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Effect of interstitial air pressure and voidage during the spouting of fluidized cohesive powder

机译:流态化凝聚粉喷出过程中间隙气压和空隙率的影响

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We experimentally investigated the spouting of fluidized cohesive powder bed of the soft wheat flour through a circular orifice of 4mm at the bottom of vessel, where the mean diameter is 46μm and the powder density is 1493kg/m3. Air is introduced at the three ways as the following, (1) only at the top, (2) only at the bottom, (3) at the top and bottom of bed where the flow rate of air is changed. The cumulative mass of powder through an orifice, the interstitial air pressure at the top of bed and the height of bed has been measured. The voidage of bed is estimated by the remained mass of powder in the vessel, the powder density, the height of bed and the inside diameter of vessel. We found that the steady flow of the fluidized cohesive powder as well as mass flow region is obtained when the same flow rate of air is simultaneously introduced at the top and bottom of the bed. Then, its tendency showed that the interstitial air pressure and voidage increases with decreasing the height of bed. And then, we confirmed that the mass flow rate of powder is in proportion to a square root of the voidage and the interstitial air pressure during the gush of cohesive powder.
机译:我们通过容器底部4mm的圆形孔口,对软质小麦粉的流化粘性粉末床进行了喷射实验,该孔的平均直径为46μm,粉末密度为1493kg / m3。空气通过以下三种方式引入:(1)仅在顶部,(2)仅在底部,(3)在改变空气流速的床的顶部和底部。测量了通过孔的粉末的累积质量,床顶部的间隙空气压力和床高度。床的空隙度通过容器中粉末的剩余质量,粉末密度,床的高度和容器的内径来估算。我们发现,当在床的顶部和底部同时引入相同流速的空气时,可获得流态化的粘性粉末的稳定流动以及质量流动区域。然后,其趋势表明,随着床高度的减小,间隙气压和空隙率增加。然后,我们确定了粉末的质量流量与粘性粉末喷出过程中空隙的平方根和间隙气压成正比。

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