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  • 1. GASFLOW Code
    • 1.1. Overview
    • 1.2. Code Approach
    • 1.3. Code Features
    • 1.4. Graphical User Interface
    • 1.5. Code V&V
    • 1.6. Application Highlights
    • 1.7. Publications
    • 1.8. Current Activities
  • 2. Tutorials
    • 2.1. Overview
    • 2.2. Sod's Shock Tube Problem
    • 2.3. Mesh Generation from CAD Models
    • 2.4. 2D Lid-driven Cavity Flow
    • 2.5. Hydrogen Diffusion into Air in a 1D Duct
    • 2.6. Supersonic Flow over a Forward-facing Step
    • 2.7. Vented Explosion of Premixed Hydrogen-Air Mixtures
    • 2.8. Transient Laminar Jet Flow at Low Mach Number Regime
  • 3. Brief User Guide
    • 3.1. Overview
    • 3.2. General User Guidance
    • 3.3. Unit System and Files
    • 3.4. Mesh Generation
    • 3.5. Geometry Definition
    • 3.6. Numerical Control
    • 3.7. Gas Species and Properties
    • 3.8. Initial and Boundary Conditions
    • 3.9. Solid Heat Structures
    • 3.10. Physical Models
    • 3.11. Restart and Output
    • 3.12. GASFLOW Parallelization
  • 4. Pre- and Post-Processing Tools
    • 4.1. GASVIEW
    • 4.2. Pyscan
    • 4.3. Create3D
  • 5. Verification and Validation
    • 5.1.Overview
    • 5.2. Fluid Dynamics
      • [AS-FD 1] Steady-State and Laminar Flow Startup
      • [AS-FD 2] Transient Compressible Flow
      • [AS-FD 3] Diffusion of Hydrogen into Air
      • [AS-FD 4] Flow past a Rectangular Block
      • [AS-FD 5] 1D Flow with an Orifice
      • [ED-FD 1] Incompressible Laminar Flow in a Lid-driven Cavity
      • [ED-FD 2] Stationary Turbulent Channel Flow
      • [ED-FD 3] Turbulent Flow between Two Parallel Plates
      • [ED-FD 4] Flow over Backward-Facing Step
      • [ED-FD 5] Transient Supersonic Flow at Mach 3 over a Forward-facing Step
      • [ED-FD 6] Large Eddy Simulations of the Turbulent Jet Flow
      • [ED-FD-7] Hydrogen Turbulent Dispersion in Nuclear Containment Compartment
      • [ED-FD 8] Buoyant Jet from Unintended Hydrogen Release
      • [ED-FD 9] Radiolytic Gas Accumulation in a Pipe
      • [ED-FD 10] Supersonic Flow at Mach 2 over a Backward Facing Step
    • 5.3. Combustion
      • [ED-CM 1] BOM Spherical Combustion Chamber
      • [ED-CM 2] SNL Flame Acceleration Measurement Facility Experiment
      • [ED-CM 3] Hydrogen Deflagration in a Multi-compartment System
      • [ED-CM 4] Hydrogen Jet Fire in a Compartment with Venting Hole
      • [ED-CM 5] Hydrogen-Air Fast Deflagration in ENACCEF Facility
      • [ED-CM 6] Detonation of Premixed H2-Air Mixture in a Hemispherical Balloon
      • [ED-CM 7] H2 Deflagration at a Refueling Station
      • [ED-CM 8] Methane-Air Explosion in LLEM
      • [ED-CM 9] Hydrogen-Methane Combution in a 20 L Spherical Vessel
    • 5.4. Heat and Mass Transfer
      • [AS-HT 1] Steady-State Heat Transfer through a Wall
      • [AS-HT 2] Pressure-Volume Work Term 1: Equilibrium Case
      • [AS-HT 3] Thermodynamic Benchmarks
      • [AS-HT 4] Uniform Energy Addition to Stagnant Fluid
      • [ED-HT 1] Natural Convection in an Air-filled Square Cavity
      • [ED-HT 2] Validation of the condensation model with COPAIN facility
      • [ED-HT 3] Heat and mass transfer of a thin film model in a channel
      • [ED-HT 4] Validation of the Film Model in the Integral Test Facility for Passive Containment Cooling
      • [ED-HT 5] Stratification Erosion Benchmark
      • [ED-HT 6] Battelle Containment HYJET Test JX7
      • [ED-HT 7] Battelle GX Tests
      • [ED-HT 8] Tests in ThAI Facility
      • [ED-HT 9] HDR Tests
      • [ED-HT 10] Phebus Thermal Hydraulic Tests
      • [ED-HT 11] Test Tosqan ISP47
      • [ED-HT 12] Test MISTRA ISP47
      • [ED-HT 13] Panda SETH Test Program
    • 5.5. Multiphase Flow
      • [AS-MP 1] Particle Terminal Velocity
      • [AS-MP 2] Water droplet evaporation
      • [ED-MP 1] Spray Single Droplet Test
      • [ED-MP 2] Spray Droplets Test 113 at IRSN TOSQAN
      • [ED-MP 3] Spray Droplets Test 101 at IRSN TOSQAN
  • 6. APPLICATION HIGHLIGHTS
    • 6.1. H2 Fuel Cell Vehicle Accident in Tunnel
    • 6.2. Hydrogen Explosion in a Refueling Station
    • 6.3. Hydrogen Explosion at Fukushima Accident
    • 6.4. Methane Explosion in the Roadway of a Coal Mine
    • 6.5. Aerosols and Droplets
      • 6.5.1. Coronavirus Aerosol Transmission
      • 6.5.2. Water Droplets
  • 7. Ongoing Development and Enhancements
    • 7.1. Combustion Modeling
      • 7.1.1. Multi-step Global Methane Combustion Models
        • 7.1.1.1. One-step Reaction Mechanism
        • 7.1.1.2. Two-step Reaction Mechanism
        • 7.1.1.3. Three-step Reaction Mechanism
        • 7.1.1.4. Four-step Reaction Mechanism
        • 7.1.1.5. Five-step Reaction Mechanism
        • 7.1.1.6. FAQ
      • 7.1.2. Laminar Flame Speed Correlations for Methane-air Mixtures
        • 7.1.2.1. Stone's Correlation
        • 7.1.2.2. Elia's Correlation
        • 7.1.2.3. Takizawa's Correlation
        • 7.1.2.4. Liao's Correlation
      • 7.1.3. Turbulent Flame Speed Correlations for Methane-air Mixtures
      • 7.1.4. Correction of Effective Turbulent Burning Velocity for Lean Hydrogen-air Mixtures
      • 7.1.5. Induction Time Model
      • 7.1.6. Detailed Chemical Kinetic Modeling
      • 7.1.7. Jet Flame Modeling
    • 7.2. Discrete Particle Modeling
      • 7.2.1. Particle mass in user-defined volumes - volpardef
      • 7.2.2. Particle injection from ring shaped volumes
    • 7.3. Heat Transfer Modeling
      • 7.3.1. Time-dependent tables for heat flux and heat transfer coefficient in sinkdef
      • 7.3.2. Thermal Radiation Model for Water Vapor and Carbon Dioxide
  • 8. INPUT FILE EXAMPLES
    • 8.1. Overview
    • 8.1. Fluid Dynamics
  • 8.2. Combustion
  • 8.3. Heat Transfer
  • 8.4. Multiphase Flow
  • 8.5. Applications
  • 9. Frequently Asked Questions
    • 9.1. How to set up models for the flashing of pressurized water?
  • 9.2. How to run GASFLOW on Windows?
  • 9.3. How to export/import WSL distribution?
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  • 7.1.7.1. Introduction
  • 7.1.7.2. Key input parameters for jet fire modeling
  • 1) Input parameter to activate jet fire modeling
  • 2) Input parameter for gas species
  • 3) Input parameters for turbulence modeling
  • 4) Input parameters for numerical control
  • 7.1.7.3. Input example

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  1. 7. Ongoing Development and Enhancements
  2. 7.1. Combustion Modeling

7.1.7. Jet Flame Modeling

7.1.7.1. Introduction

Version: GASFLOW-MPI 2.1 Revision 4860 (March 30, 2025) or a more recent revision.

Fuel Type: We currently support hydrogen and methane as fuel types. However, new fuel types can be easily implemented to meet user requirements.

When using the Eddy Dissipation model, the combustion is assumed to be infinitely fast, which means the fuel and oxidizer react instantaneously as soon as they are mixed, without any delay. This simplification can lead to inaccuracies in situations where the combustion process is controlled by the chemical kinetics, rather than the turbulent mixing. For example, if the ignition is delayed by 0.3 seconds in the example bove, the Eddy Dissipation model would predict the mixtures to be burned immediately as soon as the ignition starts. However, this may not be an accurate representation of the actual combustion behavior, especially for cases with significant ignition delay or slow chemical reactions. For example, it may overpredict the pressure due to the very fast combustion.

To address this limitation, a better approach is to combine the finite-rate chemical kinetics model with the Eddy Dissipation model. This hybrid approach can more accurately capture the combustion process when the chemical kinetics dominate the overall behavior, such as in transient simulations.

On the other hand, for steady-state simulations of jet flames, the combustion is often dominated by the turbulent mixing rather than the chemical kinetics. In such cases, the Eddy Dissipation model alone may be sufficient, as the infinite-rate combustion assumption would be a reasonable approximation.

7.1.7.2. Key input parameters for jet fire modeling

1) Input parameter to activate jet fire modeling

Activate the Eddy-Dissipation/Finite-Rate (ED/FR) for hydrogen jet flame modeling

iburn = 3, ; Activate the ED-FR model for hydrogen jet flame modeling

iburn3_ed = 1, ; Activate the reaction rate calculated by EDM

iburn3_fr = 1, ; Activate the reaction rate calculated by finite rate

iburn1_forev = 1, ; One-step forward reaction for H2-O2 combustion

iburn1_freqfact_for = 5.0e+12, ; Frequency factor

iburn1_tact_for = 9.375e+3, ; Activation temperature (Ea/R)

iburn1_n_for = 0, ; Temperature exponentional factor

Ignition starts at 0.0 s and the duration is 0.01 s.

burndef(1:10,1) = 30, 34, 1, 2, 4, 5, 1, 2000, 0, 0.01, ; Ignitor

Activate the Eddy Dissipation model for methane jet flame modeling

iburn = 7, ; Activate the ED-FR model for hydrogen jet flame modeling

iburn7_fr = 1,; Activate FR model. Must be 1 for premixed combustions.

iburn7_ed = 1, ; Activate EDM

ireastep = 1, ; One-step global CH4-O2 combustion

ich4reaopt = 1,

Ignition starts at 0.0 s and the duration is 0.01 s.

burndef(1:10,1) = 4, 5, 1, 2, 20, 24, 1, 2000, 0, 0.01, ; Ignitor

2) Input parameter for gas species

Gas spieces for hydrogen jet flame

mat = 'h2', 'o2', 'n2', 'h2o', ; gas spieces for hydrogen jet flame

Gas spieces for methane jet flame

mat = 'ch4', 'o2', 'n2', 'h2o', 'co2', ; gas spieces for methane jet flame

3) Input parameters for turbulence modeling

Turbulence model as well as mass/momentum/energy diffusion must be switched on in jet flame simulations.

tmodel   = 'ke',   ; turbulence model
idiffmom = 1,      ; momentum diffusion (0: off | 1: on; must be 1 if tmodel /= 'none')
idiffme  = 1,      ; mass and energy diffusion (0: off | 1: on)

Because the simulation results of the jet flame are sensitive to the initial and boundary conditions of the turbulence model, it is important for the user to choose appropriate values for epsval and tkeval according to the specific conditions of their simulation. In the example below, the initial turbulence conditions (0 s) in the entire computational domain is set up in turbdef(1:12,1), and the turbulent boundary conditions (0-9999 s) at the jet nozzle is given by turbdef(1:12,2).

turbdef(1:12,1) = 1, 'im1', 1, 'jm1', 1, 'km1', 1, 1, 1, 0, 0.0, 0.0,
turbdef(1:12,2) = 3, 3, 1, 2, 21, 23, 1, 2, 2, 0, 0.0, 9999.0,
tkeval = 100.0, 1.5e5,  
epsval = 1000.0, 1.0e5,

4) Input parameters for numerical control

cflnum   = 0.25,  ; CFL number for advection
cfldiff  = 0.25,  ; CFL number for diffusion
ifvl     = 1,     ; advection scheme (0: donor cell | 1: van Leer)

It is recommended to limit the CFL (Courant-Friedrichs-Lewy) numbers for advection (cflnum) and diffusion (cfldiff) to around 0.25 to ensure numerical stability. The user can set these values between 0 and 1. Using a bigger CFL number will result in a larger time step, which can reduce the overall simulation time. However, this approach must be applied with caution, as excessively high CFL numbers can also lead to numerical instability in the simulation. The user should increase the CFL values gradually and monitor the simulation closely for any signs of instability, such as diverging results or unphysical oscillations.

7.1.7.3. Input example

This example demonstrates how to set up GASFLOW-MPI to model vertical and horizontal CH4-air jet flames. The user will need to refine the mesh and set appropriate initial and boundary conditions for their specific application.

Previous7.1.6. Detailed Chemical Kinetic ModelingNext7.2. Discrete Particle Modeling

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12KB
ingf_ch4_vertical_jet_flame
11KB
ingf_ch4_horizontal_jet_flame
Vertical methane jet flame (injection velocity: 300 m/s, nozzle diameter: 10 cm)
Horizontal methane jet flame (injection velocity: 300 m/s, nozzle diameter: 10 cm)