Numerical Investigation of the Effect of Vortex Finder Diameter Ratio on Cyclone Separator Performance

Document Type : Original Article

Authors
1 Assistant professor, Department of Mechanical Engineering, Bozorgmehr University of Qaenat, Qaen, Iran
2 B.Sc, Department of Mechanical Engineering, Bozorgmehr University of Qaenat, Qaen, Iran
Abstract
In this study, the effect of the vortex finder diameter ratio on the particle separation efficiency and pressure drop of a cyclone separator was numerically investigated. Computational fluid dynamics (CFD) simulations were performed using ANSYS Fluent 21. Five vortex finder diameter ratios (D₂/D₁ = 0.25, 0.5, 1, 2, and 4) were examined to evaluate their influence on cyclone performance. Air was considered as the continuous phase with an inlet velocity of 1 m/s, while solid particles with a diameter of 10 μm were used as the dispersed phase. The simulation results showed that increasing the vortex finder diameter ratio from 0.25 to 0.5 significantly reduced the pressure drop, whereas further increases in the diameter ratio resulted in only minor changes in pressure drop. The cyclone with a diameter ratio of 0.5 achieved a particle separation efficiency of 100%, while the cyclone with a diameter ratio of 4 was unable to separate the particles effectively. Furthermore, considering both separation efficiency and pressure drop, the cyclone equipped with a cylindrical vortex finder (D₂/D₁ = 1) exhibited the most favorable overall performance compared with the other investigated diameter ratios. These findings demonstrate that the vortex finder diameter ratio is a critical design parameter and that selecting an appropriate geometry can significantly improve cyclone performance while reducing energy losses.
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[1] J. Gimbun, T. G. Chuah, T. S. Y. Choong, and A. Fakhru’l-Razi, "Prediction of the effects of cone tip diameter on the cyclone performance," Journal of Aerosol Science, Vol. 36, No. 8, pp. 1056–1065, 2005, DOI: 10.1016/j.jaerosci.2004.10.014.
[2] B.-K. Lee, K.-R. Jung, and S.-H. Park, "Development and application of a novel swirl cyclone scrubber—(1) Experimental," Journal of Aerosol Science, Vol. 39, No. 12, pp. 1079–1088, 2008, DOI: 10.1016/j.jaerosci.2008.07.010.
[3] P. Baltrenas, M. Pranskevicius, and A. Venslovas, "Optimization of the new generation multichannel cyclone cleaning efficiency," Energy Procedia, Vol. 72, pp. 188–195, 2015, DOI: 10.1016/j.egypro.2015.06.027.
[4] H. Safikhani and P. Mehrabian, "Numerical study of flow field in new cyclone separators," Advanced Powder Technology, Vol. 27, No. 2, pp. 379–387, 2016, DOI: 10.1016/j.apt.2016.01.011. (in Persian)
[5] A.-N. Huang, N. Maeda, D. Shibata, T. Fukasawa, H. Yoshida, H.-P. Kuo, and K. Fukui, "Influence of a laminarizer at the inlet on the classification performance of a cyclone separator," Separation and Purification Technology, Vol. 174, pp. 408–416, 2017, DOI: 10.1016/j.seppur.2016.09.053.
[6] D. Misiulia, A. G. Andersson, and T. S. Lundström, "Effects of the inlet angle on the collection efficiency of a cyclone with helical-roof inlet," Powder Technology, Vol. 305, pp. 48–55, 2017, DOI: 10.1016/j.powtec.2016.09.050.
[7] V. Kumar and K. Jha, "Effects of convergent-divergent vortex finders on the performance of cyclone separators using computational fluid dynamics simulations," Simulation, Vol. 96, No. 1, pp. 31–42, 2020, DOI: 10.1177/0037549719846570.
[8] Y. Yao, M. Shang, Z. Huang, T. Zhou, M. Zhang, H. Yang, and J. Lyu, "Effects of the inlet duct length on the performance of a dense medium cyclone: An experimental and numerical study," Chemical Engineering Research and Design, Vol. 187, pp. 41–50, 2022, DOI: 10.1016/j.cherd.2022.08.031.
[9] D. Kumar, V. Kumar, and K. Jha, "Effects of hyperboloid vortex finder and inlet angle on the cyclone flow pattern and separation efficiency," Chemical Engineering Research and Design, Vol. 204, pp. 81–96, 2024, DOI: 10.1016/j.cherd.2024.02.017.
[10] D. Kumar, K. Jha, V. Kumar, and L. S. Brar, "Performance evaluation of cyclone separators with elliptical cross-section using large-eddy simulation," Powder Technology, Vol. 438, Art. no. 119660, 2024, DOI: 10.1016/j.powtec.2024.119660.
[11] K. Zhang, Z. Yan, Z. Sun, H. Yang, and G. Yang, "Performance evaluation and prediction model for novel elliptical cyclone separators," Separation and Purification Technology, Vol. 354, Art. no. 128888, 2025, DOI: 10.1016/j.seppur.2024.128888.
[12] K. S. Babu, S. P. Sivapirakasam, and S. Venkatesh, "CFD-based evaluation of performance enhancement in a baffle-integrated settling chamber coupled with a cyclone separator," Powder Technology, Vol. 469, Art. no. 121767, 2026, DOI: 10.1016/j.powtec.2025.121767.
[13] E. Dehdarinejad, M. Bayareh, F. Parvaz, S. H. Hosseini, and G. Ahmadi, "Performance analysis of a gas cyclone with a converging-diverging vortex finder," Chemical Engineering Research and Design, Vol. 193, pp. 587–599, 2023, DOI: 10.1016/j.cherd.2023.04.012. (in Persian)
[14] H. A. Chaghakaboodi and M. Saidi, "Numerical study of gas-solid flow in a square cyclone separator with different vortex finders," Chemical Engineering Research and Design, Vol. 194, pp. 621–635, 2023, DOI: 10.1016/j.cherd.2023.05.001. (in Persian)
[15] S. B. Pope, Turbulent Flows. Cambridge, U.K.: Cambridge University Press, 2000, DOI: 10.1017/CBO9780511840531.
[16] S. I. Pishbin and M. Moghiman, "Optimization of cyclone separators using genetic algorithm," International Review of Chemical Engineering, Vol. 2, No. 6, pp. 683–691, 2010. (in Persian)
[17] K. Elsayed and C. Lacor, "Optimization of the cyclone separator geometry for minimum pressure drop using mathematical models and CFD simulations," Chemical Engineering Science, Vol. 65, No. 22, pp. 6048–6058, 2010, DOI: 10.1016/j.ces.2010.08.042.
 
 

  • Receive Date 03 July 2025
  • Revise Date 23 December 2025
  • Accept Date 24 December 2025
  • First Publish Date 24 December 2025
  • Publish Date 23 July 2026