Structure of Laminar Permanently Blue, Opposed-Jet Ethylene-Fueled Diffusion Flames. Appendix E

Abstract The structure and state relationships of laminar soot-free (permanently blue) ethylene-fueled diffusion flames at various strain rates were studied both experimentally and computationally using an opposed-jet configuration. Measurements of gas velocities, temperatures, and compositions were carried out along the stagnation stream line. Corresponding predictions of flame structure were obtained, based on numerical simulations using several contemporary reaction mechanisms for methane oxidation. Flame conditions studied included ethylene-fueled opposed-jet diffusion flames having stoichiometric mixture fractions of 0.7 with measurements involving strain rates of 60–240 s −1 and predictions involving strain rates of 0–1140 s −1 at normal temperature and pressure. It was found that measured major gas species concentrations and temperature distributions were in reasonably good agreement with predictions using mechanisms due to GRI-Mech (Version 1.2, 1995) and Peters (1993) and that effects of preferential diffusion significantly influence flame structure even when reactant mass diffusivities are similar. Oxygen leakage to fuel-rich conditions and carbon monoxide leakage to fuel-lean conditions both increased as strain rates increased. Furthermore, increased strain rates caused increased fuel concentrations near the flame sheet, decreased peak gas temperatures, and decreased concentrations of carbon dioxide and water vapor throughout the flames. State relationships for major gas species and gas temperatures were found to exist over a broad range of strain rates, providing potential for significant computational simplifications for modeling purposes in some instances.

[1]  W. Jones,et al.  The Calculation of the Structure of Laminar Counterflow Diffusion Flames Using a Global Reaction Mechanism , 1988 .

[2]  Robert J. Kee,et al.  The computation of stretched laminar methane-air diffusion flames using a reduced four-step mechanism , 1987 .

[3]  Arthur Henry Lefebvre,et al.  Gas turbine combustor design problems , 1980 .

[4]  C. Sung,et al.  Further studies on effects of thermophoresis on seeding particles in LDV measurements of strained flames , 1996 .

[5]  G. Faeth,et al.  Hydrodynamic Suppression of Soot Emissions in Laminar Diffusion Flames , 1996 .

[6]  N. Peters,et al.  Reduced Kinetic Mechanisms for Applications in Combustion Systems , 1993 .

[7]  G. Faeth,et al.  Generalized state relationships for scalar properties in nonpremixed hydrocarbon/air flames , 1990 .

[8]  C. Sung,et al.  On the structure of nonsooting counterflow ethylene and acetylene diffusion flames , 1996 .

[9]  G. Faeth,et al.  Effects of Hydrodynamics on Soot Formation in Laminar Opposed-Jet Diffusion Flames , 1996 .

[10]  K. M. Leung,et al.  Detailed Kinetic Modeling of C, - C, Alkane Diffusion Flames , 1995 .

[11]  R. Axelbaum,et al.  The Effect of Flame Structure on Soot-Particle Inception in Diffusion Flames , 1995 .

[12]  G. Faeth,et al.  Soot formation in hydrocarbon/air laminar jet diffusion flames☆ , 1996 .

[13]  Robert J. Santoro,et al.  Soot inception in a methane/air diffusion flame as characterized by detailed species profiles , 1985 .

[14]  Robert W. Bilger,et al.  Reaction rates in diffusion flames , 1977 .

[15]  Kuang C. Lin,et al.  Soot nucleation and growth in acetylene air laminar coflowing jet diffusion flames , 1996 .

[16]  Reginald E. Mitchell,et al.  Experimental and numerical investigation of confined laminar diffusion flames , 1980 .