Modeling ethylene combustion from low to high pressure

With the same reaction set, data have been modeled successfully from two ethylene-oxygen combustion systems at greatly different pressures. New data are from the Princeton flow reactor, a lower temperature (850–950 K) and high-pressure (5–10 atm) data set (=2.5). The second set is for a high-temperature ( Several reaction sets were tested, but only the present set demonstrated good agreement in both cases. A key difference between this set and previous ones lies in the modeling of the complex C2H3+O2 reaction. New rate constants were calculated based on recent findings regarding the potential energy surface of the C2H3+O2 system. In the 850–1600 K range that is crucial in these experiments, the product set CH2CHO+O was found to contribute much less than reported in earlier studies, and the HCO+CH2O channel dominated. The present reaction set predicted the species profiles in both cases with reasonable accuracy, allowing us to interpret and compare the reaction pathways over a wide range of conditions. In the low-pressure flame, C2H4 is mainly consumed by abstraction, while in the high-pressure system, abstraction (mainly by OH instead of H) competes with H addition that forms C2H5. In both cases, abstraction forms C2H3 that reacts with O2 to make HCO and CH2O and eventually CO and CO2 However, higher levels of C2H5 and HO2 at the high-pressure, lower temperature flow reactor condition drive distinct pathway differences. The key role of HO2 chemistry is particularly emphasized through the reaction CH2O+HO2. Model comparisons support a lower value of the rate constant for this reaction, consistent with that recommended by Hochgreb and Dryer.

[1]  P. R. Westmoreland Thermochemistry and Kinetics of C2H3+ 02 Reactions , 1992 .

[2]  P. R. Westmoreland,et al.  Forming benzene in flames by chemically activated isomerization , 1989 .

[3]  Phillip R. Westmoreland,et al.  Tests of published mechanisms by comparison with measured laminar flame structure in fuel-rich acetylene combustion , 1988 .

[4]  James A. Miller,et al.  The Oxidation of Allene in a Low-Pressure H2 / O2 / Ar-C3 H4 Flame , 1995 .

[5]  R. R. Baldwin,et al.  Relative rate study of the addition of HO2 radicals to C2H4 and C3H6 , 1986 .

[6]  Henry F. Schaefer,et al.  The C2H5 + O2 Reaction Mechanism: High-Level ab Initio Characterizations , 2000 .

[7]  R. R. Baldwin,et al.  Elementary reactions in the oxidation of alkenes , 1981 .

[8]  B. K. Carpenter Ring Opening of Dioxiranylmethyl Radical: A Caution on the Use of G2-Type ab Initio MO Methods for Mechanistic Analysis , 2001 .

[9]  H. Hamann,et al.  High pressure range of addition reactions of HO. II. Temperature and pressure dependence of the reaction HO+CO⇔HOCO→H+CO2 , 1996 .

[10]  C. P. Lazzara,et al.  Molecular beam mass spectrometry applied to determining the kinetics of reactions in flames. I. Empirical characterization of flame perturbation by molecular beam sampling probes , 1974 .

[11]  D. Gutman,et al.  Kinetics of polyatomic free radicals produced by laser photolysis. 3. Reaction of vinyl radicals with molecular oxygen , 1984 .

[12]  Stephen J. Klippenstein,et al.  A THEORETICAL ANALYSIS OF THE REACTION BETWEEN ETHYL AND MOLECULAR OXYGEN , 2000 .

[13]  P. Dagaut,et al.  A Kinetic Modeling Study of Propene Oxidation in JSR and Flame , 1992 .

[14]  D. B. Smith,et al.  A comparative study of methane and ethane flame chemistry by experiment and detailed modelling , 1988 .

[15]  A. Dean,et al.  Chemical activation analysis of the reaction of ethyl radical with oxygen , 1990 .

[16]  K. Morokuma,et al.  Ab Initio and RRKM Calculations for Multichannel Rate Constants of the C2H3 + O2 Reaction , 1996 .

[17]  Stanislav I. Stoliarov,et al.  Kinetics of the C2H3 + H2 ⇄ H + C2H4 and CH3 + H2 ⇄ H + CH4 Reactions , 1996 .

[18]  Wing Tsang,et al.  Chemical Kinetic Data Base for Combustion Chemistry. Part I. Methane and Related Compounds , 1986 .

[19]  Y. Hidaka,et al.  Shock-tube and modeling study of ethylene pyrolysis and oxidation , 1999 .

[20]  James A. Miller,et al.  The effect of allene addition on the structure of a rich C2H2/O2/Ar flame☆ , 1996 .

[21]  I. R. Slagle,et al.  Kinetics of the reaction of vinyl radical with molecular oxygen , 1995 .

[22]  Michael Louis Vermeersch A variable pressure flow reactor for chemical kinetic studies: Hydrogen, methane and butane oxidation at 1 to 10 atmospheres and 880 to 1,040 K , 1991 .

[23]  P. R. Westmoreland,et al.  Measured Flame Structure and Kinetics in a Fuel-Rich Ethylene Flame 1 1 This report was prepared as , 1998 .

[24]  Robert J. Kee,et al.  PREMIX :A F ORTRAN Program for Modeling Steady Laminar One-Dimensional Premixed Flames , 1998 .

[25]  Raymond W. Walker,et al.  Evaluated kinetic data for combustion modelling supplement I , 1994 .

[26]  Richard A. Yetter,et al.  Comparison of global and local sensitivity techniques for rate constants determined using complex reaction mechanisms , 2001 .

[27]  M. Frenklach,et al.  A detailed kinetic modeling study of aromatics formation in laminar premixed acetylene and ethylene flames , 1997 .

[28]  Simone Hochgreb,et al.  A comprehensive study on CH2O oxidation kinetics , 1992 .

[29]  Richard A. Yetter,et al.  Flow Reactor Studies of Carbon Monoxide/Hydrogen/ Oxygen Kinetics , 1991 .