Kinetic patterns of dehydration of extracted raffinate of persimmon pulp

As a result of the conducted research, kinetic patterns of the drying process were obtained, which are necessary to determine the rational duration of dehydration and identify its mechanism based on the study of hygroscopic characteristics of raffinate crushed pulp of persimmon fruits. For crushed p...

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Main Authors: A. E. Makarov, A. H.-Kh. Nugmanov, I. Yu. Aleksanyan, P. D. Osmolovskiy, S. M. Arabov
Format: Article
Language:Russian
Published: North-Caucasus Federal University 2025-01-01
Series:Современная наука и инновации
Subjects:
Online Access:https://msi.elpub.ru/jour/article/view/1681
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author A. E. Makarov
A. H.-Kh. Nugmanov
I. Yu. Aleksanyan
P. D. Osmolovskiy
S. M. Arabov
author_facet A. E. Makarov
A. H.-Kh. Nugmanov
I. Yu. Aleksanyan
P. D. Osmolovskiy
S. M. Arabov
author_sort A. E. Makarov
collection DOAJ
description As a result of the conducted research, kinetic patterns of the drying process were obtained, which are necessary to determine the rational duration of dehydration and identify its mechanism based on the study of hygroscopic characteristics of raffinate crushed pulp of persimmon fruits. For crushed pulp of persimmon fruits, dewatering of raffinate is advisable to be carried out with convective supply of thermal energy by a heated air stream that moves orthogonally along the trajectory of the dried product. The above research results do not conflict with the results of other scientists, which makes it possible to use them in the engineering practice of the food industry in the design of plants for dehydration of plant products. It is noted that the dry raffinate from blanched persimmon contains a large proportion of dietary fiber and swelling capacity. The conducted studies allowed us to identify rational operating parameters of convective drying of fruit raffinate, namely: the speed of the drying agent equal to 2.5 m/s, its temperature 75 ° C and the filling level of the working space of the drum – 1/2 with a maximum theoretical productivity of Y =208 (kg / (m3· hour)). The temperature of the coolant differs from the final temperature of the product by 15-20 ° C, as a result of which the limiting temperature of the drying agent is assumed to be about 75 ° C, which is justified by experimental data at a higher temperature of the coolant relative to the recommended one in the article.
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spelling doaj-art-07d429bf8d964c77ac8283f9a28bdc4f2025-08-20T02:49:26ZrusNorth-Caucasus Federal UniversityСовременная наука и инновации2307-910X2025-01-01049811110.37493/2307910X.2024.4.101638Kinetic patterns of dehydration of extracted raffinate of persimmon pulpA. E. Makarov0A. H.-Kh. Nugmanov1I. Yu. Aleksanyan2P. D. Osmolovskiy3S. M. Arabov4PASTAPITZARussian State Agrarian University – Moscow Timiryazev Agricultural Academy (RSAU – MTAA)Astrakhan State Technical UniversityLipetsk Rapeseed Research Institute – the Branch of V.S. Pustovoit All- Russian Research Institute of Oil CropsAstrakhan State University of Architecture and Civil EngineeringAs a result of the conducted research, kinetic patterns of the drying process were obtained, which are necessary to determine the rational duration of dehydration and identify its mechanism based on the study of hygroscopic characteristics of raffinate crushed pulp of persimmon fruits. For crushed pulp of persimmon fruits, dewatering of raffinate is advisable to be carried out with convective supply of thermal energy by a heated air stream that moves orthogonally along the trajectory of the dried product. The above research results do not conflict with the results of other scientists, which makes it possible to use them in the engineering practice of the food industry in the design of plants for dehydration of plant products. It is noted that the dry raffinate from blanched persimmon contains a large proportion of dietary fiber and swelling capacity. The conducted studies allowed us to identify rational operating parameters of convective drying of fruit raffinate, namely: the speed of the drying agent equal to 2.5 m/s, its temperature 75 ° C and the filling level of the working space of the drum – 1/2 with a maximum theoretical productivity of Y =208 (kg / (m3· hour)). The temperature of the coolant differs from the final temperature of the product by 15-20 ° C, as a result of which the limiting temperature of the drying agent is assumed to be about 75 ° C, which is justified by experimental data at a higher temperature of the coolant relative to the recommended one in the article.https://msi.elpub.ru/jour/article/view/1681persimmon fruit pulpextractionraffinatehygroscopic characteristicsdrying kineticsrational modesprocess time
spellingShingle A. E. Makarov
A. H.-Kh. Nugmanov
I. Yu. Aleksanyan
P. D. Osmolovskiy
S. M. Arabov
Kinetic patterns of dehydration of extracted raffinate of persimmon pulp
Современная наука и инновации
persimmon fruit pulp
extraction
raffinate
hygroscopic characteristics
drying kinetics
rational modes
process time
title Kinetic patterns of dehydration of extracted raffinate of persimmon pulp
title_full Kinetic patterns of dehydration of extracted raffinate of persimmon pulp
title_fullStr Kinetic patterns of dehydration of extracted raffinate of persimmon pulp
title_full_unstemmed Kinetic patterns of dehydration of extracted raffinate of persimmon pulp
title_short Kinetic patterns of dehydration of extracted raffinate of persimmon pulp
title_sort kinetic patterns of dehydration of extracted raffinate of persimmon pulp
topic persimmon fruit pulp
extraction
raffinate
hygroscopic characteristics
drying kinetics
rational modes
process time
url https://msi.elpub.ru/jour/article/view/1681
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