Abstract
A mathematical model for the thermal oxidation of coal in a pseudo-fluidized catalyst bed is suggested. A three-phase system: catalyst, gas and coal, is considered. The boundary conditions for the pulse operation of the reactor are discussed.
Abstract
Описана математическая модель процесса переработкя в псевдоожиженном слое каталинзатора. Рассматривается трехфазная система: катализатор, газ, уголь. Обсуждаются граничные условия для реактора, работающего в импульсном режиме.
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Azhishchev, N.A., Bykov, V.I. Mathematical model for the thermal oxidation of coal in pseudo-fluidized catalyst bed. React Kinet Catal Lett 27, 235–237 (1985). https://doi.org/10.1007/BF02070449
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DOI: https://doi.org/10.1007/BF02070449