Table 2. Effects of initial sugar concentration of corncob hydrolysate on malic acid production in shake flasks.
Initial total sugar (g/L) | Residual sugar(g/L) | Cell biomass (g/L) | Malic acid*(g/L) | productivity(g/L h) | yield(g/g) |
---|---|---|---|---|---|
50 | 0 | 12.75±0.68 | 5.90±0.53 | 0.06±0.005 | 0.12 |
60 | 0 | 15.50±0.52 | 6.03±0.62 | 0.06±0.006 | 0.11 |
70 | 3.62 | 20.86±0.13 | 11.42±3.91 | 0.12±0.040 | 0.17 |
80 | 6.88 | 26.66±0.58 | 11.58±2.18 | 0.12±0.022 | 0.16 |
90 | 12.34 | 30.88±0.20 | 12.66±1.05 | 0.13±0.010 | 0.16 |
110 | 21.87 | 32.13±0.20 | 15.27±2.18 | 0.16±0.023 | 0.17 |
130 | 43.18 | 27.45±0.52 | 10.29±2.70 | 0.11±0.028 | 0.12 |
* Malic acid was obtained after hydrolysis of PMA with H2SO4.