Sugar factories produce 5-8 kg/100 kg beet of carbonatation sludge. De
pending on the filtering plant, this sludge occurs as a fluid system (
less than or equal to 60% dry substance) or in solid form. The studies
reported here serve to characterize the flow behaviour of this waste
product as a plastic non-Newtonian medium. The paper describes the the
oretical principles of theology, the conduct of the measurements and e
valuation of the experiments. Flow curves for dry substance contents o
f 50%, 55% and 60% in a temperature range of 20 to 70 degrees C were e
stablished. Sludge throughput equations were derived for ranges of pra
ctical importance and a transport optimization exercise conducted for
what can also be described as a Cassonian medium. The indicated method
of analysis can also be applied in modified form to the hydraulic tra
nsport of sludge from settling tanks.