ASSESSING THE EFFECT OF JUICE PROPERTIES AND OPERATING CONDITIONS ON THE HEAT TRANSFER IN ROBERT EVAPORATORS
By R. BROADFOOT and K.G. DUNN
HEAT transfer data were obtained in a pilot Robert evaporator of 20 m2 heating
surface area for a wide range of juice processing conditions. The process
variables which were varied included juice brix, juice boiling temperature, juice
level and heat flux. An optimum juice level corresponding to the maximum heat
transfer coefficient (HTC) was found to exist for each set of processing
conditions. In general the optimum juice level was lower for juice at lower brix
and higher for juice at higher brix. Heat transfer data were also obtained from
evaporator stations at Tableland, Isis and Broadwater Mills. The data allowed
calculation of the HTC values for the evaporators in a clean condition
(designated HTCclean) and the reduction in HTC due to the deposition of scale.
An improved correlation for predicting the HTC in clean Robert evaporators was
developed based on the data from the pilot evaporator and the factory
evaporators. The selected correlation for HTCclean was determined to be a
function of the vapour condensation coefficient (rate of vapour condensed per
unit area of heating surface) and the viscosity of the juice. The viscosity of the
juice is a function of the brix and temperature of the juice. The heat transfer data
from the factory evaporators were analysed to determine the magnitude of the
scaling effect. The results showed large variability of the influence of scaling
among mills, and from operating cycle to operating cycle. In general, higher
rates of scaling were experienced at the first and final effect positions for the
quadruple set and for the first, final and penultimate evaporators for the
quintuple evaporator sets. Use of the new correlation for HTC will improve the
reliability of modelling to determine the investment required for upgrading
evaporator stations e.g. for specifying additional evaporator area and changes to
the configuration of the station.