Table 1.
Experiment | Substrate | Feeding strategy based on qs (g g−1 h−1) | Goals |
---|---|---|---|
FB1 | Glycerol | Batch on glycerol–step-wise decrease of qs glycerol: 0.338–0.063–0.054–0.029–0.014–0.005 g g−1 h−1 | Determination of strain physiological parameters Characterization of recombinant expression profile |
FB2 | Glycerol | Batch on glycerol–repression phase on glycerol (qs = 0.29 g g−1 h−1)–de-repression phase on glycerol (qs = 0.035 g g−1 h−1) | Mimic optimized industrial process comprising of three phases |
FB3 | Sorbitol | Batch on sorbitol–step-wise increase of qs sorbitol: 0.033–0.060–0.127–0.176–0.197 g g−1 h−1 |
Determination of strain physiological parameters Characterization of recombinant expression profile |
Glycerol pulse at a final concentration of 10 g L−1 at highest qs sorbitol | qs in presence of both substrates | ||
FB4 | Mixed feed | Batch on glycerol–repression phase on glycerol (qs = 0.33 g g−1 h−1)–de-repression phase on glycerol (qs = 0.054 g g−1 h−1)–mixed-feed: glycerol (qs = 0.054 g g−1 h−1) and sorbitol (qs = 0.070 g g−1 h−1)–mixed-feed: glycerol (qs = 0.026 g g−1 h−1) and sorbitol (qs = 0.015 g g−1 h−1) | Analyze physiology and productivity in mixed feed environment |
FB5 | Mixed feed | batch on glycerol– repression phase on glycerol (qs = 0.33 g−1 h−1)–mixed-feed: glycerol (qs = 0.040 g−1 h−1) and sorbitol (qs = 0.055 g g−1 h−1) | Verify increased STY in mixed feed environment |
FB6 | Mixed feed | batch on glycerol–repression phase on glycerol (qs = 0.23 g g−1 h−1)–mixed-feed: glycerol (qs = 0.026 g g−1 h−1) and sorbitol (qs = 0.027 g g−1 h−1)–mixed-feed: glycerol (qs = 0.026 g g−1 h−1) and sorbitol (qs = 0.061 g g−1 h−1) |
Verify increased STY in mixed feed environment Identification of qs glycerol/qs sorbitol ratio allowing highest productivity and STY |