Abstract
The constant-rate fed-batch production of the polygalacturonic acid bioflocculant REA-11 was studied. A controlled sucrose-feeding strategy resulted in a slight improvement in biomass and a 7% reduction in flocculating activity compared with the batch process. When fed with a 3 g l-1 urea solution, the flocculating activity was enhanced to 720 U ml-1 in 36 h. High cell density (2.12 g l-1) and flocculating activity (820 U ml-1) were obtained in a 10-l fermentor by feeding with a sucrose-urea solution, with values of nearly two times and 50% higher than those of the batch process, respectively. Moreover, the residual sucrose declined to 2.4 g l-1, and residual urea decreased to 0.03 g l-1. Even higher flocculating activity of 920 U ml-1 and biomass of 3.26 g l-1 were obtained by feeding with a sucrose-urea solution in a pilot scale fermentation process, indicating the potential industrial utility of this constant-rate feeding strategy in bioflocculant production by Corynebacterium glutamicum. © 2010 Society for Industrial Microbiology.
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Wu, H., Li, Q., Lu, R., Wang, Y., Zhuang, X., & He, N. (2010). Fed-batch production of a bioflocculant from Corynebacterium glutamicum. Journal of Industrial Microbiology and Biotechnology, 37(11), 1203–1209. https://doi.org/10.1007/s10295-010-0767-9
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