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Number of results
2013 | 34 | 4 | 435-448

Article title

MATHEMATICAL MODELLING AND STATIONARY CHARACTERISTICS OF A TWO-PHASE FLUIDISED-BED BIOREACTOR WITH EXTERNAL AERATION

Content

Title variants

Languages of publication

EN

Abstracts

EN
A mathematical model for a two-phase fluidised bed bioreactor with liquid recirculation and an external aerator was proposed. A stationary nonlinear analysis of such a bioreactor for an aerobic process with double-substrate kinetics was carried out. The influences of a volumetric fraction of solid carriers in the liquid phase, the rate of active biomass transfer from the biofilm to the liquid, the concentration of carbonaceous substrate, the mean residence time of the liquid and the efficiency of the external aerator on the steady state characteristics of the bioreactor were described. A method for determination of the minimal recirculation ratio related to oxygen demand and fluidised bed conditions was presented. On the basis of the obtained results, it is possible to choose reasonable operating conditions of such plants and to determine constraints, while considering acceptable concentrations of a toxic substrate being degraded.

Publisher

Year

Volume

34

Issue

4

Pages

435-448

Physical description

Dates

published
1 - 12 - 2013
online
22 - 01 - 2014

Contributors

  • Cracow University of Technology, Department of Chemical and Process Engineering, ul. Warszawska 24, 31-155 Kraków, Poland
  • Cracow University of Technology, Department of Chemical and Process Engineering, ul. Warszawska 24, 31-155 Kraków, Poland

References

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  • Schügerl K., 1997. Three-phase-biofluidization. Application of three-phase fluidization in the biotechnology - A review. Chem. Eng. Sci., 52, 3661-3668. DOI: 10.1016/S0009-2509(97)88926-9.[Crossref]
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  • Tang W.T., Wisecarver K., Fan L.S., 1987b. Dynamics of a draft tube gas-liquid-solid fluidized bed bioreactor for phenol degradation. Chem. Eng. Sci., 42, 2123-2134. DOI: 10.1016/0009-2509(87)85033-9.[Crossref]
  • Wisecarver K.D., Fan L.S., 1989. Biological phenol degradation in a gas-liquid-solid fluidized bed reactor. Biotechnol. Bioeng., 33, 1028-1038. DOI: 10.1002/bit.260330812.[Crossref]
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  • Rodgers M., Zhan X.-M., 2003. Moving-medium biofilm reactors. Rev. Environ. Sci. Biotechnol., 2, 213-224. DOI: 10.1023/B:RESB.0000040467.78748.1e.[Crossref]
  • Russo M.E., Maffettone P.L., Marzocchella A., Salatino P., 2008. Bifurcation and dynamical analysis of a continuous biofilm reactor. J. Biotechnol., 135, 296-303. DOI: 10.1016/j.jbiotec.2008.04.003.[WoS][Crossref]
  • Schügerl K., 1997. Three-phase-biofluidization. Application of three-phase fluidization in the biotechnology - A review. Chem. Eng. Sci., 52, 3661-3668. DOI: 10.1016/S0009-2509(97)88926-9.[Crossref]
  • Seker S., Beyenal H., Salih B., Tanyolac A., 1997. Multi-substrate growth kinetics of Pseudomonas putida for phenol removal. Appl. Microbiol. Biotechnol., 47, 610-614. DOI: 10.1007/s002530050982.[Crossref]
  • Sevillano X., Isasi J. R., Penas F. J., 2008. Feasibility study of degradation of phenol in fluidized bed bioreactor with a cyclodextrin polymer as biofilm carrier. Biodegrad., 19, 589-597. DOI: 10.1007/s10532-007-9164-0.[Crossref]
  • Tang W.T., Fan L.S., 1987a. Steady state phenol degradation in a draft-tube, gas-liquid-solid fluidized-bed bioreactor. AIChE J., 33, 239-249. DOI: 10.1002/aic.690330210.[Crossref]
  • Tang W.T., Wisecarver K., Fan L.S., 1987b. Dynamics of a draft tube gas-liquid-solid fluidized bed bioreactor for phenol degradation. Chem. Eng. Sci., 42, 2123-2134. DOI: 10.1016/0009-2509(87)85033-9.[Crossref]
  • Wisecarver K.D., Fan L.S., 1989. Biological phenol degradation in a gas-liquid-solid fluidized bed reactor. Biotechnol. Bioeng., 33, 1028-1038. DOI: 10.1002/bit.260330812.[Crossref]
  • Worden R.M., Donaldson T.L., 1987. Dynamics of a biological fixed film for phenol degradation in a fluidizedbed bioreactor. Biotechnol. Bioeng., 30, 398-412. DOI: 10.1002/bit.260300311. [Crossref]

Document Type

Publication order reference

Identifiers

YADDA identifier

bwmeta1.element.-psjd-doi-10_2478_cpe-2013-0036
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