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Enhanced Reaction Kinetics in Stationary Two-Phase Flow through Porous Media.

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Multiphase flow dynamics significantly impact mixing-driven reactions in porous media. Product formation accelerates beyond diffusive time and depends on nonwetting phase flow rates, unlike previous unsaturated flow findings.

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Area of Science:

  • Environmental science
  • Chemical engineering
  • Geophysics

Background:

  • Understanding multiphase flow and reactive transport in porous media is crucial for environmental and industrial applications.
  • Nonwetting immiscible phases can be immobile (unsaturated flow) or mobile (multiphase flow).
  • Previous studies show varying reaction product trends based on flow rate or Péclet number under unsaturated conditions.

Purpose of the Study:

  • To investigate the impact of multiphase flow dynamics on mixing-driven reactions.
  • To address experimental and numerical challenges in studying these interactions.
  • To assess how product formation is affected by stationary two-phase flow conditions.

Main Methods:

  • Utilized an optimized chemiluminescence reaction.
  • Employed an experimental setup for separate reactant injection.
  • Maintained a stationary two-phase flow system.

Main Results:

  • Reaction product mass increased faster than Fickian beyond diffusive time.
  • Global kinetics initially rose, then decreased with fluctuations due to nonwetting phase displacement.
  • Product formation was dependent on the nonwetting phase flow rate for a given wetting phase flow rate.

Conclusions:

  • Multiphase flow significantly alters reactive transport compared to unsaturated flow.
  • Nonwetting phase flow rate is a critical parameter influencing reaction product formation.
  • Experimental insights into complex porous media flow and reaction dynamics were gained.