“…Moreover, the flame temperature decreased downstream due to the low reactivity and radiative heat losses. Thus, the vigorously burning reaction kernel sustained stationary combustion processes in the flow in the vicinity of the burner rim (flame attachment) and held the trailing diffusion flame zone downstream, as described in detail elsewhere [18][19][20][21]. The heat-release rate, oxygen consumption rate, velocity, temperature, oxygen mole fraction, local equivalence ratio, and mixture fraction at the reaction kernel wereq k = 177 J/cm 3 s, −ω O 2 ,k = 0.000488 mol/cm 3 s, |v k | = 0.313 m/s, T k = 1478 K, X O 2 ,k = 0.050, φ local,k = 0.61, and ξ k = 0.048, respectively.…”