Ian Wark Research Institute, University of South Australia, Mawson Lakes, SA 5095, Australia.
Langmuir. 2010 Jun 1;26(11):8061-74. doi: 10.1021/la904481d.
Film thinning experiments have been conducted with aqueous films between two air phases in a thin film pressure balance. The films are free of added surfactant but simple NaCl electrolyte is added in some experiments. Initially the experiments begin with a comparatively large volume of water in a cylindrical capillary tube a few millimeters in diameter, and by withdrawing water from the center of the tube the two bounding menisci are drawn together at a prescribed rate. This models two air bubbles approaching at a controlled speed. In pure water, the results show three regimes of behavior depending on the approach speed; at slow speed (<1 microm/s) it is possible to form a flat film of pure water, approximately 100 nm thick, that is stabilized indefinitely by disjoining pressure due to repulsive double-layer interactions between naturally charged air/water interfaces. The data are consistent with a surface potential of -57 mV on the bubble surfaces. At intermediate approach speed (approximately 1-150 microm/s), the films are transiently stable due to hydrodynamic drainage effects, and bubble coalescence is delayed by approximately 10-100 s. At approach speeds greater than approximately 150 microm/s, the hydrodynamic resistance appears to become negligible, and the bubbles coalesce without any measurable delay. Explanations for these observations are presented that take into account Derjaguin-Landau-Verwey-Overbeek and Marangoni effects entering through disjoining pressure, surface mobility, and hydrodynamic flow regimes in thin film drainage. In particular, it is argued that the dramatic reduction in hydrodynamic resistance is a transition from viscosity-controlled drainage to inertia-controlled drainage associated with a change from immobile to mobile air/water interfaces on increasing the speed of approach of two bubbles. A simple model is developed that accounts for the boundaries between different film stability or coalescence regimes. Predictions of the model are consistent with the data, and the effects of adding electrolyte can be explained. In particular, addition of electrolyte at high concentration inhibits the near-instantaneous coalescence phenomenon, thereby contributing to increased foam film stability at high approach speeds, as reported in previous literature. This work highlights the significance of bubble approach speed as well as electrolyte concentration in affecting bubble coalescence.
在薄膜压力平衡中,通过在两个空气相间的水溶液薄膜进行了薄膜变薄实验。这些薄膜没有添加表面活性剂,但在一些实验中添加了简单的 NaCl 电解质。最初,实验开始时,在直径几毫米的圆柱形毛细管中,水的体积比较大,通过从管中心抽取水,两个边界弯月面以规定的速度被拉在一起。这模拟了两个以受控速度接近的气泡。在纯水中,结果表明,根据接近速度,有三种行为状态;在低速(<1 微米/秒)下,可以形成约 100nm 厚的纯水平膜,由于自然带电的气/水界面之间的排斥双层相互作用引起的 disjoining 压力,该膜可以无限期稳定。数据与气泡表面的-57mV 表面电位一致。在中等接近速度(约 1-150 微米/秒)下,由于流体动力排水效应,薄膜是瞬态稳定的,并且气泡聚结延迟约 10-100s。在接近速度大于约 150 微米/秒时,流体动力阻力似乎变得可以忽略不计,并且气泡没有任何可测量的延迟而聚结。提出了这些观察结果的解释,这些解释考虑了进入 disjoining 压力、表面流动性和薄膜排水中的流体流动状态的 Derjaguin-Landau-Verwey-Overbeek 和 Marangoni 效应。特别是,有人认为,流体动力阻力的急剧降低是从由粘度控制的排水到由速度控制的排水的转变,这与两个气泡接近速度增加时,从不可移动的气/水界面到移动的气/水界面的转变有关。开发了一个简单的模型,该模型解释了不同薄膜稳定性或聚结状态之间的边界。模型的预测与数据一致,并且可以解释添加电解质的影响。特别是,在高浓度下添加电解质抑制了瞬时聚结现象,从而有助于在高接近速度下增加泡沫膜稳定性,如前文献所述。这项工作强调了气泡接近速度以及电解质浓度在影响气泡聚结方面的重要性。