Relative Influences of Inertia and Polymeric Viscoelastic Effects on Nusselt Numbers within Rotating Couette Flows

IF 1.8 Q3 MECHANICS
Fluids Pub Date : 2023-09-22 DOI:10.3390/fluids8100258
Phil Ligrani, Valerie Hietsch, Mengying Su
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Abstract

In past investigations of elastic instabilities and elastic turbulence, almost no attention has been devoted to the effects and influences of inertial phenomena. Within the present investigation, Nusselt number data are provided to illustrate the relative influences of inertia and polymeric viscoelastic phenomena within a rotating Couette flow (RCF) environment. Data are provided from experimental measurements of local surface heat transfer characteristics for different flow passage heights, one radial position, and different values of disk rotational speed for polyacrylamide polymer concentrations ρ of 0 ppm, 100 ppm, 150 ppm, and 300 ppm. With this approach, data for a wide range of shear rate γ˙ values, Weissenberg numbers, and first normal stress difference values are provided. Nusselt number data are provided as dependent upon a newly developed P′ parameter, equal to ReEI/Re0.22, which collapse into a single distribution over the range of P′ values considered which range from 0 to about 182. Such characteristics indicate that the P′ parameter provides an appropriate means to simultaneously account for the relative influences of inertia and polymeric viscoelastic effects. The use of such a power law dependence for Re additionally gives P′ values which are dominated by ReEI values when the Weissenberg number Wi is greater than the elastic instability transition onset value. The experimental conditions associated with this value correspond to the change from inertia domination (with buoyance influences) to polymeric viscoelastic domination which occurs for shear rates in the vicinity of 11 to 12 s−1. For Weissenberg numbers greater than the onset value, Nusselt numbers associated with H = 5 mm are generally the highest values measured, with magnitudes that steadily increase with γ˙. Associated Nusselt numbers become as high as about 3.0, whereas zero-shear rate values (obtained with zero rotation) are in the vicinity of 1.0. At lower Weissenberg number magnitudes (below the transition onset value), Nusselt numbers cover a wide range of values as experimental conditions and configuration are varied, as a consequence of the complicated and simultaneous influences of inertia, buoyancy, and dilute polymer presence.
转动库埃特流中惯性和聚合物粘弹性效应对努塞尔数的相对影响
在过去对弹性不稳定性和弹性湍流的研究中,几乎没有注意到惯性现象的作用和影响。在本研究中,提供了努塞尔数数据来说明旋转库埃特流(RCF)环境中惯性和聚合物粘弹性现象的相对影响。实验测量了聚丙烯酰胺聚合物浓度ρ为0 ppm、100 ppm、150 ppm和300 ppm时,不同流道高度、径向位置和不同盘转速下的局部表面传热特性。利用这种方法,提供了大范围剪切速率γ˙值、Weissenberg数和第一正应力差值的数据。努塞尔数数据的提供依赖于一个新开发的P '参数,等于ReEI/Re0.22,它在P '值范围内坍缩成一个单一的分布,范围从0到大约182。这些特征表明,P '参数提供了一个适当的手段,同时考虑惯性和聚合物粘弹性效应的相对影响。当Weissenberg数Wi大于弹性失稳过渡起始值时,利用Re的幂律依赖性还可以得到由ReEI值主导的P '值。与此值相关的实验条件对应于从惯性主导(受浮力影响)到聚合物粘弹性主导的变化,剪切速率在11至12 s−1附近发生。对于大于初始值的Weissenberg数,与H = 5 mm相关的Nusselt数通常是测量到的最高值,其大小随γ˙而稳步增加。相关的努塞尔数高达3.0左右,而零剪切速率值(以零旋转获得)在1.0附近。在较低的Weissenberg数量级(低于跃迁起始值)下,由于惯性、浮力和稀聚合物存在的复杂和同时影响,实验条件和构型的变化,Nusselt数覆盖了很宽的范围。
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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来源期刊
Fluids
Fluids Engineering-Mechanical Engineering
CiteScore
3.40
自引率
10.50%
发文量
326
审稿时长
12 weeks
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