| Literature DB >> 32315915 |
Ayan Banerjee1, Tripti Sharma1, Abhilek K Nautiyal1, Diptarka Dasgupta1, Saugata Hazra2, Thallada Bhaskar1, Debashish Ghosh3.
Abstract
This work was aimed to strategically scale-up the yeast lipid production process using Reynolds number as a standard rheological parameter from 50 mL to 50 L scale. Oleaginous yeast Rhodotorula mucilaginosa IIPL32 was cultivated in xylose rich corncob hydrolysate. The fermentation process for growth and maturation was operated in fed-batch with two different C/N ratios of 40 and 60. The hydrodynamic parameters were used to standardize and represent the effect of rheology on the fermentation process. The growth pattern of the yeast was found similar in both shake flask and fermenter with the maximum growth observed at 48 h. The lipid yield increased from 0.4 g/L and 0.5 g/L to 1.3 g/L and 1.83 g/L for 50 mL to 50 L for C/N ratio 40 and 60 respectively. The increase in productivity during the growth phase and lipid accumulation during the maturation phase showed that the scale-up strategy was successful.Entities:
Keywords: Rheology; Scale-up; Shake flask; Stirred tank fermenter; Yeast single cell oil
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Year: 2020 PMID: 32315915 DOI: 10.1016/j.biortech.2020.123329
Source DB: PubMed Journal: Bioresour Technol ISSN: 0960-8524 Impact factor: 9.642