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Heat Transfer Coefficient at Minimum Fluidization Velocity for Gas-Solid Fluidized Beds

机译:气固流化床最小流化速度的传热系数

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A semi-empirical correlation for heat transfer coefficients between dense gas-solid quiescent fluidized beds and surfaces is presented. Surface heat transfer coefficients at the minimum fluidization condition were measured using a local heat transfer probe in a 5 cm × 30 cm transparent walled, fluidized bed. The initial bed height was held constant at 17.0 cm in all cases. The powders tested were glass, sand, graphite, polypropylene and aluminum with sizes in the range from 25 μm to 1789 μm. The fluidizing medium used was air with the bed operated at atmospheric temperature and pressure. Two different distributor plates were utilized during the experiments, i.e., sintered and perforated distributor plate. Time averaged, local heat transfer coefficients acquired were averaged over repeated measurements at different times.
机译:呈现了致密气体固体静态流化床和表面之间的传热系数的半经验相关性。使用局部传热探针在5cm×30cm透明的壁式的流化床中使用局部传热探针测量最小流化条件下的表面传热系数。在所有情况下,初始床高度在17.0厘米处保持恒定。测试的粉末是玻璃,砂,石墨,聚丙烯和铝,尺寸在25μm至1789μm的范围内。使用的流化介质是空气,床在大气温度和压力下操作。在实验期间使用两块不同的分配器板,即烧结和穿孔分配板。时间平均,获取的局部传热系数在不同时间的重复测量上平均。

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