Producing Hydrogen-Rich Gases by Steam Reforming of Syngas Tar Over CaO/MgO/NiO Catalysts
The objective of this study was to develop nanosized CaO, MgO, and NiO catalysts for tar removal in biomass gasification, significantly enhancing the quality of the produced gases. Catalysts were tested in a fixed-bed reactor for biomass tar steam reforming. Toluene was chosen as a model syngas tar compound. For this purpose, pure Ca(OH)2, Mg(OH)2, and Ni(OH)2 precursors were successfully synthesized via a facile solvothermal method. Subsequent calcination of the metal hydroxide precursor at 450 °C resulted in nanosized CaO, MgO, and NiO. Different analytical techniques such as XRD, TEM, SEM, and BET were used to characterize the synthesized nanomaterials. Bulk NiO, CaO, and MgO nanomaterials and a physical mixture of CaO/MgO/NiO (equal NiO/CaO/MgO ratio) were used as catalysts for the steam gasification of toluene. Research showed higher toluene conversions, which resulted in increases in H2 yield as well as CO and CO2 selectivity. Mixed metal oxide CaO/MgO/NiO catalyst exhibited higher performance on toluene conversion, resulting in higher H2 yield and CO2 selectivity.
A. A. Rownaghi and R. L. Huhnke, "Producing Hydrogen-Rich Gases by Steam Reforming of Syngas Tar Over CaO/MgO/NiO Catalysts," ACS Sustainable Chemistry and Engineering, vol. 1, no. 1, pp. 80 - 86, American Chemical Society (ACS), Jan 2013.
The definitive version is available at https://doi.org/10.1021/sc300042e
Chemical and Biochemical Engineering
National Science Foundation (U.S.)
Keywords and Phrases
Biomass gasification; Gas cleaning and conditioning; Mixed metal oxide catalysts
International Standard Serial Number (ISSN)
Article - Journal
© 2013 American Chemical Society (ACS), All rights reserved.
01 Jan 2013
This work has been supported in part by the National Science Foundation EPSCoR program under Grant no. EPS 0814361 and the Director of the Oklahoma Agricultural Experiment Station.