A 20m3 working volume of a bioreactor is used for producting penicillin. What would be the sugar concentration (So) you choose if oxygen transfer rate is not the limiting reactant? Given data: Impeller speed =1.5rps(90rpm) Number of blades =8; flat, turbine types of blade =1mPas=1.2103kg/m3 Aeration rate =1vvm Ratio of gassed to ungassed power, P/P=0.4 Driving force for OTR =6103kg/m3 Specific O2 uptake =0.65mmolO2/kg cell Also, the kinetic data are given as vmax=0.5h1 Specific sugar consumption rate of cells =1.0kg/kg cell.h KLa=2103(VPg)0.6VS0.667 A 20m3 working volume of a bioreactor is used for producting penicillin. What would be the sugar concentration (So) you choose if oxygen transfer rate is not the limiting reactant? Given data: Impeller speed =1.5rps(90rpm) Number of blades =8; flat, turbine types of blade =1mPas=1.2103kg/m3 Aeration rate =1vvm Ratio of gassed to ungassed power, P/P=0.4 Driving force for OTR =6103kg/m3 Specific O2 uptake =0.65mmolO2/kg cell Also, the kinetic data are given as vmax=0.5h1 Specific sugar consumption rate of cells =1.0kg/kg cell.h KLa=2103(VPg)0.6VS0.667