Droplet size scaling of water-in-oil emulsions under turbulent flow.

The size of droplets in emulsions is important in many industrial, biological, and environmental systems, as it determines the stability, rheology, and area available in the emulsion for physical or chemical processes that occur at the interface. While the balance of fluid inertia and surface tension in determining droplet size under turbulent mixing in the inertial subrange has been well established, the classical scaling prediction by Shinnar half a century ago of the dependence of droplet size on the viscosity of the continuous phase in the viscous subrange has not been clearly validated in experiment. By employing extremely stable suspensions of highly viscous oils as the continuous phase and using a particle video microscope (PVM) probe and a focused beam reflectance method (FBRM) probe, we report measurements spanning 2 orders of magnitude in the continuous phase viscosity for the size of droplets in water-in-oil emulsions. The wide range in measurements allowed identification of a scaling regime of droplet size proportional to the inverse square root of the viscosity, consistent with the viscous subrange theory of Shinnar. A single curve for droplet size based on the Reynolds and Weber numbers is shown to accurately predict droplet size for a range of shear rates, mixing geometries, interfacial tensions, and viscosities. Viscous subrange control of droplet size is shown to be important for high viscous shear stresses, i.e., very high shear rates, as is desirable or found in many industrial or natural processes, or very high viscosities, as is the case in the present study.

[1]  Ming Li,et al.  The Relationship Between Oil Droplet Size and Upper Ocean Turbulence , 1998 .

[2]  H. P. Grace DISPERSION PHENOMENA IN HIGH VISCOSITY IMMISCIBLE FLUID SYSTEMS AND APPLICATION OF STATIC MIXERS AS DISPERSION DEVICES IN SUCH SYSTEMS , 1982 .

[3]  S. Saito,et al.  EFFECT OF DISPERSED-PHASE VISCOSITY ON THE MAXIMUM STABLE DROP SIZE FOR BREAKUP IN TURBULENT FLOW , 1977 .

[4]  Haitao Xu,et al.  The Role of Pair Dispersion in Turbulent Flow , 2006, Science.

[5]  J. Salager,et al.  Pharmaceutical Emulsions and Suspensions , 2000 .

[6]  Suzanne M. Kresta,et al.  Correlation of mean drop size and minimum drop size with the turbulence energy dissipation and the flow in an agitated tank , 1998 .

[7]  David Julian McClements,et al.  Food Emulsions: Principles, Practice, and Techniques , 1998 .

[8]  Carolyn A. Koh,et al.  Measurement and Calibration of Droplet Size Distributions in Water-in-Oil Emulsions by Particle Video Microscope and a Focused Beam Reflectance Method , 2010 .

[9]  D. E. Brown,et al.  Drop size distribution of stirred non-coalescing liquid—liquid system , 1972 .

[10]  F. B. Sprow Distribution of drop sizes produced in turbulent liquid—liquid dispersion , 1967 .

[11]  J. Hinze Fundamentals of the hydrodynamic mechanism of splitting in dispersion processes , 1955 .

[12]  Lawrence L. Tavlarides,et al.  The effect of continuous-phase viscosity on the unsteady state behavior of liquid-liquid agitated dispersions , 1987 .

[13]  Alvin W. Nienow,et al.  The dependency on scale of power numbers of Rushton disc turbines , 1987 .

[14]  F. V. Dieren,et al.  Droplet break-up in a stirred water-in-oil emulsion in the presence of emulsifiers , 1994 .

[15]  Fernando Leal-Calderon,et al.  Emulsion Science: Basic Principles , 2003 .

[16]  Richard V. Calabrese,et al.  Drop breakup in turbulent stirred‐tank contactors. Part I: Effect of dispersed‐phase viscosity , 1986 .

[17]  Thomas Danner,et al.  Emulsification in turbulent flow 1. Mean and maximum drop diameters in inertial and viscous regimes. , 2007, Journal of colloid and interface science.

[18]  L. Tavlarides,et al.  The Analysis of Interphase Reactions and Mass Transfer in Liquid-Liquid Dispersions , 1981 .

[19]  D. French-McCay Oil spill impact modeling: Development and validation , 2004, Environmental toxicology and chemistry.

[20]  H. Peerhossaini,et al.  Droplets formation in turbulent mixing of two immiscible fluids in a new type of static mixer , 2003 .

[21]  M. Stamatoudis,et al.  Effect of the Number of Impeller Blades on the Drop Sizes in Agitated Dispersions , 2005 .

[22]  G. Marti-Mestres,et al.  Pharmaceutical Emulsions and Suspensions : Second Edition, Revised and Expanded , 2000 .

[23]  R. A. De Bruijn,et al.  Tipstreaming of drops in simple shear flows , 1993 .

[24]  R. Shinnar,et al.  Stabilizing Liquid-Liquid Dispersions by Agitation , 1961 .

[25]  Joseph Katz,et al.  Turbulent shearing of crude oil mixed with dispersants generates long microthreads and microdroplets. , 2010, Physical review letters.

[26]  Geoffrey Ingram Taylor,et al.  The formation of emulsions in definable fields of flow , 1934 .

[27]  Reuel Shinnar,et al.  On the behaviour of liquid dispersions in mixing vessels , 1961, Journal of Fluid Mechanics.

[28]  E. D. Sloan,et al.  Direct conversion of water droplets to methane hydrate in crude oil , 2009 .

[29]  Johan Sjöblom,et al.  Encyclopedic Handbook of Emulsion Technology , 2001 .

[30]  Grant B. Deane,et al.  Scale dependence of bubble creation mechanisms in breaking waves , 2002, Nature.