A kinetic modelling study of ammonia oxidation in a flow reactor

被引:0
|
作者
Lin, Jianting [1 ,2 ]
Zhang, Zhezi [1 ]
Holden, Samuel Ronald [1 ]
Wang, Huanran [1 ,2 ]
Zhang, Yuanyuan [1 ,3 ]
Li, Xianchun [1 ,2 ]
Cheng, Fangqin [1 ,3 ]
Zhang, Dongke [1 ]
机构
[1] Centre for Energy (M473), The University of Western Australia, 35 Stirling Highway, Crawley, WA,6009, Australia
[2] School of Chemical Engineering, University of Science and Technology Liaoning, Anshan,114051, China
[3] State Environmental Protection Key Laboratory of Efficient Utilization Technology of Coal Waste Resources, Shanxi University, Taiyuan,030006, China
关键词
Kinetic parameters;
D O I
10.1016/j.ijhydene.2024.12.214
中图分类号
学科分类号
摘要
Kinetic modelling of ammonia oxidation in plug flow was performed using Ansys Chemkin-Pro over a range of initial ammonia concentration (2–10%), temperature (1000–1400K) and equivalence ratio (0.8–1.0), to seek mechanistic interpretation of peculiar but interesting phenomena observed experimentally in a flow reactor configuration. where an increase in ammonia initial concentration led to increased ammonia conversion for temperatures up to 1165K, above which the trend was reversed as observed in the experimentation. The simulated results satisfactorily replicated the trends in the experimental measurements and identified key radicals and reaction pathways responsible for the peculiar behaviour. Furthermore, the nitric oxide concentration in the reactor exit stream for oxidation of 10% initial ammonia concentration sharply increased from 0 ppm at 1325K to 497 ppm at 1350K, then decreased with further increasing temperature, which can be attributed to the greater exothermicity of oxidation at higher ammonia initial concentrations. © 2024 The Authors
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页码:429 / 438
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