Numerical simulation of an industrial radiant tube burner using OpenFOAM

This study presents a numerical investigation into the effects of physical models on the prediction accuracy of the wall temperature distribution in an industrial radiant tube burner. Utilizing a reacting flow solver based on OpenFOAM, we explored the effects of various physical models, including th...

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Main Authors: Namsu Kim, Young Tae Guahk, Chang-bog Ko
Format: Article
Language:English
Published: Elsevier 2024-06-01
Series:Fuel Communications
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S2666052024000141
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author Namsu Kim
Young Tae Guahk
Chang-bog Ko
author_facet Namsu Kim
Young Tae Guahk
Chang-bog Ko
author_sort Namsu Kim
collection DOAJ
description This study presents a numerical investigation into the effects of physical models on the prediction accuracy of the wall temperature distribution in an industrial radiant tube burner. Utilizing a reacting flow solver based on OpenFOAM, we explored the effects of various physical models, including those for chemistry, combustion, heat transfer, and radiation properties. The choice of combustion model significantly influences prediction accuracy, playing a more dominant role than the chemistry mechanism. Moreover, the simulations captured a distinctive triple flame structure inside the burner, representing the coexistence of rich premixed, non-premixed, and lean premixed flame structures. Conditional scatter plots displayed the development of both premixed and non-premixed flame structures, converging on the fuel-lean side. Notably, accurate prediction of wall temperature distribution depends on the incorporation of a precise heat transfer model, coupled with a detailed radiation property model. Regarding the distribution of tube surface temperature in the main radiation zone (a distance from the burner nozzle greater than 1 m), the most accurate prediction exhibits a maximum deviation of less than 56 K and an average deviation of 24 K compared to experimental results. The simulation closely matched experimental data for exhaust concentration of NO within an error margin of 20 ppm. However, discrepancy was observed in the CO concentration, which was attributed to the simplified representations of fuel chemistry and composition, as well as the difficulties in accurately capturing the unsteady flame dynamics near the wall.
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spelling doaj.art-9b82505fba174194b488cac351bbc28c2024-04-20T04:17:49ZengElsevierFuel Communications2666-05202024-06-0119100119Numerical simulation of an industrial radiant tube burner using OpenFOAMNamsu Kim0Young Tae Guahk1Chang-bog Ko2Energy Convergence System Research Department, Korea Institute of Energy Research, Daejeon 34129, South KoreaCorresponding author.; Energy Convergence System Research Department, Korea Institute of Energy Research, Daejeon 34129, South KoreaEnergy Convergence System Research Department, Korea Institute of Energy Research, Daejeon 34129, South KoreaThis study presents a numerical investigation into the effects of physical models on the prediction accuracy of the wall temperature distribution in an industrial radiant tube burner. Utilizing a reacting flow solver based on OpenFOAM, we explored the effects of various physical models, including those for chemistry, combustion, heat transfer, and radiation properties. The choice of combustion model significantly influences prediction accuracy, playing a more dominant role than the chemistry mechanism. Moreover, the simulations captured a distinctive triple flame structure inside the burner, representing the coexistence of rich premixed, non-premixed, and lean premixed flame structures. Conditional scatter plots displayed the development of both premixed and non-premixed flame structures, converging on the fuel-lean side. Notably, accurate prediction of wall temperature distribution depends on the incorporation of a precise heat transfer model, coupled with a detailed radiation property model. Regarding the distribution of tube surface temperature in the main radiation zone (a distance from the burner nozzle greater than 1 m), the most accurate prediction exhibits a maximum deviation of less than 56 K and an average deviation of 24 K compared to experimental results. The simulation closely matched experimental data for exhaust concentration of NO within an error margin of 20 ppm. However, discrepancy was observed in the CO concentration, which was attributed to the simplified representations of fuel chemistry and composition, as well as the difficulties in accurately capturing the unsteady flame dynamics near the wall.http://www.sciencedirect.com/science/article/pii/S2666052024000141Radiant tube burnerOpenFOAMIndustrial burnerComputational fluid dynamicsTriple flame
spellingShingle Namsu Kim
Young Tae Guahk
Chang-bog Ko
Numerical simulation of an industrial radiant tube burner using OpenFOAM
Fuel Communications
Radiant tube burner
OpenFOAM
Industrial burner
Computational fluid dynamics
Triple flame
title Numerical simulation of an industrial radiant tube burner using OpenFOAM
title_full Numerical simulation of an industrial radiant tube burner using OpenFOAM
title_fullStr Numerical simulation of an industrial radiant tube burner using OpenFOAM
title_full_unstemmed Numerical simulation of an industrial radiant tube burner using OpenFOAM
title_short Numerical simulation of an industrial radiant tube burner using OpenFOAM
title_sort numerical simulation of an industrial radiant tube burner using openfoam
topic Radiant tube burner
OpenFOAM
Industrial burner
Computational fluid dynamics
Triple flame
url http://www.sciencedirect.com/science/article/pii/S2666052024000141
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