期刊文献+

基于CFD双a型燃气辐射管燃烧的传热特性 被引量:5

Heat transfer characteristic of double-a type gas fried radiant tube by CFD simulation
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摘要 运用亚音速烧嘴技术和烟气循环技术,设计了一种烟气高循环倍率的新型双a型辐射管,采用涡耗散燃烧模型和离散坐标辐射模型计算其燃烧传热过程。结果表明:42.6%的CH4在烧嘴内燃烧,57.4%的CH4在辐射管中心管内长度为800mm、直径为40mm的区域内燃烧;辐射管中心管内,循环烟气使火焰和气体等温线呈“椭圆型”分布,三通管和支管内,流动惯性使气体等温线呈“偏心圆”分布;双a型辐射管热效率为70.8%,壁面最高温度1065℃,最大温差79℃,中心管壁周向温差0~21℃,三通管及支管管壁周向温差0~15℃,整个辐射管管壁径向温差0~2.5℃。 Combustion and heat transfer in double -a radiant tube (RT) were studied by Computa-tional Fluid Dynamics (CFD) in 3D condition.The Eddy-Dissipation combustion model and Discrete Ordinates radiation model were used in the simulation .The designed double -a RT is equipped with flue gas circulation tube and subsonic speed burner .The results show that the 42.6% of CH4 burned in the region diameter of 50mm in the burner, 57.4%of CH4 burned in the center tube with the length 800mm, diameter of 40mm.The flame shape and gas isotherm in the center tube is “elliptically dis-tributed” as a result of gas circulation.The gas isotherm in branch tube is “Eccentric circle distribu-ted” due to gas inertia.The efficiency of double a radiant tube is 70.8% with the maximum surface temperature of 1065℃and maximum temperature difference of 79℃.The circumferential temperature difference in center and branch tube surface is 0~21℃and 0~15℃respectively.The radial temper-ature difference in the tube surface is 0~2.5℃.
出处 《冶金能源》 2014年第1期14-19,共6页 Energy For Metallurgical Industry
基金 国家"十二五"科技支撑计划资助项目(No.2011BAE13B09) 中央高校基本科研业务费专项资金(FRF-SD-12-006B)资助
关键词 辐射管 烟气循环 温度分布 温差 radiant tube gas circulation temperature distribution temperature difference
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参考文献15

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同被引文献41

  • 1伍成波,许鹏彦,杨进,沈小军,李廷豪.U型辐射管的表面温度分布实验研究[J].过程工程学报,2008,8(S1):189-192. 被引量:9
  • 2欧俭平,马爱纯,占树华,蒋绍坚,萧泽强.U型蓄热式辐射管表面温度分布数值模拟研究[J].金属热处理,2005,30(1):74-77. 被引量:13
  • 3杨思安,姜泽毅,张欣欣,杨立新.P型蓄热式辐射管的表面温度分布[J].工业炉,2005,27(2):1-4. 被引量:6
  • 4吴筱,黄国强,梁红英.天然气燃烧中NO_x减排的数学模型[J].化工进展,2007,26(1):109-112. 被引量:9
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  • 6Tiwari M K, Mukhopadhyay A, Sanyal D. Parameter optimization through performance analysis of model based control of a batch heat treatment furnace with low NOx radiant tube burner. Energy Conv- ers Manage, 2005, 46(13/14) : 2114.
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  • 10Rafidi N, Blasiak W, Jewartowski M, et al. Increase of the ef- fective energy from the radiant tube equipped with regenerative system in comparison with conventional recuperative system. IFRF Combust J, 2005 ( 3 ) : 1.

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