An obvious advantage of continuous evaporating crystallizers with stir
ring systems is the possibility to operate at very low temperature dif
ferences. This enables the design of equipment for a crystallization s
cheme providing a double-effect evaporation: The vapour from the evapo
rating crystallizers for raw sugar and after-product is the heating me
dium for the white sugar evaporating crystallizer. Model calculations
are introduced and the consequences of such lay-outs for the evaporati
ng station and the power plant of a sugar factory are described. Accor
dingly, the sole production of white sugar of EEC quality 2 results in
operational steam requirements of 15.3 kg/100 kg beet. Just in time f
or the 1994 beet campaign such lay-outs and equipment for a crystalliz
ation with double-effect evaporation have been installed in the sugar
factories of Gustrow and Klein Wanzleben. Gustrow sugar factory has al
ready started operation during the 1994 beet campaign. The report give
s a survey of the operating conditions and results.