A pseudo-homogeneous model, considering the axial and radial heat mass transfer characteristics of an oxidative coupling methane (OCM) packed-bed catalytic reactor, was utilized to represent its thermal reaction performance in a wide range variation operating conditions investigated this research. This is another step towards distinguishing direct contribution reactions indirect reactor's struc...

This research study investigates the modelling and simulation of biomass anaerobic dark fermentation in bio-hydrogen production a continuous plug flow reactor. A CFD multiphase full transient model long-term horizons was adopted to biohydrogen mode. Both discharge biomass, which prevents accumulation solid parts, recirculation liquid phase ensure constant access nutrient solution. The effect hy...