Abstract

H2 rich gas produced from Scenedesmus almeriensis biomass residue after lipidic extraction by low temperature catalytic gasification is addressed. The pyrolysis–gasification behavior under different atmospheres (CO2/He, H2O/He and CO2+H2O/He) were investigated using thermal gravimetric analysis. The conversion of the biomass takes place into three stages, according to its composition and corresponding to: loose of water bonded (30–200°C), major pyrolysis involving devolatilization (200–500°C) and decomposition of bio-char produced (500–800°C). The calculated apparent activation energy for the main pyrolysis stage was 97kJmol−1. Ni-based supported alumina catalysts (Ni, Ni–Pt and Ni–Rh) were prepared by impregnation. The catalyst influence on the final gas composition as well as in its HHV determined in mixed CO2+H2O/He gasification carried out in a double fixed bed reactor configuration with the catalyst located in the second bed upstream. Parallel and secondary reactions as reforming of tar and char together with WGS and Boudouard also take place favoring gas fraction yield with a value close to 0.3Nm3 of gas per kg of biomass. The catalytic role of Ni–Pt/Al2O3 catalyst in further reforming of the gas resulting from the gasification improves H2 content even at low temperature interval (600–700°C).

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