A study was undertaken of the heat exchange possible in a milk powder
plant consisting of milk treatment, a four-effect evaporator fitted wi
th a thermovapour recompressor and a spray drier fitted with a fluidiz
ed bed secondary drier. The study utilized the techniques of process i
ntegration analysis and grand composite curve matching. Of particular
interest was the optimum utilization of vapours within the evaporator.
It was shown that with a minor redesign of the evaporator and utiliza
tion of some vapour in the milk treatment section of the plant, a 6% r
eduction in total energy consumption of the milk powder plant was poss
ible. If heat exchange between inlet and outlet air of the spray drier
was not considered practical, preheating spray drier air with vapour
from the evaporator resulted in a 10% reduction in energy consumption.
Other minor heat exchange possibilities were also revealed. It was co
ncluded that the use of vapour from the evaporator, and increased stea
m consumption in the evaporator, may lead in some designs to decreased
plant thermal energy consumption overall. As well as the process inte
gration study, formulae are presented for calculating the change in th
ermal economy of an evaporator when vapour is extracted for use in oth
er sections of the plant. The use of process integration studies needs
to be given consideration in overall design of energy-intensive dairy
plant.