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Process simulation of formation and emission of NO and N _2O during coal decoupling combustion in a circulating fluidized bed combustor using Aspen Plus

机译:Aspen Plus在循环流化床燃烧室煤解耦燃烧中NO和N _2O形成与排放过程模拟。

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摘要

A process simulation model of coal decoupling combustion in a 30kW circulating fluidized bed (CFB) combustor has been developed for predicting NO and N _2O emissions based on the built-in modules/blocks provided by Aspen Plus software as well as the external subroutines from FORTRAN compiler. The gas-solid hydrodynamics in the decoupling CFB combustor and macro-chemical reaction kinetics of coal combustion have been included in the process simulation model of CFB coal decoupling combustion. The profiles of average bed temperature and concentrations of gas components along the CFB riser height can be successfully predicted by the developed process simulation model. The effects of excess air percentage, first stage stoichiometry, and the introduction position of secondary air on concentrations of the emitted gaseous components, especially concentrations of NO and N _2O can be simulated by the developed process simulation model. The contribution ratios of all relevant combustion reactions to emissions of NO and N _2O can be quantitatively predicted. A good agreement between the simulated and measured results can be obtained during CFB coal decoupling combustion process under a large variation range of the CFB operation conditions.
机译:基于Aspen Plus软件提供的内置模块/模块以及FORTRAN的外部子程序,已开发出了30kW循环流化床(CFB)燃烧器中煤解耦燃烧的过程模拟模型,用于预测NO和N _2O排放。编译器。 CFB煤解耦燃烧过程模拟模型中已经包括了CFB分离器燃烧室中的气固流体动力学和煤燃烧的宏观化学反应动力学。通过开发的过程模拟模型可以成功预测沿CFB提升管高度的平均床层温度和气体成分浓度。可以通过开发的过程模拟模型来模拟过量空气百分比,第一阶段化学计量和二次空气的引入位置对排放的气态组分浓度(尤其是NO和N _2O浓度)的影响。可以定量预测所有相关燃烧反应对NO和N _2O排放的贡献率。在CFB煤解耦燃烧过程中,CFB工况变化范围较大的情况下,模拟结果与实测结果吻合良好。

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