Abstract
A transient two-dimensional numerical simulation of Inconel spraying in a high-velocity oxygen-fuel (HVOF) torch barrel was performed. The gas flow is treated as a continuum multicomponent chemically reacting flow, whereas particles are modeled using a stochastic particle spray model, fully coupled to the gas flow. The calculated results agree well with experimental data and show important statistical aspects of particle flow in the torch.
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Abbreviations
- A p :
-
Particle surface ares (m2 )
- A‖:
-
Projected surface area (m2 )
- C d :
-
Drag coefficient
- c :
-
Total molar concentration (mole m-3)
- C vs :
-
Solid specific heat (J/kg/K)
- C Vl :
-
Liquid specific heat (J/kg/K)
- D p :
-
Particle diameter (m)
- E p :
-
Particle internal energy (J)
- e :
-
Total thermal internal energy per unit mass (J/kg)
- e m :
-
Specific energy of solid atT m (J/kg)
- e p :
-
Specific energy of particle (J/kg)
- Fp :
-
Drag force (kg ⋅ m/s2)
- Δ fHo i :
-
Heat of formation of speciesi at absolute zero (J/kg)
- h :
-
Heat transfer coefficient (J/m2 /K/s)
- h i :
-
Specific enthalpy of speciesi (J/kg)
- I :
-
Unit dyadic
- i :
-
Unit vector inx direction
- j :
-
Unit vector iny direction
- K :
-
Thermal conductivity (J/m/K/s)
- k :
-
Turbulent kinetic energy per unit mass (m2/s2)
- L :
-
Latent heat of fusion (J/kg)
- M i :
-
Molecular weight
- M :
-
Mass flow rate (kg/s)
- m p]:
-
Particle mass (kg)
- P :
-
Momentum (kgm/s)
- P‖:
-
Component of P parallel to wall (kg.m/s)
- Prt :
-
Turbulent Prandtl number
- p :
-
Pressure (N/m2)
- q :
-
Heat flux (J/m2/s)
- Re :
-
Reynolds number
- Sct :
-
Turbulent Schmidt number
- T :
-
Temperature (K)
- T m :
-
Melting temperature (K)
- T p :
-
Particle temperature (K)
- t :
-
Time (s)
- t :
-
Unit vector parallel to wall
- U :
-
Component of u parallel to wall (m/s)
- u :
-
x component of u (m/s)
- u :
-
Fluid velocity (m/s)
- U p :
-
Particle velocity (m/s)
- V :
-
Inflow velocity (m/s)
- V cell :
-
Volume of computational cell (m )
- v :
-
y component of u (m/s)
- x :
-
Radial coordinate (m)
- x i :
-
Mole fraction of speciesi
- x p :
-
Particle position (m)
- y :
-
Axial coordinate (m)
- α:
-
Fluid volume fraction
- ε:
-
Dissipation rate of turbulent kinetic energy (m2/s3)
- εp :
-
Surface emissivity of particle
- η:
-
Efficiency
- λ :
-
Second viscosity coefficient (kg/m/s)
- μ:
-
Viscosity (kg/m/s)
- v:
-
Kinematic viscosity (m2/s)
- p:
-
Total mass density (kg/m3 )
- pi:
-
Partial mass density of speciesi (kg/m3)
- σ:
-
Stefan-Boltzmann constant (J/m2 /K4/s)
- τ :
-
Shear stress (kg/m/s2)
- ϕ:
-
Viscous dissipation (kg/m/s3)
- χ:
-
Particle degree of melting
- D:
-
Derriere (back) cell face
- F:
-
Front cell face
- f:
-
Gas around particle
- L:
-
Left cell face
- p:
-
Particle
- R:
-
Right cell face
- t:
-
Turbulence
- w:
-
Wall
- T:
-
Transpose
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Chang, C.H., Moore, R.L. Numerical simulation of gas and particle flow in a high-velocity oxygen-fuel (HVOF) torch. JTST 4, 358–366 (1995). https://doi.org/10.1007/BF02648636
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DOI: https://doi.org/10.1007/BF02648636