Macrokinetic model of pyrolysis of carbonaceous feedstock in a tubular reactor


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Abstract

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.

About the authors

V. I. Bykov

Emanuel Institute of Biochemical Physics

Email: bykov@deom.chph.ras.ru
Russian Federation, ul. Kosygina 4, Moscow, 119334

S. M. Lomakin

Emanuel Institute of Biochemical Physics

Email: bykov@deom.chph.ras.ru
Russian Federation, ul. Kosygina 4, Moscow, 119334

S. B. Tsybenova

Emanuel Institute of Biochemical Physics

Email: bykov@deom.chph.ras.ru
Russian Federation, ul. Kosygina 4, Moscow, 119334

S. D. Varfolomeev

Emanuel Institute of Biochemical Physics

Author for correspondence.
Email: bykov@deom.chph.ras.ru
Russian Federation, ul. Kosygina 4, Moscow, 119334


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