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首页> 外文期刊>Applied thermal engineering: Design, processes, equipment, economics >An investigation on the heat transfer model for immersed horizontal tube bundles in a pressurized fluidized bed
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An investigation on the heat transfer model for immersed horizontal tube bundles in a pressurized fluidized bed

机译:加压流化床中浸渍水平管束传热模型的研究

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摘要

In order to predict the heat transfer coefficient between the immersed horizontal tube bundles and the pressurized fluidized bed, different types of heat transfer models research process for the horizontal tube surface are presented. The accuracy of these models has been analyzed with the data of pressurized experiments, which indicates the limitation of these models in the application of pressurized fluidized bed. A new semi-empirical emulsion renewal model is proposed which takes the advantages of thermal contact resistance model and heat penetration model into account and modifies the correlation for gas convection heat transfer calculation at elevated pressure. The total experimentally reported 89 points from different sources with pressures ranging 0.1-1.6 MPa, particle diameter 240-700 mu m are predicted within the absolute average deviation of 10.25%, which is much lower compared with other models for the same data. The satisfactory description for the influence rule of bed pressure, temperature, gas velocity and particle diameter on the heat transfer coefficient was also given from the model.
机译:为了预测浸渍水平管束和加压流化床之间的传热系数,提出了水平管表面的不同类型的传热模型研究过程。通过加压实验的数据分析了这些模型的准确性,这表明在加压流化床中的应用中的限制。提出了一种新的半经验乳液更新模型,其考虑了热接触电阻模型和热渗透模型的优点,并修改了升高压力下气体对流传热计算的相关性。通过实验总报告的来自不同来源的89点,压力范围为0.1-1.6MPa,粒径240-700μm在10.25%的绝对平均偏差范围内预测,与相同数据的其他模型相比远低得多。还给出了模型的床压力,温度,气体速度和粒径对传热系数的影响规律的令人满意的描述。

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