Heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containers

Heat transfer during the freezing of guava pulp conditioned in large containers such as in stacked boxes (34 L) and buckets (20 L) and unstacked drums (200 L) is discussed. The air velocities across the cross-section of the tunnel were measured, and the values in the outlet of the evaporator were us...

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Main Authors: W. M. Okita, M. J. Reno, A. P. Peres, J. V. Resende
Format: Article
Language:English
Published: Brazilian Society of Chemical Engineering 2013-12-01
Series:Brazilian Journal of Chemical Engineering
Subjects:
CFD
Online Access:http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000400013&lng=en&tlng=en
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spelling doaj-0067c3a66d4d4928a68c9feb9e0fefd12020-11-25T01:11:38ZengBrazilian Society of Chemical EngineeringBrazilian Journal of Chemical Engineering0104-66322013-12-0130481182410.1590/S0104-66322013000400013S0104-66322013000400013Heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containersW. M. Okita0M. J. Reno1A. P. Peres2J. V. Resende3Universidade Federal de LavrasUniversidade Federal de LavrasUniversidade Federal de LavrasUniversidade Federal de LavrasHeat transfer during the freezing of guava pulp conditioned in large containers such as in stacked boxes (34 L) and buckets (20 L) and unstacked drums (200 L) is discussed. The air velocities across the cross-section of the tunnel were measured, and the values in the outlet of the evaporator were used as the initial conditions in computational fluid dynamics (CFD) simulations. The model tested was turbulent standard k-ε. The CFD-generated convective heat transfer coefficients were mapped on the surfaces for each configuration and used in procedures for the calculation of freezing-time estimates. These estimates were compared with the experimental results for validation. The results showed that CFD determined representative coefficients and produced good correlations between the predicted and experimental values when applied to the freezing-time estimates for the box and drum configurations. The errors depended on the configuration and the adopted mesh (3-D grid) construction.http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000400013&lng=en&tlng=enCFDAirflowHeat transferFruit pulpFreezing time
collection DOAJ
language English
format Article
sources DOAJ
author W. M. Okita
M. J. Reno
A. P. Peres
J. V. Resende
spellingShingle W. M. Okita
M. J. Reno
A. P. Peres
J. V. Resende
Heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containers
Brazilian Journal of Chemical Engineering
CFD
Airflow
Heat transfer
Fruit pulp
Freezing time
author_facet W. M. Okita
M. J. Reno
A. P. Peres
J. V. Resende
author_sort W. M. Okita
title Heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containers
title_short Heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containers
title_full Heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containers
title_fullStr Heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containers
title_full_unstemmed Heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containers
title_sort heat transfer analyses using computational fluid dynamics in the air blast freezing of guava pulp in large containers
publisher Brazilian Society of Chemical Engineering
series Brazilian Journal of Chemical Engineering
issn 0104-6632
publishDate 2013-12-01
description Heat transfer during the freezing of guava pulp conditioned in large containers such as in stacked boxes (34 L) and buckets (20 L) and unstacked drums (200 L) is discussed. The air velocities across the cross-section of the tunnel were measured, and the values in the outlet of the evaporator were used as the initial conditions in computational fluid dynamics (CFD) simulations. The model tested was turbulent standard k-ε. The CFD-generated convective heat transfer coefficients were mapped on the surfaces for each configuration and used in procedures for the calculation of freezing-time estimates. These estimates were compared with the experimental results for validation. The results showed that CFD determined representative coefficients and produced good correlations between the predicted and experimental values when applied to the freezing-time estimates for the box and drum configurations. The errors depended on the configuration and the adopted mesh (3-D grid) construction.
topic CFD
Airflow
Heat transfer
Fruit pulp
Freezing time
url http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000400013&lng=en&tlng=en
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