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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Study on the particle distribution of a two-pass circulating fluidized bed evaporator with baffle
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Study on the particle distribution of a two-pass circulating fluidized bed evaporator with baffle

机译:带有挡板的两程循环流化床蒸发器的颗粒分布研究

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A liquid solid circulating fluidized bed evaporator is designed and built to enhance the heat transfer and prevent and remove fouling in a two-pass evaporator. The effects of the operating parameters, such as circulation flow rate, amount of added particles, and height of the baffles, on the fluidization and distribution of solid particles in the two-pass circulating fluidized bed evaporator are systematically investigated using the charge-coupled device image measurement and acquisition system. Polyoxymethylene particle is used in the experiment. The circulation flow rate ranges from 10.66 m(3)/h to 19.14 m(3)/h, the amount of added particles changes from 0.5% to 2.0%, and the height of the baffles are 0.073, 0.1, 0.15, and 0.2 m. The particle distribution in the up-flow bed is uniform, whereas that in the down-flow bed is uneven. This study primarily investigates the particle distribution in the down-flow bed, which becomes increasingly uniform when the circulation flow rate is increased or when the height of the baffle is reduced, except when the baffle height is 0.2 m. When the circulation flow rate is low, the distribution becomes increasingly uneven as more particles are added. However, when the circulation flow rate is high, the amount of added particles has little influence on the particle distribution. Finally, two phase diagrams are established to show the optimal range of the operating parameters. These findings may serve as a valuable reference for the industrial application of the fluidized bed heat transfer enhancement and fouling prevention technology in multi-pass evaporators with baffles. (C) 2016 Elsevier B.V. All rights reserved.
机译:设计并制造了液固循环流化床蒸发器,以增强热传递并防止和消除两程蒸发器中的积垢。使用电荷耦合装置系统地研究了运行参数(例如循环流量,添加的颗粒数量和挡板的高度)对两遍循环流化床蒸发器中固体颗粒的流化和分布的影响图像测量和采集系统。实验中使用了聚甲醛颗粒。循环流量从10.66 m(3)/ h到19.14 m(3)/ h,添加的颗粒量从0.5%更改为2.0%,挡板的高度为0.073、0.1、0.15和0.2米上流床中的颗粒分布是均匀的,而下流床中的颗粒分布是不均匀的。这项研究主要研究下流床中的颗粒分布,当循环流量增加或折流板高度降低时,除流板高度为0.2 m时,颗粒分布变得越来越均匀。当循环流量低时,随着添加更多的颗粒,分布变得越来越不均匀。然而,当循环流速高时,添加的颗粒量对颗粒分布几乎没有影响。最后,建立了两个相图以显示操作参数的最佳范围。这些发现可为流化床传热和防垢技术在带挡板的多程蒸发器中的工业应用提供有价值的参考。 (C)2016 Elsevier B.V.保留所有权利。

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