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Heat Transfer Characteristics of Hydrocarbon Fuel in a Horizontal Small Tube under Different Pressures

机译:压力下水平小管中碳氢燃料的传热特性

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Experiments for heat transfer of a kerosene hydrocarbon fuel in a small horizontal tube have been conducted at subcritical and supercritical pressures. Parameters included the pressure of 2.0-5.0 MPa, mass flux of 822-2466 kg/ (m~2·s) and heat flux up to 1500 kW/m~2. The wall temperature and heat transfer performance at various operating conditions were captured in the experiments. Based on the results, the normal, improved and deteriorated heat transfer characteristics of the fuel were analyzed in detail. The effects of heat flux, pressure and mass flux on the heat transfer were discussed respectively. The heat transfer performed better when working pressure approached critical pressure. The deterioration in the large change of thermophysical properties region didn't occur at supercritical pressures. In the test, the increase of mass flux could enhance the heat transfer. But the effect of the enhancement decreased with mass flux increase. As to the pressure drop characteristics, low pressure and high mass flux both contributed to the increase of flow resistance.
机译:已经在亚临界和超临界压力下进行了小型水平管中煤油烃类燃料传热的实验。参数包括:2.0-5.0 MPa的压力,822-2466 kg /(m〜2·s)的质量通量和高达1500 kW / m〜2的热通量。实验中记录了在各种操作条件下的壁温和传热性能。基于结果,详细分析了燃料的正常,改进和恶化的传热特性。分别讨论了热通量,压力和质量通量对传热的影响。当工作压力接近临界压力时,传热效果更好。在超临界压力下没有发生热物理性质区域大变化的恶化。在测试中,质量通量的增加可以增强热传递。但是,随着质量通量的增加,增强效果降低。关于压降特性,低压和高质量通量都有助于流动阻力的增加。

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