Modelling of penetration of horizontal supersonic nozzles in high temperature fluidised beds

Supersonic nozzles have been applied in various jet-induced fluidised bed attrition processes such as jet milling and Fluid Coking. In jet-induced particle attrition, the penetration length into the bed of the jet issuing from the supersonic nozzle is a critical property that affects the attrition mechanisms. A numerical model was developed to predict the penetration length of jets issuing from a horizontal supersonic nozzle in high temperature fluidised beds, based on an Eulerian–Eulerian multiphase model and Granular kinetic theory. The predicted jet penetration lengths are in very good agreement with the experimental data and the predictions of Li's empirical correlation [Li, “Penetration of High Velocity Horizontal Gas Jets Into a Fluidized Bed at High Temperature”, in Fluidization XIII, S. D. Kim, Y. Kang, J. K. Lee, Y. C. Seo, Eds., Gyeong-ju, Korea 2010; Engineering Conferences International, Gyeong-ju, Korea 2010, pp. 893–900.]. The simulation results have also demonstrated that the fluidisation velocity and bed temperature have little influence on jet penetration length. © 2013 Canadian Society for Chemical Engineering

[1]  David G. Schaeffer,et al.  Instability in the evolution equations describing incompressible granular flow , 1987 .

[2]  D. Grecov,et al.  Numerical simulation of single and multiple gas jets in bubbling fluidized beds , 2009 .

[3]  C. Briens,et al.  Particle attrition mechanism with a sonic gas jet injected into a fluidized bed , 2007 .

[4]  N. Ellis,et al.  CFD simulation of gas–solid bubbling fluidized bed: A new method for adjusting drag law , 2009 .

[5]  Mojtaba Ghadiri,et al.  Fluidised-bed jet milling of pharmaceutical powders , 2004 .

[6]  F. Taghipour,et al.  Experimental and computational study of gas¿solid fluidized bed hydrodynamics , 2005 .

[7]  W. Jones,et al.  The prediction of laminarization with a two-equation model of turbulence , 1972 .

[8]  D. Jeffrey,et al.  Kinetic theories for granular flow: inelastic particles in Couette flow and slightly inelastic particles in a general flowfield , 1984, Journal of Fluid Mechanics.

[9]  C. Briens,et al.  Effect of a shroud on entrainment into a submerged jet within a fluidized bed , 2008 .

[10]  M. Syamlal,et al.  MFIX documentation theory guide , 1993 .

[11]  Rajamani Krishna,et al.  Comparative analysis of CFD models of dense gas–solid systems , 2001 .

[12]  Dimitri Gidaspow,et al.  Hydrodynamics of Fiuidizatlon and Heat Transfer: Supercomputer Modeling , 1986 .

[13]  Fariborz Taghipour,et al.  CFD Modeling of the Hydrodynamics and Reaction Kinetics of FCC Fluidized-Bed Reactors , 2005 .

[14]  P. Griffith,et al.  Modeling the Injection of Gas-Liquid Jets into Fluidized Beds of Fine Particles , 2008 .

[15]  Jiyu Zhang,et al.  Numerical simulation and verification of a gas-solid jet fluidized bed , 1996 .

[16]  S. Savage Streaming motions in a bed of vibrationally fluidized dry granular material , 1988, Journal of Fluid Mechanics.

[17]  Britt Halvorsen,et al.  Numerical simulation of particulate flow by the Eulerian-Lagrangian and the Eulerian-Eulerian approach with application to a fluidized bed , 2005, Comput. Chem. Eng..

[18]  Cedric Briens,et al.  High velocity attrition nozzles in fluidized beds , 2007 .

[19]  Yang Wang,et al.  Studies on the inclined jet penetration length in a gas—solid fluidized bed , 1997 .

[20]  Tingwen Li,et al.  Numerical simulation of horizontal jet penetration in a three-dimensional fluidized bed , 2008 .

[21]  J. Grace,et al.  CFD modelling of a liquid–solid fluidized bed , 2007 .

[22]  Ulrich Renz,et al.  Verification of Eulerian simulation of spontaneous bubble formation in a fluidized bed , 1998 .

[23]  D. Gunn Transfer of heat or mass to particles in fixed and fluidised beds , 1978 .

[24]  L. Behie,et al.  Jet momentum dissipation at a grid of a large gas fluidized bed , 1970 .

[25]  D. Gidaspow,et al.  A bubbling fluidization model using kinetic theory of granular flow , 1990 .