INVESTIGATION OF THE KINETICS OF THE MIXING PROCESS AT VARIABLE SPREADS HEAT SUPPLY

The investigation of the kinetics of mixing creamy vegetable spreads with a variable heat supply. The time of each of the periods of re-mixing. Stirring at a temperature of 65 °C optimum convective mixing period was 2.5 minutes. Convective mixing duration after the beginning of crystallization of th...

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Main Authors: A. N. Ostrikov, A. V. Gorbatova
Format: Article
Language:Russian
Published: Voronezh state university of engineering technologies 2015-04-01
Series:Vestnik Voronežskogo Gosudarstvennogo Universiteta Inženernyh Tehnologij
Subjects:
Online Access:https://www.vestnik-vsuet.ru/vguit/article/view/238
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spelling doaj-d6e6e3e0dc824e8593d592d0608257af2021-07-29T08:04:57ZrusVoronezh state university of engineering technologies Vestnik Voronežskogo Gosudarstvennogo Universiteta Inženernyh Tehnologij2226-910X2310-12022015-04-0102101310.20914/2310-1202-2015-2-10-13202INVESTIGATION OF THE KINETICS OF THE MIXING PROCESS AT VARIABLE SPREADS HEAT SUPPLYA. N. Ostrikov0A. V. Gorbatova1Voronezh State University of Engineering TechnologiesVoronezh State University of Engineering TechnologiesThe investigation of the kinetics of mixing creamy vegetable spreads with a variable heat supply. The time of each of the periods of re-mixing. Stirring at a temperature of 65 °C optimum convective mixing period was 2.5 minutes. Convective mixing duration after the beginning of crystallization of the product (i.e., by stirring at a temperature of 30 ... 15 ° C) was 5 minutes. The second period at a temperature of 65 ° C was 2.2 min. Mixing diffusion time during 9 minutes to crystallize the product. The entire mixing process was conditionally divided into three temperature-time periods: 1 a period of intense agitation; 2 during product cooling to a crystallization temperature; 3 the product during crystallization. The investigations of the process at different speeds working body were to choose the best, to get good distribution of all components in the minimum time. The result was that the spread manufactured according to the proposed formulation meets the optimal mixing time stirrer speed is 150 rev / min (during intensive stirring), 10 rev / min (during cooling of the product to a crystallization temperature) and 15 rev / min during crystallization. The optimal mixing time using the dependence of the dimensionless concentration of a key component of the mixing time. The result was the optimum time for process spread 4.7 min at 65 ° C. Conducted research to determine the optimal mixing time in the crystallization of the product, it was 14 minutes. The increase in the mixing time required for uniform distribution of components in the mixture in small quantities.https://www.vestnik-vsuet.ru/vguit/article/view/238mixingspreadfunctional productconcentration
collection DOAJ
language Russian
format Article
sources DOAJ
author A. N. Ostrikov
A. V. Gorbatova
spellingShingle A. N. Ostrikov
A. V. Gorbatova
INVESTIGATION OF THE KINETICS OF THE MIXING PROCESS AT VARIABLE SPREADS HEAT SUPPLY
Vestnik Voronežskogo Gosudarstvennogo Universiteta Inženernyh Tehnologij
mixing
spread
functional product
concentration
author_facet A. N. Ostrikov
A. V. Gorbatova
author_sort A. N. Ostrikov
title INVESTIGATION OF THE KINETICS OF THE MIXING PROCESS AT VARIABLE SPREADS HEAT SUPPLY
title_short INVESTIGATION OF THE KINETICS OF THE MIXING PROCESS AT VARIABLE SPREADS HEAT SUPPLY
title_full INVESTIGATION OF THE KINETICS OF THE MIXING PROCESS AT VARIABLE SPREADS HEAT SUPPLY
title_fullStr INVESTIGATION OF THE KINETICS OF THE MIXING PROCESS AT VARIABLE SPREADS HEAT SUPPLY
title_full_unstemmed INVESTIGATION OF THE KINETICS OF THE MIXING PROCESS AT VARIABLE SPREADS HEAT SUPPLY
title_sort investigation of the kinetics of the mixing process at variable spreads heat supply
publisher Voronezh state university of engineering technologies
series Vestnik Voronežskogo Gosudarstvennogo Universiteta Inženernyh Tehnologij
issn 2226-910X
2310-1202
publishDate 2015-04-01
description The investigation of the kinetics of mixing creamy vegetable spreads with a variable heat supply. The time of each of the periods of re-mixing. Stirring at a temperature of 65 °C optimum convective mixing period was 2.5 minutes. Convective mixing duration after the beginning of crystallization of the product (i.e., by stirring at a temperature of 30 ... 15 ° C) was 5 minutes. The second period at a temperature of 65 ° C was 2.2 min. Mixing diffusion time during 9 minutes to crystallize the product. The entire mixing process was conditionally divided into three temperature-time periods: 1 a period of intense agitation; 2 during product cooling to a crystallization temperature; 3 the product during crystallization. The investigations of the process at different speeds working body were to choose the best, to get good distribution of all components in the minimum time. The result was that the spread manufactured according to the proposed formulation meets the optimal mixing time stirrer speed is 150 rev / min (during intensive stirring), 10 rev / min (during cooling of the product to a crystallization temperature) and 15 rev / min during crystallization. The optimal mixing time using the dependence of the dimensionless concentration of a key component of the mixing time. The result was the optimum time for process spread 4.7 min at 65 ° C. Conducted research to determine the optimal mixing time in the crystallization of the product, it was 14 minutes. The increase in the mixing time required for uniform distribution of components in the mixture in small quantities.
topic mixing
spread
functional product
concentration
url https://www.vestnik-vsuet.ru/vguit/article/view/238
work_keys_str_mv AT anostrikov investigationofthekineticsofthemixingprocessatvariablespreadsheatsupply
AT avgorbatova investigationofthekineticsofthemixingprocessatvariablespreadsheatsupply
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