首页> 外文期刊>International Journal of Heat and Mass Transfer >Time periodic flow boiling heat transfer of R-134a and associated bubble characteristics in a narrow annular duct due to flow rate oscillation
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Time periodic flow boiling heat transfer of R-134a and associated bubble characteristics in a narrow annular duct due to flow rate oscillation

机译:由于流量振荡,R-134a的时间周期性沸腾传热及窄环形管道中的相关气泡特性

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An experiment is conducted here to investigate the effects of the imposed time periodic refrigerant flow rate oscillation in the form of nearly a triangular wave on refrigeriant R-134a flow boiling heat transfer and associated bubble characteristics in a horizontal narrow annular duct with the duct gap fixed at 2.0 mm. The results indicate that when the imposed heat flux is close to that for the onset of stable flow boiling, intermittent flow boiling appears in which nucleate boiling on the heated surface does not exist in an entire periodic cycle. At somewhat higher heat flux persistent boiling prevails. Besides, the refrigerant flow rate oscillation only slightly affects the time-average boiling curves and heat transfer coefficients. Moreover, the heated wall temperature, bubble departure diameter and frequency, and active nucleation site density are found to oscillate periodically in time as well and at the same frequency as the imposed mass flux oscillation. Furthermore, in the persistent boiling the resulting heated wall temperature oscillation is stronger for a longer period and a larger amplitude of the mass flux oscillation. And for a larger amplitude of the mass flux oscillation, stronger temporal oscillations in the bubble characteristics are noted. The effects of the mass flux oscillation on the size of the departing bubble and active nucleation site density dominate over the bubble departure frequency, causing the heated wall temperature to decrease and heat transfer coefficient to increase at reducing mass flux in the flow boiling, opposing to that in the single-phase flow. But they are only mildly affected by the period of the mass flux oscillation. However, a short time lag in the wall temperature oscillation is also noted. Finally, a flow regime map is provided to delineate the boundaries separating different boiling regimes for the R-134a flow boiling in the annular duct.
机译:在此进行实验,以研究近似周期性地以三角波形式施加的周期性周期性制冷剂流量振荡对制冷剂R-134a流动沸腾传热和水平窄环形管道中固定了管道间隙的相关气泡特性的影响。在2.0毫米结果表明,当所施加的热通量接近于稳定流动沸腾开始时的热通量时,出现间歇流动沸腾,其中在整个周期性循环中不存在被加热表面上的核沸腾。在较高的热通量下,持续沸腾占主导。此外,制冷剂流量的振荡仅对时间平均沸腾曲线和传热系数产生轻微影响。而且,发现加热的壁温,气泡离开的直径和频率以及活性成核位点密度也随着施加的质量通量振荡而及时地周期性地振荡。此外,在持续沸腾中,所得到的加热的壁温度振荡在更长的时间内更强并且质量通量振荡的幅度更大。并且对于较大的质量通量振荡,注意到气泡特性中较强的时间振荡。质量通量振荡对离去气泡的大小和活性成核位点密度的影响在气泡离去频率上占主导地位,导致加热的壁温降低,传热系数增加,从而降低了流沸腾中的质量通量,与在单相流中但是它们仅受质量通量振荡周期的轻微影响。然而,还注意到壁温振荡的短时滞。最后,提供了一个流态图,以描绘分隔R-134a在环形管道中沸腾的流态的边界。

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