Abstract
Abstract
We have recently reported on the impact of CO2 on biomass gasification and its ability to more effectively gasify biomass than steam. Continuing this investigation has led to understanding the impact of heating rates and different reaction environments. This article presents the results from the gasification of various biomass feedstocks. Heating rates were varied from 1 to 100°C min−1 to ballistic rates (∼500°C min−1). Gasification media investigated include H2O/N2, CO2, CO2/N2/H2O, and O2/N2. Global activation energies for pyrolysis were found to be significantly higher than for gasification, whereas those for the grasses were significantly lower than the woods, possibly indicating a catalytic effect during pyrolysis of the high mineral content herbaceous feedstocks. CO2 pyrolysis (110–450°C) activation energy values for lignin, cellulose, and biomass were 22–49, 202–230, and 28–72 kJ mol−1, respectively, and CO2 gasification (500–700°C) values for lignin and biomass were 12–38 and 9–57 kJ mol−1, although cellulose did not exhibit significant mass loss in the gasification interval 500–700°C. Using a least squares fit on the rate of mass loss fraction, the global decomposition reaction during pyrolysis for lignin in either medium was found to be third order, whereas that for cellulose was first order and for the various biomass samples either first or second order. The most significant difference in biomass processing in CO2, when compared with steam gasification, occurred above 750°C where nearly all of the biomass was converted to volatiles with less than 2% ash remaining after CO2 gasification. Only when pure CO2 was used as the gasification medium under a slow heating rate did complete processing of the components to volatile products occur. Gas chromatography analysis has shown the effect of CO2 on product distribution. Data are presented focusing on the relation between gasification medium, feedstock selection, and major chemical species evolution.
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