 1993, SIAM J. Sci. Comput..

[12]  J. Büchs,et al.  Characterisation of the gas-liquid mass transfer in shaking bioreactors. , 2001, Biochemical engineering journal.

[13]  J. Büchs,et al.  Power consumption in shaking flasks on rotary shaking machines: II. Nondimensional description of specific power consumption and flow regimes in unbaffled flasks at elevated liquid viscosity. , 2000, Biotechnology and bioengineering.

[14]  J Büchs,et al.  Quasi-continuous combined scattered light and fluorescence measurements: a novel measurement technique for shaken microtiter plates. , 2005, Biotechnology and bioengineering.

[15]  Frank Kensy,et al.  The baffled microtiter plate: Increased oxygen transfer and improved online monitoring in small scale fermentations , 2009, Biotechnology and bioengineering.

[16]  Nicolas Szita,et al.  Oxygen Transfer Characteristics of Miniaturized Bioreactor Systems , 2013, Biotechnology and bioengineering.

[17]  David Pollard,et al.  A review of advanced small‐scale parallel bioreactor technology for accelerated process development: Current state and future need , 2011, Biotechnology progress.

[18]  J. Büchs,et al.  Advances in shaking technologies. , 2012, Trends in biotechnology.

[19]  J Büchs,et al.  Introduction to advantages and problems of shaken cultures. , 2001, Biochemical engineering journal.

[20]  W. Duetz,et al.  Microtiter plates as mini-bioreactors: miniaturization of fermentation methods. , 2007, Trends in microbiology.

[21]  Krist V Gernaey,et al.  Application of microbioreactors in fermentation process development: a review , 2009, Analytical and bioanalytical chemistry.