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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 >Comparison between rotation swirler and non-rotation swirler in a horizontal swirling flow pneumatic conveying
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Comparison between rotation swirler and non-rotation swirler in a horizontal swirling flow pneumatic conveying

机译:水平旋流气动输送旋转旋流与非旋转旋流的比较

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This paper proposes an application of a rotation swirler to swirling flow pneumatic conveying for reducing the conveying velocity and pressure drop decrease. A comparison with the swirling flow pneumatic conveying generated by a non-rotation swirler and axial flow pneumatic conveying was made, the total pressure drop decrease, minimum conveying velocity, energy consumption, and additional pressure drop decrease were evaluated experimentally. In addition, the cross-section profiles of the particle velocity and particle fluctuation velocity along a pipeline near the minimum pressure drop decrease were measured by the Ply (Particle Image Velocimetry) technique. The pipeline was a 5-m-long horizontal straight acrylic pipe with an inside diameter of 80 mm. Polyethylene particles of diameter of 23 mm were used as the conveying materials. The initial swirl number was varied from 0 to 0.66. The solid mass flow rates of 0.1, 0.28, and 0.47 kg/s were applied, and the superficial air velocity was varied from 9 to 16 m/s. It is revealed that the total pressure drop decrease and power consumption of the swirling flow using the rotation swirler exhibit the smallest values among all cases in the region of low air velocity, and are almost the same as the axial flow in the high air velocity region. The particle velocity and particle fluctuation velocity of the swirling flow originated by the rotation swirler are almost the same as the axial flow in the acceleration regime, but become larger than that of the axial flow near the bottom of the pipeline in the fully developed regime. (C) 2019 Elsevier B.V. All rights reserved.
机译:本文提出了旋转旋流仪的旋转流动气动输送,以降低输送速度和压降降低。通过实验评估了与由非旋转旋流和轴向流动气动输送产生的旋流气动输送产生的旋流气动输送的比较,总压降降低,最小输送速度,能量消耗和额外的压降减少。另外,通过Ply(颗粒图像速度计量)技术测量沿着最小压降下降的管道沿线轴的剖视图和颗粒波动速度的横截面轮廓。管道是5米长的水平直丙烯酸管,内径为80毫米。使用直径为23mm的聚乙烯颗粒作为输送材料。初始旋流数量从0变化到0.66。施加0.1,0.28和0.47kg / s的固体质量流量,浅表空气速度从9-16m / s变化。据透露,使用旋转旋流的旋流的总压降减小和功耗在低空气速度区域中的所有情况下表现出最小的值,并且与高空气速度区域中的轴向流几乎相同。由旋转旋流器起源于旋转旋流的旋流流动的粒子速度和粒子波动速度与加速度方案中的轴向流量几乎相同,但变得大于完全发达的方案中管道底部附近的轴向流动的速度。 (c)2019年Elsevier B.V.保留所有权利。

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