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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 of electrostatic charge generation in gas-solid fluidized beds in turbulent versus pre-turbulent flow regime
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Comparison of electrostatic charge generation in gas-solid fluidized beds in turbulent versus pre-turbulent flow regime

机译:湍流与湍流流动状态下气固流化床静电电荷产生的比较

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In this work, the effect of gas velocity on the electrostatic charge generation in gas-solid fluidized beds was studied with a specific focus on the transition to turbulent flow regime. Experiments were conducted at a pressure of 2600 kPa (abs) with fluidizing gas velocities of 1.5, 3, and 5 times of U-mf (pre-turbulent regimes) and 7.5 times of U-mf (turbulent regime). Increasing the gas velocity and transitioning to the turbulent flow regime improved particle-wall contacts; and thus, augmented the extent of wall fouling, which indicates the increase in bed electrostatic charge generation. The amount of fouling was approximately five times larger in turbulent flow regime (7.5 U-mf) in comparison to that for the lowest gas velocity examined in bubbling flow regime (1.5 U-mf). The particles coating on the column wall consisted of a thick bottom layer which extended to a height of approximately 1 m above the distributor plate, and a thin top layer which extended to the top of the column near the outlet. The particles net specific charge in the top and bottom layers did not vary with the increase in gas velocity. However, the net charge of these particles increased. The fine particles entrained from the bed had a net negative charge resulting in a net positive charge to be left behind in the bed contributing to the increase in the magnitude of wall fouling at higher gas velocities, especially in turbulent flow regime. (C) 2017 Elsevier B.V. All rights reserved.
机译:在这项工作中,研究了气体速度对气固流化床中的静电电荷产生的影响,采用特定于转变为湍流的流动状态。实验在2600kPa(ABS)的压力下进行,流化气体速度为1.5,3和5倍的U-MF(预湍流制度)和7.5倍的U-MF(湍流状态)。增加气体速度并过渡到湍流状态改善的粒子壁触点;因此,增强了墙壁污垢的程度,这表明床静电电荷产生增加。与在鼓泡流动状态(1.5u-MF)中检查的最低气体速度相比,污垢量在湍流状态(7.5u-MF)中的污垢量大约为5倍。柱壁上的颗粒涂覆由厚的底层组成,该厚底层延伸到分配板上方约1米的高度,以及薄的顶层,该薄层延伸到出口附近塔的顶部。顶层和底层中的颗粒特定电荷不会随气体速度的增加而变化。然而,这些颗粒的净电荷增加了。从床中夹带的细颗粒具有净负电荷,导致在床上留下的净正电荷导致覆盖的净电荷有助于在较高气体速度下墙壁污垢的大小增加,尤其是在湍流状态下。 (c)2017 Elsevier B.v.保留所有权利。

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