• Title/Summary/Keyword: galactose feeding strategy

Search Result 2, Processing Time 0.015 seconds

Effect of Galactose Feeding Strategy on Heterologous Human Lipocortin-I Production in the Fed-Batch Culture of Saccharomyces cerevisiae Controlled by the GAL10 Promoter

  • Chung, Bong-Hyun;Kim, Byung-Moon;Rhee, Sang-Ki;Park, Young-Hoon;Nam, Soo-Wan
    • Journal of Microbiology and Biotechnology
    • /
    • v.5 no.4
    • /
    • pp.224-228
    • /
    • 1995
  • Fed-batch fermentations were conducted to produce human lipocortin-I (LC1), a potential anti-inflammatory agent, from recombinant Sacchromyces cerevisiae carrying a galactose-inducible expression system. The cell growth, expression level of LC1, and the plasmid stability were investigated under various LC1 induction modes performed by three different galactose feeding strategies. Galactoe was fed to induce the expression of LCl from the beginning (initial induction) of culture or when the cell concentration reached 120 OD (mid-phase induction) or 300 OD (late induction). Among the three galactose-induction modes tested, the initial induction mode yielded the best result with respect to a final expression level of LC1. Fedbatch fermentation with initial induction mode produced LC1 at a conentration of 220 mg/l, which corresponded to 1.38- and 1.53-fold increases over those produced by mid-phase and late induction modes.

  • PDF

Scale-up of Recombinant Hirudin Production from Saccharomyces cerevisiae

  • Kim, Chul-Ho;K. Jagannadha Rao;Youn, Duk-Joong;Rhee, Sang-Ki
    • Biotechnology and Bioprocess Engineering:BBE
    • /
    • v.8 no.5
    • /
    • pp.303-305
    • /
    • 2003
  • Scale-up of hirudin production from Saccharomyces cerevisiae from bench-scale to pilot-scale was carried out based on constant volumetric oxygen transfer coefficient (K$\sub$L/a). Fed-batch mode of cultivation using step-wise feeding strategy of galactose was employed for the production of hirudin in a 30-L and a 300-L pilot-scale fermentor. The final hirudin concentrations were achieved 390 mg/L and 286.1 mg/L, and the volumetric productivities were 80.4% and 90.7% with the 30-L and 300-L fermentors, respectively, compared to the productivity of the 5-L bench-scale fermentor.