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Investigation of the pressure drop increase in a square free-vortex cyclonic separator operating at low particle concentration

机译:低颗粒浓度在低颗粒浓度下运行的平方自由涡旋旋风分离器的压降调查

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This paper reports experimental and numerical results obtained in a free-vortex gas-solid separator, in which the classic conical-section of the device is replaced by a larger square chamber, where the vortex is free to evolve. An adjustable vortex-limiting plate is introduced at the cross-section in order to allow the inversion of the coherent structure and guarantee a natural vortex length of the swirling flow according to the inlet velocity in the separator. Both single- phase and multiphase flows were analyzed. hi the latter case, only very low particle concentrations, between 100 and 500 mg/m(3), were considered. Compared to the classic cyclonic separators, the new geometry showed advantages in performance, such as a smaller pressure drop. Moreover, unexpected behavior was observed, since the pressure drop increased by an average of 10% when the particles were injected into the flow at the low concentrations considered. (C) 2020 Elsevier B.V. All rights reserved.
机译:本文报告了在自由涡旋气固分离器中获得的实验性和数值结果,其中器件的经典圆锥部分被更大的方形室取代,其中涡流是自由进化的。 在横截面上引入可调节的涡流板,以允许相干结构的反转,并根据分离器中的入口速度保证旋流的天然涡流长度。 分析了单相和多相流。 在后一种情况下,考虑后一种情况,仅考虑100至500mg / m(3)之间的非常低的颗粒浓度。 与经典的旋风分离器相比,新几何形状在性能方面表现出优点,例如较小的压降。 此外,观察到意外的行为,由于当颗粒注入到所考虑的低浓度的流动中时,压降增加了10%的平均值。 (c)2020 Elsevier B.V.保留所有权利。

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