对竖直及水平窄缝环形流道内单相水受迫对流换热进行了实验研究。
An experimental study on forced convection heat transfer of single-phase water in vertical and horizontal narrow annuli was performed.
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.
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