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- W1997753074 abstract "Pyrolysis and steam gasification of nickel-loaded Yallourn coal were carried out in a fluidized bed reactor at ambient pressure. The pyrolysis mode was influenced by the addition of nickel catalyst. The yield of total volatile matter decreased whereas the gas yield markedly increased, when compared with uncatalysed pyrolysis. This is considered to result from tar decomposing on the catalyst and being converted to gases and deposited carbon. For the catalysed steam gasification, ≈ 80 wt% of coal conversion was achieved at 873 K and the gas yield was twelve times as much as that for the uncatalysed reaction. The homogeneous equilibrium in the gas phase controlled the composition of the product gas. The product gas contained little tarry material and a negligible amount of hydrogen sulphide. Nickel was efficiently recovered from the residue by an ammonia-leaching method." @default.
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- W1997753074 date "1985-06-01" @default.
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- W1997753074 title "Nickel-catalysed gasification of brown coal in a fluidized bed reactor at atmospheric pressure" @default.
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- W1997753074 doi "https://doi.org/10.1016/0016-2361(85)90012-2" @default.
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