“…(3) (Smith et al, 1990;Justen et al, 1998b) N Fl = ͩ 0.91N P W D i ͪ 1/2 (4a) (Platzer and Noll, 1983;Justen et al, 1996) N Fl, g = N Fl ͩ N P, g N P ͪ (4b) (Justen et al, 1998b) N Ae = Q air ND i, bottom 3 (5) (Bailey and Ollis, 1986;Atkinson and Mavituna, 1991) P, gassed impeller power; k , geometric constant; D i , impeller diameter; W, impeller blade height; V L , volume of liquid; N Fl , ungassed flow number; N Fl,g , gassed flow number; N P , ungassed power number; N P, g , gassed power number; Q air , volumetric air flow rate; D i ,bottom , diameter of bottom impeller. To calculate EDCF for each impeller, total gassed power must be appropriately distributed to each of the three impellers in the fermentor.…”