TABLE 1.
Production of exopolymers with glucose and its analogs by A. pullulansa
| Carbon source | Final pHb | Cell dry wt (mg/ml) | Yield (mg/ml)c | Specific yield (mg/mg [dry wt] of cells)d | Mol% of:
|
|
|---|---|---|---|---|---|---|
| Glucosee | Mannosef | |||||
| Glucose (2%) | 6.19 | 9.79 | 3.21 ± 0.35 | 0.34 | 87 ± 3 | 13 ± 3 |
| 3-O-Methylglucose (2%) | 7.47 | 1.74 | 0.47 ± 0.10 | 0.36 | 57 ± 6 | 43 ± 6 |
| Glucosamine (2%) | 5.75 | 3.94 | 0.70 ± 0.11 | 0.21 | 30 ± 7 | 70 ± 7 |
| N-Acetylglucosamine (2%) | 7.62 | 3.15 | 0.51 ± 0.12 | 0.22 | 43 ± 4 | 57 ± 4 |
| 2-Deoxyglucose (2%) | 6.82 | 0.43 | 0.35 ± 0.08 | 1.09 | 54 ± 5 | 46 ± 5 |
| Mannose (2%) | 5.40 | 7.56 | 2.63 ± 0.07 | 0.35 | 89 ± 4 | 11 ± 4 |
The data are data for 5-day cultures grown at 30°C, and the values are means based on triplicate experiments. The values for controls included to account for medium or exopolymer carryover were as follows: for cell dry weight, 0.23 ± 0.00 mg/ml; and for yield, 0.17 ± 0.01 mg/ml. The control values should be subtracted from the gross values shown.
The initial medium pH was adjusted to 6.5 to 6.7 prior to sterilization.
Total amount of exopolymers, including pullulan.
Specific yield of exopolymers, including pullulan.
Moles percent of glucose = [glucose/(glucose + mannose)] × 100.
Moles percent of mannose = [mannose/(glucose + mannose)] × 100.