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Industrial Biotransformations

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Glutaryl amidase<br />

Pseudomonas sp.<br />

3) Flow scheme<br />

pH<br />

Fig. 3.1.1.41 – 2<br />

4) Process parameters<br />

yield: 95 %<br />

reactor type: repetitive batch, fixed bed reactor<br />

reactor volume: 1,000 L<br />

capacity: 90 t · a –1<br />

residence time: 4 h<br />

start-up date: 1973<br />

company: Asahi Kasei Chemical Industry Co., Ltd., Japan, and Toyo Jozo, Japan<br />

5) Product application<br />

● 7-ACA is an intermediate for semisynthetic cephalosporins.<br />

6) Literature<br />

NaOH H<br />

HO<br />

N<br />

HO<br />

O<br />

E<br />

O<br />

OH<br />

EC 3.1.1.41<br />

● Christ, C. (1995) Biochemical production of 7-aminocephalosporanic acid, in: Ullmann’s Encyclopedia<br />

of <strong>Industrial</strong> Chemistry, Vol. B8 (Arpe, H.-J. ed.) pp. 240–241, VCH Verlagsgesellschaft,<br />

Weinheim<br />

● Matsumoto, K. (1993) Production of 6-APA, 7-ACA, and 7-ADCA by immobilized penicillin<br />

and cephalosporin amidases, in: <strong>Industrial</strong> Application of Immobilized Biocatalysts (Tanaka,<br />

A, Tosa, T., Kobayashi, T. eds.) pp. 67–88, Marcel Dekker Inc., New York<br />

● Tsuzuki, K., Komatsu, K., Ichikawa, S., Shibuya, Y. (1989) Enzymatic synthesis of 7-aminocephalosporanic<br />

acid (7-ACA), Nippon Nogei Kagaku Kaishi 63 (12), 1847<br />

● Verweij, J., de Vroom, E. (1993) <strong>Industrial</strong> transformations of penicillins and cephalosporins,<br />

Rec. Trav. Chim. Pays-Bas 112 (2), 66–81<br />

H 2N<br />

O<br />

O<br />

N<br />

S<br />

O<br />

COOH<br />

O<br />

O<br />

O<br />

N<br />

S<br />

COOH<br />

O<br />

O<br />

331

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