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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 >Wall effects on the velocities of a single sphere settling in a stagnant and counter-current fluid and rising in a co-current fluid
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Wall effects on the velocities of a single sphere settling in a stagnant and counter-current fluid and rising in a co-current fluid

机译:壁对单个球体在停滞和逆流流体中沉降并在并流流体中上升的速度的影响

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Experimental results were obtained on the steady settling of spheres in quiescent media in a range of cylindrical tubes to ascertain the wall effects over a relatively wide range of Reynolds number values. For practical considerations, the retardation effect is important when the ratio of the particle diameter to the tube diameter (λ) is higher than about 0.05. A new empirical correlation is presented which covers a Reynolds number range Re = 53-15,100 and a particle to tube diameter ratio λ<0.88. The absolute mean deviation between the experimental data and the presented correlation was 1.9%. The well-known correlations of Newton, Munroe and Di Felice agree with the presented data reasonably well. For steady settling of spheres in a counter-current water flow, the slip velocity remains practically the same as in quiescent media. However, for rising spheres in a co-current water flow, the slip velocity decreases with increasing co-current water velocity, i.e., the wall factor decreases with increasing co-current water velocity. Consequently, the drag coefficient for rising particles in co-current water flow increases with increasing water velocity.
机译:通过在一定范围的圆柱管中的静态介质中稳定地沉降球体,以确定雷诺数值的相对较大范围内的壁效应,获得了实验结果。出于实际考虑,当粒径与管径之比(λ)大于约0.05时,延迟效果很重要。提出了一种新的经验相关性,该相关性涵盖了雷诺数范围Re = 53-15,100和粒子与管径比λ<0.88。实验数据与给出的相关性之间的绝对平均偏差为1.9%。牛顿,芒罗和迪菲利斯的众所周知的相关性与给出的数据相当吻合。为了使球体在逆流水流中稳定沉降,滑移速度实际上保持与静态介质相同。但是,对于并流水流中的上升球体,滑移速度随着并流水速的增加而减小,即壁因子随并流水速的增加而减小。因此,并流水流中上升颗粒的阻力系数随水速的增加而增加。

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