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APV Dryer Handbook - Umbc

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of conveyor necessary to support the product does not allow through-flow<br />

or where the product form is not suitable for this method of airflow. The most usual<br />

method of heating is by steam through heat exchangers mounted in the side<br />

plenums or above the band, although direct oil and gas firing are sometimes<br />

used. In such cases, the products of combustion are normally introduced to a hot<br />

well or duct at an elevated temperature from where they are drawn off, and<br />

mixed with circulating air in each zone or section of the dryer.<br />

Another alternative with direct firing is to use a series of small individual burners<br />

positioned so that each serves one or more zones of the dryer. Typical single pass<br />

dryers of modular construction are illustrated in Figures 11 and 12.<br />

With this type and size of dryer, the average product throughput is about 5600<br />

lbs/hr (2550 kg/h) and involves an evaporation of 1600 lbs/h (730 kg/h)<br />

moisture. It is not unusual, however, to find equipment with evaporative<br />

capacities of 3000 lbs/h (1350 kg/h). Such outputs involve a large band area<br />

with correspondingly large floor area requirements. Various types of feeding<br />

arrangements are available to spread or distribute the wet product over the<br />

width of the band. Here again, the nature of the feed is an important prerequisite<br />

for efficient drying. Steam heated, finned drums have been used as a means<br />

of producing a partially dried, preformed feed. While the amount of pre-drying<br />

achieved is reflected in increased output for a given dryer size or, alternatively,<br />

enables a smaller dryer to be used, these items are usually much more costly<br />

than many of the mechanical extruders which are available.<br />

Generally, these extruders operate with rubber covered rollers moving over<br />

a perforated die plate with feed in the form of pressed cakes, or more usually,<br />

as the discharge from a rotary vacuum filter. The pressure type employ a gear<br />

pump arrangement with extrusion taking place through a series of individual<br />

nozzles, while some use screw feeds which are usually set up to oscillate to<br />

obtain effective coverage of the band. Alternate designs include rotating cam<br />

blade or conventional bar-type granulators, although the latter often produce<br />

a high proportion of fines because of the pronounced shearing effect. This makes<br />

the product rather unsuitable due to the entrainment problems which can occur.<br />

25

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