An industrial perspective on bioreactor scale-down: what we can learn from combined large-scale bioprocess and model fluid studies.

For industrial bioreactor design, operation, control and optimization, the scale-down approach is often advocated to efficiently generate data on a small scale, and effectively apply suggested improvements to the industrial scale. In all cases it is important to ensure that the scale-down conditions are representative of the real large-scale bioprocess. Progress is hampered by limited detailed and local information from large-scale bioprocesses. Complementary to real fermentation studies, physical aspects of model fluids such as air-water in large bioreactors provide useful information with limited effort and cost. Still, in industrial practice, investments of time, capital and resources often prohibit systematic work, although, in the end, savings obtained in this way are trivial compared to the expenses that result from real process disturbances, batch failures, and non-flyers with loss of business opportunity. Here we try to highlight what can be learned from real large-scale bioprocess in combination with model fluid studies, and to provide suitable computation tools to overcome data restrictions. Focus is on a specific well-documented case for a 30-m(3) bioreactor. Areas for further research from an industrial perspective are also indicated.

[1]  Michael Lester,et al.  Feasibility of an in situ measurement device for bubble size and distribution , 2007, Bioprocess and biosystems engineering.

[2]  Alvin W Nienow,et al.  The scale-up of microbial batch and fed-batch fermentation processes. , 2007, Advances in applied microbiology.

[3]  Pfefferlé,et al.  A special reactor design for investigations of mixing time effects in a scaled-down industrial L-lysine fed-batch fermentation process , 1999, Biotechnology and bioengineering.

[4]  Dirk Weuster-Botz,et al.  Scale-down and parallel operation of the riboflavin production process with Bacillus subtilis , 2007 .

[5]  Gen Larsson,et al.  Influence of oxygen starvation on the respiratory capacity of Penicillium chrysogenum , 1985, Applied Microbiology and Biotechnology.

[6]  E. Postma,et al.  Kinetics of growth and glucose transport in glucose‐limited chemostat cultures of Saccharomyces cerevisiae CBS 8066 , 1989, Yeast.

[7]  M. Lilly,et al.  Effect of cycling dissolved oxygen concentrations on product formation in penicillin fermentations , 1982, European journal of applied microbiology and biotechnology.

[8]  Serafim Bakalis,et al.  Using positron emission particle tracking (PEPT) to study the turbulent flow in a baffled vessel agitated by a Rushton turbine: Improving data treatment and validation , 2011 .

[9]  Beth Junker,et al.  Sustainable reduction of bioreactor contamination in an industrial fermentation pilot plant. , 2006, Journal of bioscience and bioengineering.

[10]  Matthias Reuss,et al.  Integration of physiology and fluid dynamics. , 2003, Advances in biochemical engineering/biotechnology.

[11]  W. Kelly,et al.  Using computational fluid dynamics to characterize and improve bioreactor performance , 2008, Biotechnology and applied biochemistry.

[12]  Alvin W. Nienow,et al.  Gas–liquid dispersion with dual Rushton impellers , 1989 .

[13]  J. Teixeira,et al.  Proof‐of‐concept of a novel micro‐bioreactor for fast development of industrial bioprocesses , 2006, Biotechnology and bioengineering.

[14]  C. McFarlane,et al.  Scale-down model to simulate spatial pH variations in large-scale bioreactors. , 2001, Biotechnology and bioengineering.

[15]  M Ahman,et al.  Response of guanosine tetraphosphate to glucose fluctuations in fed-batch cultivations of Escherichia coli. , 1995, Journal of biotechnology.

[16]  J. Heijnen,et al.  Characterization of an experimental miniature bioreactor for cellular perturbation studies , 2006, Biotechnology and bioengineering.

[17]  Alvin W. Nienow,et al.  Mixing in large-scale vessels stirred with multiple radial or radial and axial up-pumping impellers: modelling and measurements , 2000 .

[18]  N. Oosterhuis,et al.  Dissolved oxygen concentration profiles in a production-scale bioreactor. , 1984, Biotechnology and bioengineering.

[19]  John D. Brooks,et al.  The Effect of Discontinuous Methanol Addition on the Growth of a Carbon-limited Culture of Pseudomonas , 1973 .

[20]  Shantanu Roy,et al.  Optimal design of radioactive particle tracking experiments for flow mapping in opaque multiphase reactors. , 2002, Applied radiation and isotopes : including data, instrumentation and methods for use in agriculture, industry and medicine.

[21]  Sven-Olof Enfors,et al.  Studies of insufficient mixing in bioreactors: Effects of limiting oxygen concentrations and short term oxygen starvation on Penicillium chrysogenum , 1988 .

[22]  E. Collet,et al.  Substrate gradient formation in the large-scale bioreactor lowers cell yield and increases by-product formation , 1998 .

[23]  R. Mudde,et al.  Computational Study of Hydrodynamics of a Standard Stirred Tank Reactor and a Large-Scale Multi-Impeller Fermenter , 2009 .

[24]  C. Hewitt,et al.  Physiological responses to mixing in large scale bioreactors. , 2001, Journal of biotechnology.

[25]  P. Mavros,et al.  FLOW VISUALIZATION IN STIRRED VESSELS A Review of Experimental Techniques , 2001 .

[26]  Gen Larsson,et al.  Comparison of the Baker's yeast process performance in laboratory and production scale , 1998 .

[27]  Alexei Lapin,et al.  Numerical simulation of the dynamics of two-phase gasliquid flows in bubble columns , 1994 .

[28]  Peter Neubauer,et al.  Scale-down simulators for metabolic analysis of large-scale bioprocesses. , 2010, Current opinion in biotechnology.

[29]  S. Enfors,et al.  A scale-down two-compartment reactor with controlled substrate oscillations: Metabolic response of Saccharomyces cerevisiae , 1993 .

[30]  Hilal Taymaz-Nikerel,et al.  Fast dynamic response of the fermentative metabolism of Escherichia coli to aerobic and anaerobic glucose pulses , 2009, Biotechnology and bioengineering.

[31]  H. Noorman,et al.  Substrate gradients in bioreactors: origin and consequences , 1996 .

[32]  Advanced methods for bioreactor characterization. , 1992, Journal of biotechnology.

[33]  K. Luyben,et al.  Experimental simulation of glucose fluctuations , 1988, Applied Microbiology and Biotechnology.

[34]  Peter Vrábel,et al.  Compartment Model Approach: Mixing in Large Scale Aerated Reactors with Multiple Impellers , 1999 .

[35]  Matthias Reuss,et al.  Coupling of mixing and microbial kinetics for evaluating the performance of bioreactors , 1982 .

[36]  K. Luyben,et al.  Scale-up of stirring as foam disruption (SAFD) to industrial scale , 2003, Journal of Industrial Microbiology and Biotechnology.