Scale-up strategy for bioreactors with Newtonian and non-Newtonian broths

In the scale-up of bioreactors one of the most 1 commonly used criteria for aerobic processes is to keep the oxygen transfer coefficient constant. Nev ertheless, the reproduction of the behaviour of a cell population at differ ent scales is not dependent just on the oxygen transfer capability but rath er on the oxygen transfer rate, that must be high enough to cope with the o xygen demand of the culture. In this work a strategy of scaleup is proposed based in geometric similarity, constant impeller tip speed, and constant o xygen transfer rate. The effects of the dissolved oxygen concentration, the scale-up ratio and the rheology of the broth are analysed.