This document presents a computational fluid dynamics (CFD) investigation of the effect of coal particle size on coal gasification in a fluidized bed. The CFD model uses Eulerian-Eulerian two-fluid modeling approach with kinetic theory of granular flow to simulate gas-solid flow behavior. Simulations were performed with two particle sizes - 0.00062 m and 0.001 m - at fluidization velocities ranging from 0.16 to 1 m/s. The results show that smaller particle size leads to better solid distribution, easier generation of bubbles, and faster fluidization. At high velocities, particle size has little effect other than on bed height expansion. The study provides insights into how particle size impacts hydrodynamics in fluid