李舟航, 唐国力, 吴玉新, 吕俊复, 李瑞欣. 基于无量纲结构因子的低质量流速内螺纹管中超临界水流动和传热性能分析[J]. 中国电机工程学报, 2018, 38(10): 3007-3014,3151. DOI: 10.13334/j.0258-8013.pcsee.171887
引用本文: 李舟航, 唐国力, 吴玉新, 吕俊复, 李瑞欣. 基于无量纲结构因子的低质量流速内螺纹管中超临界水流动和传热性能分析[J]. 中国电机工程学报, 2018, 38(10): 3007-3014,3151. DOI: 10.13334/j.0258-8013.pcsee.171887
LI Zhouhang, TANG Guoli, WU Yuxin, LYU Junfu, LI Ruixin. Identification of Non-dimensional Tube Geometry Parameter for Heat Transfer of Supercritical Water in Internally Ribbed Tubes[J]. Proceedings of the CSEE, 2018, 38(10): 3007-3014,3151. DOI: 10.13334/j.0258-8013.pcsee.171887
Citation: LI Zhouhang, TANG Guoli, WU Yuxin, LYU Junfu, LI Ruixin. Identification of Non-dimensional Tube Geometry Parameter for Heat Transfer of Supercritical Water in Internally Ribbed Tubes[J]. Proceedings of the CSEE, 2018, 38(10): 3007-3014,3151. DOI: 10.13334/j.0258-8013.pcsee.171887

基于无量纲结构因子的低质量流速内螺纹管中超临界水流动和传热性能分析

Identification of Non-dimensional Tube Geometry Parameter for Heat Transfer of Supercritical Water in Internally Ribbed Tubes

  • 摘要: 无量纲结构因子的合理选取对超临界及超超临界循环流化床锅炉中低质量流速内螺纹管的性能比较及通用换热关联式的发展具有重要意义。文中使用经过实验验证的数值模型,对具有不同几何结构的内螺纹管流动和传热特性进行了分析。结果表明,在无量纲结构因子βW=1.92~3.80、质量流速200~800kg/(m2·s)、热流/质量流速比0.35~1.5k J/kg的范围内,βW能准确描述内螺纹管中超临界水的对流换热特性。βW相同时,内肋螺旋效应的有效作用区域(边界层对数区初段y+=30~100)中流场旋流强度基本一致,内螺纹管的传热性能也基本相同。肋结构对垂直上升流动超临界水换热的影响在Bo=10-5~10-4、βW<2.58范围内最为明显,在此范围之外,其影响大小明显弱于强物性变化作用和浮升力作用。最后,指出发展精度更高的强制对流换热关联式是提出准确的内螺纹管超临界水对流换热关联式的基础。

     

    Abstract: Internally ribbed tubes(IRT) are widely used in water walls of ultra-supercritical circulating fluidized bed(CFB) boilers and normally operated under low mass fluxes. Currently a great variety of tube geometries exist in related studies and practical operations of IRT. It’s essential to develop a proper non-dimensional tube geometry parameter, to facilitate the performance comparison and development of general Nusselt correlation for different IRT. This work numerically investigated flow and heat transfer of supercritical water in IRT with various geometries. Results show that different IRT with the same β W have nearly identical heat transfer performance, as a result of very similar distribution of swirl flow in the boundary region of y+ = 30~100. The geometry effect is overwhelmed in most of the range studied, expect in the region of Bo = 10-5~10-4 and β W < 2.58, where an increase in β W leads to an obvious heat transfer enhancement. Finally, it is pointed out that more future work should target to the development of more accurate Nusselt correlation for purely forced convection flow.

     

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