Influence of slit structure in hydrocyclone conical section on solid-liquid separation performance

被引：0
|
作者：
Duan J. [1 ]
Huang S. [1 ,2 ]
Gao C. [1 ,2 ]
Chen A. [2 ]
Huang Q. [2 ,3 ]
机构：
[1] School of Chemical Engineering and Technology, Qingdao University of Science and Technology, Qingdao, 266042, Shandong
[2] Qingdao Institute of Bioenergy and Bioprocess Technology, Chinese Academy of Sciences, Qingdao, 266101, Shandong
[3] Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing
来源：
Huagong Xuebao/CIESC Journal | 2019年 / 70卷 / 05期
关键词：
Experimental validation; Flow; Hydrocyclone; Pressure drop; Separation; Separation efficiency; Slit structure;
D O I：
10.11949/j.issn.0438-1157.20181389
中图分类号：
学科分类号：
摘要：
A new type of hydrocyclone with a tangentially slitted structure is designed. The experimental study on the effect of the length, position, number and style of the slit on the separation performance of the hydrocyclone is carried out. It is shown that compared with the traditional hydrocyclone, the pressure drop of the slit-cone hydrocyclone is significantly reduced. The separation efficiency of the hydrocyclone tends to increase at first and then decrease when the length of the slit increases from 10 mm to 50 mm, and an optimal slit length of 20 mm is observed. In the process of moving the 20 mm slit upward from the first 6 mm slit at the bottom of the cone, the influence of the second slit position on the separation efficiency of the hydrocyclone is similar to that of the slit length. That is to say, it tends to increase at first and then decrease, and there is an optimal distance of 80 mm between the first slit and the second one. When keeps the cross-section area of the slits equaling to that of underflow in the traditional hydrocyclone under the conditions of optimized slit length and position, it is found that the separation efficiency of one slit in the cone is better than that of two, and the style of two-slits located at opposite direction is the best among all the cases investigated. Compared with the classical hydrocyclone, the separation efficiency in the optimal slit-cone hydrocyclone can decrease only 1.48% while the absolute pressure drop can reduce as high as 36.84% at a high flow rate. Therefore, it is a promising hydrocyclone for industrial applications to save energy consumption. © All Right Reserved.
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页码：1823 / 1831
页数：8
相关论文
共 44 条
  • [1] Bradley D., The Hydrocyclone: International Series of Monographs in Chemical Engineering, (2013)
  • [2] Svarovsky L., Thew M., Hydrocyclones: Analysis and Applications, (2013)
  • [3] Svarovsky L., Solid-Liquid Separation, (2000)
  • [4] Vieira L.G.M., Damasceno J.J.R., Barrozo M.A.S., Improvement of hydrocyclone separation performance by incorporating a conical filtering wall, Chemical Engineering and Processing, 49, 5, pp. 460-467, (2010)
  • [5] Mognon J.L., da Silva J.M., Bicalho I.C., Et al., Modular mini-hydrocyclone desilter type of 30 mm: an experimental and optimization study, Journal of Petroleum Science and Engineering, 129, pp. 145-152, (2015)
  • [6] Zhao L., Jiang M.H., Xu B., Et al., Development of a new type high-efficient inner-cone hydrocyclone, Chemical Engineering Research and Design, 90, 12, pp. 2129-2134, (2012)
  • [7] Zhao L., Li Y., Xu B., Et al., Design and numerical simulation analysis of an integrative gas-liquid-solid separation hydrocyclone, Chemical Engineering & Technology, 38, 12, pp. 2146-2152, (2015)
  • [8] Ma Y., Wang Z.B., Jin Y.H., Simulation of oil-phase concentration field in vane-guided hydrocyclone, CIESC Journal, 62, 2, pp. 420-426, (2011)
  • [9] Ma Y., Jin Y.H., Wang Z.B., Simulation the flow field in hydrocyclone with two different kinds of inlet structure, Chemical Industry and Engineering Progress, 28, pp. 497-501, (2009)
  • [10] Xu Y.X., Liu Y., Zhang Y.H., Et al., Effect of shear stress on deoiling of oil-contaminated catalysts in a hydrocyclone, Chemical Engineering & Technology, 39, 3, pp. 567-575, (2016)
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