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. 1999 Dec;65(12):5265–5271. doi: 10.1128/aem.65.12.5265-5271.1999

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
a

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. 

b

The initial medium pH was adjusted to 6.5 to 6.7 prior to sterilization. 

c

Total amount of exopolymers, including pullulan. 

d

Specific yield of exopolymers, including pullulan. 

e

Moles percent of glucose = [glucose/(glucose + mannose)] × 100. 

f

Moles percent of mannose = [mannose/(glucose + mannose)] × 100.