Tcholakova S, Denkov N D, Golemanov K, Ananthapadmanabhan K P, Lips A
Laboratory of Chemical Physics & Engineering, Faculty of Chemistry, Sofia University, 1 James Bourchier Avenue, Sofia, Bulgaria.
Phys Rev E Stat Nonlin Soft Matter Phys. 2008 Jul;78(1 Pt 1):011405. doi: 10.1103/PhysRevE.78.011405. Epub 2008 Jul 24.
In a recent Letter [N. D. Denkov, Phys. Rev. Lett. 100, 138301 (2008)] we calculated theoretically the macroscopic viscous stress of steadily sheared foam or emulsion from the energy dissipated inside the transient planar films, formed between neighboring bubbles or drops in the shear flow. The model predicts that the viscous stress in these systems should be proportional to Ca 1/2, where Ca is a capillary number and n=1/2 is the power-law index. In the current paper we explain our model in detail and develop it further in several aspects: First, we extend the model to account for the effects of viscous friction in the curved meniscus regions, surrounding the planar films, on the dynamics of film formation and on the total viscous stress. Second, we consider the effects of surface forces (electrostatic, van der Waals, etc.) acting between the surfaces of the neighboring bubbles or drops and show that these forces could be important in emulsions, due to the relatively small thickness of emulsion films (often comparable to the range of action of surface forces). In contrast, the surface forces are usually negligible in steadily sheared foams, because the dynamic foam films are thicker than the extent of surface forces, except for foams containing micrometer-sized bubbles and/or at very low shear rates. Third, additional consideration is made for bubbles or drops exhibiting high surface viscosity, for which we demonstrate an additional contribution to the macroscopic viscous stress, created by the surface dissipation of energy. The new upgraded model predicts that the energy dissipation at the bubble or drop surface leads to power-law index n<1/2 , whereas the contribution of the surface forces leads to n>1/2 , which explains the rich variety of foam or emulsion behaviors observed upon steady shear. Various comparisons are made between model predictions and experimental results for both foams and emulsions, and very good agreement is found.
在最近的一篇快报[N. D. 登科夫,《物理评论快报》100, 138301 (2008)]中,我们从瞬态平面液膜内耗散的能量出发,理论计算了稳定剪切泡沫或乳液的宏观粘性应力,这些瞬态平面液膜形成于剪切流中相邻气泡或液滴之间。该模型预测,这些体系中的粘性应力应与Ca的1/2次方成正比,其中Ca是毛细管数,n = 1/2是幂律指数。在本文中,我们详细解释我们的模型,并在几个方面进一步拓展:首先,我们扩展模型以考虑围绕平面液膜的弯曲弯月面区域中的粘性摩擦对液膜形成动力学和总粘性应力的影响。其次,我们考虑相邻气泡或液滴表面之间作用的表面力(静电、范德华力等)的影响,并表明由于乳液液膜厚度相对较小(通常与表面力作用范围相当),这些力在乳液中可能很重要。相比之下,在稳定剪切的泡沫中,表面力通常可忽略不计,因为动态泡沫液膜比表面力作用范围厚,除了含有微米级气泡的泡沫和/或在非常低的剪切速率下。第三,对表现出高表面粘度的气泡或液滴进行了额外考虑,我们证明了由能量的表面耗散对宏观粘性应力产生的额外贡献。新的升级模型预测,气泡或液滴表面的能量耗散导致幂律指数n < 1/2,而表面力的贡献导致n > 1/2,这解释了在稳定剪切时观察到的泡沫或乳液行为的丰富多样性。对泡沫和乳液的模型预测与实验结果进行了各种比较,发现吻合得非常好。