The sugar industry in Australia, as in many other parts of the world, has e
xpanded rapidly in recent years greatly increasing the burden on processing
stations in sugar factories. Consequently, boiling houses and centrifugal
stations have often become production bottlenecks, requiring installation o
f new equipment, or significant upgrades of existing plant. Meanwhile, of c
ourse, sugar quality and recovery must be maintained, which requires (among
st other things) optimisation of crystal growth rates, Thus, the SRI embark
ed on a rigorous analysis of growth rates, and the effects of factors such
as grade of massecuite, stages in the boiling operation and variations in p
an design, aiming to establish benchmark figures for factory performance. F
urther research has centred on the use of model-based control, using growth
equations derived from laboratory and factory experiments to enhance effic
iency, and the comparison of such systems with conventional conductivity co
ntrol. Productivity gains of 10% are anticipated when model-based control s
chemes are applied to batch pans with good circulation and heat transfer pr
operties.
Important work now underway seeks to determine circulation velocities and f
low directions, allowing batch and continuous pan designs to be evaluated q
uantitatively, and to validate and refine computational fluid dynamics pred
ictions.