Model of Complex Heat Transfer in the Package of Rectangular Steel Sections

During heat treatment of rectangular steel sections, a heated charge in the form of regularly arranged packages is placed in a furnace. The article presents a model of a complex heat transfer in such a package using the thermo-electric analogy. The model considers the following types of heat transfe...

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Main Authors: Rafał Wyczółkowski, Marek Gała, Vazgen Bagdasaryan
Format: Article
Language:English
Published: MDPI AG 2020-12-01
Series:Applied Sciences
Subjects:
Online Access:https://www.mdpi.com/2076-3417/10/24/9044
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author Rafał Wyczółkowski
Marek Gała
Vazgen Bagdasaryan
author_facet Rafał Wyczółkowski
Marek Gała
Vazgen Bagdasaryan
author_sort Rafał Wyczółkowski
collection DOAJ
description During heat treatment of rectangular steel sections, a heated charge in the form of regularly arranged packages is placed in a furnace. The article presents a model of a complex heat transfer in such a package using the thermo-electric analogy. The model considers the following types of heat transfer: conduction in section walls, conduction and natural convection within gas, heat radiation between the walls of a section, as well as contact conduction between the adjacent sections. The results of our own experimental research were used for calculations of heat resistance applying to natural convection and contact conduction. We assumed that the material of sections was low-carbon steel and the gas was air. The result of the calculations of the presented model is total thermal resistance <i>R<sub>to</sub></i>. The calculations were performed for the temperature range 20–700 °C for four geometrical cases. Due to the variability of conditions for contact heat conduction, we assumed that total thermal resistance for a given charge is contained within a value range between <i>R</i><sub><i>to</i>-min</sub> and <i>R</i><sub><i>to</i>-max</sub>. We established that the value of <i>R<sub>to</sub></i> depends significantly on the section’s geometry. The larger the section sizes, the greater the changes of <i>R<sub>to</sub></i>. The minimal and maximal values of <i>R<sub>to</sub></i> for all packages were 0.0051 (m<sup>2</sup>·K)/W and 0.0238 (m<sup>2</sup>·K)/W, respectively. The correctness of model calculations was verified with the use of experimental data.
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spelling doaj.art-3cfd875b46aa4dc0894517558b6a13622023-11-21T01:20:27ZengMDPI AGApplied Sciences2076-34172020-12-011024904410.3390/app10249044Model of Complex Heat Transfer in the Package of Rectangular Steel SectionsRafał Wyczółkowski0Marek Gała1Vazgen Bagdasaryan2Department of Production Management, Czestochowa University of Technology, Armii Krajowej 19, 42-200 Częstochowa, PolandFaculty of Electrical Engineering, Czestochowa University of Technology, Armii Krajowej 17, 42-200 Częstochowa, PolandInstitute of Civil Engineering, Warsaw University of Life Sciences-SGGW, Nowoursynowska 166, 02-787 Warsaw, PolandDuring heat treatment of rectangular steel sections, a heated charge in the form of regularly arranged packages is placed in a furnace. The article presents a model of a complex heat transfer in such a package using the thermo-electric analogy. The model considers the following types of heat transfer: conduction in section walls, conduction and natural convection within gas, heat radiation between the walls of a section, as well as contact conduction between the adjacent sections. The results of our own experimental research were used for calculations of heat resistance applying to natural convection and contact conduction. We assumed that the material of sections was low-carbon steel and the gas was air. The result of the calculations of the presented model is total thermal resistance <i>R<sub>to</sub></i>. The calculations were performed for the temperature range 20–700 °C for four geometrical cases. Due to the variability of conditions for contact heat conduction, we assumed that total thermal resistance for a given charge is contained within a value range between <i>R</i><sub><i>to</i>-min</sub> and <i>R</i><sub><i>to</i>-max</sub>. We established that the value of <i>R<sub>to</sub></i> depends significantly on the section’s geometry. The larger the section sizes, the greater the changes of <i>R<sub>to</sub></i>. The minimal and maximal values of <i>R<sub>to</sub></i> for all packages were 0.0051 (m<sup>2</sup>·K)/W and 0.0238 (m<sup>2</sup>·K)/W, respectively. The correctness of model calculations was verified with the use of experimental data.https://www.mdpi.com/2076-3417/10/24/9044steel sectionheat treatmentcomplex heat transferthermo-electric analogythermal resistance
spellingShingle Rafał Wyczółkowski
Marek Gała
Vazgen Bagdasaryan
Model of Complex Heat Transfer in the Package of Rectangular Steel Sections
Applied Sciences
steel section
heat treatment
complex heat transfer
thermo-electric analogy
thermal resistance
title Model of Complex Heat Transfer in the Package of Rectangular Steel Sections
title_full Model of Complex Heat Transfer in the Package of Rectangular Steel Sections
title_fullStr Model of Complex Heat Transfer in the Package of Rectangular Steel Sections
title_full_unstemmed Model of Complex Heat Transfer in the Package of Rectangular Steel Sections
title_short Model of Complex Heat Transfer in the Package of Rectangular Steel Sections
title_sort model of complex heat transfer in the package of rectangular steel sections
topic steel section
heat treatment
complex heat transfer
thermo-electric analogy
thermal resistance
url https://www.mdpi.com/2076-3417/10/24/9044
work_keys_str_mv AT rafałwyczołkowski modelofcomplexheattransferinthepackageofrectangularsteelsections
AT marekgała modelofcomplexheattransferinthepackageofrectangularsteelsections
AT vazgenbagdasaryan modelofcomplexheattransferinthepackageofrectangularsteelsections