二次曲线拟合法波纹管管内传热系数研究

针对波纹传热表面结构复杂难以测量管壁温度的特点,提出了二次曲线拟合法测量波纹管传热系数的方法,研究结构参数对波纹管传热特性的影响规律,为开发和设计结构合理的波纹管换热器提供依据。用W illson拟合曲线分离法,对一定的结构参数波纹管经一次拟合建立传热特性与介质物理性质的准数关系式。在此基础上,对不同的结构波纹管进行实验,并对实验结果进行二次拟合确定结构参数的影响。用该方法得到的波纹管对流传热系数准数关联式,在实验范围内计算误差小于15%。减小侍测侧与非侍测侧传热系数的比值,可进一步提高测量精度。

单管传热系数不确定度的理论与实验分析

利用测量不确定度的方法对不同单管在蒸发和冷凝工况时的性能进行对比。分别给出了单管蒸发和冷凝传热过程中综合传热系数、管内传热系数和管外传热系数的数学模型,并在此基础上研究3个传热系数以及相关参数的不确定度评定方法。分别以蒸发和冷凝工况为实例,得出3个传热系数的不确定度及其分量,从而得出影响不确定度的因素,进而为减小测量不确定度指明改进方向。

Turbulent Heat Transfer and Pressure Drop in Tube Fitted with Square-cut Twisted Tape

Heat transfer,friction factor and thermal enhancement factor characteristics of a double pipe heat exchanger fitted with square-cut twisted tapes（STT） and plain twisted tapes（PTT） are investigated experimentally using the water as working fluid.The tapes（STT and PTT） have three twist ratios（y=2.0,4.4 and 6.0） and the Reynolds number ranges from 2000 to 12000.The experimental results reveal that heat transfer rate,friction factor and thermal enhancement factor in the tube equipped with STT are significantly higher than those fitted with PTT. The additional disturbance and secondary flow in the vicinity of the tube wall generated by STT are higher compared to that induced by the PTT is referred as the reason for better performance.Over the range considered,the Nusselt number,friction factor and thermal enhancement factor in a tube with STT are respectively,1.03 to 1.14,1.05 to 1.25 and 1.02 to 1.06 times of those in tube with PTT.An empirical correlation is also formulated to match with experimental data of Nusselt number and friction factor for STT and PTT.