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Computational study of heat transfer from the inner surface of a circular tube to force high temperature liquid metal flow in laminar and transition regions

机译:从圆管内表面传热以强迫高温液态金属在层流和过渡区流动的计算研究

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摘要

Heat transfer through forced convection from the inner surface of a circular tube to force the flow of liquid sodium in the laminar and transition regions were numerically analysed for two types of tube geometries (concentric annular and circular tubes) and two types of equivalent diameters (hydraulic and thermal equivalent diameters). The unsteady laminar three-dimensional basic equations for forced convection heat transfer caused by a step heat flux were numerically solved until a steady state is attained. The code of the parabolic hyperbolic or elliptic numerical integration code series (PHOENICS) was used for calculations by considering relevant temperature dependent thermo-physical properties. The concentric annular tube has a test tube with inner and outer diameters of 7.6 and 14.3 mm, respectively, has a heated length of 52 mm, and an L/d of 6.84. The two circular tubes have inner diameters of 6.7 and 19.3 mm with L/d of 7.76 and 2.69, respectively, and a heated length of 52 mm. The inlet liquid temperature, inlet liquid velocity, and surface heat flux were equally set for each test tube as T ~( in )≅573 to 585 K, u ~( in ) = 0.0852 to 1 m/s, and q  = 2×10_(5)to 2.5×10_(6)W/m_(2), respectively. The increase in temperature from the leading edge of the heated section to the outlet of the circular tubes (with a hydraulic diameter of d ~( H ) = 6.7 mm and a thermal equivalent diameter d ~( te ) = 19.3 mm) was approximately 2.70 and 1.21 times as large as the corresponding values of the concentric annular tube with an inner diameter of 7.6 mm and an outer diameter of 14.3 mm, respectively. A quantity in the laminar and transition regions was suggested as the dominant variable involved in the forced convection heat transfer in the circular tube. The values of the local and average Nusselt numbers, Nu ~( z )and Nu ~( av ), respectively, for a concentric annular tube with d ~( H ) = 6.7 mm and for a circular tube with d ~( H ) = 6.7 mm were calculated to examine the effects of q , T ~( in ), and Pe on heat transfer. The general correlation in the laminar and turbulent regions for a high temperature liquid metal was identified for the circular tube with a hydraulic diameter.
机译:对于两种类型的管几何形状(同心环形和圆形管)和两种类型的等效直径(液压),通过圆管内表面的强制对流以迫使液体钠在层流和过渡区中流动的传热进行了数值分析。和热等效直径)。数值求解了由阶跃热通量引起的强迫对流换热的非定常层流三维基本方程,直到达到稳态为止。通过考虑相关的温度相关的热物理性质,将抛物线双曲线或椭圆形数值积分代码系列(PHOENICS)的代码用于计算。同心环形管的试管内径和外径分别为7.6和14.3 mm,加热长度为52 mm,L / d为6.84。这两个圆形管的内径分别为6.7和19.3 mm,L / d为7.76和2.69,加热长度为52 mm。将每个试管的入口液体温度,入口液体速度和表面热通量均等设置为T〜(in)≅573至585K,u〜(in)= 0.0852至1m / s,q = 2×分别为10_(5)至2.5×10_(6)W / m_(2)。从加热部分的前端到圆管出口的温度升高(水力直径d〜(H)= 6.7 mm,热当量直径d〜(te)= 9.319.3 mm)约为2.70分别是内径为7.6mm和外径为14.3mm的同心圆管的相应值的1.21倍。层流和过渡区域的数量被认为是圆形管中强制对流传热的主要变量。对于d〜(H)= 6.7 mm的同心环形管和d〜(H)=的圆管,局部和平均Nusselt数的值分别为Nu〜(z)和Nu〜(av)计算了6.7毫米,以检查q,T〜(in)和Pe对传热的影响。对于具有水力直径的圆形管,确定了高温液态金属在层流和湍流区域中的一般相关性。

著录项

  • 来源
    《Heat and mass transfer》 |2018年第9期|2853-2869|共17页
  • 作者

    K. Hata; K. Fukuda; S. Masuzaki;

  • 作者单位

    Graduate School of Maritime Sciences, Kobe University;

    Graduate School of Maritime Sciences, Kobe University;

    National Institute for Fusion Science;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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