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A structured mathematical model of PHA biopolymer production process

Treść / Zawartość
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The paper describes a mathematical model of PHA biopolymer production process by Pseudomonas putida KT2442 where the octanoic acid is used as a substrate. The process is modeled using mass balances for fed-batch cultivation. Proper fitting to experimental data is obtained by identification of the model parameters. The model exhibits good agreement with experiments and its possible application for control is considered in the paper.
Rocznik
Strony
351--360
Opis fizyczny
Bibliogr. 7 poz., rys., tab., wzory
Twórcy
autor
  • Department of Computing and Control Engineering, Institute of Chemical Technology, Prague, Technická 5. 166 28 Prague 6. Czech Republic
  • Department of Computing and Control Engineering, Institute of Chemical Technology, Prague, Technická 5. 166 28 Prague 6. Czech Republic
autor
  • Department of Computing and Control Engineering, Institute of Chemical Technology, Prague, Technická 5. 166 28 Prague 6. Czech Republic
autor
  • Department of Computing and Control Engineering, Institute of Chemical Technology, Prague, Technická 5. 166 28 Prague 6. Czech Republic
autor
  • Department of Computing and Control Engineering, Institute of Chemical Technology, Prague, Technická 5. 166 28 Prague 6. Czech Republic
autor
  • Department of Computing and Control Engineering, Institute of Chemical Technology, Prague, Technická 5. 166 28 Prague 6. Czech Republic
Bibliografia
  • [1] M. H. Choi, J. Xu, J. K. Rho, X. P. Zhao and S. Ch. Yoon: Enhanced production of longer side-chain polyhydroxyalkanoic acid with ω-aromatic group substitution in phaZ-disrupted Pseudomonas fluorescens BM07 mutant through unrelated carbon source cometabolism and salicylic acid β-oxidation inhibition. BioresourceTechnology, 101(12), (2010), 4540-4548.
  • [2] P. Hrnčiřík, J. Vovsík and J. Náhlík: A new on-line indicator of biopolymer content in bacterial cultures. In Proc. of 11th IFAC Symp. on Computer Applicationsin Biotechnology, Leuven, Belgium, (2010), 192-196.
  • [3] P. Hrnčiřík, F. Černý , J. Náhlík, J. Vovsík, J. Mareš and P. Lovecká: Bioproduction of mcl-PHAs biopolymers - process states and control. In Proc. of18th Int. Conf. on Process Control, Tatransk´a Lomnica, Slovakia, (2011), 211-215.
  • [4] G. C. Okpokwasili and C. O. Nweke: Microbial growth and substrate utilization kinetics. African J. Biotechnology, 5(4), (2005), 305-317.
  • [5] P. Panand Y. Inoue: Polymorphism and isomorphism in biodegradable polyesters. Progress in Polymer Science, 34(7), (2009), 605-640.
  • [6] S. Ray and C. A. Peters: Changes in microbiological metabolism under chemical stress. Chemosphere, 71(3), (2008), 474-483
  • [7] Z. Suna, J. Ramsaya, M. Guaya and B. Ramsay: Enhanced yield of mediumchain- length polyhydroxyalkanoates from nonanoic acid by co-feeding glucose in carbon-limited, fed-batch culture. J. Biotechnology, 143(4), (2009), 262-267.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-50daad2c-1d6d-4fca-ab68-68c721786355
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