Abstract
This work focuses on using renewable sources as feedstock for the microbial production of carotenoids, valuable compounds for various industries. Xanthophyllomyces dendrorhous, which mainly synthesize astaxanthin and β-carotene, was used for the process. We proposed two strategies to achieve high production yields, the correct oxygen supply to the medium and the adoption of a fed-batch mode. Two factors related to the medium's oxygen transfer at a flask scale (working volume and agitation) were evaluated. Astaxanthin production was successfully correlated with the oxygen transfer coefficient (kLa) using a mesquite pods-based medium (MEM) and a chemically defined one (YM). kLa correlations were then used to set the conditions at a reactor scale. An optimum kLa of 16.86 h−1 was adequate to promote astaxanthin production in MEM (1824.13 μg/L). Meanwhile, in YM, optimum production (1656.24 μg/L) was obtained at the highest evaluated levels (17.77 h−1). Thus, a higher oxygen transfer rate is required to produce carotenoids in YM compared with MEM. Astaxanthin production was thus evaluated using a fed-batch process at flask and reactor scales. Reached production levels with fed-batch cultivation were 4465.12 μg/L (flask) and 4130.23 μg/L (reactor). This study demonstrated the correlation between oxygen transfer and carotenoids' production and the potential utilization of mesquite feedstock in a fed-batch bioprocess to improve carotenoids' yield by X. dendrorhous.
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