Mixing enhancement due to viscoelastic instability in serpentine microchannels at very large Weissenberg numbers

K. Nolan, A. Agarwal, S. Lei, E. Dalton
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引用次数: 1

Abstract

The flow of shear-thinning viscoelastic fluids is investigated experimentally in a serpentine microchannel at very large Weissenberg numbers (Wi > 104) undergoing elastic instability. The effects of geometric curvature on local flow instability and the consequent heat transfer enhancement are reported. Unlike previous studies where fluids with large zero-shear viscosities (up to 300 mPa.s) were used, we employ a working fluid with a lower viscosity (η0 = 9 mPa.s) more suited to microfluidic heat transfer applications while exhibiting viscoelastic characteristics. This results in Elasticity number (EI = Wi/Re) flows an order of magnitude larger than previously reported in the literature with apparent viscosities close to the solvent viscosity under flow conditions. Detailed Micro Particle Image Velocimetry (μPIV) measurements reveal the local enhancements due to instantaneous flow structures which result in vigorous local mixing at sub-critical Reynolds numbers. In addition the pressure drop increase is moderate as mixing occurs locally and the flow is maintained undisturbed elsewhere throughout the flow path.
在非常大的Weissenberg数下,蛇形微通道中粘弹性不稳定性导致的混合增强
实验研究了剪切减薄粘弹性流体在具有弹性不稳定性的非常大Weissenberg数(Wi > 104)的蛇形微通道中的流动。本文报道了几何曲率对局部流动不稳定性的影响以及由此引起的换热增强。与之前的研究不同,我们使用了具有大零剪切粘度(高达300 mPa.s)的流体,我们使用了具有较低粘度(η0 = 9 mPa.s)的工作流体,更适合于微流体传热应用,同时表现出粘弹性特性。这导致弹性数(EI = Wi/Re)流动比先前文献报道的大一个数量级,表观粘度接近流动条件下的溶剂粘度。详细的微粒子图像测速(μPIV)测量结果显示,瞬时流动结构导致亚临界雷诺数下剧烈的局部混合,从而导致局部增强。此外,压降的增加是适度的,因为混合发生在局部,流动在整个流路的其他地方保持不受干扰。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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