Steady state characteristics of a three-phase fluidizedbed bioreactor with partial biomass recirculation

• Autorzy: Skoneczny Szymon , Tabiś Bolesław

Identyfikatory

DOI

10.24425/cpe.2019.126102

• Języki publikacji: EN

Abstrakty

EN

The paper presents modeling and simulation results of the operation of a three-phase fluidized bedbioreactorwith partial recirculation of biomass. The proposed quantitative description of the bioreactortakes into account biomass growth on inert carriers, microorganisms decay and interphase biomasstransfer. Stationary characteristicsof the bioreactorand local stability of steady-states were determined.The influence of microbiological growth kinetics on the multiplicity of steady-states was discussed.The relationship between biofilm growth and boundaries of fluidized bed existence was shown

Słowa kluczowe

EN

fluidized bed; bioreactor; mathematical modeling; steady states

PL

łóżko wodne; bioreaktor; modelowanie matematyczne; stan ustalony

• Wydawca: Komitet Inżynierii Chemicznej i Procesowej Polskiej Akademii Nauk
• Czasopismo: Chemical and Process Engineering
• Rocznik: 2019
• Tom: Vol. 40, nr 1
• Strony: 77--–86
• Opis fizyczny: Bibliogr. 9 poz., wykr.

Twórcy

autor

Skoneczny Szymon

• Cracow University of Technology, Department of Chemical and Process Engineering,ul. Warszawska 24, 30-155 Kraków, Poland

autor

Tabiś Bolesław

• Cracow University of Technology, Department of Chemical and Process Engineering,ul. Warszawska 24, 30-155 Kraków, Poland

Bibliografia

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• 2. Kwon S., Yoo I-K, Lee W.G., Chang H.N., Chang Y.K. 2001. High-rate continuous production of lactic acidbyLactobacillus rhamnosusin a two-stage membrane cell-recycle bioreactor.Biotechnol Bioeng., 73, 25–34.DOI: 10.1002/1097-0290(20010405)73:1<25::AID-BIT1033>3.0.CO;2-N.
• 3. Olivieri G., Russo M.E., Marzocchella A., Salatino P., 2011. Modeling of an aerobic biofilm reactor with double-limiting substrate kinetics: Bifurcationaland dynamicalanalysis.Biotechnol.Prog.,27, 1599–1613.DOI: 10.1002/btpr.690.
• 4. Onysko K.A., Robinson C.W., Budman H.M., 2002. Improved modelling of the unsteady-state behaviour ofan immobilized-cell, fluidized-bed bioreactor for phenol biodegradation.Can. J. Chem. Eng., 80, 239–252.DOI: 10.1002/cjce.5450800209.
• 5. Park Y., Davis M.E., Wallis D.A., 1984. Analysis of a continuous, aerobic, fixed-film bioreactor. II. Dynamicbehavior.Biotechnol. Bioeng., 26, 468–476. DOI: 10.1002/bit.260260510.
• 6. Seker S., Beyenal H., Salih B., Tanyolac A., 1997. Multi-substrate growth kinetics ofPseudomonas putidaforphenol removal.Appl. Microbiol. Biotechnol., 47, 610–614. DOI: 10.1007/s002530050982.
• 7. Seydel R., 2009. Practical bifurcation and stability analysis. 3rdedition, Springer, New York. DOI: 10.1007/978-1-4419-1740-9.
• 8. Tang W., Fan L., 1987. Steady state phenol degradation in a draft-tube, gas-liquid-solid fluidized-bed bioreactor.AIChE J., 33, 239–249. DOI: 10.1002/aic.690330210.
• 9. Tang W., Wisecarver K., Fan L., 1987. Dynamics of a draft tubegas-liquid-solid fluidized bed bioreactor for phenoldegradation.Chem. Eng. Sci., 42, 2123–2134. DOI: 10.1016/0009-2509(87)85033-9.

Uwagi

PL

Opracowanie rekordu w ramach umowy 509/P-DUN/2018 ze środków MNiSW przeznaczonych na działalność upowszechniającą naukę (2019).