QI, Xiaoni ;LIU, Yongqi ;XU, Hongqin ;LIU, Zeyan ;LIU, Ruixiang . Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor. Strojniški vestnik - Journal of Mechanical Engineering, [S.l.], v. 60, n.7-8, p. 495-505, april 2018. ISSN 0039-2480. Available at: <https://www.sv-jme.eu/sl/article/modeling-thermal-oxidation-of-coal-mine-methane-in-a-non-catalytic-reverse-flow-reactor/>. Date accessed: 19 nov. 2024. doi:http://dx.doi.org/10.5545/sv-jme.2013.1393.
Qi, X., Liu, Y., Xu, H., Liu, Z., & Liu, R. (2014). Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor. Strojniški vestnik - Journal of Mechanical Engineering, 60(7-8), 495-505. doi:http://dx.doi.org/10.5545/sv-jme.2013.1393
@article{sv-jmesv-jme.2013.1393,
author = {Xiaoni Qi and Yongqi Liu and Hongqin Xu and Zeyan Liu and Ruixiang Liu},
title = {Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor},
journal = {Strojniški vestnik - Journal of Mechanical Engineering},
volume = {60},
number = {7-8},
year = {2014},
keywords = {lean-methane; reverse flow reactor;thermal oxidation, modeling},
abstract = {Inspired by detailed designs of industrial porous burners, the combustion of methane–air mixtures in a non-catalytic reverse-flow reactor was studied numerically. The governing equations are the unsteady state equations of conservation of mass and chemical species, with separate energy equations for the solid and gas phases. These equations were solved using the commercial CFD code Fluent. In order to reveal the actual thermal oxidation in porous media, the user defined function (UDF) is used to extend the ability of FLUENT. The model has been used to investigate the effects of operating conditions such as the mixture inlet approach velocity (0.15 to 0.8 m/s) and methane concentration (0.3 to 0.7%) on the oxidation of methane within non-catalytic reactors packed with ceramic monolith blocks under adiabatic conditions. The calculated values of methane conversion showed good agreement with the corresponding available experimental data. Moreover temperature distribution characteristics in the oxidation bed were studied in order to maintain the autothermicity of TFRR with a high enough temperature in the hot zone.},
issn = {0039-2480}, pages = {495-505}, doi = {10.5545/sv-jme.2013.1393},
url = {https://www.sv-jme.eu/sl/article/modeling-thermal-oxidation-of-coal-mine-methane-in-a-non-catalytic-reverse-flow-reactor/}
}
Qi, X.,Liu, Y.,Xu, H.,Liu, Z.,Liu, R. 2014 April 60. Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor. Strojniški vestnik - Journal of Mechanical Engineering. [Online] 60:7-8
%A Qi, Xiaoni %A Liu, Yongqi %A Xu, Hongqin %A Liu, Zeyan %A Liu, Ruixiang %D 2014 %T Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor %B 2014 %9 lean-methane; reverse flow reactor;thermal oxidation, modeling %! Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor %K lean-methane; reverse flow reactor;thermal oxidation, modeling %X Inspired by detailed designs of industrial porous burners, the combustion of methane–air mixtures in a non-catalytic reverse-flow reactor was studied numerically. The governing equations are the unsteady state equations of conservation of mass and chemical species, with separate energy equations for the solid and gas phases. These equations were solved using the commercial CFD code Fluent. In order to reveal the actual thermal oxidation in porous media, the user defined function (UDF) is used to extend the ability of FLUENT. The model has been used to investigate the effects of operating conditions such as the mixture inlet approach velocity (0.15 to 0.8 m/s) and methane concentration (0.3 to 0.7%) on the oxidation of methane within non-catalytic reactors packed with ceramic monolith blocks under adiabatic conditions. The calculated values of methane conversion showed good agreement with the corresponding available experimental data. Moreover temperature distribution characteristics in the oxidation bed were studied in order to maintain the autothermicity of TFRR with a high enough temperature in the hot zone. %U https://www.sv-jme.eu/sl/article/modeling-thermal-oxidation-of-coal-mine-methane-in-a-non-catalytic-reverse-flow-reactor/ %0 Journal Article %R 10.5545/sv-jme.2013.1393 %& 495 %P 11 %J Strojniški vestnik - Journal of Mechanical Engineering %V 60 %N 7-8 %@ 0039-2480 %8 2018-04-05 %7 2018-04-05
Qi, Xiaoni, Yongqi Liu, Hongqin Xu, Zeyan Liu, & Ruixiang Liu. "Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor." Strojniški vestnik - Journal of Mechanical Engineering [Online], 60.7-8 (2014): 495-505. Web. 19 Nov. 2024
TY - JOUR AU - Qi, Xiaoni AU - Liu, Yongqi AU - Xu, Hongqin AU - Liu, Zeyan AU - Liu, Ruixiang PY - 2014 TI - Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor JF - Strojniški vestnik - Journal of Mechanical Engineering DO - 10.5545/sv-jme.2013.1393 KW - lean-methane; reverse flow reactor;thermal oxidation, modeling N2 - Inspired by detailed designs of industrial porous burners, the combustion of methane–air mixtures in a non-catalytic reverse-flow reactor was studied numerically. The governing equations are the unsteady state equations of conservation of mass and chemical species, with separate energy equations for the solid and gas phases. These equations were solved using the commercial CFD code Fluent. In order to reveal the actual thermal oxidation in porous media, the user defined function (UDF) is used to extend the ability of FLUENT. The model has been used to investigate the effects of operating conditions such as the mixture inlet approach velocity (0.15 to 0.8 m/s) and methane concentration (0.3 to 0.7%) on the oxidation of methane within non-catalytic reactors packed with ceramic monolith blocks under adiabatic conditions. The calculated values of methane conversion showed good agreement with the corresponding available experimental data. Moreover temperature distribution characteristics in the oxidation bed were studied in order to maintain the autothermicity of TFRR with a high enough temperature in the hot zone. UR - https://www.sv-jme.eu/sl/article/modeling-thermal-oxidation-of-coal-mine-methane-in-a-non-catalytic-reverse-flow-reactor/
@article{{sv-jme}{sv-jme.2013.1393},
author = {Qi, X., Liu, Y., Xu, H., Liu, Z., Liu, R.},
title = {Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor},
journal = {Strojniški vestnik - Journal of Mechanical Engineering},
volume = {60},
number = {7-8},
year = {2014},
doi = {10.5545/sv-jme.2013.1393},
url = {https://www.sv-jme.eu/sl/article/modeling-thermal-oxidation-of-coal-mine-methane-in-a-non-catalytic-reverse-flow-reactor/}
}
TY - JOUR AU - Qi, Xiaoni AU - Liu, Yongqi AU - Xu, Hongqin AU - Liu, Zeyan AU - Liu, Ruixiang PY - 2018/04/05 TI - Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor JF - Strojniški vestnik - Journal of Mechanical Engineering; Vol 60, No 7-8 (2014): Strojniški vestnik - Journal of Mechanical Engineering DO - 10.5545/sv-jme.2013.1393 KW - lean-methane, reverse flow reactor,thermal oxidation, modeling N2 - Inspired by detailed designs of industrial porous burners, the combustion of methane–air mixtures in a non-catalytic reverse-flow reactor was studied numerically. The governing equations are the unsteady state equations of conservation of mass and chemical species, with separate energy equations for the solid and gas phases. These equations were solved using the commercial CFD code Fluent. In order to reveal the actual thermal oxidation in porous media, the user defined function (UDF) is used to extend the ability of FLUENT. The model has been used to investigate the effects of operating conditions such as the mixture inlet approach velocity (0.15 to 0.8 m/s) and methane concentration (0.3 to 0.7%) on the oxidation of methane within non-catalytic reactors packed with ceramic monolith blocks under adiabatic conditions. The calculated values of methane conversion showed good agreement with the corresponding available experimental data. Moreover temperature distribution characteristics in the oxidation bed were studied in order to maintain the autothermicity of TFRR with a high enough temperature in the hot zone. UR - https://www.sv-jme.eu/sl/article/modeling-thermal-oxidation-of-coal-mine-methane-in-a-non-catalytic-reverse-flow-reactor/
Qi, Xiaoni, Liu, Yongqi, Xu, Hongqin, Liu, Zeyan, AND Liu, Ruixiang. "Modeling Thermal Oxidation of Coal Mine Methane in a Non-Catalytic Reverse-Flow Reactor" Strojniški vestnik - Journal of Mechanical Engineering [Online], Volume 60 Number 7-8 (05 April 2018)
Strojniški vestnik - Journal of Mechanical Engineering 60(2014)7-8, 495-505
© The Authors, CC-BY 4.0 Int. Change in copyright policy from 2022, Jan 1st.
Inspired by detailed designs of industrial porous burners, the combustion of methane–air mixtures in a non-catalytic reverse-flow reactor was studied numerically. The governing equations are the unsteady state equations of conservation of mass and chemical species, with separate energy equations for the solid and gas phases. These equations were solved using the commercial CFD code Fluent. In order to reveal the actual thermal oxidation in porous media, the user defined function (UDF) is used to extend the ability of FLUENT. The model has been used to investigate the effects of operating conditions such as the mixture inlet approach velocity (0.15 to 0.8 m/s) and methane concentration (0.3 to 0.7%) on the oxidation of methane within non-catalytic reactors packed with ceramic monolith blocks under adiabatic conditions. The calculated values of methane conversion showed good agreement with the corresponding available experimental data. Moreover temperature distribution characteristics in the oxidation bed were studied in order to maintain the autothermicity of TFRR with a high enough temperature in the hot zone.