Simulation of object motion in a bubbling fluidized bed using a Monte Carlo method

• Published in: Chemical engineering science Vol. 96; pp. 26 - 32
• Main Authors: Garcia-Gutierrez, L.M., Soria-Verdugo, A., Garcia-Hernando, N., Ruiz-Rivas, U.
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 07.06.2013
• Subjects: Bubbling; Bubbling bed; Chemical engineering; Circulation time; Computer simulation; Fluidized beds; Gas fluidization; Monte Carlo; Monte Carlo method; Monte Carlo methods; Object motion; Sinking and rising velocity; Trajectories; Two dimensional; Gas fluidization; Object motion; Sinking and rising velocity; Monte Carlo; Circulation time; Bubbling bed
• DOI: 10.1016/j.ces.2013.02.067
• ISSN: 0009-2509

The motion of a large neutrally-buoyant object immersed in a 2D bubbling fluidized bed was simulated using a Monte Carlo method. The object vertical trajectory within the bed was simulated for a range of dimensionless gas velocities using a simple 1D model. The main characteristics of the object motion were obtained from the trajectory simulation and compared with experimental evidence giving good results. On a second step, the time scale of the motion is introduced in the simulated data by means of well-known 2D correlations for the bubble and dense phase velocity. The circulation time of an object (from the instant when it leaves the freeboard and sinks in the dense phase till the moment it reappears back in the surface) was then obtained and compared with experimental data, showing a general agreement. Finally, an extrapolation for a 3D fluidized bed was made following a similar procedure. •The motion of a neutrally-buoyant object in a bubbling fluidized bed was analyzed.•A 1D Monte Carlo method was employed to simulate the motion.•Some experimental data obtained in a 2D fluidized bed was used in the method.•Experimental and simulated circulation times are in a good agreement for the 2D bed.•The method was extrapolated to a 3D bed and compared to experimental measurements.