Details

Title

Continuous mathematical models of airlift bioreactors: Families, affinity, diversity and modelling for single-substrate kinetics

Journal title

Chemical and Process Engineering

Yearbook

2012

Numer

No 2 June

Authors

Keywords

airlift biorector ; single-substrate kinetics ; mathematical modelling ; simulation ; multiphase reactors

Divisions of PAS

Nauki Techniczne

Coverage

291-309

Publisher

Polish Academy of Sciences Committee of Chemical and Process Engineering

Date

2012

Type

Artykuły / Articles

Identifier

ISSN 0208-6425

References

Báleš Vl. (1999), Mathematical and experimental modelling of phenol degradation in air-lift bioreactors, Environ. Eng. Policy, 1, 209, doi.org/10.1007/s100220050024 ; Boyadjiev Ch. (2006), On the modelling of an airlift reactor, Int. Journal Heat Mass Transf, 49, 2053, doi.org/10.1016/j.ijheatmasstransfer.2006.01.015 ; Camarasa E. (2001), Development of a complete model for an air-lift reactor, Chem. Eng. Sci, 56, 493, doi.org/10.1016/S0009-2509(00)00253-0 ; E. García Calvo (1991), Prediction of gas holdup and liquid velocity in airlift loop reactors containing highly viscous Newtonian liquids, Chem. Eng. Sci, 46, 2951, doi.org/10.1016/0009-2509(91)85165-T ; Gavrilescu M. (1998), Concentric-tube airlift bioreactors. Part I: Effects of geometry on gas holdup, Bioprocess Eng, 19, 37, doi.org/10.1007/s004490050480 ; Grzywacz R. (2008), Experimental verification of hydrodynamic models for airlift reactor, Technical Journal - Mechanics. Cracow University of Technology, 5-M, 105, 151. ; Grzywacz R. (2009), Influence of construction and process parameters on gas holdup coefficient in downcomer of airlift reactor, Inż. Aparat. Chem, 48, 76. ; Grzywacz R. (2006), Effect of operational conditions on the aeration of an airlift reactor. Analysis of the steady states, Chem. Process Eng, 27, 1361. ; Heijnen J. (1997), A simple hydrodynamic model for the liquid circulation velocity in a full scale two- and three-phase internal airlift reactor operating in the gas recirculation regime, Chem. Eng. Sci, 52, 2527, doi.org/10.1016/S0009-2509(97)00070-5 ; Kanai T. (2000), Dynamic modelling and simulation of continuous airlift bioreactors, Bioproc. Eng, 23, 213, doi.org/10.1007/s004499900154 ; Kanai T. (1996), Simulation of airlift bioreactors: Steady-state performance of continuous culture processes, Comp. Chem. Eng, 20, 1089, doi.org/10.1016/0098-1354(95)00225-1 ; Korpijarvi J. (1999), Hydrodynamics and mass transfer in an airlift reactor, Chem. Eng. Sci, 54, 2255, doi.org/10.1016/S0009-2509(98)00439-4 ; Marchuk J. (1980), Distributed parameter model of an airlift fermentor, Biotechnol. Bioeng, 22, 1189, doi.org/10.1002/bit.260220607 ; Pawlowsky U. (1973), Mixed culture biooxidation of phenol. I. Determination of kinetic parameters, Biotechnol. Bioeng, 15, 889, doi.org/10.1002/bit.260150506 ; Sikula I. (2008), Modelling of enzymatic reaction in an airlift reactor using an axial dispersion model, Chemical Papers, 62, 10, doi.org/10.2478/s11696-007-0073-9 ; Vial Ch. (2001), A simple method for regime identification and flow charactersation in bubble columns and airlift reactors, Chem. Eng. Proc, 40, 135, doi.org/10.1016/S0255-2701(00)00133-1 ; Znad H. (2004), Modelling and simulation of airlift bioreactors, Biochem. Eng. Journal, 21, 73, doi.org/10.1016/j.bej.2004.05.005

DOI

10.2478/v10176-012-0027-9

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