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- W2022676820 abstract "The catalytic performances of natural Ca-based catalysts (dolomite and limestone) and synthetic Ca-based catalysts, used for improving biomass steam gasification, were fully investigated in a circulating spout-fluid bed reactor. In comparison to the catalytic role in biomass gasification, the synthetic Ca-based catalyst, 20% CaO/Al2O3 (20CaAl), displayed a better catalytic effect on the biomass carbon conversion reaction and tar reforming reaction than natural Ca-based catalysts, but the latter played a better role in the reforming reaction of light hydrocarbon because it contained small quantities of iron oxides. For the two types of Ca-based catalysts, the optimal operating temperature was about 860 °C to upgrade the quality of gas product and increase H2 yield. The catalytic activity of synthetic Ca-based catalysts was visibly improved with the increment of CaO loading, and the preferential range of CaO loading was 12.5−20%. In comparison to the lifetime, 20CaAl (the synthetic catalyst) displayed bette..." @default.
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- W2022676820 date "2010-04-28" @default.
- W2022676820 modified "2023-10-01" @default.
- W2022676820 title "Effects of Ca-Based Catalysts on Biomass Gasification with Steam in a Circulating Spout-Fluid Bed Reactor" @default.
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- W2022676820 doi "https://doi.org/10.1021/ef100081w" @default.
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