A two-stage fed-batch process was designed to enhance erythritol productivi
ty by the mutant strain of Candida magnoliae, The first stage (or growth st
age) was performed in the fed-batch mode where the growth medium was fed wh
en the pH of the culture broth dropped below 4.5, The second stage (or prod
uction stage) was started with addition of glucose powder into the culture
broth when the cell mass reached about 75 g dry cell weight l(-1), When the
initial glucose concentration was adjusted to 400 g l(-1) in the productio
n stage, 2.8 g l(-1) h(-1) of overall erythritol productivity and 41% of er
ythritol conversion yield were achieved, which represented a fivefold incre
ase in erythritol productivity compared with the simple batch fermentation
process. A high glucose concentration in the production phase resulted in f
ormation of organic acids including citrate and butyrate, An increase in di
ssolved oxygen level caused formation of gluconic acid instead of citric ac
id.