Macrokinetic model of pyrolysis of carbonaceous feedstock in a tubular reactor

详细

A macrokinetic model of pyrolysis of carbonaceous feedstock in a tubular reactor was proposed. It was shown that, under unsteady-state conditions (at oscillating temperature of feedstock heating), higher conversions can be reached in comparison with steady-state conditions, which agrees with experimental data on flash pyrolysis of biomass in a tubular reactor during heating–cooling cycles.