For a specific bioreactor configuration, the power requirement for a Rushton-turbine impeller agitating an unaerated Newtonian fluid in the turbulent regime will be
- (A)
proportional to the stirring speed of the impeller
- (B)
proportional to the square of the stirring speed of the impeller
- (C)
proportional to the cube of the stirring speed of the impeller
- (D)
inversely proportional of the stirring speed of the impeller
