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CALCULATION AND EXPERIMENTAL VERIFICATION OF HEAT TRANSFER COEFFICIENT FOR LOW PRESSURE METHANOL EVAPORATOR

机译:低压甲醇蒸发器传热系数的计算与实验验证

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Natural refrigerants are attracting attention due to their environmental neutrality. They have good thermalproperties, but their evaporation pressures at near room temperatures are just a few kPa. There is limitedinformation regarding evaporation of methanol at low-pressures. Empirical correlations for boiling heattransfer coefficient that were developed at atmospheric pressure levels tend to give high errors. In this paperwe show an experimental data for pool boiling of methanol in pressure region 0.3–18 kPa and heat fluxes10–45 kW/m~2. The results are compared to calculations based on eight empirical heat transfer coefficientcorrelations. Since all of them yielded noticable errors, we suggested new constants for the power lawequation that allow more accurate prediction of heat transfer coefficient.
机译:天然制冷剂由于其环境中性而备受关注。它们具有良好的热性能,但在室温附近的蒸发压力仅为几千帕。关于在低压下蒸发甲醇的信息有限。在大气压水平下产生的沸腾传热系数的经验相关性往往会产生很高的误差。在本文中,我们显示了在压力范围0.3–18 kPa和热通量10–45 kW / m〜2下甲醇池沸腾的实验数据。将结果与基于八个经验传热系数相关性的计算结果进行比较。由于它们都产生了明显的误差,因此我们提出了幂律方程的新常数,可以更准确地预测传热系数。

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