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- W2081871942 abstract "In the present study the catalytic steam gasification of MSW to produce hydrogen-rich gas or syngas (H2 + CO) with calcined dolomite as a catalyst in a bench-scale downstream fixed bed reactor was investigated. The influence of the catalyst and reactor temperature on yield and product composition was studied at the temperature range of 750–950 °C, with a steam to MSW ratio of 0.77, for weight hourly space velocity of 1.29 h−1. Over the ranges of experimental conditions examined, calcined dolomite revealed better catalytic performance, at the presence of steam, tar was completely decomposed as temperature increases from 850 to 950 °C. Higher temperature resulted in more H2 and CO production, higher carbon conversion efficiency and dry gas yield. The highest H2 content of 53.29 mol%, and the highest H2 yield of 38.60 mol H2/kg MSW were observed at the highest temperature level of 950 °C, while, the maximum H2 yield potential reached 70.14 mol H2/kg dry MSW at 900 °C. Syngas produced by catalytic steam gasification of MSW varied in the range of 36.35–70.21 mol%. The char had a highest ash content of 84.01% at 950 °C, and negligible hydrogen, nitrogen and sulphur contents." @default.
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- W2081871942 date "2009-01-01" @default.
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- W2081871942 title "Hydrogen-rich gas from catalytic steam gasification of municipal solid waste (MSW): Influence of catalyst and temperature on yield and product composition" @default.
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- W2081871942 doi "https://doi.org/10.1016/j.ijhydene.2008.09.070" @default.
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