Abstract
Xanthan gum production was studied using sugarcane broth as the raw material and batch fermentation by Xanthomonas campestris pv. campestris NRRL B-1459. The purpose of this study was to optimize the variables of sucrose, yeast extract, and ammonium nitrate concentrations and to determine the kinetic parameters of this bioreaction under optimized conditions. The effects of yeast extract and ammonium nitrate concentrations for a given sucrose concentration (12.1–37.8 g L−1) were evaluated by central composite design to maximize the conversion efficiency. In a bioreactor, the maximum conversion efficiency was achieved using 27.0 g L−1 sucrose, 2.7 g L−1 yeast extract, and 0.9 g L−1 NH4NO3. This point was assayed in a shaker and in a bioreactor to compare bioreaction parameters. These parameters were estimated by the unstructured kinetic model of Weiss and Ollis (Biotechnol Bioeng 22:859–873, 1980) to determinate the yields (Y P/S), the maximum growth specific rate (μ max), and the saturation cellular concentration (X*). The parameters of the model (μ max, X*, m, λ, α, and β) were obtained by nonlinear regression. For production of xanthan gum in a shaker, the values of μ max and Y P/S obtained were 0.119 h−1 and 0.34 g g−1, respectively, while in a bioreactor, they were 0.411 h−1 and 0.63 g g−1, respectively.
Similar content being viewed by others
References
Mulchandani, A., Luong, J. H. T., & Leduy, A. (1988). Biotechnology and Bioengineering, 32, 639–646. doi:10.1002/bit.260320508.
Ashtaputre, A. A., & Shah, A. K. (1995). Applied and Environmental Microbiology, 61(3), 1159–1162.
García-Ochoa, F., Santos, V. E., Casas, J. A., & Gómez, E. (2000). Biotechnology Advances, 18, 549–579. doi:10.1016/S0734-9750(00)00050-1.
Pradella, J. G. C. (2006) Biopolímeros e Intermediários Químicos, Centro de Gestão e Estudos Estratégicos, Relatório Técnico no 84 396–205, Laboratório de Biotecnologia Industrial—LBI/CTPP, São Paulo, pp. 119.
Skaracis, G. N., Kalogiannis, S., & Iakovidou, G. (2003). Process Biochemistry, 39, 249–256. doi:10.1016/S0032-9592(03)00067-0.
Harcum, S. W., & Yoo, S. D. (1999). Bioresource Technology, 70, 105–109 short communication. doi:10.1016/S0960-8524(99)00013-9.
Moraine, R. A., & Rogovin, P. (1971). Biotechnology and Bioengineering, 13, 381–391. doi:10.1002/bit.260130305.
De Vuyst, L., Vermiere, A., Van Loo, J., & Vandamme, E. J. (1987). Mededelingen van de Faculteit landbouwwetenschappen—Rijksuniversiteit Gent, 52, 1881–1900.
Pons, A., Dussap, C. G., & Gros, J. B. (1990). Bioprocess Engineering, 5, 107–114. doi:10.1007/BF00388188.
García-Ochoa, F., Santos, V. E., & Alcon, A. (1995). Enzyme and Microbial Technology, 17, 206–217. doi:10.1016/0141-0229(94)00009-G.
Letisse, F., Lindley, N. D., & Roux, G. (2003). Biotechnology Progress, 19, 822–827. doi:10.1021/bp0257168.
Cadmus, M. C., Knutson, C. A., Lagoda, A. A., Pittsley, J. E., & Burton, K. A. (1978). Biotechnology and Bioengineering, 20, 1003–1014. doi:10.1002/bit.260200703.
Margaritis, A., & Zajic, J. E. (1978). Biotechnology and Bioengineering, 20, 939–1001. doi:10.1002/bit.260200702.
Pinches, A., & Pallent, L. J. (1986). Biotechnology and Bioengineering, 28, 1484–1496. doi:10.1002/bit.260281006.
Souw, P., & Demain, A. L. (1980). Journal of Fermentation Technology, 58, 411–416.
Nakajima, S., Funahashi, H., & Yoshida, T. (1990). Journal of Fermentation and Bioengineering, 70(6), 392–397. doi:10.1016/0922-338X(90)90120-L.
Alves, R. S. A. (1991), Dissertação, Escola de Química, Universidade Federal do Rio de Janeiro, Rio de Janeiro, Brasil.
De Vuyst, L., & Vermeire, A. (1994). Applied Microbiology and Biotechnology, 42, 187–191.
Umasankar, H., Annadurai, G., Chellapandian, M., et al. (1996). Bioprocess Engineering, 14(6), 307–309. doi:10.1007/BF00369474.
Lima, M. A. G. A. (1999) Tese de doutorado, Escola de Química, Universidade Federal do Rio de Janeiro, Rio de Janeiro, Brasil.
Serrano-Carreón, L., Corona, R. M., Sánchez, A., & Galindo, E. (1998). Process Biochemistry, 33(2), 133–146. doi:10.1016/S0032-9592(97)00039-3.
Amanullah, A., Satti, S., & Nienow, A. W. (1998). Biotechnology Progress, 14, 265–269. doi:10.1021/bp9800079.
Shu, C.-H., & Yang, S.-T. (1990). Biotechnology and Bioengineering, 35, 454–468. doi:10.1002/bit.260350503.
Ramírez, M. E., Fucikovsky, L., García-Jiménez, F., et al. (1988). Applied Microbiology and Biotechnology, 29, 5–10. doi:10.1007/BF00258343.
Chhabra, R. P., Richardson, J. F. (1999). Non-Newtonian flow in the process industries fundamentals and engineering applications p. 436. Great Britain: Butterworth Heinemann.
Marquardt, D. W. (1963). Journal of the Society for Industrial and Applied Mathematics, 11, 431–441. doi:10.1137/0111030.
Gill, S. (1951). A process for the step-by-step integration of differential equations in an automatic computing machine. Proceedings of the Cambridge Philosophical Society, 47, 96–108. doi:10.1017/S0305004100026414.
Weiss, R. M., & Ollis, D. F. (1980). Biotechnology and Bioengineering, 22, 859–873. doi:10.1002/bit.260220410.
Luedeking, R., & Piret, E. L. (1959). Journal of Biochemical and Microbiological Technology and Engineering, 1, 393–412. doi:10.1002/jbmte.390010406.
Borzani, W. (2001). Engenharia bioquímica. In W. Borzani, U. A. Lima, E. Aquarone, & W. Schmidell (Eds.), Biotecnologia Industrial, v. 2(1st ed.). São Paulo: Blücher.
El-Salam, M. H. A., Fadel, M. A., & Murad, H. A. (1994). Journal of Biotechnology, 33, 103–106. doi:10.1016/0168-1656(94)90103-1.
García-Ochoa, F., García-León, M. A., & Romero, A. (1990). Chemical and biochemical engineering, 4, 15–20.
Acknowledgments
The authors wish to thank the CNPq and FAPEMIG—Brazil—for its financial support.
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Faria, S., Vieira, P.A., Resende, M.M. et al. A Comparison Between Shaker and Bioreactor Performance Based on the Kinetic Parameters of Xanthan Gum Production. Appl Biochem Biotechnol 156, 45–58 (2009). https://doi.org/10.1007/s12010-008-8485-8
Received:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s12010-008-8485-8