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首页> 外文期刊>International Journal of Heat and Mass Transfer >Effects of Rayleigh-Benard convection on spectra of viscoplastic fluids
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Effects of Rayleigh-Benard convection on spectra of viscoplastic fluids

机译:Rayleigh-Benard对流对粘塑性流体光谱的影响

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Direct Numerical Simulations (DNS) have been conducted to analyse velocity and temperature spectra in unsteady three-dimensional Rayleigh-Benard convection (differentially heated horizontal walls, i.e. heated from below and cooled from above whereas the other walls are adiabatic) at high nominal Rayleigh number of viscoplastic fluids obeying a Bingham model in cubic domains and the corresponding Newtonian cases with same nominal Rayleigh and Prandtl numbers for reference purposes. The simulations have been carried out for nominal Rayleigh numbers of 10~7 and 10~8 for a representative value of nominal Prandtl number (i.e. Pr = 320 which corresponds to a 0.05% by weight Carbopol-water solution). The effects of yield stress on velocity and temperature spectra and heat transfer characteristics of the flow fields have been investigated in terms of isotherms, path lines, apparently unyielded regions and mean Nusselt number, along with the power spectral densities of temperature and velocity fluctuations. It has been found that thermal convection strengthens (weakens) with increasing nominal Rayleigh number Ra (Bingham number Bn). Consistent with this observation, the range of flow structures becomes larger with higher (smaller) values of Ra (Bn). Additionally, it has been observed that the decay of the power spectral densities of temperature fluctuations in the viscous-convective range is close to the inverse of frequency f(i.e. it scales as f~(-1)) for Pr > 1 in both Newtonian (i.e. Bn = 0) and Bingham fluid cases with moderate values of Bn. The fluid motion (including its unsteady features) weakens and the mean Nusselt number drops progressively with an increase in Bingham number.
机译:已经进行了直接数值模拟(DNS),以在高标称瑞利数下对不稳定的三维Rayleigh-Benard对流(水平加热的壁,即从下方加热并从上方冷却,而其他壁是绝热)进行分析的速度和温度谱。服从Bingham模型在立方域中的粘塑性流体以及具有相同名义Rayleigh和Prandtl数的相应牛顿实例,以供参考。对于标称普朗特数的代表值(即,Pr = 320,其对应于0.05重量%的Carbopol-水溶液),已经针对标称瑞利数10〜7和10〜8进行了模拟。研究了屈服应力对等温线,路径线,明显的非屈服区域和平均努塞尔特数以及温度和速度波动的功率谱密度等方面的影响,对速度和温度谱以及流场的传热特性的影响。已经发现,随着对流瑞利数Ra(宾汉数Bn)的增加,热对流会增强(减弱)。与该观察结果一致,当Ra(Bn)值较高(较小)时,流动结构的范围变大。此外,已经观察到,在两个牛顿方程中,对于Pr> 1,粘性对流范围内温度波动的功率谱密度的衰减都接近于频率f的倒数(即,它缩放为f〜(-1))。 (即Bn = 0)和Bn中等的Bingham流体病例。流体运动(包括其不稳定的特征)减弱,并且平均宾塞尔值随着宾汉姆数的增加而逐渐下降。

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