Abstract
The disparity of secondary metabolites in Penicillium chrysogenum between two scales of penicillin G fermentation (50 L as pilot process and 150,000 L as industrial one) was investigated by ion-pair reversed-phase liquid chromatography tandemed with hybrid quadrupole time-of-flight mass spectrometry. In industrial process, the pools of intracellular L-α-aminoadipyl-L-cysteinyl-D-valine (LLD-ACV) and isopenicillin N (IPN) were remarkably less than that in the pilot one, which indicated that the productivity of penicillin G might be higher in the large scale of fermentation. This conclusion was supported by the higher intracellular penicillin G concentration as well as its higher yield per unit biomass in industrial cultivation. The different changing tendencies of IPN, 6-aminopenicillanic acid and 6-oxopiperide-2-carboxylic acid between two processes also suggested the same conclusion. The higher content of intracellular LLD-ACV in pilot process lead to a similarly higher concentration of bis-δ-(L-α-aminoadipyl)-L-cysteinyl-D-valine, which had an inhibitory effect on ACV synthetase and also subdued the activity of IPN synthetase. The interconversion of secondary metabolites and the influence they put on enzymes would intensify the discrepancy between two fermentations more largely. These findings provided new insight into the changes and regulation of secondary metabolites in P. chrysogenum under different fermentation sizes.
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Acknowledgment
The authors are grateful for the financial support from the National Natural Science Foundation of China (key program grant no. 20736006), the National Basic Research Program of China (“973” Program no. 2007CB714301), international collaboration project of MOST (2006DFA62400), Key Projects in the National Science & Technology Pillar Program (no. 2007BAD42B02), and Innovation Fund of Tianjin University.
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Cao, YX., Qiao, B., Lu, H. et al. Comparison of the secondary metabolites in Penicillium chrysogenum between pilot and industrial penicillin G fermentations. Appl Microbiol Biotechnol 89, 1193–1202 (2011). https://doi.org/10.1007/s00253-010-2910-y
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DOI: https://doi.org/10.1007/s00253-010-2910-y