A fundamental analysis of continuous flow bioreactor and membrane reactor models with tessier kinetics

Chemical Engineering Communications

Volumn 199, Issue 3, 2012, Pages 417-433

  Nelson, M I ^a   Balakrishnan, E ^b   Sidhu, H S ^c  

^a UNIVERSITY OF WOLLONGONG   (Australia)

^b SULTAN QABOOS UNIVERSITY   (Oman)

^c UNIVERSITY OF NEW SOUTH WALES   (Australia)

Author keywords

Bioreactor; Kinetics; Membrane reactor; Modeling; Stirred tank

Indexed keywords

CONTINUOUS FLOWS; FIXED BED REACTOR; FLOW REACTORS; FUNDAMENTAL ANALYSIS; MEMBRANE REACTOR; RESIDENCE TIME; STEADY STATE; STEADY-STATE OPERATION; STIRRED TANK;

BIOCONVERSION; ENZYME KINETICS; KINETICS; MODELS; RECYCLING;

BIOREACTORS;

EID: 84856995591     PISSN: 00986445     EISSN: 15635201     Source Type: Journal    
DOI: 10.1080/00986445.2010.525155     Document Type: Article

References (28)

1. Annuar, M. S. M., Tan, I. K. P., Ibrahim, S., and Ramachandran, K. B. (2008). A kinetic model for growth and biosynthesis of medium-chain-length poly-(3-hydroxyalkanoates) in Pseudomonas putida, Braz. J. Chem. Eng.,25, 217-228.
2. Bernard, O., Hadj-Sadok, Z., Dochain, D., Genovesi, A., and Steyer, J. P. (2001). Dynamical model development and parameter identification for an anaerobic wastewater treatment process, Biotechnol. Bioeng., 75, 424-438.
3. Beyenal, H., Chen, S. N., and Lewandowski, Z. (2003). The double substrate growth kinetics of Pseudomonas aeruginosa, Enzyme Microb. Techncl., 32, 92-98.
4. Deschênes, J.-S., Desbiens, A., Perrier, M., and Kamen, A. (2006a). Multivariable nonlinear control of biomass and metabolite concentrations in a high-cell-density perfusion bioreactor, Ind. Eng. Chem. Res., 45, 8985-8997.
5. Deschênes, J.-S., Desbiens, A., Perrier, M., and Kamen, A. (2006b). Use of cell bleed in a high cell density perfusion culture and multivariable control of biomass and metabolite concentrations, Asia-Pac. J. Chem. Eng., 1, 82-91.
6. Guisasola, A., Petzet, S., Baeza, J. A., Carrera, J., and Lafuente, J. (2007). Inorganic carbon limitations on nitrification: Experimental assessment and modelling, Water Res., 41, 277-286.
7. Herbert, D., Elsworth, R., and Telling, R. C. (1956). The continuous culture of bacteria: A theoretical and experimental study, J. Gen. Microbiol., 14, 601-622.
8. Lawrence, A. W., and McCarty, P. L. (1970). Unified basis for biological treatment design and operation, J. Sanit. Eng. Div., 96, 757-778.
9. Liu, H.-W., and Wu, S.-C. (1995). Periodical operation of continuous bioreactor, J. Chin. Inst. Chem. Eng., 26, 233-243.
10. Liu, H.-S., Wu, S.-C., and Lin, S.-C. (1998). Theoretical analysis of frequency response in continuous bioreactor, Chem. Eng. Commun., 164, 13-34.
11. McHenry, J., and Werker, A. G. (2002). Characterization of bioactivity in treatment wetlands utilising an enzymatic assay, paper presented at CSCE/EWRI of ASCE Environmental Engineering Conference.
12. Nelson, M. I., and Sidhu, H. S. (2006). Evaluating the performance of a cascade of two bioreactors, Chem. Eng. Sci., 61, 3159-3166.
13. Nelson, M. I., Balakrishnan, E., Sidhu, H. S., and Chen, X. D. (2008a). A fundamental analysis of continuous flow bioreactor models and membrane reactor models to process industrial wastewaters, Chem. Eng. J., 140, 521-528.
14. Nelson, M. I., Kerr, T., and Chen, X. D. (2008). A fundamental analysis of continuous flow bioreactor and membrane reactor models with death and maintenance included, Asia-Pac. J. Chem. Eng., 3, 70-80.
15. Neumann, M. B., and Gujer, W. (2008b). Underestimation of uncertainty in statistical regression of environmental models: Influence of model structure uncertainty, Environ. Sci. Techno., 42, 4037-4043.
16. Pavlostathis, S. G., and Giraldo-Gomez, E. (1991). Kinetics of anaerobic treatment, Water Sci. Technol., 24, 35-59.
17. Pirt, S. J. (1965). The maintenance energy of bacteria in growing cultures, Proc. R. Soc. Lond. Ser.-B, 163, 224-231.
18. Schulze, K. L., and Lipe, R. S. (1964). Relationship between substrate concentration, growth rate, and respiration rate of escherichia coli in continuous culture, Arch. Microbiol., 48, 1-20.
19. Shuler, M. L., and Kargi, F. (2002). Bioprocess Engineering,2nd ed., Prentice Hall, Upper Saddle River, N.J.
20. Sivaprakasam, S., Mahadevan, S., and Bhattacharya, M. (2007). Biocalorimetric and respirometric studies on metabolic activity of aerobically grown batch culture of Pseudomonas aeruginosa, Biotechnol. Bioprocess. Eng., 12, 340-347.
21. Sömezişik, M., Tanyolaç, D., Şeker, S., and Tanyolaç, A. (1998). The double-substrate growth kinetics of Sulfolobus solfataricus a thermophilic sulfur-removing archeabacterium, Biochem. Eng. J., 1, 243-248.
22. Tessier, G. (1936). Les lois quantitatives de la croissance, Ann. Physio. Physiochim. Bio., 12, 527-573.
23. Wang, Z., Wang, L., Wang, B. Z., Jiang, Y. F., and Liu, S. (2008). Bench-scale study on zero excess activated sludge production process coupled with ozonation unit in membrane bioreactor, J. Environ. Sci. Health. A, 43, 1325-1332.
24. Wu, S.-C., Lin, C.-C., and Liu, H.-S. (1999). Theoretical analysis of a continuous bioreactor subject to cyclic feed concentration, J. Chin. Inst. Chem. Eng., 30, 151-160.
25. Yoon, S.-H., Kim, H.-S., and Yeom, I.-T. (2004). The optimum operational condition of membrane bioreactor (MBR): Cost estimation of aeration and sludge treatment, Water Res., 38, 37-46.
26. Yurt, N., Beyenal, H., Sears, J., and Lewandowski, Z. (2003). Quantifying selected growth parameters of Leptothrix discophora SP-6 in biofilms from oxygen concentration profiles, Chem. Eng. Sci., 58, 4557-4566.
27. Yurt, N., Sears, J., and Lewandowski, Z. (2002). Multiple substrate growth kinetics of Leptothrix discophora SP-6, Biotechnol. Prog., 18, 994-1002.
28. Zenaitis, M. G., Sandhu, H., and Duff, S. J. B. (2002). Combined biological and ozone treatment of log yard run-off, Water Res., 36, 2053-2061.