Abstract
In the present study the catalytic steam gasification of biomass to produce hydrogen-rich gas with calcined dolomite and Nano-NiO/γ-Al2O3 as catalyst in an externally heated fixed-bed reactor was investigated. The influence of the catalyst and reactor temperature on gasification performance was studied at the temperature range of 700–900°C. Over the ranges of experimental conditions examined, Nano-NiO/γ-Al2O3 and calcined dolomite both revealed better catalytic performance, at the presence of steam tar was completely decomposed as temperature increases from 800 to 900°C. A higher temperature resulted in more H2 and CO2 production, and dry gas yield. The highest H2 content of 51.02 V% and the highest H2 yield of 1.66 m3/kg biomass were observed at the highest temperature level of 900°C.
Notes
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