Abstract

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 Rto. 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 Rto-min and Rto-max. We established that the value of Rto depends significantly on the section’s geometry. The larger the section sizes, the greater the changes of Rto. The minimal and maximal values of Rto for all packages were 0.0051 (m2·K)/W and 0.0238 (m2·K)/W, respectively. The correctness of model calculations was verified with the use of experimental data.

Highlights

  • In the practice of the industrial heat treatment of steel products, in many situations, there is a need to heat a porous charge [1]

  • The quantitative analysis relates to determining the value of individual resistances, whereas the quantitative analysis consists of determining the share of the individual mechanisms in the heat transfer that occurs while heating the package

  • The value of Rto mostly depends on the heat transfer conditions that exist between adjacent layers of the package

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Summary

Introduction

In the practice of the industrial heat treatment of steel products, in many situations, there is a need to heat a porous charge [1]. Due to heat treatment operations having a significant influence on energy consumption, production efficiency, pollutant emission, as well as the quality of the end product, they must be carefully controlled with the use of automatic control systems. This is connected with the selection of an optimal heating curve for each given case. Two-phase structure (steel-gas) of the discussed packages, there is a complex heat flow in their area. A model used to control the heated packages of sections must comprise a procedure of calculating the value of resistance

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