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The effect of heating direction on flow boiling heat transfer of R134a in micro-channels

机译:加热方向对微通道R134a流沸热传热的影响

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This paper presents effects of heating directions on heat transfer performance of R134a flow boiling in micro-channel heat sink.The heat sink has 30 parallel rectangular channels with cross-sectional dimensions of 500μm width 500μm depth and 30mm.length.The experimental operation condition ranges of the heat flux and the mass flux were 13.48 to 82.25 W/cm2 and 373.3 to 1244.4 kg/m2s respectively.The vapor quality ranged from 0.07 to 0.93.The heat transfer coefficients of top heating and bottom heating both were up to 25 kW/m2K.Two dominate transfer mechanisms of nucleate boiling and convection boiling were observed according to boiling curves.The experimental results indicated that the heat transfer coefficient of bottom heating was 13.9% higher than top heating in low heat flux, while in high heat flux, the heat transfer coefficient of bottom heating was 9.9%.higher than the top heating, because bubbles were harder to divorce the heating wall.Anda modified correlation was provided to predict heat transfer of top heating.
机译:加热方向上的R134a的传热性能本文呈现的效果流动沸腾在微通道换热sink.The散热器具有与500微米宽度500微米的深度和30mm.length.The实验操作条件范围的横截面尺寸30个平行矩形通道的热通量和质量通量分别为13.48到82.25 W / cm 2且373.3至1244.4公斤/米2·秒respectively.The蒸气质量从0.07到不等顶部加热和底部加热的0.93.The传热系数两者都是高达25千瓦/ m2K.Two核沸腾和对流沸腾的支配转移机制是根据沸腾curves.The实验结果观察表明,底部加热的传热系数较高13.9%,比低的热通量的顶部加热,而在高的热通量,则底部加热的传热系数为9.9%.higher比顶部加热,因为气泡均难以离婚wall.Anda修改的相关物所提供的加热预测顶部加热的热传递。

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