Investigating Dual Inlet Cyclone Separator Performance: Effects of Vortex Finder Diameter, Shape, and Particle Diameter on Separation Efficiency and Pressure Drop

Authors

  • Saikat Barua Faculty of Mechanical and Manufacturing Engineering, Universiti Tun Hussein Onn Malaysia, 86400 Parit Raja, Johor, Malaysia
  • Mohd Faizal Mohideen Batcha Center for Energy and Industrial Environment Studies (CEIES), Faculty of Mechanical and Manufacturing Engineering, Universiti Tun Hussein Onn Malaysia, 86400 Parit Raja, Johor, Malaysia
  • Azriszul Mohd Amin Faculty of Mechanical and Manufacturing Engineering, Universiti Tun Hussein Onn Malaysia, 86400 Parit Raja, Johor, Malaysia
  • Akmal Nizam Mohammed Faculty of Mechanical and Manufacturing Engineering, Universiti Tun Hussein Onn Malaysia, 86400 Parit Raja, Johor, Malaysia
  • Makatar Wae-hayee Energy Technology Research Center, Faculty of Engineering, Prince of Songkla University, Hatyai, Songkhla 90110, Thailand

DOI:

https://doi.org/10.37934/arfmts.121.2.90105

Keywords:

Cylone separator, bortex finder, CFD, K-ε RNG

Abstract

The diameter and shape of the vortex finder of cyclone separator plays a significant role in separation efficiency and pressure drop. Currently, there have been many studies conducted on the shape and ratio of vortex finder of cyclone separator. This paper aims to compare numerical results of Raynold stress turbulence model RSM with K-ε RNG numerical analysis results and analyse the effect of further variation of the vortex finder diameter and shape of dual inlet cyclone separators. Five variation of vortex finder diameters namely 291mm, 310mm, 330mm, 348mm, and 366mm, four types of vortex finder shapes namely normal (cylindrical), spiral, divergent and spiral-divergent have been studied with different particle diameter and constant inlet velocity. The result obtained from this study suggests that increasing the vortex finder diameter have negative effect on separation efficiency. It also shows that increasing the vortex finder diameter consistently decrease the pressure drop. From the result, it is been found that the 291mm vortex finder has higher separation efficiency than the rest. Analysis with different vortex shapes, the spiral-divergent shape proved to be best in terms of separation efficiency.

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Author Biographies

Saikat Barua, Faculty of Mechanical and Manufacturing Engineering, Universiti Tun Hussein Onn Malaysia, 86400 Parit Raja, Johor, Malaysia

saikatuthm@gmail.com

Mohd Faizal Mohideen Batcha, Center for Energy and Industrial Environment Studies (CEIES), Faculty of Mechanical and Manufacturing Engineering, Universiti Tun Hussein Onn Malaysia, 86400 Parit Raja, Johor, Malaysia

mfaizal@uthm.edu.my

Azriszul Mohd Amin, Faculty of Mechanical and Manufacturing Engineering, Universiti Tun Hussein Onn Malaysia, 86400 Parit Raja, Johor, Malaysia

azriszul@uthm.edu.my

Akmal Nizam Mohammed, Faculty of Mechanical and Manufacturing Engineering, Universiti Tun Hussein Onn Malaysia, 86400 Parit Raja, Johor, Malaysia

akmaln@uthm.edu.my

Makatar Wae-hayee, Energy Technology Research Center, Faculty of Engineering, Prince of Songkla University, Hatyai, Songkhla 90110, Thailand

wmakatar@eng.psu.ac.th

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Published

2024-09-30

How to Cite

Barua, S. ., Mohideen Batcha, M. F. ., Mohd Amin, A. ., Mohammed, A. N. ., & Wae-hayee, M. . (2024). Investigating Dual Inlet Cyclone Separator Performance: Effects of Vortex Finder Diameter, Shape, and Particle Diameter on Separation Efficiency and Pressure Drop. Journal of Advanced Research in Fluid Mechanics and Thermal Sciences, 121(2), 90–105. https://doi.org/10.37934/arfmts.121.2.90105

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Articles