Stability studies of recombinant Saccharomyces cerevisiae in the presence of varying selection pressure.
A recombinant yeast plasmid carrying the Ieu2 gene for auxotrophic complementation and a reporter gene for beta-galactosidase under the control of Gal10 promoter was studied in Saccharomyces cerevisiae. Growth, product formation, and plasmid stability were studied in defined, semi-defined, and complex media. The biomass concentration and specific activity were higher in complex medium than in defined medium, which was selective for the growth of plasmid-containing cells, leading to a 10-fold increase in volumetric activity. However, plasmid instability was very high in complex media with 50% plasmid-free cells emerging in the culture within 75 h of cultivation. In order to control instability, the growth rates of the plasmid-containing and plasmid-free cells were determined in semi-defined media, which consisted of defined medium supplemented with different concentrations of yeast extract. Below a critical concentration of yeast extract (0.05 g/L), the plasmid-containing cells had a growth rate advantage over the plasmid-free cells. This was possibly because, at this concentration of yeast extract, the availability of leucine became the rate-determining factor in the specific growth rate of plasmid-free cells. A feeding strategy was designed which maintained a low concentration of the residual yeast extract in the medium and thus continuously provided the plasmid-containing cells with a competitive advantage over the plasmid-free cells. This resulted in high stability as well as high cell density under non-selective conditions, which led to a 10-fold increase in the volumetric activity compared to that achieved in defined selective media. A simple mathematical model was formulated to verify the experimental data. The important state variables and process parameters, i.e., biomass concentration, beta-galactosidase expression, sucrose consumption, yeast extract consumption, and specific growth rates of the two cell populations, were evaluated. These variables and parameters along with the differential equations based on material balances as well as the experimental results obtained were used in a mathematical model for the fed-batch cultivation. These correctly verified the experimental data and clearly illustrated the concept behind the success of the fed-batch strategy under yeast extract starvation.
Centre for Biotechnology, Jawaharlal Nehru University, New Delhi, 110 067 India.
Jagdish C
JC
Gupta
K J
KJ
Mukherjee
D019149:Bioreactors; D002452:Cell Count; D002478:Cells, Cultured; D003198:Computer Simulation; D003470:Culture Media; D015966:Gene Expression Regulation, Fungal; D007930:Leucine / Q000378:metabolism; D008954:Models, Biological; D010957:Plasmids / Q000378:metabolism*; D011994:Recombinant Proteins / Q000096:biosynthesis / Q000235:genetics; D011995:Recombination, Genetic; D012441:Saccharomyces cerevisiae / Q000235:genetics* / Q000254:growth & development* / Q000378:metabolism; D012641:Selection, Genetic; D012680:Sensitivity and Specificity; D013395:Sucrose / Q000378:metabolism; D001616:beta-Galactosidase / Q000096:biosynthesis / Q000235:genetics
D003470:Culture Media; D011994:Recombinant Proteins; D013395:Sucrose; D001616:beta-Galactosidase; D007930:Leucine