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Heat-Transfer Model of the Rotary Ash Cooler Used in Circulating Fluidized-Bed Boilers

机译:循环流化床锅炉用旋转灰冷却器的传热模型

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摘要

Rotary ash coolers are widely used in circulating fluidized-bed (CFB) boilers for bottom ash cooling, attributed to their high efficiency and excellent reliability. However, they are mostly still designed empirically, and one of the most important reasons is due to the lack of an appropriate heat-transfer model. In this paper, a comprehensive heat-transfer model was developed and the model parameters were determined by experiments. Against the literature findings, the experimental results showed that the dimensionless thickness of gas film used in the thermal contact resistance calculation is different for different ash particle sizes. The new model was further applied to predict the heat-transfer characteristics for a rotary ash cooler used in a commercial 300 MWe CFB boiler. It was found that the heat-transfer coefficients of ash-air and air-water are close but much lower than that of ash-water, indicating that the heat transfer of ash-water dominates in the total heat transfer. In addition, the ash temperature decreases rapidly in the first half of the roller when the heating surfaces are uniformly arranged along the axis, and the outlet temperatures of ash and cooling water vary approximately linearly with the ash flow rate. In comparison to the industrial data, the model well predicts the axial distributions of the temperature and heat-transfer coefficient and the heat-transfer amount with engineering acceptable accuracy. On the basis of the modeling results, it is suggested that the roller could be more compact by rearranging more heating surfaces into the first half of it.
机译:旋转灰冷却器因其高效和出色的可靠性而被广泛用于循环流化床(CFB)锅炉的底部灰冷却。但是,它们大多仍是凭经验设计的,最重要的原因之一是由于缺乏合适的传热模型。本文建立了一个综合的传热模型,并通过实验确定了模型参数。与文献发现相反,实验结果表明,对于不同的灰分粒径,用于热接触电阻计算的气膜无量纲厚度是不同的。新模型进一步应用于预测商用300 MWe CFB锅炉中使用的旋转式灰冷却器的传热特性。研究发现,灰空气与空气的传热系数相近,但比灰水的传热系数低得多,这表明灰水的传热在总传热中占主导地位。另外,当加热表面沿轴线均匀布置时,灰分温度在辊的前半部分迅速降低,并且灰分和冷却水的出口温度大致随灰分流速线性变化。与工业数据相比,该模型能够以工程上可接受的精度很好地预测温度和传热系数以及传热量的轴向分布。根据建模结果,建议通过将更多的加热表面重新布置到辊的前半部分中,可以使辊更加紧凑。

著录项

  • 来源
    《Energy & fuels》 |2010年第maraaapr期|p.2570-2575|共6页
  • 作者单位

    Key Laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Thermal Engineering,Tsinghua University, Beijing 100084, People's Republic of China;

    rnKey Laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Thermal Engineering,Tsinghua University, Beijing 100084, People's Republic of China;

    rnKey Laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Thermal Engineering,Tsinghua University, Beijing 100084, People's Republic of China;

    rnKey Laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Thermal Engineering,Tsinghua University, Beijing 100084, People's Republic of China;

    rnKey Laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Thermal Engineering,Tsinghua University, Beijing 100084, People's Republic of China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    A: area (m~2); c_p: specific heat capacity (J kg~(-1) ℃~(-1)); D,d; diameter (m); h: heat-transfer coefficient (W m~(-2)℃~(-1); L: length (m); et al;

    机译:A:面积(m〜2);c_p:比热容(J kg〜(-1)℃〜(-1));D;d;直径(米);h:传热系数(W m〜(-2)℃〜(-1);L:长度(m);等;

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