Abstract
Liquid circulation velocity was studied in externalloop air-lift bioreactors of laboratory and pilot scale, respectively for different gas input rates, downcomer-to-riser cross-sectional area ratio, A D/AR and liquid phase apparent viscosities.
It was found that, up to a gas superficial velocity in the riser v SGR ≈ 0.04 m/s the dependency of v SLR on v SGR is in the following form: v SLR = a v bSGR , with the exponent b being 0.40. Over this value of v SGR, only a small increase in liquid superficial velocity, v SLR is produced by an increase in v SGR.
A D/AR ratio affects the liquid superficial velocity due to the resistance in flow and overall friction.
For non-Newtonian viscous liquids, the circulation liquid velocity in the riser section of the pilot external-loop airlift bioreactor is shown to be dependent mainly on the downcomer-to-riser cross-sectional area ratio, A D/AR, the effective (apparent) liquid viscosity, η eff and the superficial gas velocity, v SGR.
The equation proposed by Popovic and Robinson [11] was fitted well, with an error of ± 20%.
Similar content being viewed by others
Abbreviations
- A D m2 :
-
downcomer cross-sectional area
- A Rm2 :
-
riser cross-sectional area
- a =:
-
coefficient in Eq. (7)
- b =:
-
exponent in Eq. (7)
- c s m−1 :
-
Coefficient in Eq. (3)
- D D m:
-
downcomer diameter
- D R m:
-
riser diameter
- g m2/s:
-
gravitational acceleration
- H D m:
-
dispersion height
- H L m:
-
ungassed liquid height
- K Pa sn :
-
consistency index
- K B =:
-
friction factor at the bioreactor bottom
- K F =:
-
friction factor
- K T =:
-
friction factor at the bioreactor top
- V L m3 :
-
liquid volume in the bioreactor
- V D m3 :
-
liquid volume in downcomer
- V R m3 :
-
liquid volume in riser
- v LDm/s:
-
downcomer linear liquid velocity
- v LR m/s:
-
riser linear liquid velocity
- v SGR m/s:
-
riser superficial liquid velocity
- v SLR m/s:
-
riser superficial liquid velocity
- \(\dot \gamma \) s−1 :
-
shear rate
- ε GD =:
-
downcomer gas holdup
- ε GR =:
-
riser gas holdup
- η eff Pa s:
-
effective (apparent) viscosity
- τ Pa:
-
shear stress
References
Blenke, H.: Loop Reactors. In: Ghose, T.K.; Fiechter, A.; Blackebrough, N. (Eds): Advances in biochemical engineering, vol. 13, pp. 121–214. Berlin: Springer Verlag, 1979
Jones, A.G.: Liquid Circulation in a draft-tube bubble column. Chem. Eng. Sci. 15 (1985) 449–462
Kawase, W.; Moo-Young, M.: Liquid circulation time in concentrictube airlift columns with non-newtonian fermentation broths. J. Chem. Tech. Biotechnol. 46 (1989) 267–274
Margaaritis, A.; Sheppard, J.: Mixing time and oxygen transfer characteristics of a double-draft-tube airlift fermentor. Biotechnol. Bioeng. 23 (1981) 2117–2135
Wachi, S.; Jones, A.G.; Elson, T.P.: Flow dynamics in a draft-tube bubble column using various liquids. Chem. Eng. Sci. 46 (1991) 657–663
Orazem, M.E.; Fan, L.T.; Erickson, L.E.: Bubble flow in the downflow section of an airlift tower. Biotechnol. Bioeng. 21 (1979) 1579–1606
Siegel, M.H.; Merchuk, J.C.; Schüger, K.: Air-lift reactor analysis interrelationships between riser, downcomer and gas-liquid separator behaviour, including gas recirculation effects. AIChEJ. 32 (1986) 1585–1596
Siegel, M.H.; Merchuk, J.C.: Mass transfer in a rectangular airlift reactor: effects of geometry and gas recirculation. Biotechnol. Bioeng. 32 (1988) 1128–1137
Hsu, Y.C.; Dudukovic, M.P.: Gas-holdup and liquid recirculation in gas-lift reactors. Chem. Eng. Sci. 35 (1980) 135–141
Weiland, P.: Untersuchung eines Airliftreaktors mit aüsserem Umlauf in Himblich auf seine Anwendung as Bioreaktor. PhD Thesis Dortmund University, Dortmund, 1978
Popovic, M.; Robinson, C.W.: External-circulation-loop airlift bioreactors: study of the liquid circulating velocity in highly viscous non-newtonian liquids. Biotechnol. Bioeng. 32 (1988) 301–312
Bello, R.A.; Robinson, C.W.; Moo-Young, M.: Mass transfer and liquid mixing in external-circulation-loop contactors. In: Moo-Young, M.; Robinson, C.W.; Vezina, C. (Eds): Advances in Biotechnology, Vol. 1. p. 547–552. Toronto: Pergamon Press, 1984
Bello, R.A.; Robinson, C.W.; Moo-Young, M.: Liquid circulation and mixing characteristics of airlift contactors. Can. J. Chem. Eng. 62 (1984) 573–577
Onken, U.; Weiland, P.: Airlift fermenters. Construction, behaviour and uses. In: Advances in Biotechnological Processes. vol. 1. pp. 67–95. New York: Alan R. Liss, Inc., 1983
Popovic, M.; Robinson, C.W.: Mixing characteristics of external-loop airlifts: non-newtonian systems. Chem. Eng. Sci. 48 (1993) 1405–1413
Verlaan, P.; Modelling and characterization of an airlift-loop bioreactor. PhD thesis, University of Wageningen, 1987
Merchuk, J.C.: Why use airlift bioreactors?. TIBTECH. 8 (1990) 66–71
Merchuk, J.C.; Stein, F.: Local holdup and liquid velocity in airlift reactors. AIChEJ 27 (1981) 377–388
Merchuk, J.C.; Stein, Y.; Mateles, R.I.: A distributed parameter model of an airlift fermenter, Biotechnol. Bioeng. 22 (1980) 1189–1211
Allen, D.G.; Robinson, C.W.: Measurement of rheological properties of filamentors fermentation broths. Chem. Eng. Sci. 45 (1990) 37–48
Gavrilescu, M.; Roman, R.V.; Efimov, V.: Rheological behaviour of some antibiotic biosynthesis liquids. Acta Biotechnol. 12 (1992) 383–396
Schumpe, A.; Deckwer, W-D.: Viscous media in tower bioreactors: hydrodynamic characteristics and mass transfer properties. Bioprocess Eng. 2 (1987) 79–84
Zaidi, A.; Bourziza, H.; Echihabi, L.: Wärmeübergang und effektives Schergefäle in Blasensäulen-Bioreaktoren mit Xanthan-Lösungen. Chem. Eng. Tech. 59 (1987) 748–749
Nishikawa, M.; Kato, H.; Hashimoto, K.; Heat transfer in aerated tower filled with non-newtonian liquid. Ind.Eng. Process Dev. 16 (1977) 133–137
Mercer, D.G.: Flow characteristics of a pilot-scale airlift fermentor. Biotechnol. Bioeng. 23 (1981) 2421–2431
Fields, P.R.; Slater, N.K.H.: Trancer dispersion in a laboratory air-lift reactor. Chem. Eng. Sci. 38 (1983) 647–653
Fan, L-S.; Hwang, S-J.; Matsuura, A.: Hydrodynamic behaviour of a draft-tube gas-liquid-solid spouted bed. Chem. Eng. Sci. 39 (1984) 1677–1688
Kawase, Yi; Moo-Young, M.: Liquid circulation time in concentrictube airlift columns with non-newtonian fermentation broths. J. Chem. Technol. Biotechnol. 46 (1989) 267–274
Chakrawarty, M.; Begum, S.; Singh, H.H.; Baruah, J.N.; Yengar, M.:gas holdup distribution in a gas-lift column. Biotechnol. Bioeng. Symp. 4 (1973) 363–378
Saxena, S.C.; Rao, N.S.; Thimmapuram, P.R.: Gas phase holdup in slurry bubble columns for two- and three- phase systems. The Chem. Eng. J. 49 (1992) 1551–1559
Weiland, P.; Onken, U.: Fluid dynamics and mass transfer in an air-lift fermentor with external-loop. Ger. Chem. Eng. 4 (1981) 42–48
Onken, U.; Weiland, P.: Hydrodynamics and mass transfer in an airlift loop fermentor. Eur. J. Appl. Microbiol. Biotechnol. 10 (1980) 31–40
Merchuk, J.C.; Stein, Y.: A distributed parameter model for an airlift fermentor. Effects of pressure. Biotechnol. Bioeng. 23 (1981) 1309–1324
Weiland, P.: Influence of draft-tube diameter on operation behaviour of airlift loop reactors. Ger. Chem. Eng. 7 (1984) 374–385
Lans, R.C.J.M. van der: Hydrodynamics of a bubble column loops reactor. PhD thesis, Delft University of Technology, Delft, 1985
Wallis, G.B.: One dimensional two-phase flow. New York, McGrawHill, 1969
Chisty, Y.: Airlift bioreactors. London-New-York: Elsevier Appl. Science, 1989
Hatch, R.T.: Experimental and theoretical studies of oxygen transfer in an airlift fermenter. PhD thesis, Massachussets Institute of Technology, Cambridge, 1973
Nicklin, D.J.; Wilkes, J.O.; Davidson, J.F.: Two-phase flow in vertical tubes. Trans. Inst. Chem. Eng. 40 (1962) 61–68
Author information
Authors and Affiliations
Additional information
The authors wish to thank Mrs. Rodica Roman for the help in experimental data collection and to Dr. Stefanluca for the financial support.
Rights and permissions
About this article
Cite this article
Gavrilescu, M., Tudose, R.Z. Study of the liquid circulation velocity in external-loop airlift bioreactors. Bioprocess Engineering 14, 33–39 (1995). https://doi.org/10.1007/BF00369850
Received:
Issue Date:
DOI: https://doi.org/10.1007/BF00369850