2010
DOI: 10.4028/www.scientific.net/amr.160-162.536
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Heat Transfer Model of Roller Quench in Strip Continuous Heat Treatment Process

Abstract: Roller quench is a rapid cooling technique used in strip continuous heat-treatment process, which is one of the most important processes in producing cold-rolled strip steel. Heat transports by contact heat transfer in roller quench, for the complex characteristics of contact heat transfer, roller quench is very difficulty to simulate. In this paper a roller quench heat transfer model is build based on Fourier-Kirchhoff differential equations. A new correlation function of contact conductance is developed from… Show more

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Cited by 3 publications
(2 citation statements)
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“…During the calculation of view factors, the number of emitted rays from each surface is 10 6 , and the calculated angular coefficient has an accuracy of 0.1% with 95% confidence. [26] After ob-taining the view factors, the radiative thermal resistance network method is used to establish the equation for the radiosity J j , as given in Equation (8).…”
Section: Boundary Conditions Thermal Conductivity and Source Termsmentioning
confidence: 99%
See 1 more Smart Citation
“…During the calculation of view factors, the number of emitted rays from each surface is 10 6 , and the calculated angular coefficient has an accuracy of 0.1% with 95% confidence. [26] After ob-taining the view factors, the radiative thermal resistance network method is used to establish the equation for the radiosity J j , as given in Equation (8).…”
Section: Boundary Conditions Thermal Conductivity and Source Termsmentioning
confidence: 99%
“…During the calculation of view factors, the number of emitted rays from each surface is 10 6 , and the calculated angular coefficient has an accuracy of 0.1% with 95% confidence. [ 26 ] After obtaining the view factors, the radiative thermal resistance network method is used to establish the equation for the radiosity J j , as given in Equation (8). i=1Nδkifalse(1goodbreak−ςkεkfalse)false(1goodbreak−Agfalse)fkiJi=ςkεkσTk4+false(1goodbreak−ςkεkfalse)εgσTg4+false(1goodbreak−ςkfalse)QkFk,$$\begin{eqnarray} && \sum_{i = 1}^N \left[{\delta_{ki} - (1 - {\varsigma }_k{\varepsilon }_k)(1 - {A}_g){f}_{k - i}} \right]{J}_i \nonumber\\ &&\quad = {\varsigma }_k{\varepsilon }_k\sigma T_k^4 + (1 - {\varsigma }_k{\varepsilon }_k){\varepsilon }_g\sigma T_g^4 + (1 - {\varsigma }_k)\frac{{{Q}_k}}{{{F}_k}}, \end{eqnarray}$$where σ is the Stefan–Boltzmann constant; ε k , T k , Q k , and F k are the emissivity, temperature (K), net radiative heat flux (W), and surface area (m 2 ) of surface k , respectively; J i represents the radiosity of surface i (W·m −2 ); δ ki and ζ k are binary functions, as shown in Equations (9) and (10).…”
Section: Mathematical Modelmentioning
confidence: 99%