Abstract
Controlling hydrogen production during supercritical water gasification (SCWG) of biomass is challenging using conventional mono-metallic catalysts. This work examines the role of Lanthanum (La) both as a catalyst and co-catalyst with Nickel (Ni), for enhancing the Water-Gas Shift (WGS) reaction to maximize hydrogen production. A stirred tank batch reactor was used with glucose as feed (model compound for biomass), from T = 400 to 500 degrees C, residence time = 5-120 min and P = 28 MPa. Compared to non-catalytic gasification, the La2O3/Al2O3 catalyst enhanced both the H-2 and CO2 production by 1.9-fold and 2.0-fold respectively. Ni-La2O3/Al2O3 catalyst increased hydrogen production (3.95 mol/mol feed) to almost thermodynamic equilibrium composition (4.15 mol/mol feed) at 120 min reaction time. By examining the fresh and spent catalysts by various physicochemical techniques, this enhancement is attributed to the Ni promoting tar cracking, while La promoted the WGS reaction and inhibits the methanation reactions. A parametric study was used to optimize reaction conditions, finding that H-2 production and carbon conversion to gaseous products increased significantly with higher reaction time and temperatures and lower feed concentrations. Almost 98% carbon was gasified at 120 min reaction time using Ni-La2O3/Al2O3 as catalyst. Using a controlled feedstock of CO and H-2 to further examine the catalytic mechanism, adding La onto the Ni/Al2O3 enhanced CO2 and H-2 production with negligible CH4 production, showing the importance of the WGS reaction to maximizing H-2 production in SCWG.