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- W2000665804 abstract "Parametric tests, biomass ratio (BR), gasifier temperature, steam to carbon mass ratio (S/C) and type of bed materials, on tar formation were performed during co-gasification of biomass and coal on an external circulating radial-flow moving bed gasifier (ECRMB). The system is composed of three decoupled reactors, i.e. a gas–solid countercurrent moving bed pyrolyzer, a radial flow moving bed gasifier and a riser-type combustor. Calcined olivine was used as both circulating heat carrier and in-situ tar destruction catalyst. It was found that the operation condition has a large impact on tar composition. Naphthalene was found to be the dominate component in all cases at quantities of 40.7–62.6%. Sulfur contents in the tar were reduced with the increasing BR. Tar compositions shift from phenolic compounds and alkyl-substituted PAHs to non-substituted PAHs with the increase of gasifier temperature. Above gasifier temperature of 800 °C phenols and one-ring aromatics were totally decomposed. Higher S/C enhanced the decomposition of naphthalene. In contrast to silica sand, olivine as bed material showed a higher decomposition effect on the phenols and higher hydrocarbons." @default.
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- W2000665804 date "2015-01-01" @default.
- W2000665804 modified "2023-09-25" @default.
- W2000665804 title "Tar formation during co-gasification of biomass and coal under different gasification condition" @default.
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- W2000665804 doi "https://doi.org/10.1016/j.jaap.2014.11.012" @default.
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