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ENHANCED FLOW BOILING OF HFE 7000 BY CHAOTIC MIXERS IN MICROCHANNELS

机译:微通道中混沌混合器增强HFE 7000的流动沸腾

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摘要

Improving mixing is an effective method to enhance flow boiling in microchannels. However, it is challenging to induce since the flow in microchannels is laminar under typical operating conditions. We report that flow boiling of 1-methoxyheptafluoropropane (HFE 7000) in a parallel microchannel array was significantly enhanced by chaotic mixers patterned on the bottom walls. The microchannel array consists of five parallel channels (height, width, length: 250 μm × 220 μm × 10 mm). The chaotic mixers consist of seven cycles with 12 staggered herringbone grooves (50 μm depth and width with 90° between two asymmetric arms) in each cycle. Its asymmetry is defined by the off center position of the apex of the herringbone groove. Compared with a smooth-wall microchannel array with identical channel dimensions, heat transfer coefficient and critical heat flux of flow boiling on HFE 7000 were enhanced up to 45 % and 61 % using chaotic mixer pairs in microchannels. Mass fluxes range from 1000 to 2200 kg/m~2-s and wall heat fluxes from 10 to 198 W/cm~2.
机译:改善混合是增强微通道中沸腾的有效方法。然而,由于在典型的操作条件下微通道中的流动是层流的,因此诱导是具有挑战性的。我们报告说,平行微通道阵列中1-甲氧基七氟丙烷(HFE 7000)的沸腾沸腾通过底壁上的混沌混合器得到了显着增强。微通道阵列由五个平行通道组成(高度,宽度,长度:250μm×220μm×10 mm)。混沌混合器由七个循环组成,每个循环中有12个交错的人字形凹槽(深度和宽度为50μm,两个不对称臂之间的夹角为90°)。它的不对称性由人字形凹槽的顶点的偏心位置定义。与具有相同通道尺寸的光滑壁微通道阵列相比,在微通道中使用混沌混合器对,HFE 7000上沸腾的传热系数和临界热通量分别提高了45%和61%。质量通量范围为1000至2200 kg / m〜2-s,壁热通量范围为10至198 W / cm〜2。

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