Hydrogenation of levulinic acid (LA) into γ-valerolactone (GVL) with Ru/C catalytic system involves homogeneous/heterogeneous reactions, multiphase mass transfer and hydrogen dissolution. The understanding of these physiochemical phenomena is fundamental to propose the performance improvement strategies in such reaction system. In this study, a pore-scale multiphase reactive transport model based on the lattice Boltzmann method (LBM) is developed to simulate the conversion of LA to GVL over Ru/C catalyst. A Carnahan-Starling equation of state (CS EOS) modified Shan-Chen pseudopotential model is applied for gas–liquid flow. The model is validated by comparing the simulation predictions with existing experimental results. Simulation results show that the intra-particle diffusion distance of hydrogen is shorter than that of LA. The LA consumption rate is found to be determined by temperature and dissolved hydrogen when the average concentration of LA is higher than a critical value (about 0.5 mol/L). Notable negative effect of LA intra-particle mass transfer on the reaction has been observed for the LA average concentration lower than 0.5 mol/L. The reaction-generated water would result in a little inhibition on LA hydrogenation. To enhance the utilization of catalyst and reduce the local transport resistant, hollow spheres or coating catalyst are more effective for this system. We demonstrate the usefulness of the present pore-scale LB model in providing guidance for efficient hydrogenation LA into GVL.
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