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Industrial Biotransformations

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Styrene monooxygenase<br />

Escherichia coli<br />

1 = styrene<br />

2 = (S)-styrene oxide<br />

Fig. 1.14.13.69 – 1<br />

1) Reaction conditions<br />

[1]: 2 % (v/v organic phase)<br />

[2]: 4.5 g · L –1 ·h –1 glucose (50 % w/v)<br />

[3]: 1 % (v/v organic phase) n-octane<br />

pH: 3.0<br />

T: 30 °C<br />

medium: two-phase system<br />

reaction type: fed-batch<br />

catalyst: whole cell<br />

enzyme: styrene monooxygenase (StyA)<br />

enzyme: reductase (StyB)<br />

strain: Escherichia coli JM101(pSPZ10)<br />

2) Remarks<br />

O 2<br />

NADPH,H +<br />

1 2<br />

EC 1.14.13.69<br />

● Glucose is added continuously with a rate of 4.5 g · L –1 ·h –1 while the organic phase is added<br />

batchwise one hour after starting the glucose feed.<br />

● The host strain E.coli JM101 was transformed with a plasmid containing the styrene monooxygenase<br />

from Pseudomonas sp. VLB120 and the alk regulatory system from P. oleovorans Gpo1.<br />

● Bis(2-ethylhexyl)phthalate is used as an apolar carrier solvent. The organic phase also contains<br />

2 % (v/v) n-octane, which is used as the inducer of the alk regulatory system.<br />

● The system is limited by mass transfer of styrene from the organic to the aqueous phase.<br />

E<br />

● 2-Phenylethanol is produced as a by-product in approximately 10 % concentration due to the<br />

ring opening reaction of the epoxide.<br />

H 2O<br />

NADP +<br />

O<br />

DSM<br />

235

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