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Cereals processing technology

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

8.3.2 Developments in blending<br />

For batch cereal operations, batch ribbon blenders are still the industry<br />

workhorse for blending. They are easily loaded, unloaded, and cleaned; by<br />

hand, by screw conveyor, or by pneumatic conveyer. Most are double ribbon<br />

blenders; that is one ribbon pushes the material toward one end, while the<br />

opposing ribbon pushes the material to the other end. The level of fill in these<br />

units is somewhat critical. For optimum blending in the shortest time, the<br />

blenders should be filled between 50–75%. In no case, however, should they<br />

be filled over the level of the ribbons. If this is done, the top part of the load is<br />

in a dead mixing zone.<br />

Microprocessors can again come into play in this unit operation in several<br />

ways. The whole unit can be mounted on load cells and serve as a receiver and<br />

weigh hopper vessel. Blending times and speeds, of course, can be controlled via<br />

programmable logic controllers (PLCs), as well as load and discharge opening<br />

and closing functions. Cycle time is always the sum of loading time, blending<br />

time, and discharge time. In order to make best use of the blending time, it pays<br />

to keep the openings for loading and discharge as large as possible. Also, as an<br />

alternative to using the blender itself as a weigh hopper, time is saved by using a<br />

weigh hopper/receiver above the blender to preweigh all dry ingredients, and a<br />

receiver below the blender big enough to accommodate several batches of dry<br />

blended ingredients. In addition to standard ribbon blenders, conical blenders<br />

can also be used.<br />

There are in addition many ways that continuous blend systems can be set up<br />

to preblend the dry ingredients, and then even add the liquid flavor mix before<br />

cooking in batches. In extrusion cooking it is customary to add the preblended<br />

drys to the extruder, and liquids to the extruder, via separate ports – more on this<br />

in Section 8.3.3.<br />

Any dry blend set up should have as a consideration the pros and cons of<br />

clean-in-place (CIP). These systems can be added easily if engineered into the<br />

initial design and layout. CIP systems also run off PLC control systems. We will<br />

limit our discussion here on liquids blending to the four basic flavor materials;<br />

water, sugar, salt and malt. The workhorse mixing vessel for these has been, and<br />

still is, the steam jacketed kettle. Liquid sucrose, dry salt, and liquid malt extract<br />

are slurried in water in a kettle equipped with agitation, and a steam jacket<br />

sufficient in capacity to heat the mix to 125ºF (52ºC). This is a high enough<br />

temperature to make a good useable slurry of such viscosity for ease of handling.<br />

If dry sugar and dry malt flour are used, these can be incorporated in the dry<br />

blend with the other dry ingredients.<br />

In making liquid flavor mixes in batches it is common to use a kettle large<br />

enough to accommodate flavor aliquots for multiple batches of dry materials.<br />

When doing so it is best to weigh the aliquots of liquid flavor for each batch of<br />

drys. Metering of liquid flavor batches introduces more chances for batch-tobatch<br />

variability than weighing the increments due to the on/off withdrawal<br />

cycles from the kettle. Slight drops in temperature can cause significant<br />

viscosity and flow character changes.

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