Optimization of Fed-Batch Fermentation for Production of Poly-$\beta$-Hydroxybutyrate in Alcaligenes eutrophus

  • Lee, In-Young (Genetic Engineering Research Institute, KIST) ;
  • Choi, Eun-Soo (Genetic Engineering Research Institute, KIST) ;
  • Kim, Guk-Jin (Genetic Engineering Research Institute, KIST) ;
  • Nam, Soo-Wan (Genetic Engineering Research Institute, KIST) ;
  • Shin, Yong-Cheol (Department of Microbiology, Gyeongsang National University) ;
  • Chang, Ho-Nam (Department of Chemical Engineering, Korea Advanced Institute of Science and Technology) ;
  • Park, Young-Hoon (Genetic Engineering Research Institute, KIST)
  • Published : 1994.06.01

Abstract

Production of poly-$\beta$-hydroxybutyrate (PHB) in fed-batch fermentation was studied. Utilization of carbon for PHB biosynthesis was investigated by using feeding solutions with different ratios of carbon to nitrogen (C/N). It was observed that at a high C/N ratio carbon source was more preferably utilized for PHB accumulation while its consumption for cellular metabolism appeared to be more favored at a low C/N value. A high cell concentration (184 g/l) was achieved when ammonium hydroxide solution was fed to control the pH, which was also utilized as the sole nitrogen source. For the mass production of PHB, two-stage fed-batch operations were carried out where PHB accumulation was observed to be stimulated by switching the ammonium feeding mode to the nitrogen limiting condition. A large amount of PHB (108 g/l) was obtained with cellular content of 80% within 50 hrs of operation.

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