The Lifting Efficiency of Coarse Particles in Vertical Pipes

Article Preview

Abstract:

A numerical method has been developed to analyze the solid-liquid two-phase flow with coarse particles in vertical pipes. Based on the numerical study, a concept of lifting efficiency has been suggested to describe the efficiency of lifting solid particles by the moving liquid. The lifting efficiency can be defined as, where vs is the average velocity of the solid particles and vl is the average speed of the liquid. It was found that when the liquid speed is lower than 3m/s, the lifting efficiency is increased when the liquid speed is increased. On the other hand if the liquid speed is more than 3m/s, the lifting efficiency will decrease if the liquid speed increases. It was also found that the speed of the particles will decrease if pipe vibration frequency is increased. However the lifting efficiency remains unchanged compared with the stationary pipes.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

1219-1224

Citation:

Online since:

July 2011

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2011 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] Xia J. Two phase flow and its application in hydraulic lifting of ocean polymetallic nodules, doctoral dissertation, China Mineral University, (2000).

Google Scholar

[2] Wasp et al. Solid-liquid flow slurry pipeline transportation, Translated by Yellow River Commission, Hydropower Publisher, Beijing (1980).

Google Scholar

[3] Fei et al. Fluid transport of slurry and particles, Tsinghua University Press, (1994).

Google Scholar

[4] Ni and Wang. The mechanism of the steady solid-liquid two-phase flow with high concentration solid phase, Part I: Theory, Journal of Hydraulics, May (2000).

Google Scholar

[5] Ni and Wang. The mechanism of the steady solid-liquid two-phase flow with high concentration solid phase, Part II: Applications, Journal of Hydraulics, May (2000).

Google Scholar

[6] Wang A, Liu N S, Lu X Y. Large eddy simulation of particle transport in fully developed vertical turbulent channel flow, Journal of Hydrodynamics(Ser. B), 2001, 16(4): 386-392.

Google Scholar

[7] Winkler C, Rani S L, Vanka S. Preferential concentration of particles in a fully developed turbulent square duct flow, International Journal of Multiphase Flow, 2004, 30: 27-50.

DOI: 10.1016/j.ijmultiphaseflow.2003.11.003

Google Scholar

[8] Liu et all. Large eddy flow simulations for two-phase flow in a 3-D ditch, Journal of Huazhong University of Science and Technology (Natural Science), 2004, 32(11): 10-12.

Google Scholar

[9] Singh P, Hesla T I, Joseph D D. Distributed Lagrange multiplier method for particulate flows with collisions, International Journal of Multiphase Flow, 2003, 29: 495-509.

DOI: 10.1016/s0301-9322(02)00164-7

Google Scholar

[10] Tsuji T, Narutomi R, Yokomine T, et al. Unsteady three-dimensional simulation of interactions between flow and two particles. International Journal of Multiphase Flow, 2003, 29: 1431-1450.

DOI: 10.1016/s0301-9322(03)00137-x

Google Scholar

[11] Dorgan A. and Loth E. Simulation of particles released near the wall in a turbulent boundary layer. International Journal of Multiphase Flow, 2004, 30: 649-673.

DOI: 10.1016/j.ijmultiphaseflow.2004.05.006

Google Scholar

[12] Li P. Uplifting of coarse particles in vertical pipes, doctoral dissertation, Tsinghua University, (2007).

Google Scholar

[13] Xia J. et al. Stagnation effect of the coarse particles in vertical pipes, Mineral Engineering, 22(3), (2002).

Google Scholar

[14] Zou W. Private communications, (2009).

Google Scholar

[15] Jiang L. Lfting speed and concentration of the coarse particles in vertical pipes, Master thesis, Tsinghua University, (2005).

Google Scholar

[16] Huang et al. Equations for dispersed particle movement in any fluid flow, Applied mathematics and mechanism 2000(3): 265.

Google Scholar

[17] Ansys12. 0 Help documents, Ansys Inc. (2009).

Google Scholar