Department of Chemical Engineering, Faculty of Chemistry, Sofia University, 1164 Sofia, Bulgaria.
Langmuir. 2011 Dec 20;27(24):14783-96. doi: 10.1021/la203474b. Epub 2011 Nov 22.
It is shown experimentally in this study that the increase of drop volume fraction can be used as an efficient tool for emulsification of viscous oils in turbulent flow. In a systematic series of experiments, the effects of drop volume fraction and viscosity of the dispersed phase on the mean, d(32), and maximum, d(V95), diameters of the drops, formed during emulsification, are quantified. The volume fraction, Φ, of the dispersed oily phase is varied between 1% and 90%, and oils with viscosity varying between 3 and 10,000 mPa.s are studied. All experiments are performed at sufficiently high surfactant concentration, as to avoid possible drop-drop coalescence during emulsification. The analysis of the experimental data shows that there is a threshold drop volume fraction, Φ(TR), at which a transition from inertial turbulent regime into viscous turbulent regime of emulsification occurs, due to the increased overall viscosity of the emulsion. At Φ < Φ(TR), d(32) and d(V95) depend weakly on Φ and are well described by known theoretical expression for emulsification in inertial turbulent regime (Davies, Chem. Eng. Sci. 1985, 40, 839), which accounts for the effects of oil viscosity and interfacial tension. At Φ > Φ(TR), both d(32) and polydispersity of the formed emulsions decrease very significantly with the increase of Φ (for the oils with η(D) > 10 mPa.s). Thus, very efficient emulsification of the viscous oils is realized. Very surprisingly, a third regime of emulsification is observed in the range of concentrated emulsions with Φ > 75%, where the mean drop size and emulsion polydispersity are found experimentally to be very similar for all oils and surfactants studied-an experimental fact that does not comply with any of the existing models of drop breakup during emulsification. Possible mechanistic explanations of this result are discussed. The experimental data for semiconcentrated and concentrated emulsions with Φ > Φ(TR) are described by a simple scaling expression, which accounts for the effects of all main factors studied.
本研究实验表明,增加液滴体积分数可作为在湍流中乳化粘性油的有效工具。在一系列系统实验中,定量研究了液滴体积分数和分散相粘度对乳化过程中形成的液滴平均直径(d(32))和最大直径(d(V95))的影响。分散油相的体积分数 Φ 在 1%到 90%之间变化,研究了粘度在 3 到 10,000 mPa·s 之间的油。所有实验均在足够高的表面活性剂浓度下进行,以避免乳化过程中可能发生的液滴聚并。实验数据分析表明,由于乳液整体粘度的增加,存在一个从惯性湍流区向乳化粘性湍流区转变的液滴体积分数阈值 Φ(TR)。在 Φ < Φ(TR)时,d(32)和 d(V95)对 Φ 的依赖性较弱,并且可以很好地用惯性湍流区乳化的已知理论表达式描述(Davies,Chem. Eng. Sci. 1985, 40, 839),该表达式考虑了油粘度和界面张力的影响。在 Φ > Φ(TR)时,形成的乳液的 d(32)和多分散性随着 Φ 的增加而显著降低(对于 η(D) > 10 mPa·s 的油)。因此,可以实现粘性油的非常有效的乳化。非常令人惊讶的是,在 Φ > 75%的浓缩乳液范围内观察到了第三个乳化区,实验发现,对于所有研究的油和表面活性剂,平均液滴尺寸和乳液多分散性非常相似-这一实验事实与乳化过程中液滴破裂的任何现有模型都不相符。讨论了对这一结果的可能的机械解释。对于 Φ > Φ(TR)的半浓缩和浓缩乳液,实验数据由一个简单的标度表达式描述,该表达式考虑了研究的所有主要因素的影响。