Lecture 4 CFD for Bluff-Body Stabilized Flames

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Lecture 4 CFD for Bluff-Body Stabilized Flames Bluff Body Stabilized flames with or without swirl are in many laboratory combustors Applications to ramjets, laboratory burners, afterburners premixed and non-premixed gaseous combustion systems studied much detail* Spray in cross-flow for afterburners Vitiated air flow Stability, blowoff, combustion dynamics * Shanbhoque, Husain, Lieuwen: Lean Blowoff of bluff body stabilized flames: Scaling and Dynamics, Prog. Energy & Comb. Sci, Vol. 35, 98-120, 2008

Issues to Consider Premixed flames flame structure and coupling with heat release and vortex motion Potential for combustion instability and LBO Proper grid resolution to resolve flame wrinkling Wall boundary conditions isothermal/adiabatic Non-premixed flames Fuel injection conditions Resolution of the fuel jet shear layer Mixing occurs downstream so grid resolution is needed in the injection region and downstream Potential for liftoff, blowout Inflow and outflow conditions are important for dynamics

The Volvo Validation Rig TARS S304545 Re 30,000-45,000, C 3 H 8 -air, φ 0.6 Exp. by Sjunnesson et al., 1992- LES TFM LES EDC LES PaSR LES G-Eq LES PPDF EXP Gas analysis + EXP LDV+CARS Fureby C.; 2006, AIAA 2006-0155 Fureby C.; 2007, AIAA 2007-0713 Fureby C.; 2009, AIAA 2008-1178

The VOLVO Afterburner Non-Reacting Flow Reacting Flow LEMLES approach determined the LES grid resolution for the Reacting case based on the Non-Reacting case result

Vortex Shedding in the VOLVO Afterburner Non-Reacting Flow Reacting Flow

Results Reactive Flow Axial profile of normalized axial velocity

Results Reactive Flow Axial locations (left to right): 0.375 a 0.950 a 1.530 a 3.750 a 9.400 a (a = bluff body size) Transverse profiles of time - averaged velocities

Instantaneous Temperature Field (EBU) Instantaneous Temperature Field (LEM)

LEMLES Results VOLVO Afterburner u v Instantaneous Temperature Instantaneous Fuel Mass Fraction Mean T Time-averaged Fuel Mass Fraction EBULES LES@GT

Non-premixed Bluff Body Swirl Flame Sydney/Sandia (Symp. 2006) 3.5 million LES cells 9 LEM cells / LES 12 LEM cell / LES 5-species, 1 step Flame Type Jet S g U j U s U e R s N29S054 Air 0.55 66 29.74 20. 76,000 SMA2 CH 4 /Air 1.59 66.3 16.26 20 32,400 SM1 CH 4 0.5 32.7 38.2 20. 54,000 El Asrag and Menon, 2005, 2006

Mean Flow Features ξ SM =0.054 ξ SMA =0.25 SM1 flame (S g =0.5) SMA2 flame (S g =1.59) El Asrag and Menon, 2005, 2006

SM1 SMA2 Flame Structure SM1 SMA2 Experimental (left) LESLEM (right), SM1 flame is an H-type flame, while SMA2 is a C-Type flame with no necking El Asrag and Menon, 2005, 2006

Cold Flow Bluff body RZ + a centerline VBB + rotational collar structure (grey) SM1 Flame, BB RZ, VBB SMA2 Flame, very small BB RZ, no VBB due to high momentum Fuel jet El Asrag and Menon, 2005, 2006

Premixed and Partially Premixed Burners Premixed Combustor Exhaust gases Partially Premixed Combustor Exhaust gases Air Air Fuel Exhaust gases Flame Region swirl Air-Fuel Mixture Air swirl Fuel Air Stagnation Point Reverse Flow Combustor (SPRFC) Operating in Non Premixed Mode

LES of the SPRF Combustor (Symp 08) Grid: 1.2 million cells Same grid for all LES -5/3 in the shear layer TKE spectra Cold Flow: Centerline Decay Initial decay similar (but not exact) to confined jet Behaves like a stagnation point flow further downstream Undapalli et al., 2008

Simulation Conditions Premixed Inlet Velocity : 137 m/s Equiv ratio : 0.58 T@inlet Pressure : 500 K : 1 atm Adiabatic outer walls Isothermal injector walls Non-Premixed Inlet Velocity : 112 m/s Overall Equiv ratio : 0.58 T@inlet Pressure : 450 K : 1 atm Adiabatic outer walls Isothermal injector walls Hot products Premixed or air 2-step Methane-air (Westbrook & Dryer 81) 2-step NO (Nicol et al. 99) prompt, thermal 7-species 12 LEM cells/les cell Undapalli et al., 2008

Cold Flow Axial Velocity Premixed

Premixed Mode: Comparisons LEMLES EBULES Near injector discrepancies due to difference in expt and model Does not show classical stagnation point type flow Similar trend for mean velocity TFLES and LEMLES show similar rms peak

Non-Premixed and Premixed Comparison Umean Premixed LEMLES Non-Premixed LEMLES Non-Reacting Urms Both modes show similar trends Agreement relatively poorer for non-premixed near the stagnation region slow convergence

Premixed Mode: Flame Comparisons Note: Exptal flame is attached! EBULES: location of peak incorrect TFLES: correct location but diffused (could be improved) LEMES: correct location and shape Cost is x5 for LEMLES! Average heat release

Non-Premixed Mode: Flame Comparisons Lifted flame seen in expt. Predicted by LEMLES Under-predicted 20% 2-step kinetics SFLES shows attached flame Unsteady flamelet may work but will be very expensive Average heat release

Premixed Mode Operating regimes Contours of Mean Fp (mass of products/mass of reactants) Regime diagram Fp x/d Pitsch 2002

Summary Comments Bluff body stabilized flames are building block problems Configuration has been used to study both stable and unstable combustion and active control Laboratory burners provide access for data acquisition and therefore, offers avenue for code validation however, test conditions in the lab may not match actual operational rigs so care must be taken to scale up from lab scale validation studies Regardless, there are practical applications as well Many of the issues relevant to gas turbine combustors are equally relevant for this type of combustor