Biotechnology & Biotechnological Equipment · 2010 · 22 citations · 26 references
Life SciencesBiotechnologyMicrobiologyEnzymologyMicrobial BiotechnologyMicrobial MetabolismFungal BiochemistryFungal BiotechnologyIndustrial FermentationMicrobial Enzyme ProductionMicrobial FermentationMicrobial GrowthBioreactor CultivationFungal Enzyme ProductionPellet Formation
α-Galactosidase production by the fungal strains Penicillium chrysogenum LN33 and Aspergillus niger M47 cultivated in shaking and stationary conditions using soya meal extract as nutrient medium was investigated. Submerged shake flask fermentation was preferred over stationary cultivation for P. chrysogenum LN33 as it gave a high α-galactosidase yield (4200U/l). Because of pellet formation the semicontinuous shake-flask fermentation was carried out for P. chrysogenum LN33 α-galactosidase production during 32 days. The maximum α-galactosidase activity by A. niger M47 (7000U/l) was obtained in stationary conditions of cultivation which is 27–28% greater as compared with the enzyme titer in shaking cultures. Air-lift laboratory bioreactor cultivation of both P. chrysogenum LN33 and A. niger M47 resulted in high-yield production of α-galactosidase (8700U/l and 11200U/l, respectively), which is of particular interest for biotechnological application in food processing.
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Naoki Asano, Haruhisa Kizu, Kyoko Ikeda et al. · European Journal of Biochemistry · 2000 · 242 citations · Full text