Experimental studies and population balance equation models for breakage prediction of emulsion drop size distributions

A population balance equation (PBE) model for pure drop breakage processes was developed from homogenization experiments and used to investigate model extensibility over a range of emulsion formulation and homogenizer operating variables. Adjustable parameters in the mechanistic breakage functions were estimated from measured drop volume distributions by constrained nonlinear least-squares optimization. Satisfactory prediction of measured bimodal distributions was achieved by the incorporation of two different breakage functions that accounted for large drop breakage due to turbulent shear and for small drop breakage due to collisions between drops and turbulent eddies. Model extensibility to different emulsion compositions and homogenizer pressures was investigated by comparing model predictions generated with the base case parameters to drop volume distributions measured under different conditions. The PBE model satisfactorily accounted for changes in the dispersed phase volume fraction and the interfacial tension with the base case parameters. By contrast, significantly improved predictions for the continuous phase viscosity or multiple formulation variables were obtained through re-estimation of the model parameters using multiple data sets in which the associated variables were systematically varied. The model was not able to satisfactorily predict drop volume distributions resulting from homogenizer pressure changes, perhaps due to the assumption of a constant pressure throughout the homogenizer. We conclude that PBE models of drop breakage can be used to reasonably predict the effects of emulsion formulation variables on drop volume distributions and have the potential for guiding experimental efforts aimed at the design of novel emulsified products.

[1]  Peter A. Williams Food Emulsions: Principles, Practice, and Techniques , 2001 .

[2]  Carlos A. Dorao,et al.  Numerical calculation of the moments of the population balance equation , 2006 .

[3]  Lawrence L. Tavlarides,et al.  Description of interaction processes in agitated liquid-liquid dispersions , 1977 .

[4]  M. Chappat Some applications of emulsions , 1994 .

[5]  W. Manger,et al.  Gaulin Homogenization: A Mechanistic Study , 2000, Biotechnology progress.

[6]  M. F. Malone,et al.  Self-similar inverse population balance modeling for turbulently prepared batch emulsions: Sensitivity to measurement errors , 2006 .

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

[8]  Laurier L. Schramm,et al.  Petroleum Emulsions: Basic Principles , 1992 .

[9]  SOLUTION OF INVERSE PROBLEMS IN POPULATION , 2010 .

[10]  Pieter Walstra,et al.  Physical chemistry of foods , 2002 .

[11]  Jin-Wook Kim,et al.  Improved orthokinetic coagulation model for fractal colloids : Aggregation and breakup , 2006 .

[12]  J. Masliyah,et al.  Rheology of Emulsions , 1992 .

[13]  Brian W. Kernighan,et al.  AMPL: A Modeling Language for Mathematical Programming , 1993 .

[14]  D. Marchisio,et al.  CFD modelling of turbulent drop breakage in a kenics static mixer and comparison with experimental data , 2007 .

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

[16]  K. Muske,et al.  Optimal operation of high-pressure homogenization for intracellular product recovery , 2004, Bioprocess and biosystems engineering.

[17]  Jack Legrand,et al.  Analysis of a new type of high pressure homogeniser. Part B. study of droplet break-up and recoalescence phenomena , 2004 .

[18]  Pieter Walstra,et al.  Principles of emulsion formation , 1993 .

[19]  Doraiswami Ramkrishna,et al.  Droplet breakage in stirred dispersions. Breakage functions from experimental drop-size distributions , 1996 .

[20]  Nigel J. Titchener-Hooker,et al.  Prediction of drop breakage in an ultra high velocity jet homogenizer , 2001 .

[21]  P. Becher,et al.  Encyclopedia of emulsion technology , 1983 .

[22]  E. Gavi,et al.  On the Importance of Mixing for the Production of Nanoparticles , 2008 .

[23]  Jérôme Bellettre,et al.  Analysis of a new type of high pressure homogeniser. A study of the flow pattern , 2004 .

[24]  Doraiswami Ramkrishna,et al.  Population Balances: Theory and Applications to Particulate Systems in Engineering , 2000 .

[25]  A. Saniere,et al.  Pipeline Transportation of Heavy Oils, a Strategic, Economic and Technological Challenge , 2004 .

[26]  T. Danner,et al.  Emulsification in turbulent flow 2. Breakage rate constants. , 2007, Journal of colloid and interface science.

[27]  J. Israelachvili The science and applications of emulsions — an overview , 1994 .

[28]  M. C. Ruiz,et al.  Analysis of breakage functions for liquid–liquid dispersions , 2004 .

[29]  Jan Prüss,et al.  A population balance model for disperse systems: Drop size distribution in emulsion , 1998 .

[30]  Basma Yaghi,et al.  Heavy Crude Oil Viscosity Reduction for Pipeline Transportation , 2002 .

[31]  Margaritis Kostoglou,et al.  Toward a unified framework for the derivation of breakage functions based on the statistical theory of turbulence , 2005 .

[32]  R. D. Vigil,et al.  CFD simulation of aggregation and breakage processes in laminar Taylor-Couette flow. , 2005, Journal of colloid and interface science.

[33]  Hans-Jörg Bart,et al.  The Droplet Population Balance Model – Estimation of Breakage and Coalescence , 2003 .

[34]  Pipeline Emulsion Transportation for Heavy Oils , 1992 .

[35]  Joakim Majander,et al.  Simulation of the population balances for liquid–liquid systems in a nonideal stirred tank. Part 2—parameter fitting and the use of the multiblock model for dense dispersions , 2002 .

[36]  P. Becher,et al.  Emulsions: Theory and Practice , 1957 .

[37]  Johannes Lyklema,et al.  Fundamentals of Interface and Colloid Science , 1991 .

[38]  W. Kelly,et al.  Using a CFD Model To Understand the Fluid Dynamics Promoting E. coli Breakage in a High‐Pressure Homogenizer , 2002, Biotechnology progress.

[39]  D. Ramkrishna,et al.  On the solution of population balance equations by discretization—II. A moving pivot technique , 1996 .

[40]  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.

[41]  Massimo Morbidelli,et al.  Role of turbulent shear rate distribution in aggregation and breakage processes , 2006 .

[42]  R. Braatz,et al.  Simulation of Mixing Effects in Antisolvent Crystallization Using a Coupled CFD-PDF-PBE Approach , 2006 .