在热虹吸流程的实验装置中测量了流动沸腾传热系数。
The heat transfer coefficient was measured in the experimental equipment.
实验结果表明，采用强化屏可使低肋管沸腾传热系数提高几倍乃至十倍。
The experiment results show that the boiling heat transfer coefficient can be 7-up to 10-fold enhanced by using shroud.
结果表明，通入空气使沸腾传热系数有所提高，并且加热表面温度有所降低。
It was found from the experimental results that air introduction can significantly enhance the boiling heat transfer and make the temperature of heated surface lower.
适当增大多孔层厚度将有利于沸腾传热系数的提高，而热虹吸高度的降低将不利于沸腾传热系数的增大。
Increasing the thick-ness of porous layer suitably was of benefit to boiling heat transfer. The coefficient of boiling heat transfer decreased as the height of thermal si-phon...
通过与常规流道中的沸腾传热系数的比较，得到了在窄缝环形流道中沸腾传热系数比常规流道中的沸腾传热系数约高1 5 %的结论。
It has been concluded that boiling heat transfer coefficient in narrow annular channel is 15 % higher than in conventional channel by comparison.
实验结果表明，机加工管的传热性能比同规格的工业光管及T型翅片管的传热性能有较大提高，在实验热负荷内其沸腾传热系数是光管的1.7~2.2倍。
The experimental results showed that the heat transfer coefficients for the porous surface tubes are 1.7~2.2 times larger than that for smooth tube.
实验结果表明，机加工管的传热性能比同规格的工业光管及T型翅片管的传热性能有较大提高，在实验热负荷内其沸腾传热系数是光管的1.7~2.2倍。
The experimental results showed that the heat transfer coefficients for the porous surface tubes are 1.7~2.2 times larger than that for smooth tube.
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