Droplet size scaling in a turbulent pipeline flow

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Abstract

The changes of a droplet breakup regime at transition from an inertial to a viscous turbulence subrange are analyzed for pipe flow. Equations for evaluation of the maximum droplet size in both breakup regimes, as well as conditions for the breakup regime transition, are formulated as functions of the Reynolds and Weber numbers for a pipeline flow. Numerical values for the coefficients of the equations derived are estimated.

Original languageEnglish
Pages (from-to)2051-2054
Number of pages4
JournalCanadian Journal of Chemical Engineering
Volume93
Issue number11
DOIs
Publication statusPublished - 1 Nov 2015
Externally publishedYes

Keywords

  • Breakup regime
  • Droplet size
  • Modelling
  • Pipeline
  • Scaling
  • Turbulence

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