期刊文献+

常压加热炉辐射段耦合传热的数值模拟 被引量:3

Numerical Simulation of Coupled Heat Transfer in the Firebox of Atmospheric Heater
下载PDF
导出
摘要 采用分区耦合的方法研究了某常压加热炉辐射段内的流动、燃烧和传热的全部工艺过程,并系统地分析了炉管表面温度和热强度分布。计算中,实现了燃烧器、炉膛、炉管整体几何结构的建模和网格划分,选用标准k-ε湍流模型、非预混燃烧模型和离散坐标辐射传热模型,将炉管黑度定为0.8,模拟得到了炉内的流场、温度场及炉管表面温度和热强度分布的详细信息。结果表明,底部燃烧器的高速射流在炉膛下部产生较大回流区,对炉膛下部烟气温度分布的均匀性至关重要;炉管管壁温度和热强度分布存在明显非均匀性,影响炉管使用寿命。炉膛温度及炉管管壁热强度模拟结果与常压炉测定数据和设计数据一致,证明了模拟计算的可行性和准确性,为常压炉的设计和优化提供理论参考。 The processes of fluid flow, combustion, heat transfer between the flue gas and tube without any simplification in the firebox of atmospheric heater were studied with the whole coupling method. The distribution of temperature and heat intensity in furnace tube was analyzed systematically. The geometrical model and the division of grid of the combustor, combustion chamber and furnace tube were generated. The standard κ-ε turbulent model, the non premixed combustion model and the discrete ordinate transfer radiation model were used to simulate the fluid flow, combustion, heat transfer in the furnace. The emissivity of the furnace tube was defined as 0.8 in the model. Detailed information about the flow field, temperature field, temperature and heat flux distribution in tube skin was obtained. Results showed that the high velocity of bottom combustors' jet flow resulted in large flue gas recirculation zone, which played an important role in the uniform temperature of flue gas in the bottom of the furnace. In addition, non-uniform distribution of temperature and heat flux existed in the furnace tube skin, which affected the service life of furnace tube. Compared with the measured and design date of the firebox temperature and the heat flux of tube skin, the simulation result was proved to be feasible and accurate. The successful simulation offered technical support to the design and improvement of atmospheric still.
出处 《石油学报(石油加工)》 EI CAS CSCD 北大核心 2011年第4期649-656,共8页 Acta Petrolei Sinica(Petroleum Processing Section)
关键词 加热炉 湍流燃烧 辐射传热 分区耦合 数值模拟 炉管表面热强度 furnace turbulent combustion radiation heat transfer whole-coupling numericalsimulation tube skin heat intensity
  • 相关文献

参考文献9

二级参考文献21

  • 1张红梅,王宗祥.轻质油裂解炉反应管的二维数学模型[J].石油学报(石油加工),1995,11(4):68-77. 被引量:22
  • 2Froment G F. Thermal Cracking for Olefins Production Fundamentals and Their Application to Industrial Problems. Chem Eng Sci,1981,36(6) :1 271 ~1 282.
  • 3Ramana M V, Patrick M P,Froment G F. The Coupled Simulation of Heat Transfer and Reaction in a Pyrolysis Furnace. Chem Eng Sci,1988,43(6) :1 223 ~ 1 229.
  • 4Saario A,Rebola A,Coelho P J,et al.Heavy fuel oil combustion in cylindrical laboratory furnace measurements and modeling[J].Fuel,2005,84(4):359-369.
  • 5Rafael V,Rogelio E.A highly radiative combustion chamber for heavy fuel oil combustion[J].International Journal of Heat and Mass Transfer,1998,41(20):3087-3097.
  • 6Colson G,Peeters F,Ruyck J De.Experiment in-flame study of a 15MW dual fuel gas/oil burner[J].Fuel,1999,78(20):1253-1261.
  • 7范维澄,万跃鹏.流动与燃烧的模型与计算[M].合肥:中国科学技术大学出版社,1991.
  • 8Fiveland W A.Discrete ordinate solutions of radiative heat transport equation for rectangular enclosures[J].J Heat Transfer,1984,106(2):699-706.
  • 9Turelove J S.Discreate ordinate solutions of the radiative heat transport equation[J].J Heat Transfer,1987,109(4):1048-1051.
  • 10Heynderickx G J,Oprins A J M,Marin G B,et al.Three-dimensional flow patterns in cracking furnaces with longflame burners[J].AIChE Journal,2001,47(2):388-399.

共引文献43

同被引文献23

  • 1M S Abdulazeem, A M Alhasan, S Abdulrahmann. Initiation of solid explosives by laser[ J]. International Journal of Thermal Sci- ence, 2011:2117 -2121.
  • 2S Ostrach. NaturM Convection in Enclosuers[J]. Heat Transfer, 1988:1175 -1190.
  • 3C J Hoogendoorn. Nur Convection in Enclosuers[J]. Heat Transit. 1986:111 -120.
  • 4B A Mayer, J W Mitchell, M M E1 - Wakil. The effect of thermal wall properties in natural convection in inclined rectangular ceils [J]. Heat transfer, 1982,104(1) :111 -117.
  • 5D M Kim, R Viskanta. Study of the effects of wall conductance on natural convection in a differentially oriented square cavity [ J], Fluid Mech, 1984,144:153 - 176.
  • 6Y H Huang, S K Aggarwal. Effect of wall conduction on natural convection in an enclosure with a central heat source[ J]. Electron packag, 1995,117:301 - 306.
  • 7D W Larson, R Viskanta. Transient combined laminar free con- vection and radiation in a rectangular enclosure[ J]. Fluid Mech, 1976,78 ( 1 ) :65 - 85.
  • 8S M E1 - Sherbiny, K G T Hollands, G D Raithby. The effect of thermal boundary conditions on natural convection in vertical and inclined air layers [ J ]. Heat Transfer, 1982, 104 ( 2 ) : 515 - 520.
  • 9D M Kim, 13. Viskanta. Effect of wall conduction and radiation on natural convection in a rectangular cavity[ J]. Numer Heat Trans- fer, 1984,7(4) :449 -470.
  • 10AHabib, B Merci, G J Heynderickx. Impact of radiation model in CFD simulation of steam cracking furnaces[ J]. Computer and Chemical Engineering, 2007,31 : 1389 - 1406.

引证文献3

二级引证文献4

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部