A three-dimensional simulation of gas/particle flow and ozone decomposition in the riser of a circulating fluidized bed

Abstract The isothermal decomposition of ozone has been implemented in the CFD code FLOTRACS-MP-3D. The code is a three dimensional (3D) multiphase computational fluid dynamics code with an Eulerian description of both gas and particle phase. The turbulent motion of the particulate phase is modeled using the kinetic theory for granular flow, and the gas phase turbulence is modeled using a sub-grid-scale model, cf. Ibsen et al. (Ind. Eng. Chem. Res. 40 (2001) 5081). The decomposition reaction is studied in a 3D representation of a 0.254 m i.d. riser, which has been studied experimentally by Ouyang et al. (Powder Technol. 75 (1993) 73). The authors obtained profiles of ozone concentration in the 10.85-m high riser by the use of a UV detector system. Furthermore, a pressure drop profile was reported. Comparison between measured and simulated time-averaged ozone concentration at different elevations in the riser shows good agreement. The 3D representation of the reactor geometry gives better predictions of the radial variation in concentration than in a similar 2D simulation, Samuelsberg and Hjertager (Adv. Multiphase Flow (1995) 679). A parameter study is performed to investigate improvements in the predicted pressure drop profile.

[1]  A. I. Lygeros,et al.  Simulation and design of fluid-catalytic cracking riser-type reactors , 1996 .

[2]  S. Sundaresan,et al.  The role of meso-scale structures in rapid gas–solid flows , 2001, Journal of Fluid Mechanics.

[3]  P. Foscolo,et al.  Generalized friction factor and drag coefficient correlations for fluid-particle interactions , 1985 .

[4]  D. Zhang,et al.  High-resolution three-dimensional numerical simulation of a circulating fluidized bed , 2001 .

[5]  O. E. Potter,et al.  Ozone decomposition in a 0.254 m diameter circulating fluidized bed reactor , 1993 .

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

[7]  C. Wen Mechanics of Fluidization , 1966 .

[8]  Tron Solberg,et al.  Evaluation of a Three-Dimensional Numerical Model of a Scaled Circulating Fluidized Bed , 2001 .

[9]  Yincheng Guo,et al.  Advanced model for turbulent gas–solid flow and reaction in FCC riser reactors , 1999 .

[10]  Jam Hans Kuipers,et al.  Mixing and segregation in a bidisperse gas-solid fluidized bed: a numerical and experimental study , 2004 .

[11]  M. Syamlal,et al.  Fluid dynamic simulation of O3 decomposition in a bubbling fluidized bed , 2003 .

[12]  Wei Ge,et al.  CFD simulation of concurrent-up gas-solid flow in circulating fluidized beds with structure-dependent drag coefficient , 2003 .

[13]  Sofiane Benyahia,et al.  Numerical Analysis of a Reacting Gas/Solid Flow in the Riser Section of an Industrial Fluid Catalytic Cracking Unit , 2003 .

[14]  Tron Solberg,et al.  Predictions of gas/particle flow with an Eulerian model including a realistic particle size distribution , 2000 .

[15]  Reghan J. Hill,et al.  INERTIAL EFFECTS IN SUSPENSION AND POROUS-MEDIA FLOWS , 2001 .

[16]  Simulation of Two-Phase Gas/Particle Flow and Ozone Decomposition in a 0.25m I.D. Riser , 1995 .