TABLE 1.
Steady stateb | Styrene feed concn (mM) | Cell concn (g CDW literaq−1) | Styrene oxide concn (mM)c | Styrene concn (mM)c | Specific epoxidation rate [U (g CDW)−1] | Acetate concn (g literaq−1) | Carbon balance (%)
|
|||
---|---|---|---|---|---|---|---|---|---|---|
Biomass | Acetate | CO2 | Sum | |||||||
I | 0 | 6.4 | 0.78 | 38 | 4 | 54 | 97 | |||
IId | 0 | 6.1 | 0.78 | 36 | 4 | 57 | 97 | |||
III | 39 | 5.9 | 19 | 1.4 | 5 | 0.76 | 35 | 4 | 60 | 99 |
IV | 79 | 5.5 | 49 | 3.9 | 15 | 0.76 | 33 | 4 | 65 | 102 |
V | 105 | 4.9 | 61 | 11 | 21 | 1.72 | 29 | 9 | 65 | 103 |
VI | 131 | 4.8 | 68 | 26 | 24 | 1.97 | 28 | 10 | 66 | 104 |
The dilution rates for the organic and aqueous phases were set at 0.1 h−1. See Materials and Methods for details. The standard deviations of duplicate measurements were below 5%. aq, aqueous phase.
The steady states refer to the experiment shown in Fig. 4.
Concentrations in the organic phase are given.
Steady-state II was established by adding the inducer DCPK to the bioreactor and the feed tank to a concentration of 1.7 mM in the organic phase.