On the steady-state drop size distribution in stirred vessels. Part II: effect of continuous phase viscosity

Sergio Carrillo De Hert, Thomas Rodgers

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    Abstract

    In Part I1 we used silicon oils with viscosities across six orders of magnitude
    to investigated the effect of the dispersed phase viscosity on the DSD
    of dilute emulsions. In this study we extended Part I by using three glucose
    aqueous solutions to thicken the continuous phases approximately an order
    of magnitude while keeping the Power number constant. It was found that
    increasing the continuous phase viscosity decreases the maximum drop size
    despite having drops well above the Kolmogorov length-scale. Our results
    are in disagreement with the mechanistic models for the turbulent inertia
    regime. The results were explained using the full turbulent energy spectrum
    proposed by Pope 2 instead of the Kolmogorov -5/3 spectrum. Our analysis
    revealed that most of the steady-state drop sizes do not fall in the isotropic
    turbulence size range.
    Original languageEnglish
    JournalAmerican Institution of Chemical Engineers Journal
    Early online date26 Jan 2019
    DOIs
    Publication statusPublished - 2019

    Keywords

    • Emulsication
    • Viscosity
    • Droplet size distribution
    • Stirred vessel
    • Drop breakup

    Research Beacons, Institutes and Platforms

    • Dalton Nuclear Institute

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