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Pool Boiling of Low-Global Warming Potential Replacements for R134a on a Reentrant Cavity Surface

机译:凹腔表面上R134a的低全球变暖潜在替代物的池沸腾

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This paper quantifies the pool boiling performance of R134a, R1234yf, R513A, and R450A on a flattened, horizontal reentrant cavity surface. The study showed that the boiling performance of R134a on the Turbo-ESP exceeded that of the replacement refrigerants for heat fluxes greater than 20 kW m(-2). On average, the heat flux for R1234yf and R513A was 16% and 19% less than that for R134a, respectively, for R134a heat fluxes between 20 kW m(-2) and 110 kW m(-2). The heat flux for R450A was on average 57% less than that of R134a for heat fluxes between 30 kW m(-2) and 110 kW m(-2). A model was developed to predict both single-component and multicomponent pool boiling of the test refrigerants on the Turbo-ESP surface. The model accounts for viscosity effects on bubble population and uses the Fritz equation to account for increased vapor production with increasing superheat. Both loss of available superheat and mass transfer resistance effects were modeled for the refrigerant mixtures. For most heat fluxes, the model predicted the measured superheat to within +/- 0.31 K.
机译:本文对平坦的水平凹腔表面上的R134a,R1234yf,R513A和R450A的池沸腾性能进行了量化。研究表明,对于热通量大于20 kW m(-2),R134a在Turbo-ESP上的沸腾性能超过了替代制冷剂的沸腾性能。平均而言,R1234yf和R513A的热通量分别比R134a低16%和19%,R134a的热通量介于20 kW m(-2)和110 kW m(-2)之间。 R450A的热通量比30 kW m(-2)和110 kW m(-2)之间的热通量平均要比R134a小57%。开发了一个模型来预测Turbo-ESP表面上测试制冷剂的单组分和多组分池沸腾。该模型考虑了粘度对气泡总数的影响,并使用Fritz方程说明了随着过热度增加而产生的蒸汽量增加。对制冷剂混合物模拟了可用的过热损失和传质阻力效应。对于大多数热通量,模型预测测得的过热度在+/- 0.31 K之内。

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