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Performance prediction of a circulating fluidized bed boiler by heat exchangers block simulation at varying load conditions

机译:变负荷条件下换热器块模拟对循环流化床锅炉性能的预测

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摘要

We propose a simplified mathematical model to describe and to predict the performance of a circulating fluidized bed boiler under varying loads. The model is a systematic approach for modeling a circulating fluidized bed boiler, which is a combination of zero-dimensional energy and mass balance model of heat exchanger blocks. Blocks of heat exchangers are integrated with the air-gas side, the water-steam side, and the solids side. Validation has been carried out by comparing calculated results with experimental data of a pilot-scale circulating fluidized bed boiler. In order to expand throughout the actual operating range, a correlation between the solids circulation rate and the superficial velocity was drawn, and overall heat transfer rates at varying loads were interpreted as representative heat transfer coefficients related with the suspension density. Boiler efficiencies and temperatures were predicted at the loads. Finally, partial load behavior of the boiler was investigated by characterizing performance parameters. This simulation model is hoped to improve the understanding of the boiler performance when operation parameters are selected.
机译:我们提出了一个简化的数学模型来描述和预测在变化负荷下循环流化床锅炉的性能。该模型是对循环流化床锅炉进行建模的系统方法,它是零维能量和换热器块的质量平衡模型的组合。热交换器的块与空气-气体侧,水-蒸汽侧和固体侧集成在一起。通过将计算结果与中试规模循环流化床锅炉的实验数据进行比较来进行验证。为了在整个实际工作范围内扩展,绘制了固体循环速率和表观速度之间的关系,并将在不同载荷下的总传热速率解释为与悬浮液密度有关的代表性传热系数。在负荷下预测了锅炉的效率和温度。最后,通过表征性能参数研究了锅炉的部分负荷行为。当选择运行参数时,该仿真模型有望增进对锅炉性能的了解。

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