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本文对超临界压力CO2在竖直加热圆管内的对流换热进行了实验研究,比较了不同流向、不同热流密度等对流动和换热的影响.实验结果表明,管内径为2 mm时,在低进口Re条件下,由于浮升力影响导致层流向湍流提前转变,对流换热增强;与向上流动相比,向下流动更易由层流转变为湍流;向下流动的换热要强于向上流动,表明浮升力对换热有很大影响.对于管内径为0.27 mm的微细圆管,当进口Re高于104时,浮升力的影响可以忽略,对流换热系数的变化完全由物性的变化尤其是cp的变化导致.

参考文献

[1] Petukhov B S.Heat Transfer and Friction in Turbulent pipe flow with Variable Physical Properties[M].New York:Academic Press,1970
[2] J D Jackson.Some Striking Features of Heat Transfer with Fluids at Pressures and Temperatures Near the Critical Point[A].武汉,2001
[3] S.M.Liao;T.S.Zhao .An experimental investigation of convection heat transfer to supercritical carbon dioxide in miniature tubes[J].International Journal of Heat and Mass Transfer,2002(25):5025-5034.
[4] Pei-Xue Jiang;Yi-Jun Xu;Jing Lv;Run-Fu Shi;S. He;J. D. Jackson .Experimental investigation of convection heat transfer of CO_2 at super-critical pressures in vertical mini-tubes and in porous media[J].Applied thermal engineering: Design, processes, equipment, economics,2004(8-9):1255-1270.
[5] 徐轶君,姜培学,张宇,任泽霈.竖直圆管中超临界压力CO2在低雷诺数下对流换热研究[J].工程热物理学报,2005(03):468-470.
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