计算流体力学
燃烧
环境科学
核工程
比例(比率)
废物管理
工程类
工艺工程
材料科学
航空航天工程
化学
物理
有机化学
量子力学
作者
Jorge Esteban Colman Lerner,Micaela Belen Del Sole,Franco Dubois,Jorge Enrique Sambeth,Atilio Andrés Porta,Miguel Andrés Peluso,Érica Yanina Sánchez
标识
DOI:10.1016/j.cherd.2024.06.009
摘要
This study presents initial findings from simulating a laboratory-scale monolithic reactor for VOC (Volatile Organic Compounds) combustion. The reactor, made of stainless steel, measures 45 cm (height) and 2.3 cm (diameter). It contains a catalyst supported by a ceramic structure, tested for toluene combustion. Using ANSYS CFD simulation software, fluid dynamics inside the reactor were accurately modeled. The simulation then focused on a specific channel within the monolith, based on comprehensive reactor data. The final stage simulated toluene combustion using the Mars-Van Krevelen mechanism. ANSYS CFD results for toluene combustion, measured by CO2 yield, closely matched experimental outcomes. The average CO2 yield of 1.16 showed a strong alignment between the simulation and the experiment. ANSYS CFD not only aids in obtaining hard-to-gather information about fluid dynamics and chemical reactions but also enables simulations of geometry changes and catalyst types once validated. It also supports exploring more complex reactions.
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