By using a few rheometrical instruments (such as a conventional rotational
viscometer equipped with a double couette sensor system. a dynamic stress r
heometer with cylindrical and plate-and-cone geometry, and Cannon-Fenske ca
pillary viscometers), it was possible to assess that yeast suspensions in t
he range 25-200 kg m(-3) behaved as Newtonian liquids. In fact, their dynam
ic viscosity (as determined under shear flow, oscillatory flow and creep) p
ractically coincided with that determined using capillary viscometers. The
relative viscosity of these suspensions at 5 degrees C was then correlated
to the yeast volumetric fraction (phi) by means of the Krieger equation, wh
ile the effect of temperature on viscosity was better described by using a
power-law model rather than the Arrhenius relationship, its empirical param
eters being dependent on yeast concentration. (C) 2000 Elsevier Science Ltd
. All rights reserved.