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Perspectives on NO Formation in Combusting Diesel Spray Systems Jennifer Labs and Terry Parker Engineering Division Colorado School of Mines Golden, CO Presented at: The 3 rd Joint Meeting of the US Sections of the Combustion Institute Chicago, IL March 18, 2003.
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Perspectives on NO Formation in Combusting Diesel Spray Systems Jennifer Labs and Terry Parker Engineering Division Colorado School of Mines Golden, CO Presented at: The 3rd Joint Meeting of the US Sections of the Combustion Institute Chicago, IL March 18, 2003
Understanding of Diesel Spray Combustion Still Evolving • Complicated by: • Transient Mixture Formation • Variable Ignition Delay • Soot-Nox Tradeoff • Soot Product of Rich Combustion • NO formed at Diffusion Flame Front and in Post-Combustion Hot Gases • NO a product of high temperature, oxygen bearing environment • The 2007 Emissions targets for diesels are exceptionally stringent
Current View of Diesel Combustion • Put forth by Flynn, et. al.* • Two Phases: • Premixed • Diffusion • Soot considered a product of fuel-rich central spray zones • NO is formed in the: • Diffusion flame front • Post-combustion hot gases ** **Flynn, P.F, R.P. Durrett, G.L. Hunter, A.O. zur Loye, O.C. Akinyemi, J.E. Dec, C.K. Westbrook, SAE Paper No. 199-01-0509.
A Unique Facility Is Used to Simulate Diesel Combustion • System Capable of 50 atm and 1000 K • System includes central air flow and side arm nitrogen flows • Temperature gradients (~ 15oC) • Cooling BaF2 windows • 3-D Translation Capabilities • Data Acquisition and Timing Control • LabVIEW software controls system timing • 8 channels, 500 kHz
The Facility Captures the Physics of Diesel Combustion • Hard wall interaction simulated with a plate on top of a packed bed • Injection System • Single shot pressure amplifier produces peak pressures of 150 MPa • Custom Lucas CAV nozzle is drilled with a single hole in the center • (0.16 mm, L/D~4)
Combusting Spray Experiments Include Extractive Gas Analysis • Experiment Measurements • Injection Line Pressure • Vessel Pressure • FTIR Calibrated for Exhaust NO, CO2, CO and H2O • Constant Cell Pressure and Temperature • Operating conditions • 873K • 12.5 atm absolute • Central air flow, 165 slpm Heated Extraction Line FTIR 10 m gas cell
Diesel Combustion is a Two-Stage Process • Ignition apparent by small, sharp pressure rise • Low level heat release between premixed burn and diffusion burn • Supported by engine data • non-zero AHRR values between premixed and diffusion
Ignition Delay for Dodecane Is Similar to Previously Published Results ** • Ignition Delay • Device and Measurement Method Dependent • Current Experimental Data for Dodecane • Agrees with Previous Published Data • Repeatable Within Fuel Type New Data Points ** Parker, T.E., MD. Forsha, H.E. Stewart, K. Hom, R.F. Sawyer, and A.K. Oppenheim, SAE Paper No. 850087.
Experimental Results are for Controlled Mass Injection Events • Nitric oxide (NO) and carbon monoxide (CO) emissions normalized by carbon dioxide (CO2) • No shaft work in simulator • Assume small fraction of fuel carbon results in soot or carbon monoxide (CO) • CO2 representative of fuel input • Experiments measured total NO produced from a single injection event • Injection duration controlled • Mass injected controlled (3-28 mg) representing light to heavy load conditions • Also controlling fraction of fuel consumed in premixed or diffusion combustion
Carbon Monoxide Results Support an Early Stage Rich Burn • High CO/CO2 levels at small injection masses • Large fraction of fuel consumed by fuel-rich premixed burn • Low CO/CO2 levels at large injection masses • Large fraction of fuel consumed by lean diffusion burn
Expected NO/CO2 Trend is Simple • NO formation rate hypothesized to be constant for steady state diffusion combustion • Low NO/CO2 levels for small injection events • Larger fraction of fuel consumed in fuel-rich premixed combustion • NO/CO2 level rising asymptotically to a constant NO production rate • Majority of fuel burned in the diffusion phase
NO/CO2 for Simulator and Test Engine is Maximized at an Intermediate Load **McCormick, R.L., M.S. Graboski, T.L. Alleman, A.M. Herring, and K.S. Tyson, Environmental Science & Technology 35(9):1742 (2001)
Injection and Combustion Time Scales Overlap • Ignition delay and start of secondary burn relatively constant • Negligible NO/CO2 for injection events shorter than ignition delay • Peak NO/CO2 production occurs when injection event begins to interact with major heat release event • Steady state reached at long injection events
NO is Destroyed Via Post-Combustion Product Re-entrainment • NO/CO2 expected to be constant at steady state • NO/CO2 levels begin to fall for both simulator and test engine experiments • From examining the data, it is postulated that: • Products of combustion re-entrained into hydrocarbon rich plume • Nitric oxide destroyed via NO re-burn • Reactions between NO and unburned hydrocarbon radicals • Radicals present in the interior of jet • Initially, formation/destruction is transient
Formation of NO during the non-steady combustion event Steady formation and transient destruction of NO during steady state combustion Steady formation and destruction during steady state combustion Three Regimes of Nitric Oxide Formation/Destruction
Conclusions • A system capable of simulating diesel combustion has been demonstrated • Gas extraction and analysis • Variable mass injection • Two-stage burning process is exhibited by the simulator, similar to those found in engine data • NO formation as a function of CO2 is peaked with the highest value coinciding with the spray interacting with the major heat release
Conclusions • Three regimes of formation for overall NO production were hypothesized • Non-constant formation rate associated with the unsteady combustion process associated with light loads • Constant formation rates and transient destruction of NO associated with the steady state combustion of the fuel • Steady production and destruction associated with sufficiently long injection events which allow the combustion event and the NO re-burn to come to steady state
Acknowledgements • Biodiesel directed studies supported by NREL, Shaine Tyson, Contract Monitor • Facility development supported by a National Science Foundation Career Award, Dr. Farley Fisher, Contract Monitor • Ongoing research support by NSF, Dr. Farley Fisher, Contract Monitor • Graduate student support, GANN award, DOE • Custom drilling of injector nozzle, Raycon Corporation • CSM contributors to the project • Dr. Tom Grover • Eric Jepsen • Dr. Heather McCann • Jon Filley
Extractive Measurements Rely on Capturing the Entire Burned Charge • “Cup” used to capture exhaust gases • Valve timing is used to control the gas quantity extracted • Extract into secondary tank • Mix for 2 minutes • Then fill cell • Monitoring CO2 mass as a function of valve open time shows when entire charge is captured • 4.0 second extraction time used
Verification: Carbon Dioxide Mass in Exhaust and Fuel • Fuel mass per injection • Capture fuel and weigh • Knowing fuel composition allows conversion to mass CO2 • Assumes all fuel carbon produces CO2 • CO2 in exhaust reported by FTIR • Similar results for diesel and methyl oleate
Characteristic Engine Simulator Injection Pressure 20-80 MPa [6] 20-170 MPa [3] 55-150 MPa Nozzle orifice diameter 0.15-0.35mm [7]0.184mm[6] 0.160 mm Nozzle L/D 2-8 [3], 4[8] 4 Number of nozzle orifices 3-8 holes 1 hole Types of nozzles used Pintle and Hole-type nozzles Hole-type nozzle Mass injection 2-24 mm3 per hole[9] 4 mm3 min 37 mm3 max Chamber Temperature 1000-1200 K [7] 700-1300 K [12] 873 K Chamber Pressure 40-120 atm [7] 50-100 atm [3] 12.5 atm Hard wall interaction length 50-60 mm [10] 100 mm Liquid Length 18 mm[1] 30 mm Chamber Pressure Change 6 MPa [3] 25 kPa Compression Ratio 16-22 [3] None Overall Stoichiometry Fuel Lean [3] Fuel Lean Comparison of Typical Diesel Engine Characteristics with the Simulator
Example of AHRR Plot • Flynn, P.F., Hunter, G.L., Durrett, R.P., Farrell, L.A., Akinyemi, W.C., SAE Paper No. 2000-01-1177
2 Stage Ignition • Curran, H.J., P. Gaffuri, W.J. Pitz, and C.K. Westbrook,.Combustion and Flame, 1998, vol. 114(1): p. 149-177. • Griffiths, J.F., P.A. Halford-Maw, and D.J. Rose, Combustion and Flame, 1993, 95(3): p. 291-306. • Chevalier, C., W.J. Pitz, J. Warnatz, and C.K. Westbrook, Twenty-Fourth Symposium (International) on Combustion (1992).