Flame attachment and kinetics studies of laminar coflow CO/H-2 diffusion flames burning in O-2/H2O
Flame attachment and kinetics studies of laminar coflow CO/H-2 diffusion flames burning in O-2/H2O
复制标题
O-2/H2O 中层流 CO/H-2 扩散火焰燃烧的火焰附着和动力学研究
DOI:
10.1016/j.combustflame.2018.06.003
复制
发表时间:
2018
影响因子:
4.4
通讯作者:
Shaozeng Sun
中科院分区:
文献类型:
--
作者:
Huanhuan Xu;Fengshan Liu;Shaozeng Sun
In this study, experimental and numerical investigations were conducted to study the attachment and oxidation process of laminar CO/H2diffusion flames burning in coflow O2/H2O at 1 atm with an inlet temperature of 400 K for both the fuel and oxidizer streams. The effects of fuel composition were investigated by considering a wide range of CO/H2mole ratio from 95%CO–5%H2to 5%CO–95%H2and also pure H2. The oxidizer has a fixed composition of 75%H2O–25%O2. The measured flame heights determined by OH*-chemiluminescence images were used to validate the flame model adopted in this work. Through numerical simulations using a two-dimensional flame code with the preheating effect, detailed reaction mechanism, and detailed thermal and transport properties, the details of flame attachment and flame structure were obtained and analysed. Although both CO and H2diffuse over the burner rim and move upstream into the oxidizer stream, the attachment point of a H2-rich syngas flame is further upstream below the burner exit than that of a CO-rich flame. This is attributed to the high reactivity of H2through reaction OH + H2= H + H2O and the high diffusivity of H2. Reaction pathways for syngas burning in the oxidizer of O2/H2O based on a detailed kinetics analysis were revealed, not only inside the fuel tube and above the fuel exit, but also near the flame sheet and in the flame attachment zone. Significant consumption of H2O was observed in the flame core due to the reverse reaction of OH + H2= H + H2O which shifts to proceed forward outside the flame in the radial direction also at higher streamwise locations if H2in the fuel flow is rich, oxidizing unburned H2to H2O.