3.3. Particles

• 3.3.1. Introduction
  • 3.3.1.1. The Spray Equation
  • 3.3.1.2. A Combined Eulerian-Lagrangian Approach
• 3.3.2. Particle Transport Model
  • 3.3.2.1. Particle Acceleration and Trajectories
  • 3.3.2.2. Particle Dispersion and Turbulence
  • 3.3.2.3. Mass and Energy Exchange between Particles and the Gas Phase
  • 3.3.2.4. Conserved scalars and transfer numbers for various applications
  • 3.3.2.5. Energy Exchange between Particles and the Gas Phase Without Mass Transfer
  • 3.3.2.6. Further Notes on Radiative Heat Transfer
  • 3.3.2.7. Input Parameters for Particle Evolution
• 3.3.3. Coupling the Lagrangian and Eulerian Fields
  • 3.3.3.1. Gas-phase environment for parcels
  • 3.3.3.2. Effect of the particle phase on the gas phase
  • 3.3.3.3. Time step control
  • 3.3.3.4. Particle-surface interactions
• 3.3.4. Verification of Particle Evolution Equations
  • 3.3.4.1. Verification of Particle Momentum and Trajectories
  • 3.3.4.2. Verification of particle heat and mass transfer
  • 3.3.4.3. Verification of Lagrangian-Eulerian Coupling
  • 3.3.4.4. Verification summary
• 3.3.5. Summary
• 3.3.6. Evaluating transport coefficients
• 3.3.7. Lagrangian Particle Capabilities
  • 3.3.7.1. Lagrangian Particle Spray: Diameter Cutoffs
  • 3.3.7.2. Lagrangian Particle Spray: Angular Spreading Sprays
  • 3.3.7.3. Alumina Absorption Model
  • 3.3.7.4. Emission Multiplier
  • 3.3.7.5. Lagrangian Particle Spray: Number Represented Function
  • 3.3.7.6. Lagrangian Particle Insertion: User Definable Mechanism