TABLE 2.
First-step cultivation
|
Second-step cultivation with γ-butyrolactone
|
|||||||||
---|---|---|---|---|---|---|---|---|---|---|
Addition to medium | Dry cell wt (g/liter) | P(3HB) content (%, wt/wt) | Concn of residual P(3HB) (g/liter)b | Dry cell wt (g/liter) | Polyester content (%, wt/wt) | Polyester composition (mol%)b
|
Concn of residual 3HB in the polymer (g/liter) | % γ-Butyrolactone
|
||
3HB | 4HB | Used for 4HBc | Unused | |||||||
Noned | 1.61 ± 0.02 | 3.23 ± 0.12 | 0.052 ± 0.003 | 2.40 ± 0.02 | 30.4 ± 0.1 | 11 ± 1 | 89 ± 1 | 0.083 ± 0.004 | 29 ± 2 | 13 ± 1 |
NaCl (170 mM)e | 1.87 ± 0.02 | 11.1 ± 0.20 | 0.206 ± 0.003 | 2.25 ± 0.04 | 33.3 ± 0.8 | 9 ± 1 | 91 ± 1 | 0.067 ± 0.007 | 31 ± 2 | 11 ± 1 |
KCl (170 mM)e | 1.73 ± 0.02 | 3.51 ± 0.08 | 0.061 ± 0.001 | 2.20 ± 0.08 | 30.6 ± 0.6 | 5 ± 1 | 95 ± 1 | 0.045 ± 0.006 | 29 ± 2 | 11 ± 1 |
Cells grown in Luria-Bertani medium were transferred to PHA synthesis mineral medium containing γ-butyrolactone (2.2 g/liter) and 0.6 g of ammonium sulfate per liter for polyester accumulation.
Calculated from gas chromatographic data.
Percent conversion of γ-butyrolactone (2.2 g/liter) to 4HB in the polymer.
All values are averages for three different experiments.
All values are averages for six different experiments.