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Heat transfer calculation methods in three-dimensional CFD model for pulverized coal-fired boilers

机译:三维CFD模型中的传热计算方法粉煤燃烧锅炉

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Computational fluid dynamics (CFD) has been used extensively to study the combustion characteristics of coalfired boilers. However, very limited of the boiler CFD studies were used to quantitatively predict the heat transfer distributions in practical boiler applications. This paper presents a systematic description on the heat transfer calculation methods in three-dimensional CH) model for coal-fired boilers. The primary objective is to provide a set of heat transfer submodels that can be easily employed to solve and analyze large scale practical boiler problems. All types of boiler heating surfaces are considered with particular focus on the heat transfer calculation of furnace water wall. It is implemented in the CFD model in terms of a thermal boundary condition (B.C.) describing the energy balance between the boiler's fire side heat transfer and water side heat absorption. The physical significance of the associated B.C. parameters and their accurate prescription are discussed in detail in this paper. It is found that furnace wall heat transfer is largely affected by the wall ash deposit conditions such that the heat transfer coefficient of furnace wall can be determined based on the thermal properties of ash. Although ash thickness may vary dramatically over furnace wall and is extremely difficult to predict, its thermal conductance was found to only vary within a small range for normally operated coal-fired boilers. Establishing the connection between the thermal conductance of wall ash deposits and the heat transfer calculation of furnace wall bypasses the tremendous difficulty and uncertainty incurred in predicting the ash thickness, and thereby, greatly simplifies the wall heat transfer calculation process. The heat transfer calculation methods introduced in this study embody the key physics associated with boiler's heat transfer process while making a reasonable balance between the level of model complexity and their applicability to practical boiler problems. In this paper they are illustrated and validated on a 330 MW tangentially-fired subcritical boiler. The results show that the predicted boiler heat transfer distributions are in close agreement with the boiler's operating data.
机译:计算流体动力学(CFD)已广泛用于研究煤火锅炉的燃烧特性。然而,使用锅炉CFD研究的非常有限度用于定量预测实际锅炉应用中的传热分布。本文提出了关于燃煤锅炉三维CH)模型的传热计算方法的系统描述。主要目标是提供一组热传递子模型,可以很容易地用于解决和分析大规模的实际锅炉问题。所有类型的锅炉加热表面都被认为特别侧重于炉水壁的传热计算。它在CFD模型中以热边界条件(B.C.)在描述锅炉的火侧传热和水侧吸热之间的能量平衡方面实现。相关的B.C的物理意义。本文详细讨论了参数及其准确的处方。发现炉壁传热主要受壁灰沉积条件的影响,使得可以基于灰的热性能来确定炉壁的传热系数。虽然炉壁的灰分厚度可能会剧烈变化并且极难预测,但其热传导被发现仅在通常操作的燃煤锅炉的少量范围内变化。建立壁灰沉积物的导热率与炉壁的传热计算之间的连接绕过预测灰厚度的巨大难度和不确定性,从而大大简化了壁传热计算过程。本研究中介绍的传热计算方法体现了与锅炉的传热过程相关的关键物理,同时在模型复杂性水平与其对实际锅炉问题的适用性之间进行合理平衡。在本文中,它们在330 MW切向次临界锅炉上进行了说明和验证。结果表明,预测的锅炉传热分布与锅炉的操作数据密切一致。

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