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MILLING TRAIN MACERATION CONTROL UTILISING NIR TECHNOLOGY
By T LLOYD; S EASTMENT; P MITCHELL
IN RECENT TIMES, Australian sugar factories have tried to maximise
throughput. This trend has continued with factory rationalisation and a
need to maximise utilisation of existing capital. The amount of
maceration applied to the crushing mills has a great effect on reducing pol
loss in final mill bagasse. It is generally recognised that other things being
equal, the more maceration the better the extraction. However the down
side is that evaporators have to be able to boil off the extra water. The
capacity of the evaporators to boil off that water in turn limits crushing
capacity. Other issues associated with higher maceration rates are the
evaporators scale quicker and the amount of steam required to maintain
crushing capacity increases. Traditional maceration rates have been
determined by using a fixed percentage of water at a daily average fibre
rate which is at least a 24 hours out of date. Near Infra Red (NIR)
measurement was introduced to Mackay sugar mills in 2006 and can be
used to determine the quantities of fibre, pol and ash contained in the
incoming cane. NIR gives a real time measurement of cane parameters
and has allowed fibre rates through the mills to be measured accurately.
Those measurements have been combined with cane crushing rates to
provide a control value for maceration addition. This accurate control of
maceration rate gives the following advantages over the traditional
method of controlling maceration flow: mills have a consistent
maceration % fibre which means there is always sufficient water to get
the required pol recovery regardless of the cane characteristics; mills are
not using extra maceration – just the right amount to give the right
balance between bagasse loss, evaporator capacity and steam availability;
more stable ESJ (Evaporator Supply Juice) brix which produces more
stable evaporator performance; consistent final bagasse moisture and
quality.