高级检索

    300 MW四角切圆锅炉掺氨燃烧CFD模拟研究

    CFD Simulation of ammonia co-firing in a 300-MW tangentially fired boiler

    • 摘要: NH3作为无碳富氢燃料,将其与煤粉直接在燃煤机组中掺烧是实现源头减碳的有效措施。本文以某300 MW四角切圆燃煤锅炉为研究对象,构建了耦合NH3/煤混燃、颗粒动力学与NOx生成路径的CFD模型,探究了掺烧位置和掺烧比例对氨/煤混燃和氮氧化物排放特性的影响。该模型采用改进的realizable k–ε湍流模型、DO辐射模型和WSGGM气体辐射模型,综合考虑煤粉热解、焦炭燃烧与氨热解/氧化过程。采用一维沉降炉实验数据对该模型进行了验证。随后,对全尺寸锅炉的模拟结果表明掺烧NH3后炉膛尾部烟气温度略有下降,且随着掺烧位置下移,NH3逃逸浓度和NO排放浓度均显著降低。相比在C层+E层掺烧氨气,在B层+C层掺烧氨气能够在相同掺氨比例有效控制NO排放,降低氨逃逸。研究成果可为燃煤机组氨燃料掺烧的工况优化与低氮燃烧控制提供理论支撑。

       

      Abstract: Ammonia (NH3), a carbon-free and hydrogen-rich fuel, can be co-fired with pulverized coal in conventional coal-fired units to reduce carbon emissions at the flame source. In this study, a 300 MW tangentially fired boiler is taken as the reference case. A three-dimensional CFD model coupling NH3/coal co-combustion, particle dynamics, and NOx formation pathways is developed to investigate how the co-firing elevation and co-firing ratio affect combustion and NOx emission characteristics. The model employs an improved realizable k–ε turbulence closure, the discrete ordinates (DO) radiation model, and the weighted-sum-of-gray-gases model (WSGGM) for gas radiative properties, and consistently accounts for coal devolatilization, char oxidation, and ammonia pyrolysis/oxidation. The modeling framework is validated against one-dimensional drop-tube furnace experiments. Subsequently, full-scale boiler simulations are performed. The results indicate that NH3 co-firing slightly lowers the flue-gas temperature near the furnace exit. Moreover, as the co-firing location is shifted to lower elevations, both NH3 slip and NO emissions decrease significantly. Under the same NH3 co-firing ratio, the B+C dual-layer configuration achieves more effective NO control and reduces NH3 slip compared with the C+E arrangement. These findings provide theoretical guidance for operating-condition optimization and low-NOx combustion control in coal-fired units co-firing ammonia.

       

    /

    返回文章
    返回