Abstract
Bioreactors are compared based on oxygen transfer rate and efficiency, mixing performance, cell mass productivity as well as with respect to enzyme and metabolite productivity.
Similar content being viewed by others
Abbreviations
- AC:
-
acetate concentration
- AL:
-
airlift tower loop reactor
- CFU:
-
colony-forming units
- CP:
-
coalescence-promoting medium
- CS:
-
coalescence-suppressing medium
- D D :
-
impeller clearance
- D M :
-
molecular diffusivity
- D S :
-
diameter of the column
- DT:
-
flat-bladed disc turbine
- D v :
-
vessel diameter
- E. act:
-
enzyme activity
- EDR:
-
energy dissipation rate
- EcoRI:
-
restriction endonuclease
- EcoR4:
-
protection plasmid
- E O 2 :
-
efficiency of oxygen transfer rate
- E X :
-
efficiency of cell mass production with respect to the specific power input
- g :
-
acceleration of gravity
- H :
-
height of column
- H v :
-
vessel height
- HV:
-
highly viscous medium
- IPTG:
-
isopropyl thiogalactoside (inducer of Lacpromoter)
- k :
-
fluid consistency factor
- k L :
-
mass transfer coefficient
- k La:
-
volumetric mass transfer coefficient
- m :
-
exponent
- N :
-
impeller speed
- n :
-
exponent
- n :
-
flow behaviour index
- P :
-
power input
- P/VL :
-
specific power input
- PR:
-
marine propeller
- P LacUV5 :
-
Lac-promoter-induced by IPTG
- P R :
-
promoter-induced with temperature shift
- ϱ O 2 :
-
oxygen transfer rate
- q g,q O 2 :
-
aeration rate, specific aeration rate with respect to liquid volume
- R :
-
density of cultivation medium
- R p :
-
product formation rate
- R X :
-
growth rate
- SpA:
-
protein A
- ST:
-
stirred tank reactor
- TCC:
-
total cell count
- t Lc :
-
liquid circulation time
- U :
-
enzyme activity unit
- u B :
-
bubble rise velocity
- u G :
-
superficial gas velocity
- V L :
-
volume of the liquid phase
- v :
-
kinematic viscosity of the cultivation medium
- W SG :
-
superficial gas velocity
- X :
-
cell mass concentration
- Y E/S :
-
yield coefficient of ethanol formation with respect to substrate consumption
- Y P/X :
-
specific product formation with respect to cell concentration
- Y X/E :
-
yield coefficient of cell growth with respect to ethanol consumption
- Y X/O 2 :
-
yield coefficient of cell growth with respect to oxygen consumption rate
- Y X/S :
-
yield coefficient of growth with respect to substrate consumption
- θ L :
-
liquid mixing time
- μ eff :
-
effective dynamic viscosity of the cultivation medium
- μ W :
-
dynamic viscosity of water
- μ max :
-
maximum specific growth rate
- σ :
-
surface tension of the cultivation medium
References
Schügerl, K.: Bioreaction Engineering. Vol. 2, 1991, Wiley, Chichester
Rüffer, M.: personal communication, 1991
Wan Liwei: Detaillierte Untersuchungen des Mischverhaltens realer Merhphasenreaktoren. Dissertation, University Hannover, Fortschritt Berichte VDI, Reihe 8: 1990, Nr. 228
Blenke, H.: Loop reactors, In: Adv. Biochem. Eng. T. K. Ghose, A. Fiechter, N. Blakebrough (Eds.), Springer, Berlin. 13, 1979, 121–214
Reuss, M.; Brammer, U.: Influence of Substrate distribution on productivities in computer controlled baker's yeast production. In “Modelling and Control of Biotechnological Processes” IFAC Symposium 1985, A. Johnson, (Ed.), Pergamon Press, Oxford, 1985. 119–124
Adler, I.; Fiechter, A.: Valuation of bioreactors for low viscous media and high oxygen transfer demand. Bioprocess Engng. 1 (1986) 51–59
Schlüter, V.; Yonsel, S.; Deckwer, W. D.: Korrelation der 02Stoffübergangskoeffizienten (kLa) in Rührreaktoren mit niederviskosen fermentationsmedien. Chem. Ing. Techn. 64 (1992) 474–475 (Synopse MS 2046/92)
Herbst, H.; Schumpe, A.; Deckwer, W. D.: Xanthan production in stirred tank fermentors: Oxygen transfer and scale-up. Chem. Eng. Technol. 1992, submitted for publication
Kawase, Y.; Moo-Young, M.: Volumetric mass transfer coefficients in aerated stirred tank reactors with Newtonian and non-Newtonian media. Chem. Eng. Res. Dev. 66 (1988) 284–288
Suh, I. S.; Schumpe, A.; Deckwer, W. D.: Xanthan production in bubble column and airlift reactors. Biotechnol. Bioeng. 39 (1990) 85–94
Oosterhuis, N. M. G.; Kossen, N. W. F.; Olivier, A. P. C.; Schenk, E. S.: Scale down and optimization studies of the gluconic acid fermentation by Gluconobacter oxydans. Biotechnol. Bioeng. 27 (1985) 711–720
Sweere, A. P. J.; Mesters, J. R.; Jansen, L.; Luyben, K. Ch. A. M.; Kossen, N. W. F.: Experimental simulation of oxygen profiles and their influence on baker's yeast production: I. One-fermentor system. Biotechnol. Bioeng. 31 (1988) 567–578
Sweere, A. P. J.; Jansen, L.; Luyben, K. Ch. A. M.; Kossen, N. W. F.: Experimental simulation of oxygen profiles and their influence on baker's yeast production: II. Two-fermentor system. Biotechnol. Bioeng. 31 (1988) 579–586
Abel, C.: Untersuchungen zum Scale down von Gelöstsauerstoffbedingungen bei Backhefe-Fermentationen. Dissertation, University of Hannover, 1990
Fröhlich, S.; Lotz, M.; Korte, T.; Lübbert, A.; Schügerl, K.; Seekamp, M.: Characterization of a pilot plant airlift tower loop bioreactor I: Evaluation of phase properties with model media. Biotechnol. Bioeng. 38 (1990) 43–55
Fröhlich, S.; Lotz, M.; Korte, T.; Lübbert, A.; Schügerl. K.; Seekamp, M.: Characterization of a pilot plant airlift tower loop bioreactor II: Evaluation of the global mixing properties of the gas phase during cultivation. Biotechnol. Bioeng. 38 (1991) 43–55
Schügerl, K.: Nonmechanically Agitated Bioreactor Systems. In: M. Moo-Young, (Ed.) Comprehensive Biotechnology. Vol. 2 C. L. Cooney; A. E. Humphrey (Vol. Eds.) Pergamon Press, Oxford, 1985, 99–118
Brandes, L.: Optimierung der Prozeßführung in einem Air-lift-Schlaufenreaktor mit rekombinanten Escherichia coli zur Produktion des Fusionsproteins aus SPA und EcoRI. Dissertation, University of Hannover, 1991
Wu Xiaoan: Überproduktion eines rekombinanten Proteins mit multi-plasmidhaltigen Escherichia coli in einem Air-lift Schlaufenreaktor. Optimierung der Prozeßführung. Dissertation, University of Hannover, 1992
Vidal-Ingigliardi, D.; Raibaud, O.: A convenient tenhnique to compare the efficiency of promoter in Escherichia coli. Nucleids Acids Research 13 (1985) 5919–5926
Bukland, B. C.; Gbewonyo, K.; Jain, D.; Glazomitzky, K.; Hunt, G.; Drew, S. W.: Oxygen transfer efficiency of hydrofoil impellers in both 8001 and 19 0001 fermentors. In: R. King (Ed.): 2nd Internat. Conference on Bioreactor Fluid dynamics, Cambridge, UK. 21–23 Sept. Elsevier, Eondon, 1988, 1–15
Möller, J.; Niehoff J.; Hotop, S.; Dors, M.; Schügerl, K.: The influence of preculture on the process performance of penicillin V production in a 100-l airlift tower loop reactor. Appl. Microbiol. Biotechnol. 37 (1992) 157–163
Möller, J.: Penicillin-Production mit einem Hochleistungsstamm von penicillium chrysogenum. Chromatographische Methoden zur Prozeßkontrolle. Dissertation, University of Hannover, 1987
Schügerl, K.: Comparison of the performances of stirred tank and airlift tower loop reactors. J. of Biotechnology 13 (1190) 251–256
Lübbert, A.; Larson, B.: Detailed investigations of the multiphase flow in airlift tower loop reactors. Chem. Eng. Sci. 45 (1990) 3047–3053
Bröring, S.; Fischer, J.; Korte, T.; Sollinger, S.; Lübbert, A.: Flow structure of the dispersed gasphase in real multiphase chemical reactors investigated by a new ultrasound-doppler technique. Can. J. of Chem. Eng. 69 (1991) 1247–1256
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Schügerl, K. Comparison of different bioreactor performances. Bioprocess Engineering 9, 215–223 (1993). https://doi.org/10.1007/BF00369405
Received:
Issue Date:
DOI: https://doi.org/10.1007/BF00369405