Effects of several calcium-based absorbents and NiO-based catalysts on absorption enhanced pyrolysis-gasification of corn stalk for H-2 production were investigated in a two-stage fixed-bed reactor. The results indicated that the addition of calcined CaCO3, calcined limestone, and calcined dolomite significantly improved the concentration and yield of H-2 in the product gas because of in situ CO2 absorption and the catalytic effects of the CaO species. The magnesium species in calcined dolomite further catalyzed the gasification process and improved CO2 absorption to increase the concentration and yield of H-2. NiO/CaO bi-functional catalysts/absorbents had a more significant catalytic effect on the gasification process than calcined dolomite: although the H-2 concentration in the product gas was lower, the yields of H-2, CO, and CO2 were higher. A large amount of CO2 generation which could not be sufficiently absorbed resulted in increased concentration and yield of CO2 in the product gas. The addition of the NiO/gamma-Al2O3 catalyst together with calcined dolomite further increased the concentration and yield of H-2 in the product gas. A product gas with a maximum H-2 concentration of 85.1 vol.% and negligible amounts of CO2 and C2+ was obtained at a NiO loading of 15 wt.%. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.