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Industrial Biotransformations

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Xylose isomerase<br />

Bacillus coagulans/Streptomyces rubiginosus/Streptomyces phaechromogenes<br />

3) Flow scheme<br />

Fig. 5.3.1.5 – 3<br />

EC 5.3.1.5<br />

4) Process parameters<br />

reactor type: continuous, fixed bed<br />

reactor volume: variable<br />

capacity: > 7 · 106 t·a –1<br />

residence time: 0.17 – 0.33 h<br />

down stream processing: 55 % fructose: chromatography; 42 % fructose:<br />

no down stream processing<br />

enzyme consumption: see remarks<br />

start-up date: 1967 by Clinton Corn Processing Co. (USA); 1974 with immobilized<br />

enzyme<br />

510

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