Abstract
During the bioconversion of tetralin in the liquid-impelled loop reactor, oxygen and tetralin are transferred from the organic-solvent phase to the aqueous phase. Mass transfer of either tetralin or oxygen is likely to be the rate-limiting step in this bioconversion. In order to establish which of the two is limiting, the overall mass-transfer coefficients (K i,L A) of both substrates were determined. Theoretical calculations did not reveal large differences. Therefore both K i,L A's were experimentally determined as well. From the results it is concluded that neither tetralin nor oxygen can be assigned to be the mass-transfer-limiting factor if tetralin is completely converted into CO2 and H2O. On the other hand, if tetralin is oxidized only partly (the aim of our synthetic studies), it very likely is the limiting substrate and process control can thus be achieved by controlling the supply of this toxic compound.
Similar content being viewed by others
Abbreviations
- ρ s kg/m3 :
-
solvent density
- vs m/s:
-
slip velocity of the drops=vs s /a-vs L /(1-a)
- vs s , vs L m/s:
-
superficial velocity of the organic-solvent phase and the aqueous phase, respectively, in the main tube of the LLR
- a :
-
holdup of organic-solvent phase in the main tube of the LLR
- d m:
-
drop diameter
- n s Pa s:
-
dynamic viscosity of the organic-solvent phase
- D L m2/s:
-
diffusion coefficient of solute in the aqueous phase
- Re L :
-
Reynolds number of the aqueous phase around the drops ρ L vs dη L
- ρ L kg/m3 :
-
density of the aqueous phase
- η L Pa s:
-
dynamic viscosity of the aqueous phase
- Sc L :
-
Schmidt number of the aqueous phase=η L /ρ -1 L D L
- g m/s2 :
-
gravitational acceleration
- F :
-
correction factor for the circulation within the droplets
- σ N m:
-
interfacial tension
- D s m2/s:
-
diffusion coefficient of solute in the organic-solvent phase
- t s:
-
time of contact
- B n :
-
coefficient
- λ n :
-
nth eigen value
References
Laane, C.; Tramper, J.; Lilly, M. D. (Eds.): Biocatalysis in organic media. Amsterdam: Elsevier, 1987
Tramper, J.; Vermuë, M. H.; Beeftink, H. H.; Von Stockar, U. (Eds.): Biocatalysis in non-conventional media. Amsterdam: Elsevier, 1992
Bruce, L. J.; Daugulis, A. J.: Solvent selection strategies for extractive biocatalysis. Biotechnol. Prog. 7 (1991) 116–124
Vermuë, M. H.; Tramper, J.: Extractive biocatalysis in a liquid-impelled loop reactor. In: Christiansen, C., Munck, J., Villadsen, J. (Eds.): Proceedings of the 5th European congress on biotechnology, pp 243–246. Copenhagen: Munksgaard 1990
Tramper, J.; Wolters, I.; Verlaan, P.: The liquid-impelled loop reactor: a new type of density-difference-mixed bioreactor. In: Laane, C., Tramper, J., Lilly, M. D. (Eds.): Biocatalysis in organic media, pp 311–316. Amsterdam: Elsevier 1987
Van Sonsbeek, H. M.; Verdurmen, R. E. M.; Verlaan, P.; Tramper, J.: Hydrodynamic model for liquid-impelled loop reactors. Biotechnol. Bioeng. 36 (1990) 940–946
Van Sonsbeek, H. M.; Van Der Tuin, S. P.; Tramper, J.: Mixing in liquid-impelled loop reactors. Biotechnol. Bioeng. 39 (1992) 707–716
Van Sonsbeek, H. M.; De Blank, H.; Tramper, J.: Oxygen transfer in liquid-impelled loop reactors using perflurocarbon liquids. Biotechnol. Bioeng. 40 (1992) 713–718
Van Sonsbeek, H. M.; Gielen, S. J.; Tramper, J.: Steady-state method for KA measurements in model systems. Biotechnol. Techn. 5 (1991) 157–162
Van Sonsbeek, H. M.: Physical aspects of liquid-impelled loop reactors. PhD thesis, Wageningen Agricultural University, Wageningen, The Netherlands, 1992
Sikkema, J.; De Bont, J. A. M.: Isolation and initial characterization of bacteria growing on tetralin. Biodegradation 2 (1991) 15–23
Sikkema, J.: Microbial transformation of tetralin, PhD thesis, Wageningen Agricultural University, Wageningen, The Netherlands, 1993
Van't Riet, K.; Tramper, J.: Basic bioreactor design. New York: Marcel Dekker 1991
Al-Aswad, K. K.; Mumford, C. J.; Jeffreys, G. V.: The application of drop-size distribution and discrete drop mass-transfer models to assess the performance of a rotating disc contractor. AIChE Journal 31 (1985) 1488–1497
Hughmark, G. A.: Liquid-liquid spray column drop size, holdup, and continuous phase mass transfer. Ind. & Eng. Fundamentals 6 (1967) 408–413
Kronig, R.; Brink, J. C.: On the theory of extraction from falling droplets. Appl. Res. A2 (1950) 142–154
Rose, P. M.; Kintner, R. C.: Mass transfer from large oscillating drops. AIChE Journal 12 (1966) 530–534
Wilke, C. R.; Chang, P.: AIChE Journal 1 (1955) 264–270
Handbook of Chemistry and Physics, 60th edition. Boca Raton, Florida, CRC press
Ju, L. K.; Lee, J. F.; Armiger, W. B.: Effect of the interfacial surfactant layer on oxygen transfer through the oil/water phase boundary in perfluorocarbon emulsions. Biotechnol. Bioeng. 37 (1991) 505–511
Ju, L. K.; Ho, C. S.: Measuring oxygen diffusion coefficients with polarografic oxygen electrodes. I. Electrolytic solutions. Biotechnol. Bioeng. 27 (1985) 1495–1499
Perry, R. H.; Green, D. W.; Maloney, J. O. (Eds.): Perry' Chemical Engineers' Handbook, 6th edition. New York: McGraw-Hill 1984
Author information
Authors and Affiliations
Additional information
The authors wish to thank W.A. Beverloo for the helpful critical comments in the preparation of the manuscript. Part of this work was financially supported by the Dutch Committee of Industrial Biotechnology.
Rights and permissions
About this article
Cite this article
Vermuë, M., Tacken, M. & Tramper, J. Tetralin and oxygen transfer in the liquid-impelled loop reactor. Bioprocess Engineering 11, 224–228 (1994). https://doi.org/10.1007/BF00387696
Received:
Issue Date:
DOI: https://doi.org/10.1007/BF00387696