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Cereals processing technology

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166 <strong>Cereals</strong> <strong>processing</strong> <strong>technology</strong><br />

with rapid product gelatinization measurements while running have greatly<br />

enhanced extrusion cooking acceptance. While all these features would seem to<br />

weigh in favor of extrusion cooking over batch, it must be pointed out that the<br />

two methods do not yet produce identical products. They have drawn closer and<br />

closer, but small differences still exist, and preference for one system over the<br />

other is a matter of finished product character choice.<br />

8.3.4 Developments in drying<br />

‘Drying’ unit operation in RTE <strong>processing</strong> is a necessary step between cooking<br />

and forming, i.e. flaking, shredding, gun puffing, etc. Most cooked grain recipes<br />

exit the cooker or extruder cooker at 25–30% moisture content. They are then<br />

dried to ranges of moisture between 9 and 17% for the forming operation. The<br />

units used for this step are still predominantly flat belt conveyor dryers – either<br />

single pass or multiple pass.<br />

The two developments that stand out are in the areas of humidity control and<br />

unit sanitation. Humidity control impinges heavily in the area of dryer<br />

efficiency, and, just as importantly or even to a greater extent, affect condition<br />

quality of product exiting the dryer. Use of humidity increases efficiency of the<br />

dryer heat use, since exhaust air carrying the entrained moisture from the<br />

product can be reduced to the bare minimum. Reducing exhaust air naturally<br />

reduces the need for heated make-up air thus cutting down on fuel usage on the<br />

supply air side of the dryer.<br />

The quality of product exiting a dryer with humidity control is greatly<br />

improved. The improvement is noted in that ‘case hardening’ of product<br />

particles during drying is much less severe. Product particles dry because the<br />

drying air sweeps away the microscopic layer of moisture from the particle<br />

surface. This causes a migration of moisture from the interior of the particle to<br />

the surface, when another, and another layer after layer of moisture are taken<br />

away. If, however, the drying air is too dry or too hot, a dry film forms on the<br />

particle surface which acts as a barrier to further moisture migration from the<br />

interior. This dried surface condition is referred to as ‘case hardened’.<br />

8.3.5 Developments in tempering<br />

The next step after drying is tempering, a step used to allow equilibration of<br />

moisture within the particles and from one particle to another. If the particles are<br />

case hardened, temper times must be much longer to allow equilibration to take<br />

place. Use of humidity greatly reduces the amount of in-process material, and<br />

equipment needed to hold it, for this temper to take place.<br />

It is hard to believe that advances can be made in a unit operation in a process<br />

that merely allows the product-in-process to just sit. Great light, however, has<br />

been shed on the tempering process in the last two decades. Early breakfast<br />

cereal scientists wondered in the very early years after World War II whether the<br />

physical and chemical changes that took place in breakfast cereal tempering

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