Macro-Mixing and Streptomyces Fradiae: Modelling Oxygen and Nutrient Segregation in an Industrial Bioreactor

0165877 - UCHP-M 20000060 RIV GB eng J - Článek v odborném periodiku
Vlaev, D. - Mann, R. - Lossev, V. - Vlaev, S. D. - Zahradník, Jindřich - Seichter, P.
Macro-Mixing and Streptomyces Fradiae: Modelling Oxygen and Nutrient Segregation in an Industrial Bioreactor.
Chemical Engineering Research and Design. Roč. 73, Part A (2000), s. 354-362. ISSN 0263-8762. E-ISSN 1744-3563.
[Symposium of Fluid Mixing /6./. Bradford, 07.07.1999-08.07.1999]
Grant ostatní: CEC INCO-COPERNICUS(XE) CIPA-CT94-0179
Výzkumný záměr: CEZ:AV0Z4072921
Kód oboru RIV: CI - Průmyslová chemie a chemické inženýrství
Impakt faktor: 0.732, rok: 2000

Some illustrative results are presented for a m3 triple-impeller stirred reactor producing tylosin (using Strepto-myces fradiae) being fed with air and a concentrated aque-ous ammonium nitrate solution. The analysis is performedfor a 3x2 (10x10) configuration of a networks-of-ozonesmodel comprising 600 zones. The gas-liquid flows, giving riseto circulation and bubble dispersion, are calculated assumingthat bubble moving independently at their rise velocity withoutdistorting the liquid flows being generated by the impellers.
Trvalý link: http://hdl.handle.net/11104/0063036