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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Modeling rheological behavior of bentonite suspensions as Casson and Robertson-Stiff fluids using Newtonian and true shear rates in Couette viscometry
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Modeling rheological behavior of bentonite suspensions as Casson and Robertson-Stiff fluids using Newtonian and true shear rates in Couette viscometry

机译:在库埃特粘度计中使用牛顿和真实剪切速率对膨润土悬浮液(如Casson和Robertson-Stiff流体)的流变行为进行建模

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The Casson model and the Robertson-Stiff model have been used to determine whether they can describe the rheology of aqueous bentonite suspensions. The assessment utilized a total of twelve sets of experimental viscometric data from literature and from this work. Equations have been presented which allowed the determination of the true shear rates experienced by the fluids within the gap of the rotational viscometer for both rheological models. Non-linear regression has been applied to determine the two rheological parameters for the Casson model and the three rheological parameters for the Robertson-Stiff model using true shear rates and Newtonian shear rates, which are used most often in the analysis of rheometric data. The results showed that both models describe well the experimental data of these bentonite suspensions with good statistical indicators. Furthermore, analysis showed that true shear rates are always higher than Newtonian shear rates for both models. The differences depend on the particular suspension and are larger at low shear rates while they become smaller at higher shear rates indicating that the fluid behavior approaches Newtonian behavior at higher shear rates. The shapes of the rheograms remained essentially unchanged indicating that the rheological parameters determined with the use of true shear rates are very similar to the rheological parameters determined with the use of Newtonian shear rates. This was further confirmed with the computation of the rheological parameters for both models and both approaches. For the Casson model differences in the yield value computed with true shear rates were at most at 7% while for the plastic viscosity at 3%. For the Robertson-Stiff model, differences of the order of 2 to 5% were observed for the K-values, of 7% for gamma_0-values while no differences were observed for the n-values. These small differences, however, do not justify use of Newtonian shear rates when analytical solutions exist which allow use of true shear rates without any compromise.
机译:已经使用Casson模型和Robertson-Stiff模型来确定它们是否可以描述膨润土水溶液的流变性。该评估总共利用了来自文献和这项工作的十二组实验粘度数据。已经提出了方程,其允许确定两种流变模型在旋转粘度计的间隙内的流体经历的真实剪切速率。已应用非线性回归来确定使用真实剪切速率和牛顿剪切速率的Casson模型的两个流变参数和Robertson-Stiff模型的三个流变参数,这是流变数据分析中最常用的参数。结果表明,两个模型都很好地描述了这些膨润土悬浮液的实验数据,并具有良好的统计指标。此外,分析表明,两种模型的真实剪切率始终高于牛顿剪切率。差异取决于特定的悬浮液,并且在低剪切速率下差异较大,而在较高剪切速率下差异较小,表明流体行为在较高剪切速率下接近牛顿行为。流变图的形状基本保持不变,表明使用真实剪切速率确定的流变参数与使用牛顿剪切速率确定的流变参数非常相似。计算这两种模型和两种方法的流变参数进一步证实了这一点。对于Casson模型,以真实剪切速率计算的屈服值差异最大为7%,而塑性粘度为3%。对于Robertson-Stiff模型,K值的差异为2%到5%,gamma_0值的差异为7%,而n值没有差异。但是,当存在分析解决方案时,这些微小的差异并不能证明使用牛顿剪切率是合理的,从而可以使用真实的剪切率而不会有任何妥协。

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