Abstract
AbstractAn experimental study has been made of the gasification of poplar bark particles exposed to a helium/water vapor atmosphere in a fixed‐bed reactor at 873–973 K. with and without silica catalyst. The effect of temperature on gas yields, calorific value and carbon conversion was evaluated for the pyrolytic conversion and steam‐char gasification stages. The kinetics of the production of various gases in catalytic steam‐char reaction has been studied.
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