On the visualization of droplet deformation and breakup during high-pressure homogenization

Abstract The properties of emulsions are strongly influenced by the size distribution of the droplets. In order to achieve droplets on a microscale, high-pressure homogenization is used to transfer stresses to the droplet surface in the flow field upstream, in and downstream the disruption unit of the homogenizer. The droplets are deformed and eventually break up when exceeding critical values. Inline measurement techniques are still very challenging, due to highly complex flow conditions on microscales, high process pressures and large velocities. In this work, the optical flow measurement technique micro particle image velocimetry (μPIV) is used to quantify the flow field, the local stresses as well as droplet deformation and breakup. A special homogenization orifice which is optical accessible enabled the visualization in the whole area of interest before, in and after the restriction up to 80 bars homogenization pressure. The study of the single-phase flow with particular focus on the local stresses showed laminar and transitional conditions at Re number ranging from 285 to 1280. Droplets of two different viscosities are then examined at these conditions while passing the orifice. At the inlet, their size, deformation and position are investigated by an automated image processing algorithm and correlated with the local velocity gradients. At the outlet and downstream, deformation and breakup of droplets are shown within the possibilities of the μPIV and discussed in relation to known droplet breakup mechanisms. Finally, the droplet size distributions offline obtained by static light scattering are compared with observed phenomena of the individual drops in order to gain insights into droplet disruption in high-pressure homogenization.

[1]  Barbara Freudig,et al.  Production of Emulsions in High‐Pressure Homogenizers – Part II: Influence of Cavitation on Droplet Breakup , 2003 .

[2]  S. T. McComas Hydrodynamic Entrance Lengths for Ducts of Arbitrary Cross Section , 1967 .

[3]  B. Massey,et al.  Mechanics of Fluids , 2018 .

[4]  Christian J. Kähler,et al.  On the effect of particle image intensity and image preprocessing on the depth of correlation in micro-PIV , 2012 .

[5]  K. Landfester,et al.  Emulsification of particle loaded droplets with regard to miniemulsion polymerization , 2013 .

[6]  S. G. Mason,et al.  Particle motions in sheared suspensions XII. Deformation and burst of fluid drops in shear and hyperbolic flow , 1961 .

[7]  Heike P. Schuchmann,et al.  Herstellen von Emulsionen in einfachen und modifizierten Lochblenden: Einfluss der Geometrie auf die Effizienz der Zerkleinerung und Folgen für die Maßstabsvergrößerung , 2008 .

[8]  Heike P. Schuchmann,et al.  Investigations on the characterization of laminar and transitional flow conditions after high pressure homogenization orifices , 2014, Microfluidics and Nanofluidics.

[9]  T. Danner,et al.  Efficient emulsification of viscous oils at high drop volume fraction. , 2011, Langmuir : the ACS journal of surfaces and colloids.

[10]  L. Fuchs,et al.  High resolution experimental measurement of turbulent flow field in a high pressure homogenizer model and its implications on turbulent drop fragmentation , 2011 .

[11]  S. Błoński,et al.  Analysis of turbulence in a micro-channel emulsifier ✩ , 2007 .

[12]  L. G. Leal,et al.  An experimental investigation of drop deformation and breakup in steady, two-dimensional linear flows , 1986, Journal of Fluid Mechanics.

[13]  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.

[14]  K. Ramamurthi,et al.  Characteristics of flow through small sharp-edged cylindrical orifices , 1999 .

[15]  Rainer Koch,et al.  Performance of Prefilming Airblast Atomizers in Unsteady Flow Conditions , 2006 .

[16]  C. Dalmazzone,et al.  Drop break-up in turbulent pipe flow downstream of a restriction , 2005 .

[17]  C. Noik,et al.  Breakup of a drop in a liquid–liquid pipe flow through an orifice , 2007 .

[18]  Y. Liao,et al.  A literature review of theoretical models for drop and bubble breakup in turbulent dispersions , 2009 .

[19]  Francesco Greco,et al.  DYNAMICS OF A LIQUID DROP IN A FLOWING IMMISCIBLE LIQUID , 2004 .

[20]  Hachimi Fellouah,et al.  The flow field in turbulent round free jets , 2012 .

[21]  H. Brenner,et al.  Particle motions in sheared suspensions , 1959 .

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

[23]  K. Landfester,et al.  Determination of the Ideal Surfactant Concentration in Miniemulsion Polymerization , 2013 .

[24]  C. Trägårdh,et al.  Analysis of the flow field in a high-pressure homogenizer , 2007 .

[25]  S. Jafari,et al.  Re-coalescence of emulsion droplets during high-energy emulsification , 2008 .

[26]  Howard A. Stone,et al.  An experimental study of transient effects in the breakup of viscous drops , 1986, Journal of Fluid Mechanics.

[27]  Thomas Maskow,et al.  Real Time Insights into Bioprocesses Using Calorimetry: State of the Art and Potential , 2006 .

[28]  Howard A. Stone,et al.  The influence of initial deformation on drop breakup in subcritical time-dependent flows at low Reynolds numbers , 1989, Journal of Fluid Mechanics.

[29]  Julio M. Ottino,et al.  Stretching and breakup of droplets in chaotic flows , 1991, Journal of Fluid Mechanics.

[30]  H. Schubert,et al.  Emulsification in High‐Pressure Homogenizers , 2001 .

[31]  R. Adrian,et al.  Out-of-focus effects on particle image visibility and correlation in microscopic particle image velocimetry , 2000 .

[32]  Heh Han Meijer,et al.  Droplet breakup mechanisms : stepwise equilibrium versus transient dispersion , 1993 .

[33]  William E. Lorensen,et al.  Marching cubes: A high resolution 3D surface construction algorithm , 1987, SIGGRAPH.

[34]  C. Trägårdh,et al.  Visualization of the drop deformation and break-up process in a high pressure homogenizer , 2005 .

[35]  Christian J. Kähler,et al.  Wall-shear-stress and near-wall turbulence measurements up to single pixel resolution by means of long-distance micro-PIV , 2006 .

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

[37]  S. Büttgenbach,et al.  High-pressure microfluidic systems (HPMS): flow and cavitation measurements in supported silicon microsystems , 2015 .

[38]  Kathleen Feigl,et al.  Emulsion processing—from single-drop deformation to design of complex processes and products , 2005 .

[39]  Andrew W. Fitzgibbon,et al.  Ellipse-specific direct least-square fitting , 1996, Proceedings of 3rd IEEE International Conference on Image Processing.

[40]  Osborne Reynolds,et al.  XXIX. An experimental investigation of the circumstances which determine whether the motion of water shall be direct or sinuous, and of the law of resistance in parallel channels , 1883, Philosophical Transactions of the Royal Society of London.

[41]  F. C. Johansen Flow through Pipe Orifices at Low Reynolds Numbers , 1930 .

[42]  Thomas Danner,et al.  Emulsification in turbulent flow: 3. Daughter drop-size distribution. , 2007, Journal of colloid and interface science.

[43]  L. G. Leal,et al.  An experimental study of drop deformation and breakup in extensional flow at high capillary number , 2001 .

[44]  L. Fuchs,et al.  Theoretical and experimental analyses of drop deformation and break-up in a scale model of a high-pressure homogenizer , 2011 .