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- Brian Y. Lattimer
- 410.737.8677
- www.haifire.com
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- Background
- Modeling approach
- Modeling Results
- Experimental Results
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- Alternative foam formulations being developed
- Performance evaluation impeding progress
- Lack of understanding of foam extinguishment mechanism
- Current small-scale tests not measuring all important parameters
- Performance a function of multiple parameters
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- Goals of study
- Accelerate the evaluation process of foam
- Develop model
- Predict full-scale performance of a foam
- Use / develop small-scale tests
- Measure performance of specific aspects of foam
- Drainage, evaporation, spreading characteristics
- Model input data
- Near term goal of predicting MIL-SPEC test
- 28 and 50 ft2 MOGAS pool fires
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- Swedish National Laboratory and Research Institute (SP)
- Small-scale tests
- Drainage and evaporation rates
- Viscosity of foam
- Large-scale foam spread tests
- Nozzle characterization
- Some velocity and mass distribution
- Modeling
- Simplified 1-D cases (channel and axisymmetric)
- Meshing of 1-D cases for 2-D case
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- SP (continued)
- Conclusion
- Modeling approach not capable of predicting very large scale tests
with hose line application
- Several studies on modeling foam drainage and evaporation
- Perssons et al. (1992, 1996, 1997), Magrabi, et al. (1997)
- Ablation model for Hi-Ex foams
- Rheology of foam
- Gardiner et al. (1998)
- Persson et al. (1998)
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- Field model
- Model foam spreading
- Unsteady shallow water equations
- Hydraulics / hydrology of river flows
- Divide space above fuel into a single layer of cells
- Cell thickness varies
- Average properties over height of foam
- Source terms from small-scale test data
- Solution drainage
- Solution evaporation
- Foam addition from nozzle
- Momentum from nozzle spray
- Shear force between foam and fuel
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- Thermal modeling
- Radiation from fire to foam
- Emissive power of fire and configuration factors
- Evaporation of foam dependent on predicted incident flux onto foam
- No predictions of foam temperatures in initial versions
- Small-scale testing shows no heat transfer to fuel until foam less
than 25 mm (1.0 in.) thick
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- Other body forces
- Shear between foam and fuel
- Shear from external air currents
- Wind
- Air entrainment into fire
- Momentum from foam application
- Surface tension
- Various boundary conditions
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- Assumptions
- No source terms
- Constant density
- Verification
- Compared against exact solutions to Riemann problem
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- Adding in source terms
- Frictional shear between the flow and the bed
- Mass losses and gains
- Validation
- 2-D solutions
- Foam flows
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- Evaporation
- Heat balance at surface
- Effective absorptivity
- Drainage
- Foam mass to predict drainage rate
- Develop a reference curve
- 75 mm thick foam layer
- Moderate irradiance level (20 kW/m2)
- Suppression
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- Solved and verified 1-D shallow water equations
- Developed and validated models for foam solution mass drained and
evaporated
- Developed model for suppression
- Implementing source terms and multiple dimensions into model
- Conducting test to support model input data development
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