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首页> 外文期刊>Experimental Thermal and Fluid Science: International Journal of Experimental Heat Transfer, Thermodynamics, and Fluid Mechanics >Experimental investigation on heat transfer characteristics of supercritical pressure water in a horizontal tube
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Experimental investigation on heat transfer characteristics of supercritical pressure water in a horizontal tube

机译:水平管中超临界水传热特性的实验研究

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In this study, heat transfer of water at supercritical pressures in a horizontal tube was investigated experimentally. The inner diameter of the tube was 26mm with a heated length of 2m. Experimental parameters included a mass flux ranging from 300 to 700kg/m~2s, a heat flux from 200 to 400kW/m~2, a pressure from 23 to 25MPa, and a bulk fluid enthalpy from 1000 to 3000kJ/kg. The results indicated that heat transfer characteristics of supercritical water are not uniformly along the circumference of the horizontal tube. Decreasing in the heat flux could decrease the non-uniformity and eliminate deterioration on the top surface of the horizontal tube. With the pressure increasing, the amount of deterioration on the top surface is increased and enhancement on the bottom surface is decreased. By comparing with results of previous investigators, the effect of flow direction and diameter on heat transfer of water were analyzed in details. The criterions of Petukhov and Jackson were selected to judge buoyancy effects in a horizontal tube. It was found that the Petukhov criterion can accurately predict the onset of buoyancy effects. Furthermore, new heat transfer correlations have been proposed, which could be used to predict heat transfer coefficients of supercritical water flowing in horizontal tubes.
机译:在这项研究中,对水平管中超临界压力下水的传热进行了实验研究。管的内径为26mm,加热长度为2m。实验参数包括:质量通量为300至700kg / m〜2s,热通量为200至400kW / m〜2,压力为23至25MPa,散装流体焓为1000至3000kJ / kg。结果表明,超临界水的传热特性沿水平管的圆周分布不均匀。热通量的减少可减少不均匀性并消除水平管顶面上的劣化。随着压力增加,顶表面上的劣化量增加并且底表面上的增强降低。通过与先前研究者的结果进行比较,详细分析了流动方向和直径对水的热传递的影响。选择Petukhov和Jackson的标准来判断水平管中的浮力效果。已经发现,Petukhov标准可以准确地预测浮力作用的开始。此外,已经提出了新的传热相关性,其可用于预测在水平管中流动的超临界水的传热系数。

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