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EXPERIMENTAL STUDY ON CONVECTIVE COEFFICIENTS IN A SLURRY BUBBLE COLUMN

机译:浆状气泡柱对流系数的实验研究

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The main objective of this work was to determine the influence of gas and slurry velocities and solid load concentration on experimental convective heat transfer coefficients (h), for a three-phase suspension in cross flow around a square in-line tube array. Experiments were performed in a pilot scale equipment conformed by a column of square cross section. In the central part of this equipment there is a bank of 49 tubes with a S_T=S_L=4.4 cm. The system used was air, tap water and sieved sand at average particle diameter of 505 μm. The velocities of liquid and gas phases were varied from 0.28 to 0.60 cm/s and from 1.36 to 2.45 cm/s, respectively; and the solid load concentration from 0 to 30% w/w. The results allow to conclude that h for a three-phase system is larger than either for a two-phase or one-phase system. The presence of solid phase enhances the heat transfer, however, this increase is less evident for high values of solid concentration.
机译:这项工作的主要目的是确定在方形串联管阵列周围的交叉流动中的三相悬浮液,气体和浆料的速度以及固体负载浓度对实验对流换热系数(h)的影响。实验在中型规模的设备中进行,该设备由方形截面的圆柱组成。在该设备的中央部分,有一排49个试管,其S_T = S_L = 4.4 cm。使用的系统是空气,自来水和筛分的沙子,平均粒径为505μm。液相和气相的速度分别从0.28至0.60 cm / s和1.36至2.45 cm / s变化。固体负载浓度为0至30%w / w。结果可以得出结论,三相系统的h大于两相系统或单相系统的h。固相的存在增强了热传递,但是,对于高浓度的固体浓度,这种增加并不明显。

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