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Local heat transfer during reflux condensation at subatmospheric pressure and with and without non-condensable gases for power plant application

机译:在低于大气压的回流冷凝过程中,在有或没有不可冷凝气体的情况下,局部热传递用于发电厂

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摘要

Reflux condensation heat transfer of steam-air flow has been studied experimentally and theoretically. Effect reflux and co-current flow configurations and flow pressure on condensation heat transfer are investigated. Particular attention was paid to phenomena occurring at the interface and produced by the high steam velocity when the system runs at very low pressure. A total of 200 data points were used to analyze the average condensation heat transfer. An analytical model based on diffusion layer theory, momentum balance and combination of heat and mass transfer, has been developed. A good accuracy was obtained between model predictions and measurements at low pressure. The heat transfer coefficient for the reflux condensation is lower than the co-current flows, because of a thicker condensate film. Comparison between experimental results and predictions shows that the wavy film and non-condensable gas effects are very pronounced for condensation at low pressure. A new equation of the F_(wave) factor is proposed.
机译:对蒸汽-空气流的回流冷凝传热进行了实验和理论研究。研究了回流和并流流动形态以及流动压力对冷凝传热的影响。当系统在非常低的压力下运行时,应特别注意界面处发生的现象以及由高蒸汽速度产生的现象。总共使用200个数据点来分析平均冷凝热传递。建立了基于扩散层理论,动量平衡以及传热和传质相结合的分析模型。在模型预测和低压测量之间获得了良好的准确性。由于冷凝膜较厚,回流冷凝的传热系数低于并流。实验结果和预测值之间的比较表明,在低压下,波浪状薄膜和不可凝气体效应对于凝结非常明显。提出了一个新的F_(波)因子方程。

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