This paper presents operating experiences with a plate evaporator empl
oyed for thick juice in the Rethen factory of Zuckerverbund Nord and m
easurements of its heat transfer behaviour. At the start of the campai
gn, operation was unstable and required changes in management. In the
second half of the campaign, an apparent heat transfer coefficient of
about 1750 W/(m2 . K) was established for the plate evaporator. By cha
nging the management on the juice side it was possible to operate the
plate evaporator for short periods under different conditions. The mea
surements showed a higher heat transfer with increasing flow velocity.
At all settings, a pulsating exit of juice into the vapour space was
observed. The plate evaporator investigated required that the heating
surfaces be wetted at a rate of about 0.1 m3 per (m2 . h), in terms of
the entering volume of juice, in order to achieve adequate operationa
l stability.