Hi'/> Experimental and analytical study on nucleate pool boiling heat transfer of R134a/R245fa zeotropic mixtures
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Experimental and analytical study on nucleate pool boiling heat transfer of R134a/R245fa zeotropic mixtures

机译:R134a / R245fa共沸混合物成核池沸腾换热的实验和分析研究

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HighlightsZeotropic mixtures presented higher CHF than that of pure components.The three-stage model of nucleate pool boiling process of zeotropic mixtures was proposed.An analytical model for the heat transfer degradation factor at P-DB point was established.AbstractIn the present study, the nucleate pool boiling heat transfer characteristics of zeotropic binary mixtures (R134a/R245fa) with different blending ratios, as well as their pure components, were experimentally investigated in a visualized pressure vessel. For each test refrigerant, the experiments were performed on a horizontal plain copper surface (10 mm × 10 mm) at the same evaporating temperature of 26 °C with the heat flux ranging from 1.2 kW/m2to 360 kW/m2. The boiling curves of test refrigerants were subdivided into up to four zones from natural convection region to bubble column region according to the visualization results. The slope of the boiling curve in bubble coalescence region was greater than that in isolated bubble region. The onset of nucleate boiling (ONB) point of zeotropic mixtures obviously lagged behind that of pure components, namely, the higher wall superheat was required, which presented the consistent variation with the temperature glide. The boiling heat transfer coefficient of zeotropic mixtures, although increasing with the increase of heat flux, was degraded compared to the corresponding ideal heat transfer coefficient, except for some specific cases with high heat flux. Based on the analysis of heat transfer degradation factors and additional mass transfer resistance, the nucleate pool boiling process of zeotropic mixtures was identified as three stages due to the presence of two inflection points, pseudo fully developed nucleate boiling (P-FDNB) point and pseudo double boiling (P-DB) point. The wall superheat of test mixtures at P-DB point was stable at a certain value and did not vary with the blending ratio. The thermodynamic fluctuation theory was introduced to describe the effect of mass transfer resistance for zeotropic mixtures at P-DB point and the calculation results showed good agreement with the experimental data.
机译: 突出显示 共沸混合物的CHF高于纯组分。 共沸混合物的核池沸腾过程三阶段模型 建立了P-DB点传热降解因子的分析模型。 摘要 在在本研究中,在可视化的压力容器中,对具有不同混合比的共沸二元混合物(R134a / R245fa)及其纯组分的核池沸腾传热特性进行了实验研究。对于每种测试制冷剂,在相同的蒸发温度26 C的水平纯铜表面(10 mm×10 mm)上进行实验,热通量范围为1.2 kW / m 2 至360 kW / m 2 。根据可视化结果,将测试制冷剂的沸腾曲线细分为从自然对流区域到鼓泡塔区域的多达四个区域。气泡聚结区沸腾曲线的斜率大于孤立气泡区的沸腾曲线的斜率。共沸混合物的核沸点(ONB)开始明显落后于纯组分,即需要更高的壁过热度,这随温度滑移呈现出一致的变化。共沸混合物的沸腾传热系数虽然随热通量的增加而增加,但与某些理想的传热系数相比,却有所降低,除了某些特定情况下具有高的热通量。根据传热降解因子和附加的传质阻力分析,由于存在两个拐点,即拟完全发展的核沸腾(P-FDNB)点和拟态,因此共沸混合物的核池沸腾过程被确定为三个阶段。双沸点(P-DB)点。在P-DB点处,测试混合物的壁过热度稳定在一定值,并且不会随着混合比的变化而变化。引入热力学涨落理论描述了共沸混合物在P-DB点的传质阻力的影响,计算结果与实验数据吻合良好。

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