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Mathematical Modelling of Conveyor-Belt Dryers with Tangential Flow for Food Drying up to Final Moisture Content below the Critical Value

机译:输送带干燥机的数学建模与切向流量的食物干燥到临界值低于最终水分含量

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This work presents the mathematical modeling of the conveyor-belt dryer with tangential flow operating in co-current, which has the advantage of improving the preservation of the organoleptic and nutritional qualities of the dried food. On the one hand, it is a more cumbersome dryer than the perforated cross flow belt dryer but, on the other hand, it has a low air temperature in the final section where the product has a low moisture content and, therefore, it is more heat sensitive. The results of the mathematical modeling allowed a series of guidelines to be developed for a rational design of the conveyor-belt dryer with tangential flow for the specific case of the moisture content of the final product &i&X&sub&F&/sub&&/i& lower than the critical one &i&X&sub&C&/sub&&/i& (&i&X&sub&F&/sub& & X&sub&C&/sub&&/i&). In fact, this work follows a precedent in which a mathematical model was developed through the differentiation of the drying rate equation along the dryer belt with the hypothesis that the final moisture content &i&X&sub&F&/sub&&/i& of the product was higher than the critical one &i&X&sub&C&/sub&&/i&. The relationships between the extensive quantities (air flow rate and product flow rate), the intensive quantities (temperatures, moisture content and enthalpies) and the dimensional ones (length and width of the belt) were then obtained. Finally, based on these relationships, the rules for an optimized design for &i&X&sub&F&/sub& & X&sub&C&/sub&&/i& were obtained.
机译:这项工作提出在顺流切向流操作,其具有改善的干燥食品的感官和营养品质的保存的优点的传送带干燥机的数学建模。在一方面,这是一个更累赘的干燥器比穿孔横流带式干燥机,但是,在另一方面,它在最后的部分,其中该产品具有低的水分含量,因此低空气温度,这是更热敏感。数学建模的结果允许与用于最终产品&安培的水分含量的特定情况下切向流的传送带干燥机的合理设计待开发的一系列准则; LT; I和X的催化剂&安培; LT ;子&安培; GT; F&安培; LT /子&安培; GT;&安培; LT / I和GT;低于临界一个&安培; LT; I和X的催化剂&安培; 副&安培; GT; C&安培; LT /子&安培; GT;&安培; LT / I和GT; (安培; LT; I和X的催化剂&安培; 副&安培; GT; F&安培; LT /子&安培; GT;&安培; LT; X&安培; 副&安培; GT; C&安培; LT /子&安培; GT;&安培; LT ; / I和GT)。事实上,这种工作如下,其中数学模型,通过沿与假设干燥器带干燥速率方程的分化开发的先例,最终水分含量&安培; LT; I和X的催化剂&安培; 副&安培; GT ; F&安培; LT /子&安培; GT;&安培; LT / I和GT;产物的比临界一个&安培更高; LT; I和X的催化剂&安培; 副&安培; GT; C&安培; LT /子&安培; GT;&安培; LT / I和GT ;.然后所获得的广泛量之间的关系(空气流量和产品流动速率),重症量(温度,水分含量和焓)和维酮(长度与带的宽度)。最后,基于这些关系,对于与放大器的优化设计规则; LT; I和X的催化剂&安培; 副&安培; GT; F&安培; LT /子&安培; GT; & X&安培; 副&安培; GT; C&安培; LT /子&安培; GT;&安培; LT / I和GT;获得。

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