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Industrial Biotransformations

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Lactate dehydrogenase<br />

Staphylococcus epidermidis<br />

Alternatively immobilized whole cells of Proteus vulgaris can be used in a fixed bed reactor:<br />

● By using small units of biomass in the form of a packed bed of immobilized cells, high amounts<br />

of the hydroxy acid can be produced. The space-time-yield is high and the costs for down-stream<br />

processing are low (conversion > 99.5 %; ee = 99.8 %; space-time yield = 180 g · L –1 ·d –1 ; enzyme<br />

consumption= 159 U · kg –1 ).<br />

● Per liter of fermentation broth 1.45 g cell mass (80 wt.-% water) can be isolated.<br />

● The emulsion of cells, chitosan and solid silica is dropped into a polyphosphate solution resulting<br />

in ionotropic gel-beads.<br />

● 1,000 g cell emulsion yields 400 g (= 800 mL) beads. The beads contain 0.25 g (wet cells) · g –1<br />

(beads).<br />

● Here electron mediators (= V) are used instead of NADH or NADPH:<br />

Fig. 1.1.1.28 – 2<br />

2 Cl -<br />

+<br />

+<br />

N N<br />

+<br />

+<br />

N N<br />

● The enzymes in the cells are capable of reducing and oxidizing the mediators. In this case the<br />

carbamoylmethylviologen is used. The following figure shows the regeneration cycle:<br />

● To avoid degassing of CO 2 the reaction is carried out under a pressure of 3 bar.<br />

O<br />

NH 2<br />

2 Cl -<br />

H2N<br />

benzyl viologen carbamoyl methyl viologen<br />

1<br />

COOH<br />

1 = 2-oxo-4-phenyl-butyric acid (OPBA)<br />

2 = 2-hydroxy-4-phenyl-butyric acid (2-HPBA)<br />

Fig. 1.1.1.28 – 3<br />

O<br />

H 2O + CO 2<br />

D-lactate-dehydrogenase<br />

2 H + + 2V + 2 V ++<br />

formate dehydrogenase (FDH)<br />

HCOOH<br />

OH<br />

(R)-2<br />

EC 1.1.1.28<br />

O<br />

COOH<br />

177

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