Effect of particle–particle interaction on the bed pressure drop and bubble flow by computational particle-fluid dynamics simulation of bubbling fluidized beds with shroud nozzle

Numerical and experimental study of a novel compact micro fluidized beds reactor for CO2 capture in HVAC

“…Snider et al [27] presented application of the hybrid Euler-Lagrange method for modeling the gasification process in large industrial fluidized bed reactors. Lim et al [28] carried out CPFD simulations in bubbling fluidized beds, and they found that bed pressure drops are similar to those obtained from experimental data.…”

“…Zhang et al [8] evaluated CO 2 14 capture from ambient air in a laboratory-scale bubbling fluidized bed using 1.0 kg adsorbents, and obtained a high pressure drop of around 2500 Pa at a low flow rate. Lim et al [28] carried out CPFD simulations in a bubbling fluidized bed containing large amounts of particles at a high flow rate, and achieved a very high pressure drop of 9450 Pa. A very high pressure drop of 7500 Pa in a large-scale fluidized bed column was also published by Chen et al [25].…”

CPFD simulation on angle of repose with hopper geometries and particle properties

“…Thus, particle–particle interaction will not have a relatively large effect. [ 50 ] However, in this study on the AOR, particle–particle interaction is predicted to be a large variable because is very close to in the part where the AOR is formed.…”

Experimental and CPFD study of gas–solid flow in a cold pilot calciner

“…widely used for numerical simulation of dilute and dense particulate systems, e.g., circulating fluidised bed riser [41], dilute pneumatic conveying [23], bubbling fluidised beds [42,55].…”