Abstract

The drying process, which is the limiting and power-consuming stage of candied fruits production, has been considered. The heat-transfer processes during the filtration drying of pumpkin candied fruit have been investigated. The filtration drying of finished candied fruits (80 °C) is the filtration of a hot heat agent (100 °C) in the direction of "candied layers – grate". As a result of experimental studies, the kinetic curves of candied fruits drying, as well as the dependence of temperature on the height of the candied fruit layer, were obtained. The experimental data confirm the zonal mechanism of the filtration drying.It was found that during the filtration drying, the upper layers, which reached their final moisture content, overheat and accumulate a considerable amount of unused energy. It was proved that the accumulated energy can be used for drying the lower layers with simultaneous cooling the upper ones. On the basis of the equation of non-stationary heat-mass transfer, the amount of heat is calculated, which will be sufficient to dry the bottom layer. The stoppage time of hot heat agent supply and start of cold heat agent supply were determined. Filtration of cold heat agent through a layer of candied fruits makes it possible to cool the layer, reduce drying time and energy costs for the process.Dried candied fruits have sufficient shelf life, good taste and organoleptic properties.

Highlights

  • Drying is the most limiting and power-consuming stage in many industries

  • The heattransfer processes during the filtration drying of pumpkin candied fruit have been investigated

  • It was proved that the accumulated energy can be used for drying the lower layers with simultaneous cooling the upper ones

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Summary

Introduction

Drying is the most limiting and power-consuming stage in many industries. In particular, in the food industry, 90 % of all products are subjected to drying [1]. The disadvantages of filtration drying are the considerable height of the material layer [8] and the considerable drying time for materials containing mainly bound moisture [9, 10]. The elimination of these disadvantages is an urgent task. Adsorbents have a short regeneration time due to their free moisture content [12] Such healthy product as candied fruits, after saturation with sucrose, is subjected to long-term drying in a stationary layer due to the available bound moisture. The reduction of drying time and energy costs during candied fruits drying remains an urgent task

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