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Industrial Biotransformations

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Lactate dehydrogenase<br />

Staphylococcus epidermidis<br />

1) Reaction conditions<br />

[1]: 0.2 M, 35.6 g · L –1 [178.18 g · mol –1 ]<br />

pH: 8.0<br />

T: 30 °C<br />

medium: aqueous<br />

reaction type: redox reaction<br />

catalyst: solubilized enzyme<br />

enzyme: (R)-lactate-NAD oxidoreductase<br />

strain: Staphylococcus epidermidis<br />

CAS (enzyme): [9028–36–8]<br />

2) Remarks<br />

1<br />

COOH<br />

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

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

E1 = D-lactate dehydrogenase<br />

E2 = formate dehydrogenase<br />

Fig. 1.1.1.28 – 1<br />

● Cofactor regeneration is carried out by formate dehydrogenase from Candida boidinii utilizing<br />

formate and producing CO 2. During cofactor regeneration no by-product is formed that needs<br />

to be separated. In the steady state of the continuously operated stirred tank reactor a total<br />

turnover number of 900 is achieved.<br />

● NAD + is added as cofactor at a concentration of 0.2 mM and ammonium formate at a concentration<br />

of 0.35 M.<br />

● The optimal working pH would have been 6.5, but a pH of 8.0 is chosen due to better solubility<br />

of the hydroxy acid.<br />

● The production is carried out in a continuously operated stirred tank reactor equipped with an<br />

ultrafiltration membrane (cut off 10,000 Da) to retain the enzymes.<br />

● For stabilization of the enzymes 0.15 % mercaptoethanol and 1 mM EDTA are added to the<br />

substrate solution.<br />

● At a conversion of 90 % the pH is shifted from 6.2 (substrate solution) to 8.0. The reason is the<br />

different pK a-values of 2-oxo-4-phenylbutyric acid (pK a = 2.3) and (R)-2-hydroxy-4-phenylbutyric<br />

acid (pK a = 3.76).<br />

● The data given relate to the above process with isolated enzymes.<br />

176<br />

O<br />

CO 2<br />

E1<br />

NADH + H + NAD +<br />

E2<br />

HCOOH<br />

OH<br />

(R)-2<br />

COOH<br />

EC 1.1.1.28

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