Numerical study on particle motions in swirling flows in a cyclone separator

2006 ◽  
Vol 15 (2) ◽  
pp. 181-185 ◽  
Author(s):  
Kazuyoshi Matsuzaki ◽  
Hideaki Ushijima ◽  
Mizue Munekata ◽  
Hideki Ohba
2012 ◽  
Vol 516-517 ◽  
pp. 976-979 ◽  
Author(s):  
Nan Gui

Swirling flows are widely used in energy engineering, such as swirling combustor, cyclone separator in pulverized coal burners. The vortex evolution and correlation between twin swirling flows are investigated via direct numerical simulation. Three typical swirl flows with different swirl number are simulated. The structure of vortex evolution, velocity correlation between the twin flows are illustrated and analyzed in detail. The results show the phase-locked correlation of flow velocity between the twin swirling jets which would be useful and helpful for improving the understanding of aerodynamics of multi-swirling systems.


Author(s):  
Bin Xiong ◽  
Xiaofeng Lu ◽  
R. S. Amano

This paper presents a numerical study of gas flow in a square cyclone separator with a double inlet. The turbulence of gas flow is computed by the use of the Reynolds stress model. The distribution of the flow field and pressure drop under different constructional details, which include changes of the shape, size and arrangement of the vortex finder are obtained. The computed results in the distributions of pressure in different sections are verified by comparison with those measured. We found that the center of the flow field is nearly on the geometric center of the cyclone. The flow fields show a feature of Rankine eddy, i.e., a strongly swirling region in the central part and a pseudo-free eddy region of weak swirling intensity near the cyclone wall. Local vortex exists at the corners where the flow changes their direction sharply, but it is less chaotic than in the general square cyclone with a single inlet. The flow field away from the outlet of the vortex finder is different from the Rankine eddy. The pressure-drop increases rapidly with the increase of the inlet velocity, and the pressure-drop increases with the decrease of the diameter of vortex finder and the increase of length of the vortex finder. The calculat ed results of this paper provide some guidance for the optimization of the square cyclone separator structure.


2010 ◽  
Vol 49 (11) ◽  
pp. 5450-5460 ◽  
Author(s):  
Jie Cui ◽  
Xueli Chen ◽  
Xin Gong ◽  
Guangsuo Yu

2011 ◽  
Vol 308-310 ◽  
pp. 232-236
Author(s):  
Wei Wang ◽  
Fang Pu Yang ◽  
Jing Bao Shi ◽  
Ming Fu Luo

With the development of the petroleum industry ,the separation technology has made progress. The cyclone separator with different structure sizes (such as taper Angle, import hole, overflow hole and bottom hole) are numerical simulated. The separating efficiency are greatly influenced by structural dimension through studied.


2019 ◽  
Vol 344 ◽  
pp. 784-796 ◽  
Author(s):  
Haili Zhou ◽  
Zhanqi Hu ◽  
Qinglong Zhang ◽  
Qiang Wang ◽  
Xuan Lv

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