Encyclopaedia Index
    
TITLE   : CONFINED TURBULENT DIFFUSION FLAME
    BY      : CHAM Development Team           - M R Malin
    FOR     : Validation of Gaseous Combustion Models
    
PURPOSE OF THE CALCULATIONS:
  - The main objective of the calculations is to validate the
      turbulent combustion models provided in the extended SCRS
      attachment for gaseous combustion.
   
- The experimental data to be simulated are the zero-swirl results for
      the gas-fired turbulent combustion chamber of Owen et al (16th Int.
      Symp. Combustion, p105, 1976).
 FLOW DETAILS :
  - The geometry comprises a 12.2cm diameter axisymmetric combustor
      into which natural gas (96% CH4) is injected centrally and axially
      to mix and burn with a heated, coaxial annular air stream.
   
- The chamber length is taken as 4 diameters in the CFD simulations.
   
- Coaxial fuel and air streams are admitted separately into the
      combustor and then burn in a turbulent diffusion flame. The inlet
      fuel/air velocity ratio is 0.05.
   
- The fuel jet enters through a pipe of 6.3cm diameter at a
      temperature of 288 K. The air jet enters through an annulus at a
      temperature of 750 K. The furnace walls are presumed isothermal
      at a temperature of 600 K.
   
- The inlet fuel/air equivalence ratio is 0.9, and the combustor
      operating pressure is 3.8 atmospheres.
MAIN FEATURES OF CFD MODEL:
   - Turbulence is represented via the k-e turbulence model.
   
- Calculations are made with 4 different combustion models:
        (a) fast-chemistry model with a one-step global irreversible
            methane reaction to form CO2 and H2O;
        (b) as (a) but with an assumed double-delta probability density
            function to account for the influence of concentration
            fluctuations;
        (c) eddy-break-up finite-rate chemistry model with a one-step
            global irreversible methane reaction (CEBU=6.0); and
        (d) as (c) but with a two-step global reaction mechanism involving
            the intermediate CO (CEBU1=6.0 and CEBU2=1.0).
   
- The calculations employ variable specific heats and heats of reaction.
   
- The flow is treated as weakly compressible.
   
- Radiative heat transfer is modelled via the P1 spherical-harmonics
       approximation for a gray medium. The wall emissivity is taken as 0.9
       and the optical thickness as 0.25 based on furnace diameter.
   
- A cylindrical-polar mesh is used with 30 radial by 40 axial cells.
    
1. OWEN FURNACE TWO-STEP EBU MODEL: VELOCITY VECTORS ( M/S )
    
2. OWEN FURNACE TWO-STEP EBU MODEL: TEMPERATURE CONTOURS ( DEG K )
    
3. OWEN FURNACE: TEMPERATURE PROFILES AT Z/D=0.6
    
4. OWEN FURNACE: TEMPERATURE PROFILES AT Z/D=1.99
    
5. OWEN FURNACE: CO2 MOLE FRACTION PROFILES AT Z/D=2.84
    
6. OWEN FURNACE: CO MOLE FRACTION PROFILES AT Z/D=2.84