Shiliang Yang

TL;DR: In this article, a comprehensive review of particle clustering in CFB risers is presented, focusing on the performance of gas-solid fluidized beds in terms of hydrodynamics and overall performance.

TL;DR: In this article, the authors investigated the scouring efficacy of three Granular Activated Carbon (GAC) particle diameters (namely, 1.20", 1.85mm, and 2.18mm) using an accelerometer to reveal the fluid dynamics.

TL;DR: In this article, a simulation of a three-dimensional bubbling fluidized bed is numerically simulated via the computational fluid dynamics coupled with the discrete element method (CFD-DEM) incorporated with heat and mass transfer, and chemical reactions.

TL;DR: In this article, a high-speed video camera and ImageJ software were used to characterize particle velocity and concentration, and membrane fouling was characterized by the rate of transmembrane pressure (TMP) rise.

TL;DR: In this article, the authors studied the segregation dynamics of the solid phase in a three-dimensional rotating drum consisting of a binary-size mixture via the Discrete Element Method (DEM) and demonstrated that the total kinetic energy, the angle of repose, the time-averaged streamwise velocity and the position of the active-passive interface are global parameters, which are not influenced by size-segregation and thereby provide a critical basis for comparing different systems of various polydispersities.