Optimized fed-batch fermentation of L-β-hydroxy isobutyric acid by Yarrowia lipolytica

Yarrowia lipolytica KCCM50506, which transforms isobutyric acid to L-#-hydroxy isobutyric acid (L-#-HIBA), was screened. Chemostat cultures were carried out in jar fermentors at dilution rates of 0.02 h^у to 0.12 h^у. L-#-HIBA fermentation-regulating factors were determined to be specific growth rate, and concentrations of glucose and isobutyric acid in fermentor from analysis of steady-state data. The specific productivity of L-#-HIBA increased as the specific growth rate increased, apparently as a growth-associated type of product formation. A fed-batch culture was carried out under optimum conditions where the concentrations of glucose and isobutyric acid in the fermentor were maintained at 23 g l^у and 9 g l^у, respectively. The concentrations of cells and L-#-HIBA obtained at the end of fermentation were 20 g l^у and 49 g l^у, respectively, corresponding to 2.0 and 2.7 times more than concentrations in batch culture.