An experimental and numerical investigation of the catalytic-rich/gaseous-lean combustion of H2/CO/air mixtures at 8 bar

• Published in: Proceedings of the Combustion Institute Vol. 38; no. 4; pp. 5443 - 5451
• Main Authors: Bolaños-Chaverri, Felipe, Mantzaras, John, Griffin, Timothy, Bombach, Rolf, Winkler, Dieter
• Format: Journal Article
• Language: English
• Published: Elsevier Inc 2021
• Subjects: Catalytic-rich/gaseous-lean gas-turbine combustion; Homogeneous ignition; NOx reduction with increasing fuel pre-conversion; Syngas and hydrogen hybrid hetero-/homogeneous combustion; Two-sided turbulent diffusion flames; Catalytic-rich/gaseous-lean gas-turbine combustion; Syngas and hydrogen hybrid hetero-/homogeneous combustion; NOx reduction with increasing fuel pre-conversion; Homogeneous ignition; Two-sided turbulent diffusion flames
• ISSN: 1540-7489; 1873-2704
• DOI: 10.1016/j.proci.2020.06.149

The catalytic-rich/gaseous-lean (R/L) combustion concept was investigated experimentally and numerically for syngas fuels with H2:CO volumetric ratios 1:0, 4:1 and 1:2, catalytic-rich stoichiometries φrich = 2–10 (including operation without air), pressure of 8 bar and air preheat of 673 K. Experiments were performed in a subscale R/L burner with optical access to both catalytic-rich and gaseous-lean stages. OH-PLIF monitored the turbulent combustion in the gaseous-lean stage, OH*-chemiluminescence assessed the propensity for homogeneous ignition in the catalytic-rich stage, and exhaust gas analysis provided the NOx and CO emissions. Two-dimensional simulations were carried out for both stages, while a 1-D opposed-jet code modeled the NOx emissions. The exothermicity of the heterogeneous reactions promoted homogeneous ignition and flame anchoring in the upstream parts of the catalytic-rich stage and allowed for complete consumption of the deficient O2 reactant, a process that could not be achieved by the catalytic pathway alone due to transport limitations. Homogeneous combustion in the catalytic-rich stage was beneficial for attaining the highest possible fuel pre-conversion. The catalyst not only initiated gaseous combustion but also mitigated potential NOx emissions from the catalytic-rich stage at the highest pre-conversions (lowest φrich) and highest CO-content mixtures. Two-sided diffusion flames were established in the gaseous-lean stage due to the recirculation of O2-rich combustion products, which was advantageous for the burner compactness. It was shown that cardinal to the R/L concept was the fact that a decreasing φrich led to an increased heat transfer from the catalytic-rich stage to the bypass air, which reduced the enthalpy in the fuel stream of the gaseous-lean stage and thus lowered the peak flame temperatures (by 400 K for H2:CO = 1:0). The reduction in flame temperatures with decreasing φrich led to a six-fold drop in NOx emissions, while CO emissions were less than 5 ppmv.