posted on 2018-03-08, 16:25authored bySusana Pedraza-de la Cuesta, Lore Keijzers, Luuk A.M. van der Wielen, Maria C. Cuellar
In multiphase fermentations where the product forms a second liquid phase
or where solvents are added for product extraction, turbulent conditions
disperse the oil phase as droplets. Surface-active components (SACs) present
in the fermentation broth can stabilize the product droplets thus forming an
emulsion. Breaking this emulsion increases process complexity and consequently
the production cost. In previous works, it has been proposed to
promote demulsification of oil/supernatant emulsions in an off-line batch
bubble column operating at low gas flow rate. The aim of this study is to test
the performance of this recovery method integrated to a fermentation,
allowing for continuous removal of the oil phase. A 500mL bubble column is
successfully integrated with a 2 L reactor during 24 h without affecting cell
growth or cell viability. However, higher levels of surfactants and emulsion
stability are measured in the integrated system compared to a base case,
reducing its capacity for oil recovery. This is related to release of SACs due to
cellular stress when circulating through the recovery column. Therefore, it is
concluded that the gas bubble-induced oil recovery method allows for oil
separation and cell recycling without compromising fermentation performance;
however, tuning of the column parameters considering increased
levels of SACs due to cellular stress is required for improving oil recovery.